Text

Reactor Containment Bldg Integrated Leakage Rate Test, Final Rept
	ML18019B042
Person / Time
Site:	Harris
Issue date:	02/28/1986
From:	; CAROLINA POWER & LIGHT CO.
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ML18019B041	List: ML18019B040; ML18019B042;
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bpb240347 sbobis PDR ADOCH, PS000400 PDR'HEARON HARRIS NUCLEAR POWER PLANT CAROLINA POWER AND LIGHT COMPANY NBW HILL, NORTH CAROLINA REACTOR CONTAINMENT BUILDING INTEGRATED LEAKAGE RATB TBST FEBRUARY 1986 UNIT 1 FINAL REPORT

I TABLE OF CONTENTS Page

1.0 INTRODUCTION

1 2.0 TEST SYNOPSIS 3.0 TEST DATA

SUMMARY

4.0 ANALYSIS AND INTERPRETATION

5.0 REFERENCES

10 TABLE 1 SENSOR LOCATIONS AND WEIGHTING FRACTIONS APPENDICES A ILRT COMPUTER PROGRAM

SUMMARY

B STABILIZATION DATA AND CALCULATIONS C TYPE A

SUMMARY

. DATA By Sensor Enviroment Mass Loss D TYPE A CALCULATIONS Mass Point Analysis Total Time Analysis E VERIFICATION TEST CALCULATIONS Mass Point Analysis F TYPE A PLOTS

. Temperature vs Time Pressure vs Time Dew Point vs Time Containment Mass vs Time Mass Point Leakage Rate vs Time Total Time Leakage Rate vs Time G VERIFICATION TEST PLOTS Average Temperature vs Time Average Pressure vs Time Average Dew Point vs Time Containment Mass vs Time Mass Point Leakage Rate vs Time H SCHEMATIC FOR LEAKAGE RATE MEASURING SYSTEM

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1.0 INTRODUCTION

A successful preoperational Integrated Leakage Rate Test (ILRT) was conducted on the Shearon Harris Nuclear Power Plant (SHNPP) Unit 1 containment between February 21 and February 25, 1986. This test was performed to demonstrate that the containment leakage under prescribed post 'accident conditions does not exceed the allowable values specified in the SHNPP Unit 1 FSAR (Reference 1) and Technical Specifications (Reference 2).

The test was conducted in accordance with the requirements of the ILRT procedure (Reference 3), Appendix J to 10CFR50 (Reference 9), ANSI 56.8 (Reference 10) and ANSI N45.4 (Reference ll).

which satisfied all acceptance criteria are summarized below.

Test results',

Mass Point Total Time Allowable Operational Type A LSF L.R.L'/day 0.048544 0.056684 0.100 0.075 Type A UCL L.R.X/day 0.051994 0.072674 0.100 0.075 Ver. Test L.R.X/day 0.1406 0.1195-.1695 Wlncludes penalties for nonstandard alignments of 0.00078%/day.

A summary of the test events and test chronology are presented in Section 2.0, Test Synopsis. Plant information, technical data, test results, and measurement system information are presented

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in Section 3.0, Test Data Summary. Test results are compared to the Acceptance Criteria in Section 4.0, Analysis and Interpretation.

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Referenced documents are listed in Section 5.0, References.

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2. 0 TEST SYNOPSIS The Containment was isolated by aligning systems in the specified post accident mcdes, except as noted in Section 4.1. -Prior to pressurization, the containment sump water levels were measured reading zero water level. A pre-test walkdown of the Containment structure. yielded no unacceptable structure deterioration. The ILRT was combined with the Structural Integrity, Test (SIT). Containment pressurization for the SIT started at '1545 on February 21, 1986. (SIT report under separate cover.) Full SIT test pressure (51.75 psig) was obtained, data taken and depressurization started.

The 24 hour2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months hold at less than.85% of.Pa'as completed at 0405 on February 24, 1986. Test pressure (41.7.psig) was reached.,at.0820 on February 24, '1986. The pressurization line was isolated from the Containment and vented.

The temperature stabilization criteria was satisfied during the six-hour period between 0820 and 1430 on February 24, 1986.

The ILRT test period began at 1445 on February 24. Initial test pressure was 41'.4085 psig. Containment. pressure and temperature. were recorded at 15 minute. intervals using.

electronic sensors and data logging devices. Reactor vessel levels and baromet.ic parameters were monitored at one hour intervals. The Containment sumps were measured hourly. The Type A test was terminated at 1445. on February '25, after twenty-four hours of data had satisfied all leakage rate acceptance criteria.

The verification test was initiated by continuously venting 5.82,SCFM of air from the Containment through a flowmeter.

The verification leakage rate calculated using the 8.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months of data from 1500 to 2330 on February 25, had verified the performance of the instrument system.

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TEST DATA

SUMMARY

3.1 Plant Information

l. Owner: Carolina Power and Light Company

2. Plant: Shearon Harris Nuclear Power Plant Unit 1

3. Location: New Hill, North Carolina

4. Containment Type: Reinforced Concrete with steel liner

5. NSSS Supplier, Type: Westinghouse

6. Date Test Completed: February 25, 1986

7. Docket Number: 50-400 3.2 Technical Data

l. Containment Net Free Air Volume: 2,266,000 cuft

2. Design Pressur'e: 45 psig

3. Peak Accident Pressure, Pa: 41 psig 4, ILRT Average Temperature Limits: 60-100 degF 3.3 Test Results -- ILRT Test

1. Test Method Absolute

2. Data Analysis Technique Mass Point

3. Test Pressure (At Completion) 41.222 psig

4. Maximum Allowable Leakage Rate, La 0.100%/day

5. 75% of La (Operational Allowable) 0.075%/day

6. Integrated Leakage Rate Test Results Mass Point Total Time Allowable Operational Type A LSF L.R.%/day 0.048544 0.056684 0.100 0. 075 Type A UCL L.R.%/day 0.051990 0.072674 0.100 0.075 Wlncludes penalties for nonstandard alignments of 0.00078%/day.

7. Imposed Verification Leakage Rate 0. 0978%/day (5. 82 SCFM)

8. Verification Test Results Leakage Rate Mass Point Analysis 0. 1406%/day

9. Verification Test Limits Uppers Lowered Mass Point Analysis 0.1695%/day 0.1195%/day 4Upper Limit = Lo + Lam + 0.25 La WLower Limit = Lo + Lam 0.25 La

10. Report Printouts The report printouts and plots for the Type A and verification test calculations are provided in Appendices B-G.

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ll. Penetrations nott in post-LOCh pos hlignxeat During ILRT Penetration Systex Leakage Rate M-17 High Head SI 22 SCCM M-18 Hot Leg Recirc 22 SCCM M-20 High Head SI 106.6 SCCM M-21 High Head SI 22 SCCM M-22 High Head SI 22 SCCM M-23 Coatainxent Spray 137 SCCM M-24 Containxent Spray 973 SCCM M-62 ILRT Pressure Sensing 22 SCCM Total 1326.6 SCCM 3.4 Integrated Leakage Rate Measurement Systex Instruxent Description Data (ao. of sensors)

l. hbsolute Texas Instrument Range: 0-75 psia Pressure Quartz Monometer hccuracy: +0.011 psia (2) Model No. )45 Sensitivity: +0.001 psia Repeatability:+0.00054 FS

2. Drybulb Range: 60-120degF Texperature Model No. NPPlh21- hccuracy: +O. ldegF (4o) 5.5-3h Sensitivity: +O.ldegF Repeatability: +O.ldegF

3. Dewpoint General Eastern Range: -40 to+14odegF Temperature Model No. 655-6llh hccuracy: +ldegF (10) Sensitivity: +0.5degF Repeatability: +0.030&degF

4. Flow Meter Brooks Range: 0-10 SCFM (2) Model No. hccuracy: +O.l SCFM 1114-0&H2Glh Sensitivity: +0.05 SCFM Repeatability: +0.05 SCFM Drybulb and dewpoint temperature sensor locationss aad aa volume fractions are provided ia Table 1.

3.5 Type B L Type C Leakage Rat~ Results The results of these tests are presented below.

Note that LLRT Leakage Rate equals Type B measured plus Type C xeasured plus the square root of the summation of the error squared.

Measured Error Hrror2 Total (scca)

Type B 2975 46.3 2148 3021.3 Type C 6162.6 50,95 2596 6213,55 Total 9137.6 68.88 4744 9206.5

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4.0 ANALYSIS AND INTERPRETATION 4.1 ILRT Test During the ILRT, eight penetrations were not in post-LOCA alignment. The total leakage rate correction for penetrations not in post-LOCA alignment and water level changes (none observed) is 0.00078%/day.

The calculated leakage rates during the Type A for LSF and 95K UCL are shown below. Adding the total leakage rate corrections for penetrations not in post-LOCA alignment yields the corrected leakage rates as follows:

Mass Point Total Time LSF UCL LSF UCL Calculated 0. 04776 0. 05121 0.05590 0.07189 Corrections 0.00078 0.00078 0.00078 0.00078 Corrected 0.04854 0.05199 0.05668 0.07267 Since the corrected 95'pper confidence levels for mass point (and total time) are less than .75La (0.075K'/day), the test results demonstrate the leakage through the primary containment and systems is within allowable limits,. Components penetrating primary containment do not exceed maximum leakage rates specified in the Shearon Harris Nuclear Power Plant Unit 1 FSAR and Technical Specifications.

4.2 Instrumentation, Data and Calculations ILRT test data were gathered through sensors and a data acquisition system. The data acquisition system received these inputs and transmitted them into a mini-computer which reduced the raw data to containment leakage. (See Appendix A for a software program description.)

4.2.1 Instrumentation The instrumentation was chosen for its stability and dependability. The instrumentation used during the ILRT satisfied all Instrument Selection Guide requirements. All instrumentation performed adequately during the test however, some dewcells produced a cyclic (random) oscillation. Although this is not a optimum sensing of dew point, these oscillations are considered within the normal operations of the sensor.

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4. 2. 2 Sensor Location and Uolume Fraction (See Table 1)

A mathematical model of the containment was developed using elevation and plan view construction drawings to define containment subvolumes boundaries. Subsequent to subvolume boundary definition, volume fractions were assigned to each subvolume in the containment. Sensors were then placed as near to the centroid of each subvolume as possible to detect changes in containment atmospheric conditions (see Reference 7). Table 1 indicates sensor location relative to volume fraction assignment. Since the ILRT was performed with all ventilation off, sensors were also placed with consideration given to air stratification and slight thermal updrafts caused by natural convection. This was especially true for those sensors in the containment where large open vertical spaces existed.

Sensors placement considered the three criteria (nearness to subvolume centroid, air stratification, and natural convection occurring in large open areas) and provided stable accurate representation of containment atmospheric conditions during the ILRT. All sensors were placed in accordance with the above considerations and operated without the disturbance of containment ventilation or chiller operation yielding highly reliable test data.

4.3 ISG Calculation 4.3.1 Test Parameters Assumed Actuals

1. La 0.100K/day same Allowable Leakage Rate

2. P 55.7 55.622 Pressure(psia) 3 ~ T 540 527.805 Drybulb Temp.(deg.R) 4.. Tdp 530 509.443 Dewpoint Temp.(deg.R)

5. t 24 Hr. same Test Duration 4.3.2 Instrument Parameters

l. Total Absolute Pressure No. of sensors: 2 Sensitivity (8): 0.001 psia Repeatability (X): 0.000375 psia 2 2 1/2 1/2 1/2 ep = [8 + X ] /N =(1.068 x 10-3)/2 = 7.552 x 10-4

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2. Water Vapor Pressure No. of sensors: 10 Sensitivity (E): 0.5degF Repeatability (X): 0.0308degF 2 2 1/2 1/2 epv(T) = [(0.5) + (0.0308) ] /10 0.158degF x 0.0124 psi/degF = 1.964xl0-3 psi

3. Temperature No. of sensors: 40 Sensitivity (E): O.ldegF Repeatability (X): 0.0432degF 2 2 1/2 1/2 eT = (O.l +[(0.00003x540)+0.027] ) /40 0.0172degR 4.3.3 ISG Equation 2 2 ISG = (2400/24)[2(7.55x10-4/55.7) +2(0.0172/540) +

2 1/2 2(1.964xl0-3/55.7) ] = 0.007'/day (Assumed) 2 2 ISG = (2400/24)[2(7.55x10-4/55.622) +2(0.0172/527.805) +

2 1/2 2(1.0136xl0-34/55.622) ] = 0.00562%'/day (Actual)

WNumerator change a result of vapor pressure to temperature slope change at actual dew point.

4.4 ILRT Data The ILRT data and calculated leakage rates are presented as reports and plots in Appendices B through G. These reports and plots illustrate a ILRT that was performed uninterrupted and without perturbation. The Type A containment mass and mass point leakage rate plot shows that the leakage rate remained essentially constant for the entire test period data.

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5. 0 REFERENCES

1. Shearon Harris Nuclear Power Plant Unit 1, FSAR 6.2.

2. Shearon Harris Nuclear Power Plant Unit 1, Technical Specifications, Section 3/4.6.

3. Shearon Harris Nuclear Power Plant Unit 1, Procedure Containment Integrated Leakage Rate Test (1-8010-P-03).

4. 1-8010-P-Ol Preoperational Local Leak Rate Testing, Type C

5. 1-8010-P-02 Preoperational Local Leak Rate Testing, Type B 6 . 1-8010-I-Ol ILRT Instrument Systems Calibration Check

7. 1-8010-I-02 ILRT Instrument Placement Verification Survey

8. 1-8020-0-01 Containment Access Penetration Seal Integrity Check

9. Code of Federal Regulations, Title 10, Part 50, Appendix J, Primary Reactor Containment Leakage Rate Testing for Water Cooled Power Reactors.

10. ANSI/ANS 56.8-1981, Containment System Leakage Testing Requirements.

ll. ANSI N45.4-1972, Leakage Rate Testing of Containment Structures for Nuclear Reactors.

12. Topical Report, BN-TOP-l, Testing Criteria for Integrated Leakage Rate Testing of Primary Containment Structure forNuclear Power Plants, Bechtel Corporation, Revision 1, dated November 1, 1972.

13. 1-8020-P-03 Local Leak Rate Testing, Airlock Inner Door Seals & Valve Chambers 10

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TABLE 1 SENSOR LOCATIONS AND WEIGHTING FRACTIONS Volume SENSOR ELEVATION AZIMUTH RADIUS FRACTIONS (in feet) (in degrees) (in feet) (in L)

DRYBULB RTD-1-ILRT-Z-l 416.5 180 + 6.4 36 0.0251 RTD-2-ILRT-Z-l 416.5 270 + 6.4 36 0.0250 RTD-3-ILRT-Z-l 416.5 0 + 6.4 36 0.0251 RTD-4-ILRT-Z-l 416.5 90 + 6.4 36 0.0250 RTD-1-ILRT-Z-2 391.5 150 + 4.8 47.5 0.0291 RTD-2-ILRT-Z-2 391.5 210 + 4.8 47.5 0.0291 RTD-3-ILRT-Z-2 391.5 270 + 4.8 47.5 0.0291 RTD-4-ILRT-Z-2 391.5 330 + 4.8 47.5 0.0291 RTD-5-ILRT-Z-2 391.5 30 + 4.8 47.5 0.0291 RTD-6-ILRT-Z-2 391.5 90 + 4.8 47.5 0.0291 RTD-7-ILRT-Z-2 391.5 e.o 0.0291 RTD-1-ILRT-Z-3 343.5 135 + 4.7 48.5 0.0309 RTD-2-ILRT-Z-3 343.5 180 + 4.7 48.5 0.0309 RTD-3-ILRT-Z-3 343.5 225 + 4.7 48.5 0.0309 RTD-4-ILRT-Z-3 343.5 270 + 4.7 48.5 0.0309 RTD-5-ILRT-Z-3 343.5 315 + 4.7 48.5 0.0309 RTD-6-ILRT-Z-3 343.5 0 + 4,7 48.5 0.0309 RTD-7-ILRT-Z-3 343.5 45 + 4.7 48.5 0.0309 RTD-8-ILRT-Z-3 343.5 90 + 4.7 48.5 0.0309 RTD-9-ILRT-Z-3 343.5 0.0 0.0309 RTD-1-ILRT-Z-4 297.5 126 + 4.8 48 0.0188 RTD-2-ILRT-Z-4 297.5 167 + 4.8 48 0.0188 RTD-3-ILRT-Z-4 297.5 200 + 4.8 48 0.0188 RTD-4-ILRT-Z-4 297.5 232 + 4.8 48 0.0188 RTD-5-ILRT-Z-4 297.5 285 + 4.8 48 0.0188

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TABLE 1 (Continued)

Volume SENSOR ELEVATION AZIMUTH RADIUS , FRACTIONS (ft) (degrees) (in feet) (in 4)

RTD-6-I LRT-Z-4 297. 5 322 + 4.8 48 0.0188 RTD-7-ILRT-Z-4 297. 5 0 + 4.8 48 0.0188 RTD-8-ILRT-Z-4 297. 5 44 + 4.8 48 0.0188 RTD-9-ILRT-Z-4 297.5 79 + 4.8 48 0.0188 RTD-10-ILRT-Z-4 297.5 0.0 0.0188 RTD-1-ILRT-Z-5 254.0 136 + 4.1 55.5 0.0230 RTD-2-ILRT-Z-5 254.0 198 + 4.1 55.5 0.0230 RTD-3-ILRT-Z-5 254.0 246 + 4.1 55.5 0.0230 RTD-4-ILRT-Z-5 254.0 314 + 4.1 55.5 0.0230 RTD-5-ILRT-Z-5 254.0 15 + 4.1 55.5 0.0230 RTD-6-ILRT-Z-5 254.0 73 + 4.1 55.5 0.0230 RTD-7-ILRT-Z-5 254.0 130 + 7.4 31 0.0230 RTD-8-ILRT-Z-5 254.0 219 + 7.4 31 0.0230 RTD-9-ILRT-Z-5 254.0 292 + 7.4 31 0.0230 RTD-10-ILRT-Z-5 254.0 2 + 7.4 31 0.0230 DEWPOINT RHD-A-ILRT-Z-1 416. 5 0.0 0.0449 RHD-A-ILRT-Z-2 391.5 270 + 4.8 47.5 0.1019 RHD-B-ILRT-Z-2 391.5 90 + 4.8 47.5 0.1019 RHD-A-ILRT-Z-3 343.5 120 + 4.7 48. 5 0.0927 RHD-B-ILRT-Z-3 343.5 240 + 4.7 48. 5 0.0927 RHD-C-ILRT-Z-3 343.5 0 + 4.7 48. 0.0927 RHD-A-ILRT-Z-4 5'8 297.5 216 + 4.8 0.0940 RHD-B-ILRT-Z-4 297.5 62 + 4.8 48 0.0940 RHD-A-ILRT-Z-5 254.0 40 + 4.1 55.5 0.1151 RHD-B-ILRT-Z-5 254.0 327 + 7.4 31 0.1151 12

APPENDIX A ILRT COMPUTER PROGRAM

SUMMARY

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QUADREX CORPORATION LEAKER PROGRAM

SUMMARY

l.0 INTRODUCTION The Type h Test is an integrated leakage rate test (ILRT) designed to verify the leak test integrity of the entire containment building. This test is performed as approximately three-year intervals as required by Appendix J of 10 CFR 50. It is performed in accordance with the American National Standard "Containment System Leakage Testing Requirements," (ANSIlANS-56.8-1981), American National Standard Ieakage Rate Testing of Primary Containment for Nuclear Power Plants," Bechtel Topical Report (BN-TOP-l).

The LEAKER program computes total time leakage rates, mass .point leakage rates, LSF leakage rates, and 95% upper confidence level (UCL) leakage rates during the course of the test from input measured values of containment pressure, temperature and dew point.

T he LBAKER program is also capable of performing the verification phase and will generate specific verifications features to aid in verifying the Type h test. Those features will be described in detail later.

The IBAKER program is designed to automate the task of sampling and reducing the data to a usable form in accordance with the above documents. This greatly limits the possibility of human error and provides intermediate results after a short delay.

This makes it possible to monitor the progress of'he test very closely in approximately real time. For each of the two test periods, the LBAKBR program samples the containment's environment and calculates the values needed to assess the status of the test. Interim results are provided as desired and the program checks to see the two test periods.

if the acceptance criteria have been satisfied for The program also produces a printout of all data .gathered as well as a record of its calculations. In addition, the data is stored on hard or floppy computer disks for future reference. The program can recover from a power failure or any other accidental interruptions of the program's execution by reloading the old data and restarting the data sampling routine at the proper location. Lastly, should one of the RTDs fail during the test, the program will detect the problem and the user can. remove that sensor from further calculations. When the test is completed, the program has the ability to recalculate all values for the test, suppressing any failed RTDs or a cell from he entire series of calculations in order to verify the results

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The LEAKER program is written in a high level language (BASIC) and is designed for

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use on a micro-computer with direct data input from

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the data acquisition system. Brief descriptions of program use, formulae used for leakage rate computations, and program logic are provided in the following paragraphs.

2.0 EXPLANATION OF PROGRAM The Quadrex LEAKER computer program is written, for use by experienced ILRT personnel, to determine containment integrated leakage rates based on the Absolute Method described in ANSI/ANS 56.8-1981 and BN-TOP-l.

Information loaded into the program prior to or at the start of the test:

a. Number of containment atmosphere drybulb temperature sensors, dew point temperature (water vapor pressure) sensors and pressure gages to be used in leakage rate computations for the specific test.

Volume fractions assigned to each of the above sensors.

c. Calibration data for above sensors.

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d. Test title.

e. Test pressure.

f. Maximum available leakage rate at test pressure.

Data recorded from the data acquisition system during the test, and used to compute leakage rates:

a. Time and date.

b. Containment atmosphere drybulb temperatures.

c. Containment atmosphere pressure(s).

d. Containment atmosphere dew point temperatures.

e. Containment free air volume.

The drybulb or dew point temperature sensors should fail during the test, the data from the sensor(s) are not used. The volume fractions for the remaining sensors are recomputed and reloaded into the program for use in ensuing leakage rate computations.

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PROGRAM LOGIC AND OPERATION

SUMMARY

The Quadrex LEAKER computer program logic flow is controlled by a set of user options after executive questions. The user options and a brief description of their associated function are presented below:

3.1 System diagnostics, self tests and executive questions as shown in Figure lA ~

3.2 The various keys listed and described below are shown in Figure 1B:

START This key initiates or suspends the system in gathering data and displaying screen.

it on the main MAINT This key redefines weighting factor values, changes the logging of data to a file, deletes a record in the file, displays the individual record's key environmental contents, and changes the individual record's content.

UPDATE If the records are key redefines changed or deleted, the entire file so that the this calculations can be made without interfering with the computer's file handling capabilities.

REPORTS This key performs the calculations of program and prints the results, PLOTS This function implements the graphics portion of the program. Any channel or leakage rate can be plotted.

MANUAL ON This key, de-activates the automatic data entry and allows manual entry.

END JOB This key will properly terminate the program.

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~ COMPUTER REPORTS AND PLOTS 4.1 Reports REPORTS does the analysis of the data accumulated by the ILRT system and then prints out a report of the results.

The types of analysis performed are: mass point, total time, environmental averages, mass loss, temperature stabilization, and data rejection. All results from the

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analysis a'e printed off a thermal printer. The subprogram REPORTS requires the user to select a valid time window or record window as listed below as a prerequisite for doing analysis.

MASS POINT The mass point analysis is based on the ANSI/ANS 56.8-1981 Standard acceptance criteria and calculations.

TOTAL TIME The total time analysis is based on the Bechtel Topical Report (BN-TOP-1) and its respective acceptance criteria and calculations.

ENUIRONMENT The environment analysis is based on the Bechtel Topical Report (BN-TOP-1) and the ANSI/ANS 56.8-1981 Standard with their respective acceptance criteria and calculations.

MASS LOSS The mass loss analysis is based on the ANSI/ANS 56.8-1981 Standard acceptance criteria and calculations.

TEMP STAB The temperature stabilization analysis is based on the Bechtel Topical Report (BN-TOP-

1) and the ANSI/ANS 56.8-1981 Standard with their respective acceptance criteria and calculations.

DATA REJECTION The data rejection analysis is based on the Bechtel Topical Report (BN-TOP-1) and the ANSI/ANS 56.8-1981 Standard, Appendix D, with their respective acceptance criteria and calculations.

4.2 Plots The Graphics subprogram allows the user to plot the mass point analysis, total time analysis, and displayed channel ne s.

Fuur t her, plots can be made in a batch mode by instrum umen t ype o a printer or a plotter. PLOTS performs autoranging on the data being plotted for axes values. PLOTS requires the user to select any valid time window or record window as a prerequisite for doing plotting.

APPENDIX B STABILIZATION DATA Cc CALCULATIONS

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<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<TENPERRTURE STRB ILI2RT ION <<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<<~<<">:

JUL IRN DFITE 55 TINE - 838 TIME TEMP TEMP BN-TOP-1 BN-TOP-1 TEMP RNS Il (DELTR) DIFF g RYG FIYG . RRTE FIYG, CR I T.

(HOURS) TENP INCR (1 HR> (2 HR> (2 HR) (4 HR>

8. 88 532.848 G. 888 529.288 B. 888 .138 8. Gee 8. GOG 25 531.348 ~ 788 529.288 e. Gee .138 8. Goe 8. GGG

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~ 75 538.589 -.297 529.288 8. 888 . 138 G.GGG G. GOG 1 ~ 88 538.371 -.218 531.286 e.eee .138 8.888 8 ~ Q.oo 1 25

~ 538.219 -. 152 538.788 8.888 .138 8. 888 G. GGO

1. 58 538.887 .132 538.486 8.888 .138 8.888 8. GOG 1 ~ 75 529 ~ 994 -.893 538. 291 8.888 .138 8.888 8. GGO 2 ~ Be 529. 986 .888 538.139 -1.867

- 1 '67 G.GGO 8. GGO

2. 25 529. 837 .869 538.828 ~ 752 .752 8.888 e. eoo

2. 58 529.766 -. 871 529.927 .568 ~ 568 8.888 8. 888

2. 75 529.?18 .848 529.856 .436 ~ 436 8.888 8. GGG

3. 88 529.666 -. 852 529.786 ~ 353 ~ 353 8.888 G. GGO

3. 25 529.687 ~ 859 529.?22 .386 ~ 386 8.888 Ge 888

3. 58 529.567 -;848 529.666 -. 268 .268 G.eeo 8. GOG

3. 75 529.531 -. 835 529.624 -o231 .231 8.888 8. Gee

4. 88 529.488 .844 529.577 -.289 .289 -.638 . 468

4. 25 529.457 ~ 838 529.532 - 198

~ .198 -.471 . 322 4 ~ 58 529.421 -.83? 529.494 -. 173 .173 -.366 . 228 4 '5 5 ~ 88 529.385 529.348

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529.458 529.418

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. 154 oi16 5.25 529.316 - 832

~ 529.387 -e 145 .145 -.226 .884

5. 58 529. 298 .826 529 '55 -. 138 ~ 138 -.199, .868 5.75 529. 263 -.827 529.324 -. 134 .134 -.183 . 861 6.ee 529. 228 - ~ 835 529.288 .138 ~ 138 -.169 .858

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++++++++++++ NRSS LOSS CRLCULRTION RESULTS JUL IRN DRTE 55 TINE - 838 REC TINE CONT NRSS NRSS NRSS NUN (DELTR AIR LOSS LOSS LOSS HOURS) NRSS INCR (1 HR) (x 24) 116 8 ~ 88 643883.8 8.8 8.8 8' 117 ~ 25 643884.4 88. 6 8.8 B.e 118 .58 643175.8 98>> 7 8.8 B.B 119 ~ 75 643232. 1 57. 1 8.8 8.8 128 1 ~ 88 643163. 6- -68. 6 -159. 8 -3834. 8 121 1. 25 643188.7 17 ~ 2 -96. 4 -2312. 5 122 l. 58 643195.6 14. 8 -28. 5 -493. 8 123 1 75

~ 643387>>4 111 ~ 8 75 2

~ -1885.4 124 2. 88 643238.9 -68. 5 -75. 3 -1888.2 125 2. 25 643256.6 17. 7 -75 9~ -1821.6 126 2.58 643187. 6 -69 ~ 8 8.8 191.3 127 2.75 643181. 1 -6. 5 126. 3 3838.9 128 F 88 643153.8. -28. 8 85. 9 2868.5 129 3.25 643283.6 58. 6 53 ~ 8 1271 '

138 3.58 643233>>4 29. 7 -45. 8 -1898. 5 131 3.75 643176.2 -57. 2 4.9 118 ~ 8 132 4 ~ 88 643213.9 3?. 8 -68. 9 -1461 ~ 4 133 4>> 25 643156 ' -57. 5 47. 2 1133>> 6 134 4 ~ 58 643118.? 37 ~ 7 114.7 2751.6 135 4. 75 643173. 4 54. 7 2.8 66. 1 136 5>> 88 643217.9 44 ~ 5 -4 8 -96. 8 5 '5 5.58 643157 '

643154.9

-68. 4 2~7

-1

~

-36. 2 2 -27. 9

-868. 8 5.75 643167 ' 12. 9 5.6 135 2

~

148 6. 88 643226 ' 58 ~ 8 -8. 6 -287.5

I l4 jW lI

+++++~++++++++++++++++++++ ENVIRONMENT LISTING ++++++++++++++++++++~+++++::

JULIAN DATE - 55 TIME - S38 REC DATE TINE TEMP VAPOR CONTAINNENT RELATIVE AIR PSIFI NUt1 PRESSURE PRESSURE HUNI DITY DENSITY VARIANCE 116 55 BS38 532e848 .213S 55.9332 54. 26 ~ 2S3S G.GGGGG 117 55 BS45 531.348 .2134 55.S666 55. 44 ~ 2S3S .8665S aas 55 8988 538.SS6 .2182 55.S26S 55. 4S ~ 2S3S .839S?

119 55 8915 538.5S9 ~ 2868 55.S885 54. 98 ~ 2S39 -.82624 128 55 8938 538.371 .2123 55.7717 57. 81 ~ 2S3S - ~ 82SS5 121 55 8945 538 '19 .289S 55.7572 56. 63 . 2S3S -.81458 122 55 1888 538.8S7 .2895 55.?445 56.?9 . 2S3S -.81264 123 55 1815 529.994 .1991 55 '444 54. 15 .2S39 .80813 124 55 1838 529o986 .2853 55.7292 56 ~ BG ~ 2S39 -. 8151S 125 55 1845 529.S37 ~ 2825 55.7235 55. 36 .2S39 .8857 8 126 55 1188 529.766 .28S9 55.7181 57 ~ 26 02S3S -o 81342 127 55 1115 529.71S .2876 55.7844 56. 9S .2S3S -. 88566 12S 55 1138 529.666 ~ 2894 55.6966 57. 68 .2S3S -. 887S?

129 55 1145 529.687 .2853 55.6947 56. 5S '2S3S -. 881S7 138 55 1288 529.567 .2819 55. 6931 55. 72 ~ 2S39 .88162 131 55 1215 529.531 .2856 55I6S44 56. SG .2S3S .GGS67 132 55 1238 529.4SS .2824 55.6S31 56. 88 ~ 2S39 .88131 133 55 1245 529+457 ~ 2856 55.6749 56. 94 ~ 2S3S .GGS17 134 55 1388 529.421 ~ 28S2 55.667S 5?e 73 .2S3S .88710 135 55 1315 529.3S5 .282S 55.66S7 56. 38 .2S3S .88091 136 55 1338 529.34S ei9S3 55.66S7 55. 12 ~ 2S39 -.88881 137 55 1345 529.316 .282S SS.6682 56. 45 .2S3S .GGS57 13S 55 1488 529.298 .2823 55 '572 56. 35 .2S3S .88296 139 55 1415 529.263 .2885 55.6555 55. 91 .2S3S .88172 148 55 1438 529.22S ~ 1951 55.6569 54. 46 .2S39 .88143

RTD RVG 55:8838 TO 55:1438 DELTR TINE (IN HOURS)

JA CONT PRESSURE 55:8838 TO 55: 1038 DELTR TINE ( IN HOURS)

i RHD RVG 55:8838 TO 55:1438 DELTR TINE (IN HOURS)

I NP NERSURED 55:8838 TO 55:1438 DELTR TINE ( XN HOURS)

APPENDIX C TYPE h

SUMMARY

DATA By Sensor Enviroment Mass Loss

IL:

'l r

I II Ql*

l

i<

Ef

'lg

RECORD NUNI)ER - 116 DRTE - 55 TINE - 839 PRESSURES 56. 1528 56.1429 RVG 56e1478 RTD'S Zl i81 74,1299 Zlr82 74.9848 Zir83 74. 1'748 Zir84 74.2829 Z2r81 73.9488 Z2r82 73.8868 Z2r83 73.9488 Z2r84 ?4.8128 Z2r85 74.8488 Z2r86 74.9128 Z2r87 74.1828 23r81 73. 6529 Z3i82 73.6528 Z3r83 73.5888 Z3r84 73.5888 23r85 73.4999 Z3r86 73.7249 Z3r97 73.6528 23rGG 73.6168 Z3r89 73. 6349 24r81 72.8248 Z4r82 72.6989 Z4r83 72.7168 Z4r84 72.7789 24r85 72.9688 Z4r86 72.7169 Z4r87 72.6268 Z4r88 72.6989 Z4 i89 72.3749 24riG 72.8688 Z5r81 67.6948 ZSr92 68.1889 ZSr83 68.99BG 25r84 67.8388 Z5r85 68.9188 25r86 68.5489 Z5i87 68.2888 ZSr88 67, 9468 Z5r89 68.5588 Z5r18 69.6388 IHRCT 8.8888 INFICT 8.8888 IHRCT 8.8888 I. N8CT 9.8889 INRCT 8.8898 INRCT 8.8888 IHRCT 8.8888 INRCT 9.9998 IHRCT 8.8889 INRCT 8.8889 RVG 72.3698 DEW CELI S RHD Zi 54.8499 RHD Z2 56.5499 RHD Z2 56. 1652 RHD Z3 54.9729 RH3 23 54.7886 RHD Z3 56.8784 RHD 24 '55.8755 RHD 24 54.6989, RHD Z5 54.8242 RHD 25 53.8378 IHFICT 8.8899 INFICT 8.8999 INRCT 8.8888 INRCT 8.8888 IHRCT 8.8888 RVG 54.9721 Rt1B I ENT PRESS 14.5388 VAPOR PRESSURE .2138 DRY PRESSURE 55.9332 FLOWS 8.8888

(

RECORD HUHIlER - 117 DATE 55 TINE 845 PRESSURES 56.9858 56.9758 56.9888 RTD'S Zl '8l 72. 8429 Zir82 72. 8248 Zlr83 72. 9599 Z ir94 73. 2389 Z2 'Gl 72.7799 Z2r82 72.7168 Z2r93 72. 7169 Z2r94 72. 8249 Z2r85 72.8248 Z2r86 72.8868 22r87 72. 8788 Z3r81 72. 7889 Z3i82 72.8868 23r83 72.7788 Z3r84 72. 7528 23r85 72. 6269 23r96 72.8429 Z3r87 72.8968 Z3r88 72. 7799 Z3r99 ?2.?889 Z4 '81 72.3388 Z4r92 72. 2128 Z4r83 72. 2849 Z4r84 72.3299 Z4 ~95 72.3929 Z4r96 72.1949 Z4r97 72. 1949 24r98 72.1488 Z4r99 72.1949 Z4r18 72.3288 Z5r91 67, 6498 Z5r92 68.1449 ZS 93 68. 1989 Z5r94 67.9289 Z5r85 68.8469 Z5r86 68.3789 25 rG? 68. 1889 ZSr98 67.9188 Z5r99 68.4688 Z5riG 69.6299 INRCT G. 8888 IHRCT 9.8898 INRCT 8.9988 IHRCT 9.9998 INRCT 8.9998 INFlCT 8.8999 INFICT 9.8899 IHRCT 8.9899 INRCT 8.8988 IHRCT 8.8888 RVG 71.6699 DEW CELLS RHD Zi 56.85?S RHD Z2 55.8784 RHD 22 54. 8191 RHD Z3 54. 4473 HD 23 55+9988 RHD Z3 54.7934 RHD Z4 55. 1268 RHD Z4 54. 3447 HD Z5 54.6268 RHD 25 52.7558 INRCT 8. 8888 I NFICT Ge 8899 HRCT 8.8988 INFlCT 8.8888 INRCT 8.8888 RVG 54.9187 RlhB I ENT PRESS 14.5388 VAPOR PRESSURE .2134 DRY PRESSURE 55.8666 FLOWS Go8889

Qi 1

14 1

I A

h U~

T%

RECORD NUMBER - 118 DRTE - 55 TIME - 988 PRESSURES 56. 8428 56.8328 RVG 56. 8379 RTD'S Zir81 71.9688 Zlr82 71 '868 Zlr83 71. 9968 Z lr84 72.3926 Z2r81 72.8688 22r82 72.8588 Z2r83 72.8328 Z2r84 72e1649 Z2r85 72.8588 Z2r86 72.8868 Z2r87 72.1848 23r81 72.1949 Z3r82 72. 1588 Z3r83 72.2128 Z3r84 72.1768 Z3r85 72.1586 Z3r86 72.3828 Z3r87 72.1949 23r88 72.1769 Z3r99 72.2366 24rei 72.8688 24r82 71.9249 Z4r83 72.8328 Z4r84 72.8686 24rBS 71. 9428 24r86 71.9248 24r87 71.7446 24r88 71 7986

~

Z4i89 71.8886 Z4rlB 72e8148 25r81 67.6488 Z5r82 68. 1628 ZSr93 68. 1269 Z5r84 67.9646 ZSr85 68.8288 Z5r86 68.2889 Z5r87 68. 1628 25r88 67.8928 ZSr89 68.4148.ZSr18 69.6829 INACT 8. 8888 INACT 9.8869 IHRCT 8.8888 IHRCT 8.8698 INRCT 8. 8888 I HFICT Bo8888 INRCT 8.8888 INRCT 6.8668 I HFICT 8 ~ 8869 IHRCT 8.8889 RVG 71.2159 DEW CELLS RHD 21 55.4473 RHD 22 53.7558 RHD 22 54. 1811 RHD 23 53.7558 RHD 23 56. 1396 RHD 23 55.3968 RHD 24 54.2422 RHD 24 54.7934 RHD 25 54.7293 RHD 25 53. 1396 IHRCT 8.8888 INRCT Bo8868 IHRCT 8.8888 INRCT B. 8888 IHFICT Oo8888 RVG 54e5172 AMBIENT PRESS 14.5388 VAPOR PRESSURE ~ 2182 DRY PRESSURE 55.8268 FLOWS e. 8999. Oe 8888 RECORD HUNEKER 119 DRTE - 55 TINE 915 PRESSURES 56. 8118 56.8828 RVG 56.8865 RTD'S 2ir81 71. 4288 Z1 r82 71.4748 Zlr83 71. 5288 Zir94 71.7869 Z2r81 71. 6728 Z2r82 71.5468 Z2r83 71. 5648 Z2r84 71.5826 22i85 71.6368 Z2r86 71 '888 Z2r87 71.6686 23r91 ?1.7899 Z3r82 71. 7449 Z3r83 71.7889 23r94 71.7888 Z3r85 71.7629 23r86 72.1768 Z3r97 71.7986 23r98 71.7989 Z3r99 71. 7889 Z4r81 71.8888 Z4r82 71.7268 Z4r93 71.7889 Z4r84 71. 7449 Z4r85 71.7628 Z4r96 71.6729 Z4r97 71.5289 Z4r88 71.5829 Z4r89 71. 7268 24r 1 8 71.8168 25r81 67.6488 Z5r82 68.1628 Z5r83 68.1268 ZSr84 6?e9646 ZSr85 68. 8188 Z5r86 68.2349 25 '87 68. 1448 Z5r88 67.8748 Z5r99 68. 3968 Z5r18 69.5849 INACT 8.8868 IHRCT B+8989 IHACT 8.8989 I HFICT Be6666 INACT 9.8868 INRCT 8. 8888 I NFI CT 8.8888 INRCT 8.8666 IHRCT 8.8888 INACT BoBBBB RVG 78. 9193 D EW CELLS RHD Zi 54.9345 RHD Z2 53'811 RHD 22 53.8499 RHD Z3 53. 9473 RHD Z3 53o4988 RHD 23 55.9473 RHD 24 54.2886 RHD Z4 53. 3447 RHD Z5 54.7886 RHD 25 52.9729 IHRCT 8.8888 INFICT 6. 8988 INRCT e. 8989 INRCT 8.8888 INRCT 8.9998 AVG 53.9622

( RPIBIENT PPESS 14'386 VRPOR PRESSURE . 2869 DRY PRESSURE 55.8885 FLOWS 8.8888 8.9898

~4 J

0

RECORD NUMIlER - 128 DRTE " 55 TINE - 938 PRESSURES 55'898 55.9798 RVG 55.9848 RTD'S Zlr81 71.1328 Zlr82 ?1.1868 Zlr83 71. 2228 2 lre4 ? l. 34SB Z2r81 71.3848 Z2r82 71.2228 Z2r83 71.2588 Z2r84 71.2768 Z2 '85 71.3488 Z2r86 71. 2768 Z2r87 71. 2948 23r81 71.5188 Z3r82 71.4928 Z3r83 71. 4748 Z3r84 71. 4568 Z3r85 71. 5188 Z3. 86 71. 8168 Z3r87 71.5188 Z3r88 71.4748 Z3r89 71.4748 Z4r81 71. 7888 'Z4r82 71. 5648 Z4r83 71.5648 Z4r84 71. 4740 Z4r85 ?1.5468 Z4r86 71.4928 Z4r87 71.3488 24r88 71. 4288 Z4r89 ?1.5648 Z4riB 71. 6548 ZSr81 67. 6228 25r82 68 '628 25r83 68. 1448 Z5r84 67.9828 25r85 68. 7748 Z5r86 68.1988 25 r87 68. 1888 Z5r88 67.8568 ZSr89 68 342'8 Z5r18

~ 69.5668 INRCT BI8888 INRCT 8.8888 INFICT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INFICT 8.8888 INRCT 8.8888 INRCT 8 F 8888 INFlCT 8.8888 RVG 78.7815 DEW CELLS RHD Zl 56.8114 RHD Z2 55.2558 RHD 22 55.6781 RHD 23 54. 3191 RHD 23 55.3784 RMD 23 54.4729 RHD Z4 53.9986 RHD 24 55. 8114 RHD 25 54.6652 RHD Z5 53.2558 INRCT 8.8888 INRCT 8.8888 I NFICT 8. 8888 INRCT 8.8888 INRCT 8.8888 RVG 54.7868 RHBIENT PRESS 14.5388 VFlPOR PRESSURE ~ 2123 DRY PRESSURE 55. 7717 FLOWS 8.8888 RECORD NUNBER 121 DRTE 55 TINE - 945 PRESSURES 55. 9728 55. 9628 FIV.G 55 '678 RTD'S 21r81 78.9348 Zir82 78. 9888 Z ir83 71.8248 Zir84 71. 8428 22i81 71.2848 Z2r82 78.9888 Z2r83 71.8688 Z2r84 71. 8688 22i85 71. 1868 Z2r86 71.8428 Z2r87 71.8428 Z3r81 71. 2948 Z3r82 71. 2948 Z3r83 71.3128 Z3r84 71.2588 Z3r85 71. 2588 Z3r86 71. 8168 Z3r87 71. 3388 Z3r88 71.2768 Z3r89 7lo2588 24 r81 71. 5828 24r82 71. 4288 24r83 71.4288 Z4r84 71.3388 Z4r85 71.3848 24r86 71. 3388 Z4r87 71. 1328 24r88 71.2588 24 r89 71.4288 Z4riB 71.4928 Z5r81 67. 6228 Z5r82 68.1448 Z5r83 68. 1268 25r84 67. 9468 Z5r85 68.7288 Z5r86 68.1888 Z5r87 68.8S48 25r88 67.8828 25r89 68.3868 ZSr18 69.5488 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 I NFICT B.BBBB INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT Bo8888 INRCT 8.8888 RVG 78.5494 DEW CELLS RHD 21 53e4729 RHD Z2 56. 1781 RHD 22 53. 1989 RHD 23 54.6989 RHD Z3 53.8114 RHD 23 56. 8378 RHD Z4 54.7422 RHD Z4 54.8863 RHD Z5 54.?422 RHD 25 53.8784 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INFlCT e.8888 RVG 54.4641 RtlB IENT PPESS 14.5388 VFIPOR PRESSURE .2898 DRY PRESSURE 55.7572 ~

FLOWS 8.8888 BoBBBB

Iq 4

4$

441I

, t I

RECORD NUNIlER - 122 DRTE - 55 TIME - 1888 PRESSURES 55. 9598 55.9498 RVG 55.9548 RTD'S Zir81 78. 7368 Z 1r82 78. 8448 2ir83 78,8448 Zir84 78 8268 Z2r81 71. 8428 Z2r82 78.8448 Z2r83 78.8888 Z2r84 78 9168

~

Z2 F85 71. 8428 22r86 78,8988 Z2r87 78. 9168 Z3r81 71.1328 Z3r82 71. 1588 Z3r83 71>> 1588 Z3r84 71. 1588 23r85 71.8968 Z3r86 71.4568 23r87 71. 1688 23r88 71.8968 23r89 71 ~ 1328 Z4r81 71.4388 Z4r82 71. 2768 24r83 71. 2488 24r84 71.15GG 24r85 71. 2768 Z4r86 71. 1868 Z4r87 71.8428 24r88 71 F 1148 24r89 71.2948 Z4ri8 71. 3668 Z5r81 67.5868 25r82 68.1448 Z5r83 68.1888 Z5r84 67.9288 Z5r85 68.6488 25r86 68.1268 ZSre? 68.8888 25r88 67.7488 ZSr89 68.2788 Z5rie 69.4948 INACT 8.8888 INRCT 8.8888 INFICT 8,8888 INRCT 8. GGGG INRCT 8.8888 INRCT .8.8888 INRCT 8.8888 INRCT 8.8888 INACT 8.8888 INFICT 8.8888 RVG 78.4178 DEW CELI S RHD 21 55.8863 RHD 22 56.7678 RHD Z2 53.2293 RHD Z3 53.6652 RHD 23 55.4858 RHD 23 52.4?29 RHD Z4 53. 6148 RHD 24 55.8378 RHD ZS 54.5242 RHD Z5 53.5378 INRCT 8.8888 INRCT 8.8888 INACT 8.8888 INACT 8.8888 INRCT 8.8888 RYG 54.4173 AMBIENT PF.'ESS 14.5388 VAPOR PRESSURE .2895 DRY PRESSURE 55.7445 FLOWS 8.8888 8.8888 RECORD NUNBER - 123 DRTE 55 TINE 1815 PRESSURES 55.9498 55.9388 RVG 55.9435 RTD'S Zir81 78. 5928- Z ir82 78. 7888 Z ir83 78.7368 2ir84 78. 6468 22r81 78.8888 22r82 78.7368 Z2r83 78.8268 Z2r84 78>> 8888 Z2,F85 78.9528 Z2r86 78.7728 Z2r87 78.7728 Z3r81 71.8248 Z3i82 71.8688 Z3r83 71.8428 Z3r84 71.8248 Z3r85 71.8868 Z3r86 71.2768 Z3r87 71. 8688 Z3r88 71.8868 Z3r89 71.8248 Z4r81 71.3488 Z4r82 71. 1688 Z4r83 71.1328 Z4r84 71.8240 24-r85 71.2228 Z4r86 71. 8968 Z4r87 78.9348 Z4r88 71.8248 24r89 71. 1868 Z4r18 ?1>>2488 Z5r81 67.5688 Z5r82 68.1268 25r83 68.1888 Z5r84 67.8928 Z5r85 68.6388 Z5r86 68.8988 ZSr87 67.9648 Z5r88 67.7128 2Sr89 68.2348 ZSr18, 69.4768 INACT 8.8888 INRCT 8.8888 INRCT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8888 INRCT 8.8888 INRCT 8. 8888 INRCT 8.8888= INRCT 8.8888 RVG 78.3237 DEW CELLS RHD 21 52. 1396 RHD Z2 49.7558 RHD Z2 53. 9?29 RHD 23 54.7934 RHD 23 53.6989 RHD 23 58.9729 RHD Z4 53.344? RHD Z4 54.1148 RHD Z5 54.4729 RHD Z5 53. 1148 INRCT 8.8888 INRCT 8.8888 INRCT e. 8888 INRCT 8. 8888 INRCT 8.8888 AVG 53>>8447 RIB I ENT PF'.ESS 14.5388 VAPOR PREc'SURE >>1991

( DRY PRESSURE 55>>7444 FLOWS 8.8888 8. 8888

tg l

h.

1 4h 1 s gr

RECORD HUNBER . 124 DFITE " 55 TINE " 1838 PRESSURES 55. 9488 55.9298 RVG 55.9345 RTD'S 78.5288 Zir82 78. 5568 Zir83 78.6288 Z ir84 78.SO29 Z2rel 78.8888 Z2r82 78. 6648 22r83 78.6648 Z2r84 78.6829 Z2r85 78.8888 Z2r86 78. 6468 Z2r87 78.6648 Z3rel 78.916e Z3r82 78.9348 23r83 78.8988 23r84 78.8988 Z3r85 78.8989 Z3r86 71 2228 Z3r87

~ 78.9789 Z3r88 78.8988 Z3r99 78.9169 Z4rel 71. 2768 Z4r82 71.8788 Z4r83 71. 8428 Z4r84 79.9169 Z4reS 71 1328 Z4r86

~ ?1 8249 Z4re?

~ 78. 8268 Z4r98 78.9349 Z4r89 71.8788 24rio ?1.1588 Z5rol 67. 5328 ZSr82 68.9999 25r93 68.8988 Z5r84 67+8748 Z5r95 68. 6128 Z5r86 68.8549 25r87 6?o9468 Z5r88 67.6768 ZSr89 68. 2168 Z5rle 69o4?69 IHRCT 8.8888 IHRCT eaeeee I NFI CT 8. 8888 I HFICT 8.8899 INRCT 8.8888 IHRCT 8.8888 IHRCT e.eeee INRCT 8.8898 IHRCT 8.8888 IHRCT 8.8988 RVC 78.2357 DEW CELLS RHD Zi 53. 1396 RHD Z2 55.3968 RHD 22 52. 9217 RHD 23 58.8114 RHD 23 55.4473 RMD 23 53.8968 RHD Z4 55.6396 RHD 24 54.8242 RHD 25 54.3968 RHD Z5 53.7165 IHRCT 8.8888 INRCT 8.8898 INRCT 8.8888 IHRCT 8.8989 INRCT 8.8888 FIYG 53.8785 RNBIENT PF!ESS 14.5388 VAPOR PRESSURE .2853 DRY PRESSURE 55.7292 FLOWS 8.8888

( .

RECORD NUNBER 125 DRTE 55 TINE 1845 PRESSURES 55.9318 55.9218 RYG 55.9268 RTD'S Zirel 78. 4388 Z lr82 78. 5388 2 ir83 78. 5388 Zlr84 78 4488

~

22rel 78.7368 22r82 78.5288 22r83 re. 61ee 22r84 ?8.6189 22r85 78,7368 Z2r86 78.5S68 22r87 79. 5748 23roi re.8889 Z3r82 78.8448 23r83 79.8448 23r84 78.8888 Z3r85 79.8449 23r86 71. 1588 Z3r87 79.8989 Z3r88 ?8.8888 Z3r89 79.8449 24rel 71. 1868 24r82 71. 8248 Z4re3 78.9788 24r84 78.8898 24~85 ? l. 8689 Z4r86 78.9349 Z4r87 78.7368 24r98 ?9.8628 Z4r89 71. 8868 24r 1 8 71. 8788 25re1 67.5148 Z5r82 68.9998 25 ~83 68.9548 25r84 67.8568 Z5r85 68.5588 25r96 67.9829 Z5r87 67.8748 25r88 67.6229 Z5r89 68.1888 Z5rie 69e4849 INRCT 8.8888 IHRCT 8.8988 INRCT 8.8889 INRCT 8.8899 IHRCT 8.8988 INRCT B.GGGG INRCT 8.8988 IHRCT, Geeeoo INRCT B.GGBG INRCT 8.8888 RVC 78.1669 DEW CELLS RHD Zi 49.8863 RHD Z2 56.6396 RHD 22 58.6268 RHD Z3 53. 9681 RHD Z3 55.2678 RHD Z3 53.8319 RHD 24 53.6989 RHD 24 54. 3191 RHD 25 54.3447 RHD 25 52+7293 IHRCT 8.8888 INRCT 8. 8898 I HFICT 8. 8988 INACT 8 8898 INRCT F 8.8888 FIVG 53. 4989 RNBIEHT PF!ESS 14.5388

( VFIPOR PRESSURE .2825 DRY PRESSURE 55'235 ~

FLOWS '.8888

/I p.aJ p

g'?

j4.

++1 I

k

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RECORD NUMIIER - 126 DATE - 55 TINE - 1188 PRESSURES 55. 9248 55. 9148 RVG SSe9196 RTD'S 2lrei 78.3228 Zir82 78.4668 Zlr83 78.4668 Zir64 76.3488 Z2rel 74.5928 Z2r82 78.4668 Z2r83 ?eo5388 Z2r84 78.5268 Z2r85 76.6468 Z2r86 ?e.466e 22re? 78.5828 Z3rei 76.7966 Z3r82 Pe.?988 Z3r83 78.7548 'Z3r84 78.7548 Z3r85 78.7546 23r86 76.8888 Z3r87 78.8268 Z3res 78. 7548 Z3reg 78.7546 Z4rel 71. 8968 24r82 78.8888 Z4r83 78. 9348 Z4r84 78 ~ 7986 24reS 76.9788 24r86 78.8628 24r87 78. 6828 Z4res 78.?726 Z4r89 76.9528 24rie 71.8868 Z5rel 67 '968 Z5r82 68.8728 Z5r83 44.8368 25r84 67.8288 Z5r85 68.5228 ZSr86 67.9648 25 '87 '7.8388 Z5r88 67.6228 ZSr89 68.1628 Z5rle 69.4648 INRCT 8.8868 INRCT 8.8886 INRCT 8 F 8888 INRCT 8.8686 INRCT "i-'0, 8888 I NRCT 8.8888 INRCT 8. 8888 INFICT 8. 8888 INRCT 8.8888 INACT 8.8888 RVG 78.8962 DEW CELLS RHD Zl 54. 8191 RHD Z2 54.8114 RHD Z2 56.6989 RHD Z3 55.2837 RHD 23 54.3447 RHD 23 51. 6396 RHD Z4 55 '293 RHD Z4 53e4681 RHD Z5 54.2293 RHD 25 53.7422 INFICT 8.8888 INFICT 8.8868 INACT 8. 8888 INRCT 8.8888 INRCT 8.8888 RVG 54.3434 AMBIENT PRESS 14. 5388 VAPOR PRESSURE .2889 DRY PRESSURE 55.7181 FLOWS 8.8888 e.csee RECORD NUNBER 127 DATE - 55 TINE - 1115 PRESSURES '+ 55 91?8 55.9878 RVG 55.9128 RTD'S 21rei 78) 3226 2lr82 78.3948 Zir83 78. 4388 Zlr84 78. 2686 Z2rel 76'15928 Z2r82 . 78. 4128 Z2r83 78.4488 22r84 ?ee4846 Z2r85 ?8.5568 Z2r66 78.4488 Z2r87 ?ee4488 Z3rei 76.7660 Z3r82 78.?366 23r83 78.7888 Z3r84 78.6828 Z3r85 78.7866 Z3r86 78'o8628 23r67 78.7728 23res ?e.6646 23r89 76. 7188 Z4rel 71'.8688 Z4r82 78.8886 Z4r83 78.8886 24r84 78. 7368 24 85 764886 Z4r86 78.8888 24r87 78.6288 24r88 ?8.7186 Z4r89 ?Bfssee 24rie 78.9346 25r81 67.4788 ZSr82 68.8366 ZSr83 68eelse Z5r84 67.8828 ZSr85 68.5646 ZSr86 67.9466 ZSr87 6?:8288 ZSres 67.5688 Z5r89 68.1268 Z5rie 69.3326 INACT 5.866e INRCT 8.8888 INRCT 8.8888 INRCT 8.8666 INRCT ei 8688 INRCT 8.8888 INRCT 8. 8888 INRCT 8.8666 INFICT e. eeee INRCT B.BBBB FIVG ?ee 8477 D EW CELLS RHD Z 1 54. 3191 RHD 22 57.8319 RHD Z2 51. 5499 RHD Z3 52. 8575 RHD Z3 54. 1652 RHD Z3 54.6989 RHD Z4 55. 3319 RHD 24 54. 2866 RHD Z5 54.2293 RHD Z5 52+6524 INRCT 8. 6688 INRCT 8. 8866 I NRCT 8.8888 INRCT '8.8888 INFICT 8. 8888 RVG 54 '698

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RI1B IENT PRESS 14'388 VRPOR PRESSURE ~ 2876 DRY PRESSURE 55 '644 r FLOWS 8.8888

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'RECORD HUNBER - 128 DATE - 55 TINE 1138 PRESSURES 55. 9118 55.9818 RVG ~ 55.9868 RTD'S 21rel 76. 2588 Zlr82 78.3846 Zir83 78. 3228 Z ir84 78. 2149 Z2rei 78. 5568 22r82 78.3848 22r83 78. 4128 Z2r84 ?ee3768 Z2r85 78.5288 Z2r86 78.3488 Z2r87 78. 3588 Z3rei 76.628e Z3r82 78.6648 Z3r83 78.6468 Z3r84 78. 5928 Z3r85 ?eo6289 Z3r86 71 8248

~ 23re? ?e.?eee 23res ?8. 6288 Z3r89 78.6469 24rei 78.9788 Z4r82 78.7548 24r83 78. 7728 24re4 ?eo7186 Z4r85 78.9166 24r86 78.7728 Z4r87 78. 5568 Z4res 78.6469 Z4r89 78.8448 Z4r i 8 78.8888 Z5r81 67. 4688 ZSr82 68.8189 Z5r83 68.8866- Z5r84 67. 7668 Z5r85 68.4688 Z5r86 67.9166 Z5r87 67.7848 ZSreS 67.5588 25r89 68 '989 ZSrl8 69.2966 INRCT e.eeee I NFICT Beeeee IHRCT 8.8888 IHRCT 8.8869 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 I NRCT 8.8698 IHRCT 8.8888 IHRCT 8.8888 RVG 69.9968 DEW CEll S RHD 21 53. 7293 RHD 22 58. 4217 RHD Z2 54.?293 RHD Z3 53olell RHD 23 55. 8114 RHD 23 54 '934 RHD 24 54. 1989 RHD Z4 54.6883 RHD 25 54. 2165 RHD ZS 52.4858 INRCT 8. 8888 IHFICT 8.8868 IHRCT 8.8888 I HFICT 8.8888 IHRCT e.eeee RVG 54.4124 RNB IEHT PF.'ESS 14. 5388 VRPOR PRESSURE .2894 DRY PRESSURE 55.6966 FLOWS 6.8888 8.8888 RECORD NUNI'ER - 129 DRTE - 55 TINE 1145 PRESSURES 55. 9858 55. 8958 RVG 55.9888 RTD'S 21rel ?eel?88 Zlr82 78. 2588 Zir83 ?ee 3848 2 ir94 ?ee1246 Z2rel 78.4668 Z2r82 78. 2868 22r83 ?eo 3488 Z2r94 78o3496 22r85 ?eo4488 Z2r86 76.2868 Z2re? 78 '948 23rel 76.5566 23r82 ?ee5928 Z3r83 78.5928 Z3r84 78.5388 Z3r85 78.5566 23re6 78.7666 Z3r87 78.6466 Z3res ?ee5568 Z3r69 79o6166 24.81 78.9348 24r82 78.7888 Z4r83 .78e7548 Z4r94 79.5746 24 85 79.8628 24r86 78.6828 Z4r97 78.5288 Z4res 78.6199 Z4r89 78.7728 24rie 78.8448 ZSrel 6704428 Z5r82 68.8189 Z5 '83 67.9826 25r64 67 '488 Z5r85 68o4329 ZSr66 67.8566 25 ie? 67.7488 25res 6?.5326 ZSr89 68e8986 Z5rie 69e2240 IHRCT ee8896 INRCT 8.8868 IHRCT 8.8888 I NFICT 9.8696 INRCT 6.9996 INRCT Boeeee IHRCT 8.8988 IHRCT 8.8696 INRCT 8.8888 INRCT 8.8888 RYG 69.9365 DEW CELLS RHD Zl 55.8968 RHD 22 Sle6148 RHD Z2 53.6268 RHD 23 55. 9114 RHD 23 54.562? RHD 23 53.2422 RHD 24 54.5242 RHD Z4 53. 6781 RHD Z5 54 '755 RHD ZS 52e7934 INFICT .8.8888 INRCT 8. 8888 IHRCT 8.8888 IHRCT B.eeee INRCT e.eeee RVG 53.8727 FINB I EHT PF.'ESS

~ 14.5388 YRf'OR PRESSURE .2853 DRY PRESSURE 55.6947 FLOWS 8.8888

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RECORD NUNBER - 138 DATE - 55 TINE - 1289 PRESSURES 55.9898 55i8988 RVG 55.8959 RTD'S Zlr81 78.1428 Zir82 78. 1788 2 ir83 78.2328 Zlr94 79.1969 Z2r81 78.4128 Z2r82 78.2148 Z2r83 78.2868 Z2re4 78 2869 22r85 78.4388 22r86 ?9.2588 Z2r87 78 ~ 2688 23r81 78 5298 Z3r82 78.5388 23r83 ?8.5388 23r84 78.5288 Z3r85, 78.5299 Z3r86 78.7188 Z3r87 7'748 Z3r88 78.5288 Z3r89 79.5389 Z4r,81 78.8628 Z4r82 79.6648 Z4r83 79.6649 24re4 79.5389 Z4r85 78.8268 Z4r86 78 6648 Z4r87 78.4488 Z4r88 7 Z4r89 78.7368 Z4riB 78.7988 Z5r81 67.4248 Z5r82 68. 9909 25r83 67 '648 25r84 67.?388 25r85 68.4328 Z5r96 67.8389 Z5r87 67 '389 Z5r88 67.4968 Zsr89 68.8548 Z5r18 69.2969 ENACT Be8888 INRCT 8.8888 INRCT 9 ~ 8888 INRCT 8.8998 ENACT 8.8888 INRCT 8.8998 INRCT 8.9988 INRCT 8.8998 INRCT 8.8888 I NFICT 8.8889 RVG 69o8966 DEW CELLS RHD 21 53.4729 RHD 22 54.5883 RHD 22 49.2422 RKD Z3 53. 8447 RHD Z3 52.2165 RKD 23 56.5627 RHD Z4 52.8968 RHD Z4 54.2934 RHD Z5 54 '883 RHD 25 53. 2165 INRCT 8.8998 INRCT 9.9999 ENACT 8.8888 I NFICT 8.8988 INRCT 8.8888 RVG 53.4241 ANB IENT PRESS 14.5389 VRPOR PREc'SURE ~ 2919 DRY PRESSURE 55.6931 FLOWS 8.8888 8.8888 l

RECORD HUNEIER - 131 DATE 55 TINE 1215 PRESSURES 55.8958 55.8859 RVG 55.8988 RTD'S Zir81 79. 8888 Z1r82 78. 2329 2lr93 ?8. 2148 2ir84 79. 9168 Z2'r81 78.4128 Z2r82 79. 1248 Z2r83 78. 2328 22r84 78. 2328 22r85 78o3588 22r86 79.2148 Z2r97 78. 2328 23r91 78.5829 Z3 ~82 78.5828 Z3r83 78.5828 Z3r94 78. 4668 Z3r85 78.4848 23r86 78.6468 23r87 78.5389 Z3r88 78. 5828 Z3r99 78.5828 Z4r81 78 8888 24r82

~ 78.6469 Z4r93 78. 6468 Z4r84 79.5299 Z4r85 79.7369 Z4r86 78.6289 Z4r87 78e4488 Z4r98 78.5929 24r89 78.7888 Z4r18 78.7369 25r81 67.4968 Z5r82 67.9828 Z5r83 67.9469 Zsr94 67.6948 Z5rBS 68.3968 Z5r86 67.8298 Zsr87 67. 7129 Z5r 98 67.4789 25r89 68.8368 Z5r18 69.1789 INRCT 8.8888 INRCT 8.9998 ENACT 8.8898 INRCT 8.9998 INRCT 8.9899 INRCT 8.8998 INRCT 8. 8888 I NFICT 8.8889 IHRCT 8.9899 INRCT 8.8899 AVG 69.8613 DEW CELLS RKD Zl 56.3969 RHD Z2 55.4858 RHD 22 55.8447 RHD 23 51. 2934 RHD Z3 52. 1652 RHD Z3 53.3832 RHD Z4 '53.5242 RHD Z4 53. 4988 RHD Zs 54.8755 RHD 25 53 ~ 1524 I NFICT 9.8888 INRCT 8. 8899 INRCT 8.8888 INRCT Be8888 INRCT 8.8888 RVG 53. 9114 RNB IEHT PRESS 14. 4498

( VRPOR PREc:SURE .2956 DRY PRESSURE 55 '844 FLOWS 8.9888

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RECORD NUMBER - 132 DFITE - 55 TIME 1238 PRESSURES 55. 8988 55. 8818 FIVG 55. 6855 RTD'S Zlr81 78. 8348 Zir82 78.1968 Zlr83 78. 1428 Zir84 76.8168 Z2r81 78.3228 22r82 78.1248 Z2r83 78. 1968 Z2r84 ?Gal?86 Z2r85 78.3228 Z2r86 78.1248 22r87 78. 1788 23r81 78.4369 Z3 '82 78.4388 Z3r83 78.4488 Z3r84 78. 3948 23r85 79 4489

~

Z3r86 78.6828 23rG? 78.4668 Z3r88 78.4388 Z3r89 78o4486 Z4r81 78.7988 Z4r82 78.5568 Z4r83 78.5928 Z4r84 78.4489 24r85 78. 7368 Z4r86 78.5568 Z4r87 78.3948 Z4r88 78o4489 Z4r89 78.6648 Z4riG 78.?898 Z5r81 67.3888 Z5r82 67.9646 ZSr83 67.9288 Z5r84 67.6766 Z5r85 68.3788 Z5r86 6?.7849 ZSre? 67.6588 ZSr88 6?o4428 Z5r89 68. 9188 25rlG 69.1766 INRCT 8.8698 INRCT 8.8899 INRCT B. 8888. I HFICT 6.6866 INRCT 8.8888 INRCT 8.8998 IHRCT 8.8888 IHRCT 8.8888 I NFICT 8.8888 INRCT 6.6899 FIVG 69.817?

DEW CELLS RHD Zl 56.6524 RHD Z2 48.4345 RHD 22 53.7558 RHD 23 55. 1652 RHD Z3 58. 8114 RHD 23 55.8378 RHD 24 54.6268 RHD Z4 54 ~ 3191 RHD ZS 53.9986 RHD Z5 53.8627 IHRCT 8.8888 INRCT 8.8668 IHRCT 8.8888 I HFICT 8 ~ 8888 INFICT 8.8888 FIVG 53+ 4882 FIMB IEHT PRESS 14.4488 VFIPOR PRESSURE .2824 DRY PRESSURE 55.6831 FLOWS 8.8888 8.8888 RECORD NUMBER - 133 DFITE - 55 TIME - 1245 PRESSURES 55.8868 55.8758 55.8885 RTD'S 2ir81 69. 9448 Zl r82 ?8. 1248 Zir83 78. 1246 Zlr84 69. 9989 Z2 r81 78.2588 Z2r82 78. 8888 22r83 78. 1688 22r84 78,1248 22rGS 78.2688 22r86 78.1248 Z2r87 79 1428 23r81

~ 76.3948 Z3r82 78.4128 23r83 78.4128 Z3r84 78. 3589 Z3r85 78.3768 Z3r86 78.7728 Z3r87 78.4388 Z3r88 78. 3948 Z3r89 78.4128 24r81 78.7548 Z4r92 78e5748 Z4r83 79.5388 Z4r84 ?6.4488 Z4 '85 78.6828 Z4r86 78.5388 Z4r87 78.3589 Z4r88 76.3946 Z4r89 78.6288 Z4r19 78.6649 ZSr81 67.3888 25r92 67.9469 25r83 67+9189 Z5r84 67.6769 25r85 68.3689 25r86 67.7129 25r87 67.6488 25r88 67.4428 ZSr89 67.9828 Z5r18 69 1526

~

INRCT 8.8696 INFICT 8.8988 I NFICT 8.8888 I NFICT 6.8698 INRCT Go8998 IHFICT 8.8898 IHRCT 8.8888 INRCT 6.6869 INRCT 8.8888 INRCT 8.8696 RVG 69.7874 DEW CELLS RHD Zi 53.6524 RHD 22 52.8447 RHD Z2 52.8863 RHD Z3 53.5883 RHD Z3 54.3?84 RHD Z3 56.6268 RHD Z4 ~

55.8242 RHD 24 53.7886 RHD Z5 53.9345 RHD 25 52 '888 INRCT .6.8898 INRCT 8.8668 IHRCT Be 8888 INFICT 8.8888 IHRCT 8.8686 RVG 53. 9881 RMBIEHT PRESS 14.4488 VRPOR PRESSURE .2856 DRY PRESSURE 55+6749 ~

FLOWS 9.8696 8.8888

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RECORD NUNIlER . 134 DFITE - 55 TINE - 1388 PRESSURES 55.8816 55. 8718 'VG 55.8768 RTD'S Zlr81 69. 9628 Zir82 78. 8788 Zlr83 78. 8348 Z 1 r84 69. 8966 Z2r81 78.2688 Z2r82 78. 8788 Z2r83 78. 1868 Z2r84 76. GSse Z2r85 78.2688 Z2r86 78. 8788 22r87 78.8888 23rei 76. 3226 Z3r82 78.3588 Z3r83 78. 3948 Z3r84 ?ee3228 Z3res 76.346e Z3ree 78.7888 Z3r87 78.4128 Z3res 78.3768 Z3r89 78.3SS6 24r81 78.7888 Z4r82 78.5828 24r83 ?8.5288 24r84 76 3766

~

Z4r85 78.6826 Z4re6 76.4668 24r87 78.3228 24reS 78.3946 24r89 78.5928 Z4rie 78.6288 Z5rei 67 '528 Z5r62 67.9166 25 ~83 67.8928 Z5r84 67.6488 Zsr85 68.3428 Z5r86 67.6946 25r87 67.6228 Z5reS 67.4868 Z5r89 67. 9828 Z5rle e9. <<66 INRCT 8.8888 IHRCT 8. 8888 INRCT 8.8888 IHRCT 8. 8866 INRCT 8.8888 IHRCT 8.8888 INRCT 8.8888 IHRCT 8. 6886 IHRCT e.eeee INRGT 8.8888 RVG 69.7589 DEW CELLS RHD Zl 55.2558 RHD Z2 56.6S24 RHD Z2 54.7886 RHD 23 53.8242 RHD 23 53.6989 RHD Z3 53.5627 RHD Z4 54. 4217- RHD Z4 54.8376 RHD Z5 53.8968 RHD Z5 53. 1524 INRCT 8.8888 INRCT 8.8866 IHRCT 8.8888 IHRCT Boeeee INRCT 8.8888 FIVG 54. 2491 RPIB IEHT PRESS 14.4488 YRPOR PRESSURE .2682 DRY PRESSLIRE 55.66?8 FLOWS 8.8888 RECORD HUNDER - 135 DRTE - 55 TINE - 1315 PRESSURES Ss.s?7e 55.8668 RVG 55.8715 RTD'S Zl hei 69. 8728 Zir82 78.8348 Zir83 69. 9988 2 1r84 69. 8546, Z2 hei 78.2588 Z2r82 78. 8168 Z2r63 78. 8788 22r84 78. 8346 22r85 78.2588 Z2r86 78.8348 Z2re? 78. 8526 23rel 76. 2S68 Z3r82 76.3228 Z3r83 78.3588 Z3r84 78. 2868 Z3r85 76 3646

~

23r86 76.5568 Z3r67 76.3766 23res 78.3226 23r89 78. 3586 Z4 i81 76.6646 Z4r62 78.4486 Z4r83 76.5828 24r64 76. 4486 Z4r85 78.6288 Z4r86 78.4666 Z4r87 76.2566 Z4res 78.3226 Z4r89 78.5386 Z4rle 78. 5388 Zsre1 67.3168 Z5r62 67.S926 Z5r83 67.8748 25r84 67.6848 Z5r85 68.3248 Z5r86 67.7126 25r87 67.5868 Z5reS 67.3888 25r89 67.9646 25ri 6 69.1166 INRCT 6.8886 IHRCT e eeee IHRCT 8. 8886 IHRCT 8.8666 INRCT 6.8668 INRCT 8.8886 IHRCT 6.6888 I NFICT 8.8666 IHRCT 8.8888 INRCT 6.8868 8VG 69.7145 DEW CELLS RHD Zl 55.8755 RHD 22 54.4729 RHD 22 53.7558 RHD 23 52. 1969 RHD Z3 53.8883 RHD Z3 53.5755 RHD Z4 53o8863 RHD 24 52. 6396 RHD 25 53.8447 RHD Z5 52.7934 IHRCT '8.8888 INRCT 8. 8866 IHRCT Boeeee IHRCT 8.8888 IH8CT 8.8888 RVG 53. 5363 RNB IEHT PRESS 14.4486 VRPOR PRESSURE o2828 DRY PRESSURE 55.6687 FLOWS 8.8888

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RECORD NUNDER - 136 DATE - 55 TINE - 1338 PRESSURES 55.8728 55.8628 RVG 55. 867e RTD'S Zirei 69. 8548 Z ir82 78.8348 Zir83 69. 9988 Zlr84 69.86ee Z2rei 78. 1428 Z2r82 69.9988 22r83 78. 1868 Z2r84 78.816e Z2r85 ?e. 16ee Z2re6 69.9988 22r87 78.8348 Z3rei 78.3648 Z3r82 78.2868 Z3r83 78.2688 Z3r84 76e2328 Z3r85 78>>2868 Z3r86 78.5828 Z3r87 78.3228 23re8 78.2868 Z3r89 78.3228 Z4r81 78. 6468 Z4r82 78. 4128 Z4r83 78.3948 Z4r84 78. 3768 Z4r85 78.5388 Z4r86 78.3948 24r87 78.2588 Z4r88 78.2686 24r89 78 '828 Z4rle ?8.5288 25r81 67.2888 Z5r82 67.8746 25r83 67 '388 Zsr84 67.5868 Z5re5 68.2788 25r86 67.6948 25r87 67;5688 Z5r88 67.3788 25re9 67. 9288 Z5r 1 8 69.8628 INACT 8.8888 INRcT 8.8888 INRCT 8.8888 IHRCT 8. 8888 INRCT 8.8888 INRCT 8.8888 IHRCT 8.8888 INRCT e.eeee IHRCT 8.8886 INRCT e.eeee RVG 69.6778 DEW CELLS RHD Zi 58.9858 RHD Z2 51.1989 RHD Z2 54.2934 RHD Z3 52. 9681 RHD Z3 53.9345 RHD Z3 54'191 RHD Z4 52. 1268 RHD Z4 52.2422 RHD Z5 53 '781 RHD Z5 53.8883 INRCT B. 8888 I HRCT 8.8886 INRCT 8.8688 INRCT B.BGBB IHRCT 8.8868 RVG 52.9327 AMBIENT PRESS 14 '488 VRPOR PRESSURE ~ 1983 DRY PRESSURE 55. 6687 FLOWS 8.8888 RECORD NUNBER 137 DRTE - 55 TINE - 1345 PRESSURES "'5 '688 55 '588 RVG 55.8638 RTD'S Zlrei 69.8888 Zlr82 69. 9268 Z ir83 69. 9448 Zir84 69.7828 Z2rel 78.8528 Z2r82 69.9446 Z2r83 69. 9988 Z2r84 69.9886 Z2r85 78.1248 Z2r86 69.9628 Z2re7 76. 8168 23rei 78.2688 Z3r82 78.2688 Z3r83 78.2588 Z3r84 ?8. 2146 23r85 78.2328 Z3r86 78.4668 Z3r87 78.3848 Z3r88 78. 2588 23r89 76.2686 Z4iei 76.6288 24r82 78.4388 Z4r83 78. 3588 Z4r84 78.2868 Z4r85 78.5748 Z4r86 78.4128 Z4re7 78. 2148 Z4r88 78.2686 Z4r89 76.4666 Z4rie 78.5288 Z5rel 67. 2888 Z5r82 67.8568 Z5r83 67.8388 Z5rS4 67.5688 ZSreS 68. 2766 Zsr86 67.6488 Z5r87 67.5588 Z5r88 67.3528 Zsr89 67. 9188 Z5rie 69.6626 IHRCT 8.8888 INRCT G.Sees INRCT 8 ~ 8888 INRCT 8.8666 INRCT B.eeee IHRCT S.eeee INRCT 8 ~ 8886 INRCT 8.8868 IHRCT S.eeee IHRCT Geeeee RVG 69.6468 DEW CELLS RHD 21 54. 1524 RHD Z2 52. 1652 RHD Z2 .51. 4729 RHD 23 54o4345 RHD Z3 54.4729 RHD Z3 55.5627 RHD 24 53.6396 RHD 24 53o5883 RHD Z5 53.6524 RHD Z5 52.7886 INRCT 8.8888 INRCT Goeeee INRCT B.BGBB IHRCT 8 ~ 8888 IHRCT S.eeee RVG 53.5468 AMBIENT PPESS 14.4488 VAPOR PRESSURE ~ 2828 DRY PRESSURE 55.6682 FLOWS 8 ~ 8888

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RECORD NUMBER - 138 DRTE - 55 TINE - 1488 PRESSURES 55.8658 55. 8548 RYG 55.8595 RTD'S Zlrei 69.?648 2ir82 69.9888 2ir83 69. 9888 Z ir84 69.?e4e 22rei 78. 8788 22r82 69.9888 Z2r83 78.8348 Z2r84 69.9e2e Z2 i85 78. 1248 Z2r86 69.9266 22r87 69.9448 Z3rei ree2149 Z3r82 78.2148 Z3r83 78,2328 Z3r84 .?e. 1968 Z3r85 ?'9.2326 Z3r86 78. 6188 23r87 78.2588 Z3r88 ?8.2148 Z3r89 76.2329 Z4r81 78. 5568 Z4r82 78.3588 Z4r83 ?e.3588 24r84 78.2146 Z4r85 78.4668 Z4r86 ?8.3588 Z4r87 ?8. 1688 24r88 ?9.2329 Z4r89 ?e.46ee 24r 1 8 78.5828 Z5rel 67.2628 Z5r82 67.8386 ZSr83 67.8928 Z5r84 67.5588 Z5r85 68. 2348 Z5r86 67.6229 Z5r87 6?as149 Z5r'88 67.3348 Z5r89 67.8748 ZSrie 68.9989 IHACT 8.8888 INRCT e.eeee INACT 8.8888 INACT 8.8868 I NFICT Beeeee IHRCT B.eeee INRCT 8.8888 INRCT 8.8869 IHRCT e.eeee I NFI CT e.eeee FIYG 69.6281 DEW CELLS RHD Zi 53.7837 RHD 22 52. 1396 RHD Z2 52.3968 RMD Z3 54.4986 RHD Z3 53.4217 RHD 23 53.8319 RHD Z4 53.7558 RHD Z4 54.5114 RHD Z5 53. 7165 RHD Z5 53.8242 IHRCT 8.8888 INFICT 8. 8869 INACT B.eeee INFICT 8.8888 INRCT ee 8888 RVG 53.4745 AMBIENT PRESS 14 ~ 4488 VAPOR PRESSURE ~ 2823 DRY PRESSURE 55. 65?2 FLOWS 8 8888

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RECORD NUMBER 139 DRTE - 55 TINE - 1415 PRESSURES 55.8618 55.8516 RVG 55.8568 RTD'S 21 81 69.7468 Zlr82 69. 9268 Zlr93 69. 8728 Zir84 69. 7169 22iei 78.8888 22r82 69.8969 Z2r83 78. 8168 Z2r84 69.9269 Z2r85 78. 1248 Z2ree 69.9266 22r87 69. 9888 23r81 79.1786 Z3r82 78. 1788 Z3r83 ?8.1966 Z3r84 78. 1688 Z3r65 78.2326 23r86 78.4388 Z3r87 78.2149 Z3r88 78.1968 Z3r99 7'968 24rei ?9.5388 Z4r82 76.3586 24r83 78.3848 24r84 76.2148 Z4r85 ?'e.4489 Z4ree 78.3948 Z4r87 76.1248 Z4r88 79.1966 Z4r99 78.3766 Z4rle 78.4668 Z5rel 6?'.2448 25r62 67.8266 Z5r83 67.?848 25r84 6?o5328 ZSr85 68.2348 25r86 6?.5868 zs. Br 67.5148 25r88 6?. 3168 Z5re9 6?e8746 Z5rle 68.9989 INACT 8.8969 IHACT 8. 8866 INACT 8.8866 INACT 8.8896 INRCT B.BBBB IHRCT e. 8886 INRCT 8. 8686 INRCT 8.8888 INACT B.BGBB IHRCT 8. 8888 RVG 69.5931 DEW CELLS RHD Zl 56. 1268 RHD 22 58.7934 RHD Z2 51. 3784 RHD 23 53. 2422 RHD 23 53.6781 RHD 23 56.6989 RHD 24 '52 7165

~ RHD Z4 51.5883 RHD Z5 53'165 RHD Z5 52.6989 INRCT 4.8888 IHRCT 8.8888 IHACT 8. 8888 IHRCT 8.8888 INRCT e.eeee RVG 53.2365 FINBIEHT PRESS 14.4488

( VAPOR PREBSURE .2ees DRY PRESSURE 55.6555 FLOWS e.eeee e.eeee

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RECORD NURSER - 148 DATE - 55 TINE 1438 PRESSURES 55.8578 55.8478 AVG SS.BS28 RTD'S Zirei 69. 7188 Zlr82 69 '728 Zlr83 69. 8188 Zlr84, 69I6568 Z2rei 78. 8168 Z2r82 69.8368 Z2r83 69.9888 22r84 69.8988 Z2r85 78.8348 Z2r86 69.8548 Z2r87 69.8988 23r81 78.1428 23r82 78. 1788 Z3r83 78.1428 Z3r84 78 '428 23r85 78.1428 Z3r86 78 '128 Z3r87 78.1968 23r88 78.1688 23r89 78e1968 Z4r81 78.5828 Z4r82 78 2868 24r83 78.2688 24r84 78 '6ee Z4r85 78.5828 Z4re6 78.2868 24re? 78.1868 24r88 78.16ee Z4r89'5r83

78. 3768 Z4rie 78.4128 Z5rel 67.2268 25r82 67. 882e 67.7668 Z5r84 67.4968.Z5r85 68.1988 ZSre6 67. 558e Z5r87 67.4788 Zsr88 67.2988 Z5r89 67.8568 25rie 68.9988 I NFICT 8.8888 INACT 8.8888 INFICT 8.8888 INACT 8. 8888 INACT B.BBBB I NFICT 8.8888 INACT 8.8888 INACT 8.8888 INACT e.eeee INACT 8. 8888 AVG 69.5583 DEN CELLS RHD 21 51 ~ 8755 RHD Z2 48.8447 RHD Z2 52.7934 RHD Z3 53. 6?81 RHD Z3 51.2837 RHD Z3 5 1 8575 RHD Z4

~ 54.5378 RHD 24 54.6?81 RHD Z5 53.5883 RHD ZS 52.767B INACT 8.8888 INFICT 8.8888 INACT 8. 8888 INACT 8.8888 INACT 8.8888 AVG 52 '969 AMBIENT PRESS 14.44ee VAPOR PRESSURE .1951 DRY PRESSURE 55.6569

'FLOWS e.eeee B.BBBB

RECORD HUNEKER 141 DATE - 55 TINE - 1445 PRESSURES 55.8548 55.8438 RVG 55e8485 RTD'S Zlr81 69 '748 Zlr82 69.8368 Zir83 69. 8368 Zlr84 69. 6928 22r81 78.8348 Z2r82 69.8368 22r83 69 '548 Z2r84 69.8728 Z2i85 78o8348 Z2r86 69.8548 22r87 69.8548 Z3r81 78.9889 23r82 - TO 1868 Z3r83

~ 78. 1868 Z3r84 78.8528 Z3r95 78.1969 23r86 78. 3488 Z3r87 78. 1688 Z3r88 78. 1248 Z3r89 78+1429 Z4r81 78. 4848 24r82 78 2868 Z4r83

~ 78.2868 Z4r84 78.1789 Z4r85 78m 4388 Z4r86 78.2868 Z4r87 78.8888 Z4r88 78. 1429 Z4r89 78 '488 Z4r18 78.3948 ZSr81 67.2988 Z5r82 67.7849 Z5. 83 67 '488 Z5r84 67.4788 Z5r85 68. 1888 25r86 67 '689 Z5r87 67a4688 Z5r88 67.2628 ZSr89 67.8388 Z5r18 68.9188 IHRCT 8.8888 IHRCT 8.8888 IHRCT O.BGBO INRCT 8.8888 IHRCT 8.8898 I HFICT 8.8888 INFICT 8.8888 IHFICT 8.8888 INRCT Bo 8888 IHRCT 8.8888 RVG 69 '385 DEW CELLS RHD Z 1 56 ~ 5883 RHD Z2 54.7165 RHD Z2 51. 7558 RHD 23 54. 2678 RHD Z3 51 ~ 9681 RHD Z3 54. 1148 RHD 24 53.8114 RHD Z4 52'691 RHD Z5 53. 8191 RMD Z5 52 '832 INRCT 8.8888 INACT 8.8899 IHRCT 8. 8888 INRCT 8.8888 IHACT 8 ~ 8888 FIVG 53.5621 RNBIEHT PRESS 14.4488 VAPOR PRESSURE ~ 2838 DRY PRESSURE 55.6455 FLOMS 8.8888 8 ~ 8888

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RECORD NUNIlER - 142 DATE - 55 TINE 1588 PRESSURES 55. 8518 55 '488 RVG 55+ 8455 RTD'S Zi~ei 69.6388 Zir82 69.8888 21~83 69,7828 Zire4 69.5848 22cel 69.9448 22r82 69.8888 22~83 69.8728 22r84 69.8368 22re5 78.8168 22~86 69.8888 22re? 69. 8188 23rei 78.1868 23~82 78.8888 23r83 78.8888 23r84 78.8528 23r85 7e.eSse 23r86 78.5748 23re? 78. 1248 23r88 78. 8888 23ie9 ?e.ie68 24rei 78.4668 24r82 78.2328 24i83 78.2328 24r84 78. 1868 24c85 78.4128 24r86 78. 2148 24ie? 78.8788 24res 78. 1248 24 89 78.3848 24rie 78.3588 25>81 67.1728 25r82 67.7668 25i83 67.7388 25r84 67.4688 25r85 68.1888 25i86 67.5328 25ie? 67.4428 25res 67. 2628 25i89 6?.8828 25rie 68.9368 INRCT 8.8888 INRCT 8.8888 INRCT Boeeee INRCT 8.8888 I NFICT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INFICT 8 ~ 8888 RVG 69.5889 DEW CELI S RHD Z 1 56. 6148 RHD 22 51.?6?8 RHD Z2 58. 3319 RHD 23 54. 9345 RHD Z3 51. 5499 RHD Z3 54.3319 RHD 24 53.5627 RHD Z4 54. 7165 RHD Z5 53.6652 RHD Z5 52.8575 INRCT 8.8888 INRCT G. 8888 INRCT 8. 8888 I NRCT 8.8888 INRCT e.eeee RVG 53.4864 Rl1BIENT PRESS 14. 4488 VAPOR PRESSURE ~ 2818 DRY PRESSURE 55. 6437 FLOWS 8.8888 RECORD NUMBER - 143 DATE - 55 TINE 1515 PRESSURES 55.8478 55.8378 RYG 55.8428 RTD'S 2lrei 69. 6388 Zli82 69.7828 Zii83 69. 7648 Zli84 69. 5668 22rel 69'628 22ie2 69+ 7648 22ie3 69. 7828 22r84 69.8888 22i85 69.9988 22i86 69.7828 22re? 69. 8888 23rel 78.8528 23re2 78.1868 23/83 78.8788 23ie4 78 8348 23re5

~ 78.8528

23. 86 78.3848 23re? 78.8888 23ies 78 8788 23r89

~ 78.8888 24iel 78.3948 24ie2 78. 1968 24i83 78. 2328 24re4 78. 1868

24. 85 78.4128 24i86 78. 2148 24ie? 78. 8528 24res 78. 8788 24 F89 78o2868 24ile 78.3488 25rei 67. 1988 25re2 67. 7488 25~83 6?e7388 25r84 67. 4688 25ie5 68. 1628 25i86 67.4968 25 ~87 67.4428 25ies 6?o2448 25i89 67. 8288 25rie 68.8648 I NFICT 8.8888 INRCT Greece INRCT B.eeee INRCT G.GGGG INACT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT G.BGGG INRCT 8.8888 INRCT Goeeee RVG 69.4889 DEW CELLS RHD Zi 51. 8242 RHD Z2 51. 6652 RHD 22 53. 1268 RHD Z3 53. 9858 RHD 23 53.6524 RHD 23 55.3968 RHD Z4 54e2934 RHD Z4 54 8114

~

RHD Z5 53e6811 RHD 25 52.8832 INRCT 8.8888 INACT B.GBGG INRCT G.eeee INACT 8+8888 INFICT eeeeee RVG 53'259 RISBIENT PRESS 14.4488

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YFIPOR PRESSURE I2812 DRY PRESSURE 55o6488 FLOWS BIBBBB e.eeee

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RECORD NUMBER - 144 DATE 55 TINE 1536 PRESSURES 55.8439 55.8338 AVG 55.9398 RTD'S Zir81 69. 5488 Zir82 69.7468 Zlr83 69. 7188 Zire4 69.5489 Z2r81 69. 9888 Z2r82 69.7188 Z2r83 69.8188 Z2re4 69.?46e

.Z2ies 69. 9888 22r86 69.7468 Z2r87 69.7648 Z3rel 79.9348 23r82 78. 8788 Z3r83 78.8528 Z3r84 69.9888 Z3r85 ?8.916e 23r86 78.3948 23r87 78.8788 Z3r88 78.8348 Z3r89 ?8.9888 Z4r81 78.3768 24r82 78. 1968 Z4r83 78.1968 24r84 78.6?99 Z4r85 78.4128 Z4r86 78. 1688 Z4r87 69.9988 Z4r88 ?8 6?99 Z4r89 76.2688 Z4rie 78.2868 Zsrei 67.1728 25r82 6?o?489 Z5r83 67.7128 Z5r84 67.4428 Z5r85 68.1268 Z5r86 67.5326 25r87 67.4968 Zsree 67.2268 Z5r89 67.7668 Zsrle 68.8829 INACT 8 ~ 8888 ENACT 8.8688 IHACT 8.8888 IHACT 8.8969 INACT 8.8888 ENACT 8.8888 INACT 8.8888 I NFICT 9.9996 IHACT e.eeee INACT 8.8898 AVG 69.4553 DEW CELLS RHD Zl 56.8378 RHD Z2 58. 1268 RHD Z2 58.7293 RHD Z3 54. 8863 RHD Z3 54.4473 RHD Z3 53.7293 RHD Z4 58.2934 RHD Z4 53.1781 RHD Z5 53.5627 RHD 25 52.8447 INACT 8.8868 INACT 8.6966 I NFICT eoeeee IHACT 8.8888 IHACT 8.8888 AVG 53.7729 flt'1B IEHT PRESS 14.4488 YAPOR PRESSURE .2945 DRY PRESSURE 55.6335 FLOWS 8.8888 RECORD NUMBER - 145 DFITE - 55 TINE - 1545 PRESSURES 55.9488 55. 8388 'YG 55. 8359 RTD'S Zirel 69. 5368 2 lr82 69. 7468 Zir83 69. 6928 Zir84 69.4946 Z2rei 69.8366 22r82 69.6748 Z2r83 69.7648 Z2r84 69.7169 Z2res 69.9628 Z2r86 69.6928 Z2r87 69.7468 23rel 69.9988 Z3r82 78.8348 Z3r83 69.9988 Z3r84 69.9628 23res 69.9866 Z3r86 78.1?88 Z3r87 78.8526 Z3re8 78. 8168 23r89 79.8799 Z4rei 78 '588 24r82 78.1248 Z4re3 78.1788 Z4r94 76.9889 Z4r85 78.2688 Z4r86 78.1788 Z4re7 69.9889 Z4r98 76.6169 24r89 79.2586 Z4rle 78.2328 Z5rel 6?.1549 Z5r62 67.7399 Z5r83 67.6948 Z5r84 67.424e ZSreS 68.8988 Z5r86 67'5149 Z5r87 67.4869 Zsree 67.2889 Z5r89 67.7668 25rie 6e.S648 IHACT Beeeee INACT 8.8886 INACT 8.8888 IHRCT eoeeee ENACT 8.8988 INACT 8.8999 IHFICT 8.8688 I NFICT 8.8968 IHFICT 8.8889 IHACT 8.8888 AVG 69s4223 DEW CELLS RHD Zi 52.8575 RHD Z2 54. 2165 RHD 22 52o6652 RHD 23 53. 6524 RHD Z3 52 '883 RHD Z3 sea4345 RHD Z4 54e2558 RHD Z4 53.4858 RHD Zs 53.5627 RKD 25 52.8832 IHflCT 8.8888 IHACT 8; 6668 NACT e.eeee ENACT 8.8888 INACT 8.8888 RVG 53+ 8287 AMBIENT PPESS 14'488 VAPOR PRESSURE ~ 1998 DRY PRESSURE 55. 6366 F I.OWS 8.8888

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RECORD NUI'IBER - 146 DATE 55 T I NE - 1688 PRESSURES 55. 8378 55.8278 RVG 55. 8328

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RTD'S Zir81 69. 5128 2 lr82 69 ~ 7188 Zir83 69. 6748 Zlr84 4768 Z2r81 69.8988 22r82 69.7188 22r83 69.8188 Z2r84 69. 6?48 22r85 69.8368 22r86 69.7188 Z2r87 69.? 188 Z3r 8 1 69. 98GG Z3r82 69.9628 Z3r83 69.9888 23r84 69.9268 Z3r85 69.9980 Z3r86 78. 3848 Z3r87 78.8348 23r88 69.9888 Z3r89 78.8168 24r81 78.3488 24r82 78.1868 Z4r83 78. 1868 Z4r84 78.8340 24r85 78.2868 Z4r86 78.1248 Z4r87 69.9448 Z4r88 78.8348 Z4r89 78. 1968 24r18 78.2588 Z5r81 67. 1548 25r 82 67. 7 128 25r83 Z5r87 67.6768 67.3888 Zsre4 Z5r88 67.4868 67.1988 ZSr85 Z5r89 INRCT'9.

68.8988 ZSr86 67o 7488 .ZSr18 67.4968

68. 8460 INACT 8.8888 INFICT 8.8888 INRCT 8.8888 INRCT 8.8808 INRCT 8.8088 INRCT 8F 8888 I NFI CT 8.8888 8. 8888 INRCT 8.8888 INRCT 8.8888 RVG 69.4876 DEW CELLS RHD 21 58.9729 RHD 22 51.4858 RHD 22 58. 8319 RHD 23 54. 7293 RHD Z3 51. 5114 RHD 23 51'4858 RHD Z4 53.2293 RHD 24 53.8575 53,5883 25 52.7293 8.8888 INACT 8.8000

~

RHD Z5 INRCT RVG

'.8888

52. 4429 RKD INRCT 8.8888 INRCT INFICT 8.8888 FII1B I ENT PRESS 14+ 4488 VFIPOR PRESSURE .1947 DRY PRESSURE 55.6373 FLOWS 8.8888

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RECORD NUNBER - 147 DFITE - 55, TINE 1615 PRESSURES 55.8348 55.8248 RVG 55.8298 RTD'S 2ir81 69.5128 Zlr82 69. 6928 Z1r83 69.6388 Zlr84 69. 4488 Z2r81 69.8548 22r82 69.6748 22r83 69.7468 Z2r84 69. 6568 Z2r85 69,8988 Z2r86 69.6388 Z2r87 69.6928 23r81 69. 9628 Z3r82 69.9988 Z3r83 69.9628 Z3r84 69.9448 Z3r85 69.9988 23r86 78.2688 23r87 78e8348 Z3r88 69.9628 Z3r89 69.9980 Z4r81 78.3228 Z4r82 78.1248 24r83 78. 1868 -24r84 69.9988 Z4r85 78.2688 Z4r86 78. 1868 Z4r87 69.9888 Z4r88 69.9628 Z4r89 78.2148 24riG 78.1968 ZSr81 67.1188 25r82 67.6948 Z5r83 67.6588 Z5r84 67.3888 Z5r85 68.8728 25r86 67.4968 ZSr87 67.3?88 ZSr88 67. 1988 25r89 67.7388 Z5r18 68.8640 I NFICT 8.8888 INRCT 8.8888 INRCT 8 8888 F INRCT 8. 8808 I NFICT 8.8888 INRCT 8.8888 INFICT 8.8888 INRCT G. GGGG I NFICT 8.8888 INRCT 8;8888 RVG 69.3918 DEW CELLS HD Zi 58.2678 RHD 22 52.5883 RHD Z2 55 8627 RHD Z3 53.2558 D 23 53 '473 RHD Z3 53+3447 RHD Z4 53.5378 RHD Z4 54.8883 D Z5 53.5499 RHD Z5 52.8447 INRCT 8.8888 INRCT 8.8888 INRCT 8 F 8888 INFICT 8.8888 INRCT 8.8888 RVG 53o2369 FIHB IENT PRESS 14.4488 VFIPOR PRESSURE ~ 2885 DRY PRESSURE 55.6285 FLOWS B.BBBG

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RECORD NUMBER - 148 DRTE 55 TINE - 1638 PRESSURES 55.8318 55.8228 RVG 55. 8265 RTD'S Zir&1 69.4768 Zir82 69.5848 Zir83 69.6288 Zir84 69.4949 Z2r81 69.7828 Z2r82 69.6288 Z2r83 69.6928 Z2r94 69.6569 Z2r85 69.8988 Z2r86 69.6568 Z2rB? 69.6748 Z3r81 69.9440 Z3r82 69. 9888 Z3r83 69.9888 Z3r84 69.9888 Z3r85 69.9980 23r86 78.8348 Z3r87 69.9628 Z3r88 69.9888 Z3r89 69.98OG Z4r81 78.2688 24r82 78.8888 Z4r83 78.8528 Z4r84 79.8349 Z4r85 ?8. 1788 Z4r86 78.9788 Z4r87 69.8988 Z4r88 69.9449 Z4r89 78 '428 Z4riB ?8.2148 Z5r81 67. 1888 ZSr92 67. 676 0 Z5r83 '67.6588 Z5r84 67.3888 25r85 68.8728 ZSr86 67.4789 ZSr87 67.3788 Z5r88 67.1728 Z5r89 67. 7128 Z5ri 9 68.7929 INRCT 8.8888 INFICT 8.9888 INRCT 8. 8888 I NFICT 9.8990 INRCT 8.8888 INRCT 8.8998 INRCT 8.8888 INRCT 9.9998 INRCT Be8888 INRCT 8.8888 FIVG 69.3549 DEW CEI LS RHD Z 1 58. 7293 RHD Z2 53. 9217 RHD 22 52.7293 RHD 23 51. 7896 RHD Z3 52.?422 RHD Z3 51. 8242 RHD Z4 54.3863 RHD Z4 53.5883 RHD 25 53.4858 RHD ZS 52.6652 INRCT 8.8899 INRCT 9;9999 INRCT 8.8888 INRCT 8.8989 INFICT 8.8988 RVG 52.7149 RNBIENT PRESS 14.4488 VRPOR PRESSURE ei967 DRY PRESSURE 55.6298 FLOWS 8.8888 RECORD NUMBER - 149 DFITE 55 TINE 1645 PRESSURES 55.8298 55. 8198 RVG 55. 8248 RTD'S Zlr81 69. 4488 Zlr82 69.6928 Zlr83 69. 6288 Zlr84 69. 4589 Z2r91 69.7828 Z2r82 69.6289 Z2r83 69.6749 Z2r84 69. 6389 Z2r85 69.8368 Z2r86 69.6288 Z2r97 69.6568 Z3r91 69.9269 Z3r82 69.8998 Z3r83 69.9888 Z3r94 69.8729 Z3r85 69.9809 23r86 78.9168 Z3r87 69.9449 Z3r88 69.8989 Z3r89 69. 9449 Z4r91 78.2688 Z4r82 78,8?89 Z4r83 79.8169 Z4r94 69. 9260 Z4r85 79.26SG Z4r96 78.8889 Z4r87 69,8989 24r88 69.9980 24'9 ?8. 1428 24r18 78. 1249 Z5r91 67.9829 Z5r92 67.6769 Z5r93 67.6498 25r84 67.3788 ZSr85 68.8188 Z5r86 67.4788 Z5r87 67.3348 25rBS 67.1368 ZSr99 6?.6949 25ri8 68.7749 INRCT 8.9998 INFICT 8.8998 INRCT 8.8888 INRCT 9.9900 INRCT 9.8989 IHRCT 8.8888 INRCT 8. 9988 INRCT 8.8989 INRCT 8.8898 INRCT 8.8888 RVG 69.3382 DEW CELLS RHD 21 52.6396 RHD Z2 54e9986 RHD Z2 54. 3191 RHD 23 52 '678 HD Z3 51. 8832 RHD 23 51. 2678 RHD Z4 53'378 RHD Z4 53.2422 HD 25 53.4217 RHD 25 52.6524 INRCT 8. 8888 INRCT 9.8998 NRCT 8.8888 INRCT 8.8888 INRCT 8. 8888 RVG 53.8512 RNB I ENT PRESS 14e4488 VRPQR PRESSURE . 1992 DRY PRESSURE 55.6248 FLOWS 8.8888

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RECOF;D t<UttBER - 156 DRTE - 55 TINE - 1789 PRESSURES 55. 8258 55. 8168 FIVG 55. 8295 RTD'S Ziroi 69. 4588 2lr82 69. 5128 21r83 69.5488 Zir84 69. 3869 Z2rol 69.7468 Z2r82 69.5848 22r63 69.6568 Z2r84 69.6566 Z2r65 69.7828 Z2r86 69.5848 22r87 69.5848 Z3rol 69.9986 Z3r62 69.9888 Z3r83 69.8728 Z3r84 69.8368 Z3r85 69.8549 Z3r86 76.8528 Z3r87 69.9448 Z3ros 69.8988 Z3r89 69.9269 24rol 78.2688 Z4r82 78.8168 Z4r83 78.8528 Z4r84 69.9989 Z4r85 78.2328 Z4r86 78.8348 Z4r87 69.8368 Z4ros 69.8909 24r89 78.1428 Z4rio 78.1248 Z5rol 67.8648 Z5r62 67. 6499 ZSr63 67.6228 Z5r84 67.3528 Z5r85 68.8368 25r86 67.3880 Z5ro7 67.3346 ZSr88 67.1368 Z5r99 67.6768 ZSrlo 68.7386 IHRCT 9.9999 IHFICT 8.8888 INRCT 8.8888 INFICT 8.8966 IHRCT 8. 8868 INFICT 8.8888 IHRCT 8.8888 INRCT 8.6669 INRCT 6.8888 INRCT 8.8888 RVG 69. 3895 DEW CELLS RHD Zl 52.5376 RHD 22 53. 9473 RHD Z2 54.6781 RHD 23 54.3832 RHD Z3 52.8968 RHD Z3 58.7886 RHD Z4 52.6989 RHD Z4 52.8447 RHD Z5 53.4888 RHD Z5 52 '934 INFICT 8.8888 INRCT 8.8999 IHRCT 8.9688 INRCT 8.,8888 INRCT Gooooo

.RVG 53.1137 RNB I EthT PRESS 14.4488 VFIPOR PRESSURE .1996 DRY PRESSURE 55.6289 FLOWS 6.9666 RECORD NUNBER 151 DRTE - 55 TINE 1715 PRESSURES 55. 8238 55. 8138 RVG 55. 8188 RTD S Zlrol 69. 3689 Zir82 69.5668 Zir83 69. 5388 Zir84 69. 3560 22rol 69. 7188 Z2r82 69.5489 Z2r83 69.6929 Z2r64 69 ~ SS49 Z2r65 69.7280 Z2r86 69.5489 Z2ro? 69.5849 23rol 69. 8549 Z3r62 69.8?28 23r83 69.8728 Z3r64 69.8366 Z3r85 69. 9989 Z3r66 76.2688 Z3r87 69.9888 Z3ros 69.8546 23r99 69. 9986 Z4r01 78.2326 Z4r82 78.9346 Z4r83 69.9989 Z4r64 69. 9446 Z4roS 76. 2148 Z4r86 69.9988 Z4r87 69. 8188 Z4ros S999 '9.

24r99 78.1869 Z4rio 78.1248 25roi 67.8826 Z5r92 67.6466 Z5r93 67.6229 Z5r84 67.3348 Z5r85 68.8366 Z5r86 67.4669 Z5r67 67.3168 Z5ros 67. 1188 Z5r69 67.6588 Z5rlo 68.7749 I HFICT 8.9699 INRCT 8.8688 IHRCT 9.8999 IHFICT 8. 6996 INRCT 9.8606 INRCT 8.8888 IHRCT 8.8888 IHFICT 6,6066 IHRCT 8.9888 IHRCT 8.8888 RVG 69. 3816 DEW CELLS RHD Z 1 55. 6811 RHD Z2 58.7934 RHD Z2 54.8?84 RHD Z3 53. 2165 RMD 23 53.9691 RHD 23 51. 3191 RHD Z4 52.4986 RMD 24 52.8376 D 25 53.3968 RHD 25 52'?837 INRCT 8..8898 INRCT 6.9660 RCT 8.8888 INRCT 8.8868 INRCT 8.9669 VG 53 ~ 8527 Rt'1BI EN 7 PRESS 14.4488

( VRPOR PRESSURE ~ 1992 DRY PRESSURE 55. 6188 F L014S ~ 8. 8888 8.6699

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RECORD NUI'IBER - 152 DFITE - 55 TINE - 1738 PRESSURES 55.8288 55. 8118 RVG 55. 8155 RTD'S Z1r81 69.4228 Zir82 69.5668 Zir83 69.5128 21r84 69. 3868 Z2r81 69.5848 Z2r82 69,5388 22r83 69.5668 Z2r84 69. 5488 Z2rGS 69.7468 22r86 69.5488 22r87 69.5668 Z3rei 69. S548 Z3r82 69.8728 Z3r83 69.8548 23re4 69. 8188 Z3r85 69.8728 Z3r86 78. 1428 Z3r87 69.8728 Z3res 69. 8188 23r89 69.8728 Z4rei 78. 1968 24r82 69.9628 Z4r83 69.9628 Z4r84 69.8S40 24r85 78.1428 24r86 69. 9888 Z4r87 69. 8188 Z4res 69.8548 24r89 78.8348 Z4rie 78. 1868 ZSre 1 67.8648 Z5r82 67.6488 Z5r83 67.6228 Z5r84 67.3168 Z5r85 68.8368 Z5r86 67.3888 Z5r87 67.3168 Z5res 67. 1888 Z5r89 67.6588 25r18 68.7288 I NFI CT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8800 INRCT 8.8888 INRCT '8.8888 INRCT 8.8888 INFICT 8.8088 INRCT 8.8888 INRCT 8.8888 FIVG 69 '737 DEW CELLS RHD Zl 53.9729 RHD Z2 55.6652 RHD Z2 53.2837 RHD Z3 53.1268 RHD Z3 52.8968 RHD Z3 52.6781 RHD Z4 52. 7165 RHD 24 52.8191 RHD Z5 53.3863 RHD Z5 52.8575 INRCT 8.8888 INRCT G.GGGG INRCT 8. 8888 I NFICT e.eeee INRcT 8.8888 RVG 53 ~ 3378 RUB IENT PRESS 14.4488 VRPOR PRESSURE ~ 2813 DRY PRESSURE 55.6142 FLOWS 8.8888 RECORD NUNBER 153 DFITE 55 TINE 1745 PRESSURES 55e8188 55.8898 RVG 55.8135 RTD'S Zlrei 69.3688 Zir82 69.4948 Zl're3 69. 4948 Zir84 69. 3688 Z2rei 69.6388 Z2re2 69.5388 Z2r83 69. 6828 Z2r84 69. S128 Z2r85 69.7648 Z2r86 69.5668 22r87 69. 5488 Z3rei 69. 8188 Z3r82 69.8188 Z3re3 69.8188 Z3r84 69. 7468 Z3r85 69. 8540 Z3r86 78.8788 Z3r87 69.8548 Z3res 69. 8368 Z3r89 69. 8540 Z4rei 78.1780 Z4r82 69.9268 24r83 69. 9628 Z4r84 69.SS48 Z4r85 78',"1608 24r86 69.9888 24r87 69. 8888 Z4res 69.8360 Z4r89 78.8348 24rie 78.8788 Z5rei 67 8648

~ Z5r82 67.6220 25r83 67.6848 25r84 67.2988 Z5re5 68. GGGG Z5r86 67.4248 Z5r87 67.2988 ZSrGS 67.1888 Z5r89 67.6488 Z5rie 68.7388 I NFICT 8.8888 INRCT 8.8888 INRCT G. 8888 INRC,T G. 8088 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 I NFICT G. 8088 INRCT 8.8888 INRCT e.eeee RVG 69.2585 DEW CELLS RHD Zi 51.7558 RHD 22 53.9888 RHD 22 49.3863 RHD Z3 55.3319 RHD Z3 53. 1268 RHD Z3 53.8575 RHD Z4 52. 7165 RHD 24 53.2886 HD Z5 53. 5499 RHD Z5 52.6811 INRCT 8.8888 INRCT G.GGGG FICT 8. GGGG INRCT 8.8888 INRCT 8.8888 VG 52+9164 ROB IENT PRESS 14.4488

( VRPOR PRESSURE ~ 1982 DRY PRESSURE 55.6153 FLOWS 8.8888

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RECORD NUMBER - 154 DRTE - 55 TINE 1886 PRESSURES 55. 8156 55.8868 RVG 55. 8185 RTD'S Zlr81 69. 4648 Zlr82 69.5386 Zlr83 69. 4768 Zir84 69.3140 Z2r81 69. 6748 22r82 69.5128 22r83 69. 5128 Z2r84 69.5126 22r85 69.6926 Z2r86 69.5388 Z2r87 69. 5388 23r81 69.8600 Z3r82 69.8188 Z3r63 69.8186 Z3r64 69. 7468 Z3r85 69.8368 Z3r66 69.9266 Z3r87 69o8368 23r88 69.8868 Z3r89 69.8360 Z4r81 78. 1248 Z4r62 69. 9988 Z4r83 69.9268 Z4r84 69 '186 24r85 78.1688 24r86 69. 9628 24r87 69.8888 Z4r88 69 '366 Z4r89 78a8528 Z4rlG 76.8766 Z5r61 67 '466 25r82 67.6646 25r63 67.5868 ZSr84 67.2888 25r85 67.9648 Z5r86 '67.3886 Z5r87 67.2628 Z5r68 67.8828 Z5r89 67.6228 Z5rlG 68.7026 INRCT 8.8886 INRCT 8. 8888 INRCT 8.8888 I NFICT 6.0600 INRCT 8.8888 INRCT 8. 8686 INFICT 8'8888 INRCT 6.6666 I NFICT 8.8888 INRCT 8.8888 RVG 69.2382 DEW CELLS RHD Zl 53.4217 RHD 22 56. 6611 RHD 22 58.8784 RHD Z3 56. 3863 RHD 23 52.3575 RHD Z3 53.9858 RKD 24 52.6524 RHD Z4 52. 9345 RHD Z5 53.3966 RHD 25 52.9473 INRCT Be8668 INRCT G. 6666 I NFICT 8. 8886 I NFICT 8.8868 INRCT Ge8888 RVG 53.5311 RNBIENT PRESS 14.4488 VFIPOR PRESSURE .2827 DRY PRESSURE 55.6878 FLOWS 8.8888 ECORD NUMBER 155 DRTE - 55 TINE 1815 PRESSURES 55.8128 55.8838 RVG 55. 8675 RTD'S Zir61 69.3148 Zlr82 69.4848 Zlr83 69.4488 Zir64 69. 2666 22r81 69.6286 Z2r82 69.4768 Z2r83 69.5848 Z2r84 69. 5126 22r65 69. 6748 22r86 69.4768 Z2r87 69.4768 Z3r61 69. 7640 Z3r62 69.7826 Z3r83 69.7828 Z3r84 69.7468 Z3r85 69.7286 Z3r66 78.6346 23r87 69.8868 Z3r88 69.7648 Z3r69 69.8180 Z4r81 76.1668 Z4r82 69.8988 24r83 69.9688 Z4r84 69.7640 Z4r65 78.8526 Z4r86 69.9268 Z4r87 69.7646 Z4rGS 69.7S20 24r89 69.9988 Z4r18 78.8528 Z5r81 67.6186 Z5r82 67.5866 25r83 67.5686 25r84 67.2888 Z5r85 67.9466 Z5r86 67.3880 Z5r67 67.2626 25r88 67.8828 Z5r89 67.6648 Z5riG 68.7386 INRCT 8.6688 INRCT 8.8668 INRCT 8.8666 INFICT 6.6660 INRCT 8.6686 INFICT 8.8686 INRCT 8.6668 INFICT 6. 6666 INRCT 8.8688 INRCT 8.8888 FIVG 69.2891 DEW CELLS RHD 21 51. 8242 RHD 22 52. 7558 RHD Z2 54. 1989 RHD Z3 55. 0627 RHD 23 53. 1652 RKD Z3 52.2678 RHD Z4 54.8378 RHD Z4 52.6969 RHD Z5 53e2678 RHD 25 52.7678 INRCT 8.8886 INFICT 6.8860 ACT 6. 8866 INRCT 8.8888 INRCT Ge8888 VG 53 1182

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ROB IENT PRESS 14.4488 VRPOR PRESSURE . 1996 DRY PRESSURE 55.'6879 FLOWS 8.8888 8.8888

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RECORD NUMBER 156 DflTE - 55 TINE - ie38 PRESSURES 55>> 8898 55. 8818 . FIVG 55. e858 RTD'S 69>> 2968 Zlr82 69.4488 Zlr83 69.4228 2 ire4 69.27ee 69.4768 Z2r82 69>>4488 Z2r83 69.5848 Z2r84 69.4768 Z2r85 69.6928 Z2r86 69.4588 Z2r87 69.4?68 Z3rel 69. 7648 23r.82 69.7468 Z3r83 69.7468 Z3r84 69.746e Z3re5 69.7648 Z3r86 69.8988 Z3re7 69.7828 Z3ree 69.7648 Z3r89 69.eeee Z4rel 78. 1868 Z4r82 69.9888 Z4r83 69.8988 Z4r84 69.7648 Z4r85 69.9888 Z4r86 69.8988 24r87 69.7288 24ree 69.7e28 Z4r89 78. 8168 Z4r 1 8 78 '168 Z5rei 67.8188 Z5r82 67.56eo Z5r83 67.5688 Z5r84 67.2628 ZSr85 67.9468 Z5r86 67 '528 Z5r87 67.2448 25ree 67.8648 Z5r89 67.6848 Z5/18 6e.7828 INflCT 8.8888 INflCT 8>>8888 INflCT 8.8888 INRCT 8.8088 IttflCT 8.8888 INRCT 8.8888 INflCT 8.8888 INRCT 8.8008 INflCT 8.8888 INRCT 8.8888 FIVG 69.1982 DEW CELLS RHD Zi 58.8242 RHD Z2 58.8968 RHD Z2 53.8968 RHD Z3 53.e575 RHD Z3 53>> 3191 RHD Z3 49.9729 RHD Z4 53.4473 RHD Z4 53.4681 RHD 25 53>>3?84 RHD Z5 52.985e INFICT 8.8888 INFICT 8.8880 INRCT 8. 8888 INflCT 8 ~ 8888 INRCT 8.8888 RYG 52. 5344 flNBI Et<T PRESS 14.4488 VflPOR PRESSURE .1954 DRV PRESSURE 55.6896 FLOWS e.eeee

( RECORD NUNBER - 157 DFITE 55 TINE 1845 PRESSURES 55.8878 55.?978 RVG 55.e828 RTD~S Zlrel 69. 2688 Z lr82 69. 4488 Z ir83 69. 3868 2lr84 69. 2248 Z2rel 69.5388 22r82 69.3868 Z2r83 69.5388 22r84 69.4228 Z2r85 69.6828 Z2r86 69.3e68 Z2r87 69.4588 Z3rei 69.7188 Z3r82 69.7468 Z3r83 69.7468 Z3r84 69.6568 Z3r85 69.7460 23re6 69.8368 23r87 69.7648 Z3r8e 69.72ee Z3r89 69.7648 Z4rei 78.8788 Z4r82 69.e988 Z4re3 69.e548 Z4r84 69.7828 Z4r85 78.8528 Z4r86 69.e988 Z4r87 69.692e Z4ree 69.7460 24r89 78.8348 Z4rie 69.99ee Z5rel 66.9928 ZSr82 67.5588 25re3 67.5328 25r84 67,2448 Z5r85 67.9468 Z5r86 67>>3348 Z5r87 67.2628 Z5ree 6?.8648 Z5r89 67.5868 Z5rie 68.7828 I t<ACT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8800 I NFIC7 8.8888 INRCT 8.8888 INFICT 8.8888 INflCT 8.8808 INflCT 8.8888 INRCT 8.8888 flYG 69 ~ 1654 DEW CELLS RHD Zi 58.5755 RHD 22 51. 2934 RHD Z2 53.9986 RHD Z3 52. 4729 RHD Z3 51 ~ 9858 RHD Z3 52 8114

~ RHD 24 54.8883 RHD Z4 53.767e HD Z5 53.3968 RHD Z5 52.7678 INflCT &.8888 INRCT 8.8888 NRCT 8. 8888 I NRCT 8 ~ 8888 INRCT 8.8888 RVG 52. 6445 RNBIENT PRESS 14.4488 VRPOR PRESSURE .1962 DRY PRESSURE 55.6e5s FLOWS 8>>8888 8>>8888

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RECORD NUMBER 158 DFITE 55 TINE - 1988 PRESSURES 55. 8848 55.7958 AVG 55. 7995 RTD'S Zirel 69.2688 Zir82 69. 4488 Zir83 69. 3868 Zir84 69. 2868 Z2rel 69 '848 22r82 69.3868 Z2r83 69.4228 Z2r84 69 4228

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Z2r85 69.6828 Z2r86 69.4848 22r87 69.4488 Z3rel 69 '1GG 23r82 69. 7188 Z3r83 69.7188 Z3r84 69.6568 Z3r85 69.7180 Z3r86 78. 8348 Z3r87 69. 7468 Z3r88 69.7188 Z3r89 69.7460 Z4rei 78. 8528 Z4r82 69. 8368 Z4r83 69.8368 Z4r84 69. 7468 Z4r85 78. 8168 Z4r86 69. 8548 24r87 69.6928 Z4r88 69. 7180 Z4r89 69. 9628 Z4rle 69. 9448 25rei 66.9748 Z5r82 6?o5320 Z5r83 67. 5328 Z5r84 67. 2448 Z5r85 67.9288 25r86 67.3168 Z5r87 67.2268 Z5ree 67. 8468 Z5r89 67 '868 Z5rie 68.7828 INACT 8.8888 INACT 8.8888 I NFI CT 8. 8888 INACT 8.8800 INACT 8.8888 INACT 8.8888 INACT e. eeee INACT G.GGGG INACT 8.8888 INACT 8.8888 FIVG 69. 1548 DEW CELLS RHD Zl 53.8883 RHD Z2 56.8784 RHD Z2 53.4888 RHD 23 50.2934 RHD 23 52.3832 RHD Z3 51. 4217 RHD Z4 53.8242 RHD 24 53.4217 RHD Z5 53. 1781 RHD 25 52o6524 INACT 8.8888 INACT 8.8008 INACT 8 8888 F INACT 8.8888 INACT 8.8888 FIVG 53. 8129 flt'1B I ENT PRESS 14.4488 VAPOR PRESSURE .1989 DRY PRESSURE 55.6886 FLOWS 8.8888 RECORD NUNBER - 159 DFITE 55 TINE 1915 PRESSURES 55. 8818 55. 7928 AVG 55. 7965 RTD'S Zlrei 69. 2868 Zlr82 69.4228 Zir83 69. 3588 Zir84 69. 1160 Z2rel 69.5668 Z2r82 69.3868 Z2r83 69. 4768 Z2r84 69. 4228 Z2r85 69.5668 Z2r86 69.3868 Z2r87 69. 4228 Z3rei 69. 6748 Z3r82 69.6748 Z3r83 69.6568 Z3r84 69.6568 Z3r85 69. 7288 23r86 "

69.9448 Z3r87 69.7188 23r88 69.6748 Z3r89 69. 7100 Z4rel 78.8348 Z4r82 69.7648 Z4r83 69.S188 Zare4 69. 7288 Z4r85 69,9628 Z4r86 69.8368 Z4r87 69.6748 Zaree 69.6740 24r89 69.9888 Z4rle 69.9268 25rei 66.9568 Z5r82 67.5320 Z5r83 67.5148 Z5r84 6?.2888 25r85 67.8928 25r86 67.3168 Z5r87 6?.2268 Z5r88 67.8288 Z5r89 67.5688 25rie 68. 6848 INACT 8;0008 INFICT 8.8888 INFICT 8.8888 I NFICT G. GGGG INFICT 8 ~ GGGG INFICT 8.8888 INACT G.GGGG INACT G. GOGO INACT 8.8888 INACT G.eeee FIVG 69.1295 DEW RHD Zl RHD Z3 RHD Z5 NACT

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CELLS

53. 1524 53.3575 8.

RHD Z2 1148 RKD Z3 RHD Z5 8888 I NFICT 54.4986 RHD Z2 52.9217 RHD Z4 52.8784 INACT 8.8888 INACT 51.2422

53. 1652 e.eeee RHD Z3 RHD Z4 8..8888 INACT 52 4473

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. AVG 53. 8158 ANB IENT PRESS 14. 4488 VFIPOR PRESSURE ~ 1989 DRY PRESSURE 55.5976 FLOWS 8.8888 e.eeee

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RECORD ttUI'1BER - 166 DATE - 55 T I NE - 1938 PRESSURES 55.?998 55.7988 RYG 55.7945 RTD'S Zlr61 69. 2428 21r92 69.3568 Zir83 69. 3328 Z1r84 69.6980 Z2r81 69.6288 Z2r82 69.3588 Z2r83 69.4488 Z2r84 69.4226 Z2r85 69. 6299 Z2r86 69,3328 Z2r87 69.3588 Z3r81 69.6746 Z3r82 69.6928 Z3r83 69.6568 Z3r84 69.6288 23r85 69.6386 Z3r66 78. 8168 23r87 69.7188 Z3r88 69.6748 Z3r89 69.7106 24r81 69.9888 24r82 69.8888 Z4r83 69.8888 Z4r84 69.7466 Z4r85 69.9986 24r86 69.8188 Z4r87 69.6568 Z4r88 69.6569 Z4r69 69.9269 Z4r19 69.9269 25r81 66.9388 25r82 67.5146 Z5r63 67.4968 Z5r84 67.2888 Z5r95 67.8748 ZSr86 67.2866 25r97 67.2688 Z5r88 67. 8288 Z5r89 67.5588 'Z5r18 68.7926 I NFICT 8.8669 INFICT 8.8888 INRCT 8.8888 INRCT 6.9606 It)RCT 8.8888 INFICT 8.8888 INACT 8.8888 INFICT 6.8660 IttRCT 8.8988 INRCT Go8888 AVG 69 '288 DEW CELLS RHD 21 51. 7678 RHD Z2 55.4986 RHD Z2 54.6652 RHD Z3 52.1268 RHD Z3 52e8968 RHD Z3 54.7165 RHD Z4 54.5114 RHD Z4 52.9688 RHD 25 53.2165 RHD 25 52.6268 iINRCT 8.8889 INRCT 9.6669 I NFICT 8. 9698 INACT 8.8888 INFICT 6.8688 RYG 53.4852 RNBIENT PRESS 14. 4488 YFIPOR PRESSURE .2824 DRY PRESSURE 55.5921 FLOWS 8.8888 ECORD NUI'1BER - 161 DRTE 55 TINE - 1945 PRESSURES 55; 7978 55. 7878 FIVG 55'?928 RTD'S Zlr61 69.1888 Zlr82 69.3688 2ir83 69. 3149 Z 1r84 69.1526 Z2r91 69.4768 Z2r82 69.2968 Z2r83 69.4848 Z2r84 69.3566 Z2r95 69.5306 Z2r86 69.2968 Z2r67 69.3586 Z3r81 69.6386 Z3r62 69.6569 23r83 69.6568 Z3r84 69.6828 Z3r65 69.6200 Z3r66 79 '526 Z3r87 69. 7198 23r98 69.6566 Z3r69 69. 6746 Z4r91 69.9986 24r82 69.7288 24r93 69.8688 Z4r94 69. 6926 Z4r95 76.9160 24r86 69.7828 Z4r87 69.6286 Z4r98 e9.6 eo 24r99 69.8969 Z4r18 69.8968 Z5r61 66.9388 Z5r82 67.5146 Z5r63 67.4966 ZSr94 67. 1968 Z5r95 6?o 8748 'Z5r86 67.2986 Z5r87 67.2986 Z5r68 67.8169 25r89 67.5588 Z5rlG 68.6846 I NFICT 8.6096 INACT 8.8988 INRCT 8.8968 INRCT 6.9606 I t<RCT 8~ 8966 It<ACT 8.8688 INFICT 9.6899 INRCT 8.9696 INRCT 8.8698 INRCT 8.8888 RYG 69. 8991 DEW CELLS RHD Zl 58. 1396 RHD Z2 52. 3191 RHD Z2 52. 1989 RHD 23 53.2559 RHD Z3 54.5883 RHD Z3 53.?886 RHD Z4 55.7678 RHD 24 52 8319 RHD Z5 53.2934 RHD Z5 52.7558 INRCT 8.8988 INRCT 8.6909 RCT 8. 8686 INRCT 8.8888 INFICT 8.6888 VG 53.6556 FINB IENT. PRESS 14.4489

( VRPOR PRESSURE .1992 DRY PRESSURE 55.5928 FLOWS 8. 8888

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RECORD NUMBER - 162 DATE - 55 TINE - 2888 PRESSURES 55.7946 55 7858 RVG 55.7895 RTD'S 21rel 69. 1526 2 ir82 69.3326 Zir63 69.2966 Zir84 69.6860 22re1 69.4488 Z2r82 69.2968 22r83 69.4768 Z2r84 69.3326 Z2r85 69.5486 Z2r86 69.3326 Z2r87 69.3588 23rei 69.6386 Z3r82 69.6388 Z3r83 69.6288 Z3r84 69.5846 Z3r85 69.6620 Z3r86 69.9888 23r67 69.6568 Z3r88 69.6288 Z3r89 69.6380 Z4rel 69.9886 24r82 69.7468 Z4r83 69.7648 Z4r84 69.6566 Z4r85 78,8348 Z4re6 69.8868 24r67 69,6626 Z4r88 69.6386 Z4r89 69.8728 24rle 69.8728 Z5rei 66.9388 25r82 67.4786 25r83 67.4788 Z5r64 67. 1986 Z5r85 67.8748 25r66 67>2266 Z5r87 67. 1966 25r88 67.8188 Z5r69 67.5328 25rle 68.7206 INRCT B. 8668 I NRCT 8.8888 IHRCT 8.8886 INRCT 8.8666 IHRCT 8. 6866 I NRCT 8.8868 INRCT 8.8888 INRCT 6.6666 I NRCT 8 ~ 8886 IHRCT 8.8888 RVG 69. 8811 DEW CELLS RHD Zi 52.6524 RHD Z2 52.7934 RHD Z2 52.8?84 RHD Z3 51. 9345 RHD Z3 52.4681 RHD Z3 48.4345 RHD Z4 53. 3191 RHD 24 52.6909 RHD 25 53.8242 RHD Z5 52.6148 INRCT 8. 8888 I HFICT 8.8666 INRCT 8.8888 I HRCT 8.8888 IHRCT 8. 8888 AVG 52.3183 FINBIEHT PRESS 14.4488 VRPOR PRESSURE ~ 1938 DRY PRESSURE 55.5957 Fl OWS 8.8888 ECORD NUt1BER - 163 DRTE - 55 TINE - 2815 PRESSURES 55. 7928 55.7838 RYG 55. 7875 RTD'S Zlrei 69.1168 Zir82 69.2788 Zlr83 69.2426 Zir84 69 6446

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22rel 69.4228 Z2r82 69.2688 Z2r83 69.3566 Z2r64 69. 3326 Z2re5 69.4468 Z2r86 69.2788 Z2r87 69.2966 Z3rel 69. 6020 Z3r62 69.6828 Z3r63 69e5848 Z3r64 69.5666 Z3r65 69. 6206 23r66 78.8528 Z3r87 69.6388 23r68 69,6626 Z3r89 69. 6386 Z4rel 69.9446 Z4r82 69.7466 24r83 69.7466 Z4r64 69. 6386 Z4rGS 78.6786 24r66 69.8688 Z4r87 69.6626 Z4r88 69. 6266 Z4r89 69.8366 Z4rie 69.8368 Z5rei 66.9386 Z5r82 67. 4780 25r63 67.4786 Z5r64 67. 1728 Z5r65 67.8S66 Z5r66 67. 2626 25r87 67. 1546 ZSr88 66.9746 25r89 67.5326 Z5rie 68. 6126 IHRCT 8.6668 IHACT Be8888 INFICT 8.6066 IHRCT G. 6606 I NFICT 8.8660 INRCT 8.8868 IHRCT 8.6666 INRCT 6. 6066 IHRCT 8.8868 IHRCT e.eeee RVG 69.8585 DEW CELLS RHD Zl 54. 1811 RHD Z2 53.3575 RHD Z2 53.2886 RHD Z3 5S. 6114 RHD Z3 54. 9661 PHD 23 56. 1781 RHD 24 51 ~ 3968 RHD Z4 52.8784 D Z5 S3.3863 RHD 25 52. 6969 INFICT 6.6868 INRCT 6.8060 CT e.eeoc INACT 8. 8688 I HFICT eo 8686 G 53m 6745 RIIB I EHT PRESS 14. 4486 VAPOR PRESSURE .2838 DRY PRESSURE 55.5837 FLOWS Ge8868

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RECORD NUNBER - 164 DATE 55 TINE 2838 t

PRESSURES 55.7988 55.7818 55.7855 RTD'S Zlrel 69. 8988 Z 1 r82 69'788 Zlr83 69.2788 Zir84 69 8930

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22re1 69.4488 Z2re2 69.2688 22r83 69.3868 Z2r84 69 2788 Z2re5 69.4488 Z2r86 69. 2788 22r87 69.2968 Z3rei 69.5300 23r82 69 '828 Z3r83 69.5668 Z3r84 69.5388 Z3r85 69. 5S46 Z3r86 69.9988 Z3r87 69.6388 Z3r88 69.6828 Z3r89 69. 6820 24rel 69.9268 Z4r82 69,6928 Z4r83 69.?188 24r84 69. 6388 Z4r85 69.8728 Z4r86 69.7288 Z4r87 69.5488 Z4r88 69. 6828 Z4r89 69.8368 Z4rle 69.8548 Z5rel 66.9828 25r82 67.4688 Z5r83 67.4428 Z5r84 67. 1548 Z5r85 67. 8568 Z5r86 67.2440 25re? 67. 1548 Z5r88 66.9748 Z5re9 67.4968 Z5rle 68. 7820 INACT 8,8888 INACT 8.8888 INACT 8.8888 INACT 8. 8888 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8888 AYG 69.8427 DEW CELLS RHD Zl 54.4858 RHD Z2 53.8832 RHD Z2 52.3575 RHD 23 51.9681 RHD Z3 51. 6396 RHD 23 51. 2886 RHD Z4 52.7886 RHD Z4 52.3784 RHD 25 53.3968 RHD Z5 52.4858 INACT 8.8888 INACT 8.8808 INACT 8.8888 INACT 8.8888 INACT 8.8888 AVG 52.6977 ANB IENT PRESS 14 ~ 4488 VAPOR PRESSURE ~ 1966 DRY PRESSURE 55.5889 Fl OWS 8.8888 ECORD NUMBER - 165 DATE - 55 TINE 2845 PRESSURES 55.78?8 55'825 RTD'S Zlre1 69.1348 Zir82 69.2428 Zir83 69. 2868 Zlr84 69. 0448 Z2rel 69.4848 Z2re2 69.2428 Z2r83 69.2968 Z2r84 69. 2600 Z2r85 69.4848 Z2re6 69.2788 Z2r87 69.2688 Z3rel 69.5128 Z3r82 69.5848 Z3r83 69.5388 Z3re4 69.4948 Z3r85 69.5300 Z3r86 69.7648 Z3r87 69.6288 Z3r88 69.5488 Z3re9 69.6820 Z4rei 69.8988 Z4r82 69.6928 Z4re3 69.6928 Z4r84 69.6288 z4re5 69.9268 Z4r86 69.7188 24r87 69.5488 Z4r88 69.5S48 24r89 69.8888 Z4rie 69. 8188 25re 1 66.9828 Z5r82 67.4688 Z5re3 67.4428 ZSr84 67. 1548 Z5r85 67.8288 25r86 67.2620 Z5r87 67. 1548 Z5re8 66.9568 Z5re9 6?.4960 ZSrle 68.6488 INACT 8. 8888 I NFlCT 8.8888 INACT 8.8888 INACT 8.8808 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8,8000 INACT eeeeee INACT e.eeee AYG 69.8139 DEW CELLS RHD 21 53.8319 RHD Z2 54.9681 RMD 22 52.,2165 RHD Z3 53.8242 RHD 23 53.9681 RHD Z3 49.6652 RHD Z4 52. 4217 RHD 24 52.4345 D Z5 53.8755 RHD Z5 52.5378 INACT 8.8888 INACT 8.8808 CT 8.8888 INACT 8.8888 INACT 8.8888 G '2o8338 AMBIENT PRESS 14. 4488 YAPOR PRESSURE .19?5 DRY PRESSURE 55.5858 FLOWS eoeeee

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RECORD NUNBER - 166 DRTE - 55 TINE 2188 PRESSURES 55m 7858 55. 7768 flVG 55. 7885 RTD'S Zirel 69.8448 Zlr82 69e2428 Zlr83 69.2248 Zir84 69.0808 Z2rel 69.4848 Z2r82 69.2428 Z2r83 69.3868 Z2r84 69.2688 Z2r85 69.4228 Z2r86 69.2788 Z2r87 69.2788 Z3rei 69.5388 Z3r82 69.5488 Z3r83 69.5488 23r84 69.4948 Z3r85 69.5388 Z3r86 69.7468 Z3re? 69.6828 Z3r88 69.5128 Z3r89 69o5668 Z4rel 69.9888 24r82 69.6928 Z4r83 69.6748 24r84 69.6828 Z4re5 69.8?28 Z4r86 69.6928 Z4r87 69.5128 Z4reS 69.54ee Z4r89 69.7828 Z4rle 69.8368 Z5rel 66.8848 Z5r82 67.4428 25r83 67.4248 Z5r84 67. 1368 Z5r85 67.8568 Z5r86 67.1900 Z5re7 67. 1368 Z5r88 66.9568 Z5r89 67.4968 25r 18 68.7820 INRCT 8. 8888 INRCT Boeeee INflCT 8.8888 INRCT B.BGGG INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8808 INRCT 8.8888 INflCT 8.8888 flVG 69.8886 DEW CELLS RHD Zl 49.7558 RHD 22 49.8627 RHD Z2 49.2422 RHD Z3 52.1140 RHD Z3 53. 3191 RHD 23 54.4858 RHD Z4 52.8832 RHD Z4 53.1148 RHD Z5 53. 3319 RHD ZS 52.4473 INflCT 8.8888 INRCT G.GGGG INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 flVG 51. 9512 fi'1D I ENT PRESS 14 '488 VFIPOR PRESSURE ol912 DRY PRESSURE 55.5893 FLOWS 8.8888 8F 8888

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RECORD NUNBER 167 DRTE 55, TINE 2115 PRESSURES 55.7838 55.7748 flVG 55.7785 RTD'S Zlrel 69.8448 Zlr82 69. 1888 Zlr83 69.1888 Zir84 68'988 Z2rel 69.3328 Z2r82 69. 1788 22r83 69.3328 22r84 69. 2248 Z2r85 69o4768 22r86 69. 2868 Z2re7 69.2688 Z3rel 69. 5128 Z3r82 69.5488 23r83 69. 5128 Z3r84 69e4768 Z3r85 69. 5308 Z3r86 69.7468 23r87 69.5668 Z3r88 69.5488 23r89 69.6288 24rei 69.8548 Z4r82 69.6288 Z4r83 69.6928 24r84 69 '668 Z4r85 69.8988 24r86 69.6748 Z4r87 69.5128 Z4r88 69.5660 Z4r89 69. 8188 Z4r 18 69.7648 Z5rei 66.8668 ZSre2 67.4428 Z5r83 67.4248 Z5r84 67. 1188 25r85 67.8828 Z5r86 67.1900 25r87 67.1188 Z5r88 66.9388 Z5r89 67.4788 ZSrie 68.5948 INRCT Goeeee INflCT 8~ 8888 INRCT 8.8888 I NFlCT 8.8880 INRCT 8.8888 INFlCT 8+8888 INRCT 8.8888 INRCT 8.8800 INflCT 8+8888 INRCT 8.8888 flvc 68.9868 DEW CELLS RHD Zi 52. 5114 RHD 22 49.7934 RHD Z2 52.9345 RHD Z3 51 o 7558 RHD 23 51. 3863 RHD Z3 52.6652 RHD 24 52.5499 RHD Z4 53. 3784 PHD 25 53.2558 RHD Z5 52.6811 INRCT 8 8888 INflCT G. GGGG FICT 8.8888 INRCT 8.8888 INflCT 8.8888 flVG 52. 2983 flNBIENT PRESS 14 ~ 4488 VflPOR PRESSURE ~ 1936 DRY PRESSURE 55.5849 FI OWS 8. 8888

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RECORD NUMBER 168 DATE - 55 TINE - 2138 PRESSURES 55. 7818 55.7728 RVG S5.7765 RTD'S Zir81 69. 8628 Z1r82 69.2248 Zlr83 69.2868 Zlr84 69. 8448 Z2r81 69.2788 22r82 69.1788 Z2r83 69. 3688 Z2r84 69. 2240 22r85 69.4848 22r86 69.2868 Z2r87 69 ~ 2248 Z3r81 69. 5120 23r82 69.5388 Z3r83 69.5128 Z3r84 69. 4588 Z3r85 69.4768 Z3r86 69. 7828 Z3r87 69.5668 Z3r88 69. 5128 Z3r89 69.5668 Z4r81 69.8548 24r82 69.6388 Z4r83 69.6388 Z4r84 69.S840 Z4r85 69.8188 Z4r86 69.6748 Z4rB? 69.4948 Z4r88 69.5388 Z4r89 69.8888 Z4riG 69.7648 ZSr81 66.8848 ZSr82 67.4248 25r83 67.4868 Z5r84 67.1888 25r85 67.8288 ZSr86 67. 1908 Z5r87 67.1188 Z5r88 66.9288 25r89 67.4688 Z5r1 8 68. 5768 IHRCT 8.8888 IHFICT 8.8888 IHRCT 8. 8888 INRCT 8.8800 INRCT 8.8888 IHRCT 8.8888 INRCT e. 8888 INRCT 8.8008 IHRCT 8.8888 IHRCT 8.8888 RVG 68. 9772 DEW CELLS RHD Z 1 51. 4858 RHD Z2 53.8319 RHD Z2 53.9345 RHD Z3 54. 9217 RHD Z3 51. 2934 RHD Z3 51. 2837 RHD Z4 52e5114 RHD 24 53. 8968 RHD Z5 53.2293 RHD 25 52.6396 IHRCT 8.8880 IHRCT 8.8008 INRCT 8.8888 INRCT 8.8888 INRCT 8. 8888 RVG 52.9854 FIC'IB I ENT PRESS 14.4488 VAPOR PRESSURE .1981 DRY PRESSURE 55.5784 FLOWS 8.8888 5

( RECORD NUNBER 169 DATE - 55 TINE - 2145 PRESSURES 55.7798 55.7788 RVG 55. 7745 RTD'S Zir81 69. 8448 2 lr82 69.2428 Zir83 69.1348 Zir84 68. 9368 Z2r81 69.3688 Z2r82 69.1?88 22r83 69.2688 Z2r84 69. 1520 Z2r85 69.4848 Z2r86 69. 1788 Z2r87 69.2868 23r81 69.4940 23r82 69.4948 Z3r83 69.4768 23r84 69o4768 23r85 69.5668 Z3r86 69.5848 Z3r87 69.5488 23r88 69.5128 Z3r89 69.5480 24r81 69.8548 Z4r82 69.6388 Z4r83 69.6288 24r84 69.5660 Z4r85 69.8368 Z4r86 69.6748 24r87 69.4948 Z4r88 69.5128 Z4r89 69.7648 Z4rlG 69. 7188 25r81 66.8668 25r82 67.4240 Z5r83 67.3888 ZSr84 67.1888 25r85 67.8288 Z5r86 67.1548 25r87 67. 1888 Z5r88 66.9828 Z5r89 67.4428 Z5r18 68.5488 IHACT 8. 8888 INRCT 8.8888 INRCT 8.0888 I HFICT G.GGGG I NFICT 8. 8888 INRCT 8.8888 INRCT G.GGGG INRCT 8.8888 INRCT, 8. 8888 INRCT Bo8888 FIVG 68. 9557 DEW CELLS RHD Zl 52.8627 RHD Z2 54.2837 RHD Z2 49. 8499 RHD 53 5627

~

RHD Z3 54.7558 RHD 23 51. 6989 RKD 24 RHD Z4 23'2e9345 5>.8863 HD Z5 53.8242 RHD Z5 52.5499 INRCT 8 8888 INRCT G.GOGO RCT 8.8888 IHRCT 8.8888 INRCT 8.8888

, VG 52. 6466 RNBIENT PRESS 14 4488 VAPOR PRESSURE .1962 DRY PRESSURE 55.5783 FLOWS 8.8888

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RECORD NUI)BER - 178 DFITE - 55 TINE - 2288 PRESSURES 55.7778 Sso7688 RVG - '5.7725 RTD'S Zir81 69.8088 Zir82 69+ 1888 Zir83 69. >>68 Zir84 68. 9368 Z2r01 69.3328 Z2r82 69.1888 22r83 69. 2688 Z2r84 69. 1788 Z2r85 69.3588 Z2r86 69 '528 Z2r87 69. 1888 23r81 69.4768 23r82 69.4948 23r83 69.4588 Z3r84 69. 4488 23r85 69. 4480 Z3r86 69.?188 Z3r87 69.5388 Z3r88 69. 5128 Z3r89 69.5668 Z4r81 69 ~ 8188 24r02 69.6828 24r83 69. 6288 Z4r84 69.5488 Z4r85 69.7828 Z4r86 69.6568 Z4r87 69. 4588 24r88 69.4948 Z4r89 69.7288 Z4r18 69.7188 Z5r81 66. 8488 Z5r82 67.3888 25r83 67.3888 Z5r84 67.8828 Z5r85 67. 7668 Zsr86 6?.1728 Zsr87 6?o8828 Z5r88 66.9828 25r89 67.4248 Z5riB 68.6488 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8. 8888 INRCT 8.8888 INRCT 8.8888 INRCT 8. 8888 RVG 68.9426 DEW CELLS RHD Zl 54.8499 RHD Z2 54.8784 RHD Z2 54. 5114 RHD Z3 52.6148 RHD Z3 52+6989 RHD Z3 51. 8832 RHD 24 53. 1652 RHD Z4 53.1781 RHD 25 53.2293 RHD Zs 52. 4217 INRCT 8.8888 INRCT 8.8088 I NFICT 8.8888 INFICT 8+ 8888 INRCT 8.8888 RVG 53+2736 RNBIENT PRESS 14.4488 VRPOP. PRESSURE .2888 DRY PRESSURE ss.srir FLOWS 8.8888 RECORD NUMBER - 171 DRTE - 55 TINE 2215 PRESSURES 55. 7768 55.7668 RVG 55.7718 RTD'S Zlr81 69.8888 Zlr82 69. 1788 21r83 69.1168 2ir84 68. 9888 Z2r81 69.3328 Z2r82 69.1528 22r83 69.2788 Z2r84 69.1788 Z2r85 69.3588 Z2r86 69.1528 22r87 69. 1788 Z3r81 69. 4588 23r82 69.4488 Z3r83 69.4588 Z3r84 69.4848 Z3r85 69. 5308 Z3r86 69.7288 Z3r87 69. 5128 23r88 69.4768 23r89 69. 5308 Z4r81 69. 8188 Z4r82 69.6288 Z4r83 69.5668 Z4r84 69.5128 24r85 69.8188 Z4r86 69.6388 Z4r87 69.4S88 Z4r88 69.4948 24r89 69.7288 Z4r18 69.7288 Z5r81 66.8388 Zsr82 67.3888 Z5r83 67.3?88 Zsr84 6?e8648 Zsr85 67.7848 25r86 67.1188 Z5r87 67.8828 25r88 66.9828 Z5r89 67.4248 Z5rlB 68 '488 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 I NFIC7 8.8808 I NFICT 8.8888 INRCT 8.8888 INFICT 8.8888 INRCT 8.0080 INACT 8.8888 INRCT 8.8888 Fl VG 68.9322 DEW CELLS RHD Zl 52.8784 RHD Z2 53.9681 RHD 22 55.5114 RHD Z3 53. 0627 RHD Z3 58 '986 RHD Z3 58.5883 RHD Z4 52.4888 RHD Z4 53.7293 RHD Z5 53+8378 RHD 25 52.6268 INFICT 8.8888 INRCT 8,8808 NRCT 8.8888 INRCT Be8888 INRCT 8.8888 AVG '52.8655 AMBIENT PRESS 14 '488 VFIPOR PRESSURE .1978 DRY PRESSURE 55.5732 FLOWS 8.8888 Bo8888

1 1

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RECORD NUNBER ,172 DFITE ' 55 TINE - 2238 PRESSURES 55. 7738 55.7638 RVG 55. 7686 v'irol RTD'S Z2rol

68. 9546 Zlr62 69.2788 Z2r82

69. 1888 69.8888 Zlr83 Z2r83

69. 8628 69.2968 Zir84 Z2r84 68.9606 69.1526 Z2roS 69.3686 Z2r86 69. 1348 Z2r87 69.1528 Z3rol 69.4586 Z3r92 69.4588 Z3ro3 69.4488 Z3r84 69.3868 Z3r85 69.3866 Z3r86- 69.6746 Z3r87 69.4948 Z3r88 69.4488 Z3r89 69. 5360 24roi 69.8188 Z4r82 69.6828 Z4r83 69.6288 Z4r84 69. 4946 Z4r85 69.7288 Z4r86 69.6828 24re? 69.4848 Z4r88 69. 3869 Z4r89 69.6748 Z4rlo 69.6928 Z5roi 66.8128 ZSr82 67. 3796 ZSr83 67.3528 ZSr84 67.8468 25r85 67.7848 25r86 67. 1186 25ro? 67.8648 25r88 66.9628 25r89 67.4868 Z5rio 68. 5460 I NFICT 8.8888 INRCT 8.8668 INRCT 8.8888 I NFI CT 8. 9606 I NFICT 8.8888 INFICT 8.8868 INRCT 8.8888 INRCT e. eo06 INRCT 8.8888 INRCT B.eeee RVG 68'881 DEW CELLS RHD Zl 51. 8242 RHD 22 51.4681 RHD Z2 52 '447 RHD Z3 53.8832, RHD 23 52.4858 RHD ZS 51.7934 RHD Z4 52.8447 RHD Z4 52.7678 RHD 25 53.2678 RHD 25 52.5378 INRCT 8.8666 INRCT 8.8999 I NFICT 8. 8868 INRCT 8.8888 INFICT 8.8968 RVG 52.4424 RthB I ENT PRESS 14.4468 VRPOR PRESSURE ~ 1947 DRY PRESSURE 55.5733 FLOWS 8.8888 RECORD NUHBER 173 DATE 55 TINE 2245 PRESSURES 55.?718 55+7628 RVG 55.7665 RTD'S Zlrol 68. 9998 Zir82 69. 1528 ZireS 69.8988 Zir84 68. 8469 22roi 69.2788 Z2r82 69. 1168 22reS 69.1788 22r84 69 1166

~

22r95 69.3689 Z2r86 69.1168 22r87 69.1528 ZSrei 69.4466 23r02 69.4228 Z3r83 69.4228 Z3r84 69.3869 ZSr65 69.4766 ZSr86 69. 5849 Z3r87 69.4768 Z3r88 69.4946 Z3r89 69.4586 Z4rei 69.7648 Z4r82 69.5666 Z4r63 69.5489 Z4r64 69.4406 Z4r85 69.8366 Z4r66 69. 6388 24r87 69.4466 Z4r68 69.4586 Z4r89 69.6926 Z4r 1 8 69.6568 25rol 66.8386 Z5r62 67.3760 Z5r83 6?.3528 25r84 67.8468 25r85 67.7386 25r66 67.1660 Z5r87 67.8468 Z5r88 66.8488 Z5r89 67.4668 ZSriO 68.5646 INRCT 8. 6998 INRCT 8.6888 INFICT 8.8686 INRCT o.eooe INRCT 8. 8868 INRCT 8.8888 INRCT 6.8888 INRCT 6 ~ 6669 INRCT . 8. 8666 INRCT 8.8888 RVG 68. 8948 DEW CELLS RHD Zi 54.9729 RHD Z2 54.5499.RHD Z2 56. 3191 RHD Z3 52. 2937 RHD 23 53. 9217 RHD Z3 52.8319 RHD Z4 53.6781 RHD Z4 52.9729 WKD Z5 53. 1781 RHD ZS 52.4688 INRCT eaooee INRCT 8. 8906 FICT 8. 8888 INRCT 8.8888 INRCT 8.8888 VG 53. 8915 Rt1B I ENT PRESS 14. 4488 VRPOR PRESSURE- .1995 DRY PRESSURE 55.5678 FLOWS 8.8888

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RECORD NUI1BER - 174 DATE - 55 T INE - 2388 PRESSURES 5S. 7698 55.7598 AVG 55e7648 R TD'S Zir81 68. 9548 lr82 69.8888 Zir83 69. 8448 2 ir84 68. 8828 Z2r81 69. 1788 Z2r82 69.8448 Z2r83 69. 1788 Z2r84 69. 1348 Z2r 85 69. 3148 Z2r86 69.8888 22r87 69.8988 Z3r81 69.4040 Z3r82 69.4228 23r83 69o3868 23r84 69.3588 23r85 69.3868 Z3r86 69.7188 Z3r87 69;4588 Z3r88 69.4848 Z3r89 69.47&8 24r81 , 69.7468 Z4r82 69.5388 Z4r83 69.6288 Z4r84 69.47&8 Z4r85 69.8888 Z4r86 69.5668 Z4r87 69.3868 24r88 69.4848 Z4r89 69.6388 Z4riG 69.6568 -Z5r81 66.7768 Z5r82 67.3528 Z5r83 67.3348 Z5r84 &7.8288 Z5r85 67.7388 Z5r86 67.8640 Z5r87 67.8288 Z5r88 66.8668 25r89 67.3788 Z5r18 68.4868 INRCT 8.8888 INRCT 8.8808 INFICT 8.8888 INRCT 8.8088 INRCT 8 F 8888 INRCT 8.8088 INRCT Gs8888 'INFICT 8.8808 INRCT 8.8888 INRCT 8.8888 RVG 68e8711 DEW CELLS RHD 21 51. 6989 RHD 22 53.7886 RHD 22 53.6268 RHD Z3 52.1811 RHD Z3 52.2678 RHD Z3 S4.4217 RHD Z4 54.8242 RHD 24 52.1268 RHD Z5 53.8114 RHD 25 52.4858 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INFICT 8.8888 RVG 52. 9495 FINBIENT PRESS 14.4488 VAPOR PRESSURE .1984 DRY PRESSURE 55.5656 FLOWS 8.8888 8.8888 ECORD NUNBER 175 DRTE 55 TINE - 2315 PRESSURES 55..7678 55.7588 RVG 55.7625 RTD'S Zlr81 68.9368 Zir82 69.1168 Zir83 69. 8268 21r84 68. 8468 Z2r81 69.2868 Z2r82 69.8628 Z2r83 69. 1888 22r84 69.8888 22r85 69.2688 Z2r86 69.8628 Z2r87 69.8988 23r81 69.3860 23r82 69.3868 Z3r83 69.3868 Z3r84 69.3588 Z3rGS 69e4488 Z3r86 69.4768 Z3r87 69.4588 Z3r88 69.4848 Z3r89 69. <<GO 24r81 69.7288 Z4r82 69.5488 Z4r83 69.4768 24r84 69.4580 Z4rGS 69.7828 Z4r86 69.5668 Z4r87 69.3868 24r88 &9.4848 24r89 69.6288 24rlG 69.6568 25r81 66. 7588 Z5r82 67.3340 Z5r83 67.3168 25r84 67.8188 25r85 67.6768 Z5r86 67.8828 Z5r 87 67.8188 Z5r88 66.8388 25r89 67.3788 Z5riG 68.4688 INRCT 8.8808 INFICT 8.8888 INRCT 8.8880 INFICT 8.8888 INRCT 8.8888 INFICT 8.8888 INRCT 8.8888 INRCT G.GGGO INRCT 8.8888 INRCT Ge8888 RVC 68.8524 DEW CELLS RHD Zl 55.3832 RHD Z2 52.4729 RHD Z2 51. 3191 RHD 23 51.8704 RHD Z3 RHD RCT Z5'3. 51. 9217 8114 RHD Z3 RHD Z5 8.8888 INRCT 58.9681 RHD Z4 52.3575 INRCT 8.8888 INRCT 52.3863 RHD Z4 8.8888 INRCT 8.8888 53.6268 8.8080 C 52 '484 NB IENT PRESS 14.4488 VRPOR PRESSURE .1954 DRY PRESSURE 55.5671 Fl OWS 8. 8888

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RECORD NUI'IBER; 176 DFITE 55 TINE - 2338 PRESSURES 55. 7658 55.7568 RYG 55.7685 RTD'S Z ire 1 68.9188 Zir82 69.8988 2 ir83 69 8888 Z lre4 68. 9188 22rel 69.2248 Z2r82 69.8888 Z2r83 69. 1348 Z2r84 69.8628 22r85 69.2968 Z2r86 69.8628 Z2r87 69.8888 Z3rel 69.3868 23r82 69.3688 Z3r83 69.3868 Z3r84 69.2968 Z3r85 69. 3868 23r86 69. 6748 Z3r87 69 '848 Z3reS 69.4848 Z3r89 69.4228 Z4rel 69.7288 Z4r82 69.5128 24r83 69.5128 Z4r84 69.4228 24r85 69.7468 Z4r86 69.5668 24r87 69.3688 Z4r88 69 '580 24r89 69.5848 Z4rie 69.6388 Z5rei 66.7588 Z5r82 67.3168 Z5r83 67.2888 Z5r84 66.9748 Z5r85 67. 7128 Z5r86 67.8468 Z5r87 67.8188 25r88 66.8388 25r89 67.3348 25rle 6S.4688 INRCT 8.8888 IHRCT 8.8888 I HFICT 8.8888 IHRCT 8.8800 INRCT 8.8888 IHRCT e.eeee IHRCT 8.8888 INRCT 8.8880 INRCT 8.8888 IHRCT 8. 8888 RVG 68.8457 DEW CELLS RHD 21 58.6268 RHD Z2 51 8832 RHD Z2 49.9473 RHD Z3 54.6811 RHD Z3 52,9729 RHD Z3 58.94?3 RHD Z4 52.9217 RHD 24 53.2886 RHD Z5 53.1148 RHD Z5 52.6652 IHRCT 8.8888 IHRCT 8.8880 INRCT 8.8888 IHRCT 8>>8888 INRCT 8.8888 RVG 52. 2873 FINBIENT PRESS 14.3888 VRPOR PRESSURE .1936 DRY PRESSURE 55.5669 FLONS 8.8888 ECORD NUNBER 177 DRTE 55 TINE - 2345 PRESSURES 55.7648 55.7548 RYG 55.7598 RTD'S Zirel 68. 8648 2ir82 69>> 8448 Zlr83 68.9988 21re4 68. 9088 Z2re1 69.1SSG Z2r82 69.8888 Z2r83 69. 1528 22r84 69. 8980 Z2r85 69.2248 Z2r86 69.8988 Z2r87 69.8448 Z3rel 69. 3580 Z3r82 69.3688 Z3r83 69.3688 Z3r84 69.2968 Z3re5 69. 3588 Z3r86 69.5668 Z3r87 69.4228 Z3r88 69.3588 Z3r89 69. 4848 Z4rel 69.?188 Z4re2 69.5388 Z4r83 69.4768 Z4r84 69. 4840 24r85 69.7188 24r86 69>>5488 Z4r87 69. 3688 Z4reS 69. 3688 Z4r89 69.6288 Z4rie 69>>6568 Z5rel 66.7488 Z5r82 67. 2988 25r83 67.2888 Z5r84 66.9748 Z5r85 . 67.6948 ZSr86 66. 9748 Z5re7 66.9928 Z5r88 66.8388 Z5r89 67.3348 25rie 6S.4688 INRCT 8.8888 INRCT 8>>8888 IHRCT G.GGGG INFICT B.GBGG IHRCT G>>8888 INRCT 8.8888 INFICT 8.8888 IHFICT 8.8888 IHRCT 8.8888 INRCT 8.8888 RYG 68.8288 DEN CELLS RHD Z 1 51. 2837 RHD Z2 53>>9858 RHD Z2 52.7837 RHD Z3 53, 8784 RHD. 23 53. 5114 RHD Z3 53.9217 RHD Z4 58.7837 RHD Z4 52. 7934 HD Z5 53. 1148 RHD Z5 52>>3968 INFICT 8.8888 IHRCT 8. 8888 RCT e.eeee I HFICT 8.8888 INRCT 8.8888 YG 52. 8127 RNB IEHT PRESS 14>> 3888 VFIPOR PRESSURE ~ 1974 DRY PRESSURE 55.5616 FLOWS 8.8888

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RECORD NUHBER - 178 DATE - 56 TINE 8

- PRESSURES 55.?618 55. 7518 RVG 55.7568 RTD'S Zlr81 68. 9888 2ir82 69. 8628 Zlr83 68.9988 Zlr84 68 7920

~

Z2r81 69. 1888 Z2r82 69. 8448 Z2r83 69.1168 Z2r84 69.8268 22r85 69.2688 Z2r86 69. 8268 22r87 69.8628 Z3r81 69.3SOG Z3r82 69.3868 Z3r83 69.3588 Z3r84 69 '788 Z3r85 69.4848 Z3r86 69.4588 23r87 69..4848 Z3r88 69.3588 Z3r89 69. 3868 Z4r81 69.6928 Z4r82 69.5128 Z4r83 69.4768 Z4r84 69. 3860 Z4r85 69. 7468 Z4r86 69.5388 Z4r87 69.3588 24r88 69. 3688 Z4r89 69.6288 Z4r18 69.6828 25r81 66. 7228 25r82 67.2808 Z5r83 67.2628 Zsr84 66.9568 zsres 67. 6488 Zsr86 67.8100 Zsr87 66.9928 Z5r88 66. 8128 Z5r89 67. 3168 Z5rlB 68.4500 INRCT 8.8888'NRCT Ge 8888 INRCT 8. 8888 INRCT 8.8808 I NFICT 8.8888 INRCT 8. 8888 I NRCT 8. 8888 INRCT 8.8880 INRCT 8.8888 INRCT 8.8888 RVG 68.8148 DEW CELI S RHD Zl 54.4986 RHD Z2 54.8378 RHD Z2 51. 4345 RHD Z3 52. 8378 RHD Z3 52.6268 RHD 23 53.7837 RHD 24 53.5242 RHD 24 53. 1524 RHD Z5 53.1396 RHD Z5 52.3575 INRCT 8.8888 INRCT 0.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 RVG . 53.8429 RNB IENT PRESS 14.3888 VAPOR PRESSURE .1991 DRY PRESSURE 55.5569 FLOWS 8.8888 RECORD NUNBER 179 DATE 56 TINE - 15 PRESSURES 55.7598 55.7588 Sse?545 RTD'S Zir81 68. 9188 Zlr82 69.8448 Zir83 68 9728 Zlr84 68. 8100 Z2r81 69.2688 Z2r82 68.9988 Z2r83 69.8628 Z2r84 69.8628 Z2r85 69.2868 Z2r86 69.8888 Z2r87 69. 8448 Z3r81 69.3320 Z3r82 69.3588 Z3r83 69. 3148 Z3r84 69.2688 Z3r85 69.2968 Z3r86 69.5128 Z3r87 69.3688 23r88 69.3328 Z3r89 69.3868 Z4r81 69.6748 Z4r82 69.4948 Z4r83 69.4768 Z4r84 69.3328 Z4r85 69.6928 Z4r86 69.4948 Z4r87 69.3148 Z4r88 69.3508 24r89 69 5848 24r18

~ 69.5848 Z5r81 66.?848 Z5r82 67.2628 Zsr83 67.2448 Z5r84 66. 9388 25r85 67.6228 Zsr86 66.9928 ZSr87 66.9568 Z5r88 66.7948 Z5r89 67.3168 ZsrlG 68.4868 I NFICT 8.8888 INRCT 8.8888 INFICT 8.8888 INRCT 8.8808 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8080 INRCT 8.8888 INRCT 8.8888 AVG 68.7964 DEW CELLS RHD Zi 53.6396 RHD Z2 58.2558 RHD 22 55.7678 RHD Z3 54. 4888 RHD 23= 51 0 6396 RHD Z3 51. 6652 RHD 24 51. 9681 RHD Z4 54.8114 RHD Z5 52.7678 RHD ZS 52.5883 INRCT 8+8888 INRCT 8.8808 NRCT 8 F 8888 INRCT 8.8888 INRCT 8.8888 RVG 52.8782 FINB I ENT PRESS 14.3888

( VFIPOR PRESSURE o1978 DRY PRESSURE 55.5567 FLOWS 8.8888

Vlf 81

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RECORD NUMBER 188 DRTE - 56 TINE " 38 PRESSURES 55.7578 55.7489 RVG 55o7525 RTD'S 'I Zlrel 68. 8469 Zir82 69.8888 Zlr83 68. 9548 Zlr84 68.8199 Z2rei 69. 1528 Z2re2 69.9268 Z2r83 69. 1168 Z2r84'3rel 68.9989 22r95 69.2249 Z2r86 69.8888 Z2re? 69. 8888 69.3149 Z3r82 69.3328 Z3r83 69.3148 Z3r84 69.2688 Z3r85 69.3689 Z3r96 69.7289 Z3re? 69.3688 Z3r88 69.3328 Z3r89 69o3580 Z4rel 69.6928 Z4r82 69.4488 Z4r83 69.4488 24r84 69.3599 Z4r85 69.6828 Z4r86 69.4588 Z4r87 69.2788 Z4r88 69.3689 24re9 69.5668 Z4rle 69.5848 Z5rel 66.7848 Z5re2 67.2629 Z5r83 67.2268 ZSr84 66.9288 Z5r85 67.6498 25r86 66.9569 25r97 66.9568 25res 66.?948 Z5r89 67.2988 Z5rie 68.4509 I NFICT 8.8888 IHRCT 8.8989 IHRcT 8.8888 INFICT 8.9909 INRCT 8.8989 INACT Boeeee IHRCT 8.8888 INRCT 8.9090 INRCT 8.8888 INRCT 8.8888 RYG 68.7983 DEW CELLS RHD Zl 56.4681 RHD 22 52.2422 RHD Z2 52.3575 RHD 23 48.9473 RHD Z3 52.8378 RHD Z3 54.4681 RHD Z4 52.7678 RHD 24 53.3832 RHD Z5 53.2293 RHD ZS 52.5499 INRCT 8.8889 IHRCT 8. 9999 INRCT 8.8888 INRCT 8.8898 INRCT 8.8898 FIVG 52 8622

~

FINBIENT PRESS 14.3888 VFIPOR PRESSURE .1978 DRY PRESSURE 55.5547 FLOWS 8.8889 8 ~ 8888 RECOPD HUNBER - 181 DATE - 56 TIME - 45 PRESSURES 55.7568 55.7468 FIVG 55. 7519 RTD'S 2 lre 1 68.8288 21r82 68. 9989 2ir93 68 ~ 9549 Z ir84 68.7740 22re1 69. 1168 Z2r82 69.8268 Z2r83 69. 8988 Z2r84 69.9889 Z2r85 69.1788 Z2r86 68.9988 Z2r97 69. 8989 Z3rel 69.3149 Z3r92 69.3149 Z3r83 69.2968 Z3r84 69+ 2788 23rGS 69.3148 Z3r96 69.4949 23r87 69.3588 23res 69. 3148 Z3r89 69.3689 Z4rel 69.6568 Z4r82 69o4768 Z4r83 69. 4489 Z4r84 69.3500 Z4r95 69. 7189 Z4r86 69.4949 Z4r87 69. 2788 Z4res 69 2?SG F

Z4r99 69.S849 Z4rie 69.5668 ZSrei 66. 6868 ZSr92 67.2449 Z5r93 67.2268 Z5r84 66.9288 ZSr95 67. 6489 Z5r86 66.9560 25r97 66.9388 Z5res 66.7768 25r89 67. 2889 Z5r le 6se4598 INACT 9.9998 INRCT 8,8988 INRCT Go 8898 I NRCT 8.9990 INRCT 8.9999 IHFICT 8.8988 INRCT 8.8989 INRCT 9.8909 INFICT 8.8889 INRCT 8 ~ 8888 Fl YG 68.7742

/

DEW CELLS RHD Zl 52.3447 RHD Z2 54.6989 RHD 22 55.8755 RHD Z3 56. 1396 RHD Z3 52.5378 RHD Z3 52.2422 RHD Z4 51. 5883 RHD Z4 53. 3969 RHD Z5 52.8863 RHD Z5 52.3863 INRCT 8. 8889 I HFICT 9.9999 NRCT 8.8888 IHRCT 8.8888 INRCT 8.8988 RVG 53.2986 RMBIEHT PRESS 14'888 VRPOR PRESSURE ~ 2818 DRY PRESSURE 55. 5588 FLOWS 8.9889

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RECORD HUNBER - 182 DRTE - S6 TINE - 188 PRESSURES 55. 7548 55.7448 RVG 55.7496 RTD'S Zirol 68. 8468 Zir62 68. 9988 Zlr83 68.9188 Zir84 68.7566 Z2rol 69.2668 Z2r82 68. 9986 22r83 69.1348 Z2r84 69 '686 Z2r85 69.2248 Z2r86 68. 9368 22r87 68.9988 23r81 69 '786 Z3r82 69.2968 Z3r83 69.2788 23r84 69.2248 Z3r85 69.2426 Z3r86 69.6748 Z3r87 69.3328 Z3r88 69.2968 Z3r89 69.3326 Z4roi 69.6386 Z4r82 69.4488 Z4r83 69.4848 Z4re4 69 '646 Z4r85 69.6288 Z4r86 69.4768 Z4ro? 69.2688 Z4roo 69.2426 24r89 69.4948 Z4rlo 69.5388 ZSroi 66.6588 Z5r82 67.2686 ZSr83 67. 1988 Z5r84 66.9628 Z5r85 67.6848 ZSr86 66.9746 Z5r87 66.9388 Z5r88 66.7488 Z5r69 67.2628 Z5rio 68.3966 INRCT 8.8888 IHRCT 8. 8888 INRCT 8.8888 INRCT 8.6606 INRCT 8.8868 INRCT 8.8888 IHRCT 8.8868 INRCT 8.6668 I NFICT 8.8868 INRCT 8.8868 RVG 68.7623 DEN CELLS RHD Zl 5 1. 8784 RHD Z2 58.8575 RHD 22 54 '422 RHD Z3 51.5114 RHD Z3 53e4681 RHD Z3 52.8627 RHD Z4 53.5242 RMD Z4 52.2556 RHD ZS 52 '473 RHD Z5 52.3968 INRCT 8.8688 INRCT 8.8666 INRCT 8.8868 IHFICT 8.8888 INRCT 8. 8888 RVG 52.5168 RNBIEHT PRESS 14 '868 VRPOR PRESSURE .1952 DRY PRESSURE 55.5538 FLOWS 8.8888 RECORD NUNBER 183 DRTE - 56 TINE 115 PRESSURES 55.7518 55.7428 RVG 55.7465 RTD'S 2lr61 68.7926 Zir82 68.9726 Zir83 68.9188 Zir84 68. 7386 Z2roi 69. 1526 Z2r82 68.9726 Z2r63 68.9966 Z2r64 68. 9726 Z2r65 69.2866 Z2r86 68.9546 Z2r87 68.9726 23roi 69. 2786 Z3r62 69.2666 Z3r63 69.2428 Z3r64 69.2666 Z3r65 69. 2426 Z3r66 69.5666 Z3r87 69.3148 Z3r08 69.2688 Z3r89 69. 2960 Z4rol 69.6288 Z4r62 69 '646 Z4r63 69.4466 Z4r84 69. 3686 Z4r65 69.6266 Z4r66 69.4228 24r87 69.2426 Z4r88 69. 2966 Z4r89 69.5486 Z4rie 69.4948 Z5roi 66.6586 Z5r62 67. 2686 Z5r83 67.1986 25r84 66,8846 Z5r85 67.5866 Z5r86 66. 9386 Z5r87 66.9266 Z5r88 66.7486 Z5r69 67.2446 ZSr 18 68'146 INRCT 8.8666 INRCT 8.8668 IHRCT 8.8668 !NRCT 6.6060 IHRCT 6.6886 INRCT 8.8668 IHRCT 8.8868 INRCT 8.8660 IHRCT oooooo IHFICT 8.8888 RVG 68.7387 DEN CELLS RHD Zl 53.4986 RHD Z2 52.2678 RHD Z2 53.8663 RHD Z3 54.0242 RHD Z3 58.7934 RHD Z3 55.8114 RHD 24 52.6781 RHD Z4 56.6242 HD Z5 52.7678 RHD ZS 52.2558 IHRCT 8eoooo INRCT 6.6666 NFICT 6. 8686 IHRCT 8.8888 INFICT 8.6686 RVG 52 '117 RNBIEHT PRESS 14.3888 VRPOR PRESSURE .1967 DRY PRESSURE 55.5498 FLO41S 8.8888

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RECORD NUNBER 184 DRTE - 56 TINE - 138 PRESSURES 55 ~ 7589 55.7488 RVG 55'?459 RTD'S 2ir81 68.7928 Zir82 68. 9368 2lr83 68.9888 Zlr84 68.6849 22r81 69.8628 Z2r82 68 '368 Z2r83 68.9988 Z2r84 68.9729 Z2r85 69.1528 22r86 68.9898 Z2r87 68.9548 23r81 69.2680 23r82 69.2688 Z3r83 69.2429 Z3r94 69.2868 23r85 69.2420 Z3r86 69.5669 23r87 69.2968 23r98 69.2788 Z3r89 69.3140 24r81 69.5848 Z4r82 69.3869 Z4r83 69.3868 Z4r84 69.3869 Z4r85 69.6288 24r86 69.4848 Z4r87 69.2429 24r88 69.2969 Z4r89 69.5128 Z4ri8 69.5488 ZSr81 66.6588 Z5r82 67.2980 Z5r83 67.1?28 Z5r94 66.8669 25r85 67. 5688 ZSr86 66.9928 25r87 66.9829. 25r88 66.7228 Z5r89 67. 2448 Z5r 1 8 68.3960 INRCT 8.8889 INRCT 8.9888 INRCT 8. 8888 INRCT 9.8808 INRCT 8.8888 INRCT 8.9889 INRCT 8.8888 INRCT 9.9909 INRCT 8.8888 INRCT 8.8988 FIVG 68.7236 DEW CELLS RHD Zi 58.2678 RHD 22 S6. 1524 RHD Z2 54.8832 RHD Z3 51.7934 RHD Z3 51. 2837 RHD 23 51. 7886 RHD Z4 54.1148 RHD 24 52.7165 RHD ZS 53. 9114 RHD 25 52. 6652 I NFICT 8. 9888 INRCT 9e9999 INRCT 8.8899 I NFICT 8. 8888 INRCT 8. 8889 FIVG 52. 8896 RNB IENT PRESS 14 '888 VRPOR PRESSURE .1988 DRY PRESSURE 55.5478 FLOWS 8. 8888 RECORD NUNBER 185 DFITE 56 TIME - 145 PRESSURES 55.?478 55.7388 RVG 55. 7425 RTD'S Zir81 68.7928 Zlr92 68. 9368 Zlr83 68.8828 Zlr84 68. 7299 22r91 69.8988 Z2r82 68. 9188 Z2r83 69. 8888 Z2r94 6e. 9?29 Z2r85 69 8268 Z2r96 68. 9888 Z2r97 68.9369 Z3r81 69.2689 Z3r82 69.2428 Z3r93 69. 2248 Z3r84 69.1888 Z3r85 69.2240 Z3r86 69.4768 Z3r97 69.2?88 23r88 69.2698 Z3r89 69.3320 Z4r81 69.6829 Z4r92 69.3868 24r93 69.3869 Z4r84 69.4949 24r95 69.5388 Z4r86 69e4949 24r97 69,2248 Z4r88 69.2789 Z4r89 69.4948 Z4r18 69.4768 Z5r81 66,6589 Z5r82 67, 1900 Z5r93 67. 1548 Z5r84 66.8489 Z5r85 67.5328 Z5r86 66.8849 Z5r87 66.8849 Z5r98 66.7848 Z5r89 67.2988 Z5r19 68.3699 INRCT 8.8998 INFICT 8o8999 INRCT 8.9988 INFICT 9.9099 I NFICT 8.8999 INFICT 9.8988 INRCT 8.8898 INRCT 9.8909 INRCT 8.8888 INRCT 8e8888 RVG 68. 7887 DEW CELLS RHD 21 54.3968 RHD Z2 54.2293 RHD 22 59.4888 RHD Z3 54.3191 RHD Z3 52.5378 RHD 23 52.5627 RHD Z4 52.6268 RHD Z4 52.7559 D Z5 S2.9681 RHD 25 52oi?81 INRCT 8.8888 INRCT 8.8988 RCT 8+8888 INRCT 8.8888 INRCT 8.8889 RVG 52.8822 RNB IENT PRESS 14.3888

( VAPOR PRESSURE ~ 19?9 DRY PRESSURE 55.5446 FLOWS 9o8888

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RECORD NUNBER - 186 DATE 56 TINE 288 PRESSURES 55.7458 55.7358 AVG 55.7488 RTD'S Zlrel 68. 73SB 2 1r 82 68.9548 Zlr83 68. 8288 Z lr84 68.6660 22rel 69.8988 Z2r82 68.9888 Z2r83 68. 9988 Z2r84 68.9188 Z2r85 69.1528 22r86 68.9888 Z2r87 68. 9188 Z3rel 69.2868 Z3r82 69.2688 Z3r83 69. 1888 Z3r84 69. 1888 Z3r85 69.26GG 23r86 69.6288 23re? 69.2688 Z3r88 69.2688 Z3r89 69.2960 Z4rel 69.5848 Z4r82 69.3588 Z4r83 69.3868 Z4r84 69.2600 Z4r85 69.4948 Z4r86 69.3588 24re? 69.2e6e 24r88 69. 2428 24r89 69.5128 Z4rie 69. 4588 Z5re1 66.5968 Z5r82 67.1548 25r83 67.1368 Z5r84 66.8388 Z5r85 67.6848 Z5re6 66.e668 Z5r 8? 66.8848 25r88 66.6868 Z5r89 67.2888 25r 1 8 68.3428 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8800 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8880 INACT 8.8888 INACT 8.8888 AVG 68.6967 DEW CELl S RHD 21 51.6652 RHD Z2 51. 6811 RHD Z2 53. 8191 RHD Z3 52. 8784 RHD Z3 52.4473 RKD Z3 53.5378 RHD 24 53.3784 RHD 24 52. 1811 RHD Z5 52.S832 RHD Z5 52.2678 INACT 8.8888 INACT 8. GGGG INACT e.eeee INACT 8.8888 INACT 8.8888 AVG 52.6467 ANBIENT PRESS 14.3888 VAPOR PRESSURE ~ 1962 DRY PRESSURE 55. 5438 FLOWS 8. 8888 RECORD NURSER - 187 DATE - 56 TINE - 215 PRESSURES 55.7438 55.7338 AVG 55.7388 RTD'S Zirei 68.7388 Zlr82 68.9888 Zlr83 68.8648 Zlr84 68.7828 Z2rei 69.8268 Z2r82 68 9188 Z2r83

~ 68.9548 Z2r84 68.9GGG Z2r85 69.1168 Z2r86 68.8828 Z2r87 68. 9188 23re1 69. 2868 Z3r82 69.1?88 Z3r83 69.2868 Z3r84 69. 1348 Z3r85 69. 2868 23r86 69.4768 Z3r87 69,2788 Z3r88 69.2868 Z3r89 69. 2248 Z4rel 69.5488 Z4r82 69.3688 24r83 69.3588 Z4r84 69. 3688 Z4r05 69;4948 Z4r86 69.3868 Z4r87 69.1780 Z4re8 69. 2428 Z4r89 69.4768 Z4rle 69.4768 Z5rel 66.5788 Z5r82 67.1548 25r83 67. 1188 ZSr84 66.8388 ZSr85 67.4968 Z5r86 66eS308 Z5r87 66+8668 25r88 66.6868 25r89 67. 1988 Z5ri 8 6S.3968 INACT 8.8888 INACT 8.8888 IHACT 8. BGGG INACT G.GGGG INACT 8.8888 INACT 8.8888 INACT 8. 8888 I NFICT 8. GGGG INACT 8.8888 INACT 8.8888 AVG 68.6768 DEW CELLS RHD Zl 52. 7165 RHD Z2 53.6989 RHD Z2 52.6652 RHD Z3 51.3704 RHD. Z3 51.8242 RHD Z3 53.4858 RHD 24 54.5627 RHD Z4 52.6652 HD Z5 52.8832 RHD Z5 52.3784 INFICT 8'8888 INACT 8.8808 ACT 8.8888 INACT 8.8888 INACT Greece VG 52.7483 AMBIENT PRESS 14. 3888 VAPOR PRESSURE ~ 1969 DRY PRESSURE 55. 5411 FLOWS e. 8888 e.eeee

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RECORD NUMBER - 188 DATE - 56 TIME - 236 PRESSURES 55. 7426 55.7328 RVG 55.7376 RTD'S Zlrei 68.7748 Zlre2 68. 9688 Z1 r63 68.8646 Zlr64 68. 7380 Z2rel 68.9726 Z2r82 68.9368 Z2r83 68.9188 Z2r64 68. 960e 22r85 69.8988 Z2r86 68.9188 Z2r87 68.9188 Z3rel 69.1888 Z3r82 69.1888 Z3r83 69.2668 Z3r84 69.1528 Z3r85 69.1880 Z3r86 69.2686 Z3r87 69.2686 23r88 69.1888 Z3r89 69.2660 Z4rel 69.5388 Z4r82 69.3688 Z4r83 69.3148 Z4r84 69.2600 Z4r85 69.5848 Z4r86 69.4646 Z4r87 69.2868 Z4r88 69.2240 Z4re9 69.4588 Z4rle 69.4588 Z5rei 66.5788 ZSr82 67.1360 ZSre3 67. 1188 Z5r84 66.8128 Z5re5 67.4688 ZSr86 66.8480 Z5r87 66.8368 Z5r88 66.6686 Z5r89 67.1728 25rle 68.2340 IHRCT 8.8888 IHRCT 8.8686 IHFICT 8. 8888 IHRCT G.eeve IHRCT 8.8888 IHRCT 8.6668 INRCT 8 8888 IHRCT

~ 6.6000 INRCT 8.8886 IHRCT 8.8688 RVG 68.6616 DEW CELLS RHD Zi 53.8319 RHD Z2 53.9681 RHD 22 58.4888 RHD Z3 51. 6146 RHD Z3 58. 8319 RHD 23 54.9681 RHD Z4 52. 7165 RHD 24 52.5114 RHD 25 52.6652 RHD Z5 52.2934 IHACT '8. 6688 IHRCT 8.6666 INRCT 8. 8888 INRCT 8.8888 IHRCT Beeeee RVG 52.5767 AMBIENT PRESS 14.3888 VAPOR PRESSURE .1957 DRY PRESSURE 55+5413 FLOWS 8.8888 RECORD NUMBER - 189 DFITE - 56 TIME 245 PRESSURES 55.7488 55. 7388 RVG 55. 7356 PTDiS Zirel 68.7388 Zir82 68. 8468 21r83 68.8280 Zlr84 68.6366 22rei 69.6448 Z2r82 68.8826 Z2r63 69.6446 Z2r84 68.8826 Z2r85 69.e62e Z2re6 68.8468 Z2r67 68.9686 Z3rel 69.1886 Z3r82 69.1?66 Z3r83 69. 1528 Z3r64 69. 1528 Z3r85 69.2420 23r66 69.4586 Z3r67 69.2248 Z3r68 69.2666 Z3r69 69.26vO Z4rel 69.5366 Z4r62- 69. 3148 24r63 69.2966 Z4r84 o9. 2426 24r65 69';6928 24r86 69.4648 24r67 69.2666 Z4r68 69.2666 Z4r89 69.4466 Z4rie 69.4766 ZSrel 66.5666 25r62 67.1180 25r63 67. 1868 Z5r84 66.7766 Z5r85 67.4666 ZSr86 66.8126 25re7 66.8386 25r88 66.6326 Z5r89 67.1?28 Z5r 1 6 68.2346 INACT 8.6668 INRCT 8.6868 IHRCT 8.6668 IHRCT 6.6660 I HFICT 6.6666 IHFICT 8.8888 INRCT 8.8866 I NRCT 8.6066 INRCT 8.8888 INRCT 8.8688 RVG 68.6578 DEW CELLS RHD Zl 52.5242 RHD Z2 52.6378 RHD Z2 53. 1148 RHD Z3 51. 1524 RHD Z3 56. 1811 RHD 23 53.2934 RHD Z4 52.8499 RHD Z4 56. 6114 HD 25 52. 7934 RHD ZS 52.2637 INRCT 8;6888 IHRCT e. 8666

<RCT Ge 8868 INRCT Greece IHRCT 8.8888 VG 51. 9675 RMB IENT PRESS 14. 3888 VAPOR PRESSURE ~ 1913 DRY PRESSURE 55. 5437 FLOWS 8.8888

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RECORD NUMBER - 198 DRTE - 56 TIME 388 PRESSURES 55.?378 55.7288 RVG 55.?325 RTD'S

,Zir81 68 7828 2 1r82

~ 68. 8188 Zlr83 68.8288 Zir84 68'128 Z2r81 69.8628 Z2r82 68 '648 Z2r83 68.9988 Z2r84 68.8648 Z2r85 69.8888 Z2r86 68.8648 22r87 68.8648 Z3r81 69.1?GG Z3r82 69. 1348 Z3r83 69.1788 23r84 69.1168 23r85 69.1788 Z3r86 69.4768 Z3r87 69.2248 Z3r88 69.1788 23r89 69.2420 24r81 69.5128 Z4r82 69.3328 Z4r83 69.2788 24r84 69.3140 Z4r85 69.4948 Z4r86 69.2968 Z4r87 69.1528 Z4rGS 69.l348 24r89 69.4488 Z4r18 69.4488 25r81 66.5428 Z5r82 67.18GG Z5r83 67.8828 25r84 66.7488 Z5r85 67.4248 Z5r86 66.8120 25r87 66.7948 ZSr88 66. 6148 25r89 67. 1368 25riG 68.2528 INRCT 8.8888 INRCT 8. 8888 IHRCT 8. 8888 INRCT 8.8888 INRCT 8.8888 IHRCT 8.8888 IHRCT 8.8888 INRCT G.GGGG IHRCT 8.8888 IHRCT 8.8888 RVG 68.6348 DEW CELLS RHD Zi 53.?422 RHD Z2 52.7934 RHD Z2 55.6524 RHD Z3 52.2678 RHD 23 58o3863 RHD 23 52.7293 RHD Z4 52.9217 RHD Z4 52.4473 RHD Z5 52.9888 RHD 25 52. 1811 IHFICT 8.8888 IHRCT G.GGGG INRCT 8.8888 INRCT 8~ 8888 IHRCT 8.8888 RVG 52.8874 RMBIEHT PRESS 14 '888 VRPOR PRESSURE .1974 DRY PRESSURE 55.5351 FLOWS 8.8888 RECORD NUMBER - 191 DRTE - 56 TIME - 315 PRESSURES 55.7358 55.7258 RVG 55. 7388 RTD'S Zlr81 68. 7828 Zlr82 68.8188 Zir83 68. 7928 Zlr84 68.5768 Z2r81 69.8888 Z2r82 68.8648 Z2r83 68.9368 22r84 68.S468 Z2r85 69.8SGG Z2r86 68+8288 Z2r87 68.8648 23r81 69. 1528 Z3r82 69. 1348 23r83 69. 1528 Z3r84 69o8988 23r85 69.1348 Z3r86 69.2688 Z3r87 69.1888 Z3r88 69. 1528 Z3r89 69.2868 24r81 69.4948 Z4r82 69. 3148 Z4r83 69. 2788 24r84 69.2240 Z4r85 69.5488 Z4r86 69.3688 Z4r87 1528 24rGS '9.

69.1700 Z4r09 69.4848 Z4riG 69.4228 Z5r8.1 66.5868 Z5r82 6?.8648 25r83 6?o8648 Z5r84 66.7488 Z5r85 67.4688 Z5r86 66.?228 Z5r87 66.7948 Z5r88 66.6328 25r89 67.1368 Z5rlG 68.2520 INRCT 8.8888 INRCT 8.8888 INRCT 8.8880 INRCT G.GGGG I NFICT 8.8808 IHRCT 8.8888 IHFICT 8.8888 INFICT 8.8800 IHRCT 8.8888 IHRCT 8.8888 RVG 68.6128 DEW CELLS RHD Zl 58.3575 RHD Z2 49.2934 RHD Z2 54.3968 RHD 23 51.3968 RHD Z3 51. 1652 RHD Z3 52'?934 RHD Z4 51. 6524 RHD Z4 58.5883 RHD Z5 52.7422 RHD 25 52+8499 INRCT 8. 8888 IHRCT 8.8880 NFICT Go 8888 INRCT 8.8888 INRCT 8~ 8888 RVG 52. 4694 RMBIENT PRESS 14.3888 VRPOR PRESSURE .1949 DRY PRESSURE 55.5351 FLOWS 8.8888 B. 8888

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RECORD HUNBER " 192 DRTE 56 TINE 330 PRESSURES 55.7330 55.7230 FIVG 55 '280 RTD'S Zlr01 68, 6840 2ir02 68.8468 Z1r03 68.8180 Zlr04 68. 5949 22r01 68.9909 Z2r02 68.8288 Z2r03 68.9540 Z2r04 68. 8466 Z2r05 69.0080 22r06 68.8108 Z2r07 68.8460 Z3r01 69.1346 23r02 69. 1520 Z3r03 69.1168 23r04 69.8888 Z3r05 69.1160 Z3r06 69.4220 Z3r07 69.2068 23r08 69. 1520 Z3r09 69.1880 Z4rel 69.5128 Z4r82 69.2788 Z4r03 69.2960 24r84 69.2240 Z4r05 69.4580 Z4r86 69.2608 Z4r07 69. 1160 Z4r08 69.1349 Z4r09 69.3320 Z4r18 69.4220 Z5r01 66. 5060 ZSr82 67.0640 Z5r03 67.0460 Z5r04 66o7220 ZSr05 67.4240 Z5r06 66.7940 25r07 66.7940 Z5r08 66.5960 Z5r09 67. 1180 Z5r 1 8 68.2700 INRCT 0.0000 INRCT 8.8008 I HRCT 0.8000 IHRCT 0.0009 I NFICT 0.8000 INRCT 0.8600 I NFICT 0.8000 INRCT 0.0909 IHRCT 8.0800 IHFICT 8.0008 FIVG 68.6855 DEW CELLS RHD Zi 49. 1140 RHD 22 53.2934 RHD Z2 50. 1268 RHD Z3 53. 2293 RHD Z3 51. 7422 RHD Z3 52.2037 RHD Z4 51.0883 RHD Z4 56'691 RHD Z5 52.5370 RHD Z5 52.3319 IHFICT 0. 0800 I HFICT 0.0000 INRCT 0.9000 INRCT 8. 8980 INACT 0.0000 RYG 51.6311 ANB IEHT PRESS 14 '880 VRPOR PRESSURE .1889 DRY PRESSURE 55.5391 FLOWS 0.0000 RECORD NUNBER 193 DATE - 56 TINE 345 PRESSURES 55. 7310 55. 7218 RVG 55.7269 RTD'S Zlr01 68. 6480 Zlr02 68. 7740 2 ir03 68. 7929 Zlr04 68. 6480 Z2rel 68. 9360 Z2r02 68.8280 Z2r03 68.8460 Z2r84 68.8460 Z2r05 68. 9720 Z2r06 68.7920 Z2r07 68.8460 Z3r01 69.1349 Z3r02 69.1340 Z3r03 69.0980 23r04 69.0620 Z3r05 69.6986 Z3r6,6 69.3680 Z3r07 69.1880 Z3r08 69.1340 Z3r09 69.1880 Z4rei 69.4400 Z4r02 69.2600 Z4r03 69.2609 Z4r04 69.2240 Z4r05 69.5480 Z4r06 69.2960 Z4r07 69.1349 Z4r08 69.1340 Z4r09 69.3860 Z4ri0 69. 3860 Z5r01 66.4880 Z5r02 67.0466 Z5r03 67.0280 Z5r04 66.7040 25r05 67.3880 25r06 66.7586 Z5r07 66.7580 '5r08 66.5780 Z5r09 67.1008 25r10 68.2346 INRCT 0.0000 INRCT 0.0000 IHRCT 0.0000 INRCT 0.6006 INRCT 0.0900 INRCT 0.0008 INRCT 9.0009 INRCT 0.0000 IHRCT e.eeee INRCT 8.8808 RVG 68.5873 DEW CEI LS RHD 21 52.9088 RHD Z2 54. 7165 RHD 22 S6.0114 RHD Z3 50. 7293 RHD 23 51. 4473 RHD 23 52. 9345 RHD Z4 51. 9986 RHD Z4 51.4729 RHD 25 52.7165 RHD ZS Sl. 9986 INRCT 0. 0000 IHRCT 0.0900 HRCT 0.0800 IHRCT 8.8800 IHFICT 0. eGee RYG 52. 7266 RNBIEHT PRESS 14. 4000 VAPOR PRESSURE o1968 DRY PRESSURE 55.5292 ~

FLOWS 8. 0008 8.8008

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RECORD NUNBER . 194 DATE 56 TINE 488 PRESSURES 55m 7388 55.7288 AVG 55.7258 RTD'S Zire 1 68.6388 Z ir82 68. 7928 Zlr83 .68. 7568 Zlr84 68.6128 22rel 68.9888 Z2r82 68. 8188 Z2r83 68.9188 Z2r84 68.7928 22r85 68.9988 22r86 68. 8468 Z2r87 68.8188 Z3rei 69.1168 Z3r82 69.1348 Z3r83 69. 1168 Z3r84, 69.8888 Z3r85 69.1348 23r86 69.2968 Z3r87 69. 1788 Z3r88 69.89SG Z3r89 69.1528 24rel 69.4768 Z4r82 69. 2788 24r83 69.2248 Z4r84 69. 1528 Z4r85 69.5388 Z4r86 69.2968 Z4r87 69.1348 Z4r88 69.1528 24r89 69.3328 Z4rie 69.3868 ZSroi 66.4788 Z5r82 67.8288 Z5r83 67. 8188 Z5r84 66.6688 Z5r85 67.3888 Z5r86 66.7228 Z5r87 66.7488 Z5r88 66.5688 Z5re9 67.8828 Z5rle 68.1628 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8880 INACT e.eeoc INACT 8.8888 INACT 8.8888 INACT 8.8800 INACT 8.8888 INACT 8.8888 AVG 68 '743 DEW CELLS RHD Zi 53. 1396 RHD Z2 58. 7165 RHD 22 53.4473 RHD Z3 52 '558 RHD Z3 49+6811 RHD Z3 52e5755 RHD Z4 52.5114 RHD Z4 50.7934 RHD Z5 52.5378 RHD Z5 52'148 INACT 8.8888 INACT G.GGGG INACT 8.8888 INACT 8.8888 INACT 8.8888 AYG 52.8411 AMBIENT PRESS 14.4888 YAPOR PRESSURE .1918 DRY PRESSURE 55.5332 FLOWS 8.8888 RECORD NUNBER - 195 DATE - 56 TINE 415 PRESSURES 55.7278 55. 7178 AVG 55.7228 RTD'S Zirei 68. 6128 Zlr82 68. 8188 Zlr83 68.7748 Zlr84 '68.5488 Z2rel 68.9888 Z2r82 68. 7928 22r83 68.8828 22r84 68.7740 Z2r85 68.9988 22r86 68. 7748 Z2re? 68.7748 Z3rei 69.8980 Z3r82 69o8988 Z3r83 69. 8988 Z3r84 69.8448 23ro5 69.8988 23r86 69 '248 Z3r87 69. 1528 Z3r88 69.8988 Z3r89 69.1348 Z4rei 69.4488 Z4r82 69. 2688 Z4r83 69.2248 24r84 69.1888 Z4r85 69e4848 24r86 69.2788 Z4r87 69.8888 Z4r88 69.8980 Z4r89 69.3328 Zarie 69.3328 25rei 66.4528 25r82 67.8180 Z5r83 66.9748 Z5r84 66.6588 Z5re5 67.3528 Z5r86 66.7220 Z5r87 66.7848 Z5r88 66.5428 Z5r89 67.8460 25r18 68.2348 INACT 8.8888 INACT 8. 8888 INACT 8.8880 INACT G.GGG0 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT G.GGGG INACT Geeeee INACT 8.8888 AVG 68.5585 DEW CELLS RHD Zi 49.4681 RHD Z2 53.8575 RHD Z2 51. 2165 RMD Z3 51. 7558 RHD Z3 58. 2165 RHD Z3 51. 7293 RHD 24 53.6989 RHD Z4 52.1781 RHD Z5 52'. 6148 RHD Z5 52 '627 IkACT 8.8888 IkACT G.GGGG INACT 8.8888 INACT Geeeee INACT 8+8888 FIVG 51. 8961 ANBIENT PRESS 14e4888 VAPOR PRESSURE .1988 DRY PRESSURE 55.5312 FLOWS 8.8888 8.8888

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RECORD HUNBER " 196 DRTE 56 TINE - 438 PRESSURES 55.7258 55. 7158 RVG 55. 7288 RTD'S Zlr81 68.5768 Zir82 68.?748 Zlr83 68.7388 Zlr84 68. 5948 Z2r81 68.9888 Z2r82 68.7568 Z2r83 68.8648 Z2r84 68. 7748 Z2r85 68.9188 22re6 68.7748 22r87 68.?748 Z3r81 69. 8988 Z3r82 69.8628 Z3r83 69.8628 Z3r84 69.8268 23r85 69. 8880 Z3r86 69.2428 23r87 69. 1348 Z3r88 69.8988 Z3r89 69.1340 24r81 69o4588 Z4r82 69.2428 Z4r83 69.2868 Z4r84 69.1528 Z4r85 69+4228 Z4r86 69.2968 Z4r87 69.8988 Z4r88 69.8988 Z4r89 69. 3148 24r18 69.3688 Z5r81 66.4348 25r82 66. 9928 Z5r83 66.9568 Z5r84 66.6328 25r85 67.3168 Z5r86 66.6580 25r87 66.?848 25r88 66.5248 Z5r89 67.8288 25r18 68.1888 IHRCT Bo8888 IHRCT 8.8888 INRCT 8.8888 INRCT G.GGBG IHRCT 8.8888 INRCT 8.8888 IHRCT 8. 8888 IHRCT 8.8888 INRCT 8 F 8888 IHRCT 8.8888 RVG 680 5363 DEW CELLS RHD 21 58.4986 RHD 22 53. 1652 RKD Z2 58. 6148 RHD Z3 52. 8883 RHD Z3 53 '832 RHD Z3 51.9729 RHD 24 58.5627 RHD Z4 58. 7837 RHD Z5 52.4986 RHD 25 51. 9888 INRCT 8.8888 INRCT G.GGGG INRCT 8.8888 IHRCT 8 F 8888 INRCT B.BGGG RVG 51.7977

'NBIEHT PRESS 14.4888 VRPOR PRESSURE .1981 DRY PRESSURE 55.5299 FLOWS 8.8888 8.8888 RECORD NUMBER 197 DRTE 56 TINE - 445 PRESSURES 55.7228 55. 7128 RVG 55. 7178 RTD'S 21r81 68. 6488 Zlr82 68.7928 Zlr83 68.7288 2lr84 68. 5228 Z2r81 68.8828 Z2r82 68.7568 Z2r83 68.8468 Z2r84 68. 8188 Z2r85 68.9368 Z2r86 68.7568 22r87 68.7748 23r81 69 8628

~

Z3r82 69.8448 Z3r83 69.8268 Z3r84 69.8888 Z3r85 69. 8620 Z3r86 69.3328 Z3r87 69+1 168 Z3r88 69.8628 Z3r89 69. 0988 24r81 69.4848 24r82 69. 1888 Z4r83 69.1888 Z4r84 69. 1168 24r85 69.3868 24r86 69.2248 Z4r87 69.8888 Z4r88 69. 8628 24r89 69.3148 Z4rlB 69.3328 25r81 66.4168 Z5r82 66. 9568 25r83 66.9388 Z5r84 66.6148 Z5r85 67.3528 Z5r86 66. 6508 Z5r87 66.6868 Z5r88 66.5868 Z5r89 67.8288 Z5rlG 68.1888 INRCT G.BBGG IHFICT 8.8888 IHRCT 8.8888 INRCT 8.8880 INRCT 8.8888 INRCT 8.8888 IHRCT 8.8888 INRCT G.GGGG INRCT 8.8888 INRCT 8.8888 RVG 68.5236 DEW CELLS RHD Zl 53. 1652 RHD Z2 58. 1989 RHD 22 58.6989 RHD Z3 47.2934 RHD Z3 58.6989 RHD 23 52.9473 RHD 24 52. 1148 RHD Z4 51.5499 HD Z5 52. 7934 RHD 25 52. 1268 INRCT 8. 8888 IHRCT G.GGGG RCT 8.8888 I NFICT 8.8888 IHRCT 8. 8888 VG 51. 4831 RNBIEHT PRESS 14 '888 VRPOR PRESSURE- ~ 1873 DRY PRESSURE 55. 5297 FLOWS K

8.8888 8.8888

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RECORD NUNBER - 198 DRTE - 56 TINE 588 PRESSURES 55. 7288 55. 7188 RVG 55.7158 RTD'S Z ir81 68.5768 Zir82 68.7928 Zlr83 68. 6848 Z ir94 68. 5499 Z2r81 68.9188 22r82 68.7568 22r83 68.8648 Z2r84 68.7389 Z2r85 68.9368 Z2r86 68.7828 Z2r87 68.7388 23r81 69.8629 Z3r82 69.8448 23r83 69.8268 Z3r84 68.9988 Z3r85 68.9909 Z3r86 69.4488 Z3r87 69.8988 23r88 69. 8448 23r89 69 '899 24r81 69.3868 Z4r82 69.2248 Z4r83 69.1888 Z4r84 69.1529 Z4r85 69.4488 Z4r86 69.2248 Z4r87 69.8888 Z4r88 68.9360 Z4r89 69.3328 24ri8 69.2968 Z5r81 66.3888 Z5r82 66.9389 Z5r83 66.9289 Z5r84 66.5968 25r85 67.2888 Z5r96 66.5960 25r87 66.6688 25r88 66,4888 25r89 66.9928 Z5ri9 68.1620 INRCT 8~ 8888 IHRCT 8.8898 IHRCT 8.8888 INRCT 8.9990 INRCT 8.9899 INRCT 8.8988 IHRCT 8.8888 IHRCT 8.9099 INRCT 8.8888 INRCT 8.8898 RVG 68.5857 DEW CELLS RHD 21 49.9345 RHD 22 52.3832 RHD Z2 51. 3447 RHD Z3 53.9858 RHD 23 52.2558 RHD Z3 54e4986 RHD 24 53.1652 RHD 24 59.25SG RHD 25 52.5242 RHD 25 51. 9691 IHRCT 8.8888 IHFICT 9.9999 INFICT 8. 8888 IHRCT 8. 8888 INRCT Bo9899 RVG 52.2865 RNBIEHT PRESS 14 '888 VFIPOR PRESSURE ~ 1938 DRY PRESSURE 55. 5228 FLOWS 8. 8888 RECORD NUNBER 199 DATE 56 TINE 515 PRESSURES 55.7178 55. 7878 RVG 55.7128 RTD'S 21r81 68.5488 Zlr82 68 '489 Zir83 68.7829 21r84 68.5229 Z2r81 68.8648 Z2r92 68.7288 Z2r93 68.8189 Z2r84 68.7389 22r85 68.9989 Z2r86 68o7828 22r87 68.7298 Z3r81 69.8089 Z3r82 69.8269 Z3r83 69.8888 Z3r84 68.9728 Z3rBS 69.9089 Z3r86 69.2699 Z3r87 69.8628 Z3r88 69.9888 23r89 69.9269 24r81 69.3589 Z4r92 69. 1169 Z4r93 69.1528 Z4r84 69.9629 Z4r85 69'.3149 24r86 69.2868 Z4r87 69.8888 24rGS 69.9080 Z4r89 69.2788 Z4riB 69.3148 Z5r81 66.3448 Z5r92 66.9209 Z5r83 66.9828 Z5r84 66.5788 25r85 67.2989 Z5r96 66.5429 Z5r87 66.6508 Z5r88 66.4889 25r89 66.9928 Z5riG 68.1629 INRCT Be8889 INFICT 8.8888 INRCT 8.8998 IHFICT 8.8909 INRCT 8 9999

~ INRCT 8.8888 INRCT 8.8889 INRCT 8.9999 IHRCT 8.8888 INRCT 8.8888 RVG 68.4751 DEW CELLS RHD Zl 53.7934 RMD Z2 54.3968 RHD Z2 52. 7165 RHD Z3 52. 9379 RHD 23 51. 9473 RHD 23 53.6268 RHD Z4 51. 4681 RHD Z4 59.8447 HD ZS 52.4729 RHD Z5 51. 7422 I NRCT 9:8988 INRCT 9.0999 RCT 9.8888 IHRCT 8. 8898 INRCT 8.8888

.RVG 52. 5111 RNB IEHT PRESS 14 '888 VRPOR PRESSURE .1952 DRY PRESSURE 55. 5168 FLOWS 8.8888 Be8898

RECORD HUt'1BER 288 DATE - S6 T I NE 538 PPESSURES 55. 7158 55e 7858 RVG 55.7188 RTD'S Zlrel 68.5768 Zlr82 68. 7828 2 1r83 68. 6488 21r84 68.4588 Z2rei 68.8648 22r82 68.7288 Z2re3 68. 8188 Z2r84 68 '828 Z2r85 68. 9188 Z2r86 68.7828 Z2r87 68.7828 23rel 69.8888 Z3r82 69. 8268 Z3r 83 68.9988 Z3re4 68. 9728 Z3r85 69. 8880 Z3r86 69.2968 Z3r87 69.8448 23r88 69.8888 Z3r89 69. 8448 24rel '69. 3328 24r82 69. 1888 Z4r83 69.1348 Z4r84 69. 8448 Z4r85 69.4488 Z4r86 69. 1888 Z4r87 68.9988 Z4r88 69. 8888 Z4r89 69.2688 24rie 69.2688 25rel 66.3268 25r82 66. 9828 ZSr83 66.8668 Z5r84 66.5428 25r85 67.2888 25r86 66. 5420 Z5r87 66.6328 Z5r88 66e4788 2Sr89 66. 9568 ZSrie 68. 1448 INRCT 8.8888 IHRCT 8.8888 IHRCT 8.8888 INFICT 8. GGGG INACT 8.8888 IkRCT 8.8888 INRCT 8.8888 INRCT G.BGGG I t<RCT 8.8888 INRCT 8.8888 FIVG 68.4694 DEW CELLS RHD Z 1 51. 9986 RHD Z2 .58.8968 RHD Z2 58.2293 RHD Z3 52. 5627 RHD Z3 52.8378 RHD Z3 51. 6524 RMD 24 51. 1524 RHD Z4 53.1524 RHD 25 52.3832 RHD 25 51. 8191 INRCT 8.8888 INRCT 8.8888 It<ACT 8.8888 IHRCT 8. 8888 IHFICT 8 ~ 8888 RVG 51.7822 RNBIENT PRESS 14.4888 VAPOR PRESSURE .1988 DRY PRESSURE 55.5288 FLOWS 8.8888 RECORD NUt'1BER - 281 DATE - 56 TINE - 545 PRESSURES 55. 7138 55.7838 RVG 5S. 7888 RTD'S Zirei 68.5488 "ir82 68. 6668 Z lre3 68.6488 Zir84 68 4328

~

Z2rei 68.8828 Z2r82 68.6848 Z2r83 68.7568 Z2r84 68.7388 Z2r85 68.8828 Z2r86 68+6668 Z2r87 68.7828 Z3rel 68.9908 Z3r82 69.8888 Z3r83 68.9988 23r84 68.9368 23r85 68.9188 Z3r86 69.3588 Z3r87 69.8448 Z3r88 69.8268 23r89 69.8448 Z4r01 69.3588 24r82 69.1348 Z4r83 69.1528 Z4r84 69.8988 Z4r85 69.4588 Z4r86 69. 1888 Z4re7 68.9548 24r88 68.9728 Z4r89 69.2688 Z4rle 69.2248 25rel 66.3268 25r82 66.8848 ZSre3 66e8668 Z5r84 66.5248 25r85 6?e2448 25r86 66.5788 25r87 66,6328 Z5r88 66.4528 25r89 66.9388 25rie 68.2888 I NFICT 8.8888 IHFICT 8.8888 IHRCT B. 8888 INRCT G.GOGG I t4FICT 8.8888 INRCT Beeeee INRCT 8.8888 INRCT eo GGGG IHRCT 8.8888 INRCT 8.8888 RVG 68.4618 DEW CELLS RHD Zl 53. 1652 RHD Z2 55.8499 RHD Z2 54. 1148 RHD 23 52.2934 RHD Z3 49.562? RHD Z3 52.6781 RHD 24 53. 1652 RHD Z4 53.3319 RHD ZS 52.3784 RHD 25 51. 9858 IHRCT 8> 8888 IkRCT 8.8888 HRCT 8. 8888 INFICT 8. 8888 INRCT e.eeee RVG 52.7824 RNBIEHT PRESS 14.4888 VRPOR PRESSURE ~ 1972 DRY PRESSURE 55. 5188 ~

FLO4IS 8.8888

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RECORD NUNBER 282 DATE 56 TINE 688 PRESSURES 55. 7118 55. 7818 AVG 55. 7868 RTD'S Zlrel 6S.4868 Zlr82 68 6848 Zir83 68. 6128 Zlr84 6e.46ee'e.6668 Z2rei 68.e288 Z2r82 68. 6388 22r83 68.6848 22r84 Z2r85 68.8828 Z2r86 68.6388 Z2r'87 68.6668 Z3rei 6e.9548 Z3r82 68.9728 Z3r83 68.9548 Z3r84 68.9368 Z3r85 69.8260 Z3r86 69.1348 Z3r87 69.8448 23ree 68.9728 23r89 69.e448 Z4rel 69.3328 Z4r82 69.8988 Z4r83 69.8988 Z4r84 69.8988 Z4r85 69.4228 Z4r86 69.1348 24r87 69.8888 Z4ree 69.eeee Z4r89 69.2688 Z4rle 69.2788 Z5rel 66. 3888 Z5r82 66.ee4e Z5r83 66.8488 Z5re4 66.5868 Z5r85 67.2888 Z5r86 66.5068 ZSr87 66.5788 25ree 66.4348 Z5r89 66.9288 ZSrie 68.1ee0 INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT 8.8800 INACT 8.8888 INACT e.eeee INACT 8.8888 INACT 8.8808 INACT 8.8888 INACT e.eeee FIVG 68.4322 DEN CELLS RHD Zl 48.8863 RHD Z2. 52.9473 RHD 22 51. 9473 RHD Z3 52.6148 RHD Z3 51. 1396 RHD Z3 53.9888 RHD Z4 51 ~ 7e86 RHD Z4 52.1396 RHD 25 52.3575 RHD Z5 51. 5883 INACT 8. 8888 INACT 8.8808 INACT 8.8888 INACT 8 ~ 8888 INACT 8.8888 FIYG 51.9125 ANBIENT PRESS 14. 4888 VAPOR PRESSURE o 1989 DRY PRESSURE 55. 5151 FLOMS 8.8888 8.8888 RECORD NUMBER - 283 DATE 56, TINE 615 PRESSURES 55.7898 55. 6998 AVG 55o7848 RTD'S Zirel 6e.46ee Zir82 6e.6668 Zlr83 6e.5948 Zir84 6e. 3968 Z2rei 6e.7388 Z2r82 68 '388 22r83 6e.7568 Z2r84 6e. 7820 Z2r85 6e.elec Z2r86 68.6668 22r87 6e.64ee Z3rel 6e. 9720 Z3r82 6e.9728 Z3r83 68.9548 Z3r84 6S.9188 Z3re5 6e. 9540 Z3r86 69.2248 Z3r87 69.8268 Z3ree 6e.9988 Z3r89 6~ 0080 Z4rei 69. 3148 Z4re2 69.1348 Z4r83 69.1168 Z4r84 69.8440'e.9728 Z4r85 69.3328 Z4r86 69'348 24r87 6e.9728 Z4ree Z4re9 69.1788 Z4rle 69.2248 25rel 66.2728 Z5r82 66.e4ee Z5r83 66.8388 Z5r84 66.4888 25re5 67.2268 Z5re6 66.4eee ZSr87 66.5688 25ree 66.39ee 25re9 66.9828 Z5rie 6e.0548 INACT G.GGGG INACT 8.8888 INACT 8.8888 INACT 8.8088 INACT B.BGGG INACT 8.8888 INACT 8.8888 INACT G.GGGG INACT 8.8888 INACT . 8.8888 AVG 68o4168 DEW CELLS RHD Zl 54 '681 RHD Z2 55. 7165 RHD 22 53.8242 RHD Z3 53. 8627 RHD Z3 51. 8499 RHD Z3 53.5114 RHD Z4 51.76?8 RHD 24 51.8114 HD Z5 52. 3319 RHD 25 51. 5114 INACT 8; 8888 INACT 8.8880

)ACT e. 8888 INACT 8. 8888 INACT 8.8888 AVG 52.7466 AMBIENT PRESS 14.4eee

( YRPOR PRESSURE- .1969 DRY PRESSURE 55. 58?1 FLOMS Goeeee

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RECORD HUNBER 284 DRTE - 56 TINE - 638 PRESSURES 55. 7868 55. 6969 RUG 55. 7818 RTD'S 21r91 68.4588 2ir82 68.6388 Zir83 68. 5768 Zir84 68. 4140 22r81 68.7298 Z2r82 68.6488 22r83 68. 8468 22r84 68. 6669 22r85 68.8288 Z2r96 68.6669 Z2r87 '68. 6488 Z3r81 6e.9549 Z3r82 68. 9188 Z3r83 68.9368 Z3r94 68. 8648 23r85 6e.9549 23r86 69.8898 Z3r87 69.8888 Z3r88 68. 9548 Z3r99 68.9729 Z4r81 69.2968 Z4r82 69.1888 24r83 69. 8988 Z4r94 69.9269 Z4r85 69.3688 Z4r86 69 '348 Z4r87 68. 9368 Z4r88 68.9540 24r89 69.2248 Z4rlO 69.2968 Z5r81 66. 2368 ZSr82 66.8129 Z5r83 66.7948 Z5r84 66.4788 Z5r85 67. 1548 25r86 66.4799 Z5r87 66.5688 Z5r88 66.3988 Z5r89 66. 9828 ZSriO 6e.lGso INRCT 8.8888 IHRCT 8.8988 IHRCT 8.8889 INRCT 8.9900 IHRCT 8.8888 INFICT 8.8888 IHRCT 8.8898 IHRCT 8.8099 I HFICT 8.8888 INFICT 8.8888 AVG 68. 4816 DEW CELI S RHD Z 1 51. 3319 'RHD Z2 48.3447 RHD Z2 51. 7559 RHD 23 52. 2934 RHD Z3 58.4888 RHD Z3 51. 6148 RHD Z4 53.2678 RHD 24 51.3963 RHD Z5 52 '447 RHD Z5 51. 7293 IHRCT 8.8889 INRCT 9.9998 IHRCT 8. 8888 IHRCT 8.8989 INRCT 8.8888 RUG 51. 4422 RNBIEHT PRESS 14.4888 VFIPOR PRESSURE ale?6 DRY PRESSURE 55.5134 FLOWS Go 8888 RECORD NUNBER - 285 DRTE - 56 TINE 645 PRESSURES 55o7848 55.6948 RVG 55.6998 RTD'S Zlr91 68.4688 Zlr82 68. 6388 21r93 68.5769 Zlr94 68. 3789 Z2r81 68.7568 22r82 68.5768 Z2r83 68.6849 Z2r84 68. 6399 22r85 68.8198 Z2r86 68.6488 22r87 68.6389 Z3r81 68. 9369 Z3r92 68.9998 23r83 68. 9188 Z3r84 68.8829 Z3r85 68.9909 Z3r96 69.2248 Z3r87 68.9729 Z3r88 68.9188 Z3r89 69.9989 Z4r91 69,2789 Z4r82 69.8889 24r83 69.8988 Z4r84 68.9729 24r95 69.2698 Z4r86 69.9988 Z4r87 68.9189 Z4r98 68.9369 Z4r89 69.1529 Z4r18 69+1799 ZSr81 66.2369 Z5r82 66.8129 Z5r83 66.7769 25r84 66.4528 25r85 6?.1369 ZSr86 66.4529 25r87 66.5429 Z5r88 66o3628 25r89 66.8669 Z5rlG 68.9369 INFICT 8.8888 IHRCT Oe8988 INRCT 9.9909 INRCT 9.8909 INRCT 8.8888 IHRCT 8.8888 INRCT 8.9988 IHRCT G. 9900 INRCT 8.8888 INRCT 8.8888 FIVG 68,.3792 DEW CELLS RHD 21 52 '883 RHD Z2 56.7678 RHD Z2 52.4986 RHD 23 54 1911

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RHD 23 53.3447 RHD 23 51. 3968 RHD 24 53.4858 RHD 24 52 7422

~

HD ZS 52.2678 RHD 25 51. 5499 INRCT 8;8888 INFICT 9.8908 RCT G. 8888 IHRCT Ge8888 INRCT 8.8888 RVG 53.8473 FINB IEHT PRESS 14.4888

( VAPOR PRESSURE .1991 DRY PRESSURE 55.4999 FLOWS 8.8888

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RECORD NUI'IBER - 286 DRTE - 56 TINE - 788 PRESSURES 55. 7818 55. 6918 RVG 55. 6968 RTD'S Zlr81 68.4328 Zir82 68.6388 Zir83 68. 5588 Z 1r84 6S. 3688 22rel 68.8188 Z2r82 68.5948 Z2r83 68.7568 Z2r84 68. 5948 Z2r85 68.7568 Z2r86 68.5768 Z2r87 68.6128 Z3r81 68. 9808 Z3r82 68.9888 23r83 68.9188 Z3r84 68.8648 Z3r85 68. 98ee Z3re6 69.2868 23r87 68.9728 Z3r88 68.9188 Z3r89 68. 9368 Z4rel 69.2688 Z4r82 69.8268 24r83 69.8268 Z4r84 69. 8888 Z4r85 69.3588 Z4r86 69.8628 Z4r87 68.8828 24r88 68.9180 Z4r89 69.1788 Z4rie 69. 1788 Z5r 81 66.2888 25r82 66.7768 Z5r83 66.7588 Z5r84 66.4348 Z5r85 67.1548 Z5r86 66.4528 25r87 66.5868 ZSr88 66.3628 Z5r89 66.8488 ZSrle 68.8728 INRCT 8.8888 INRCT 8.8888 INFICT 8.8888 INRCT 8.8808 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT B.eeee INRCT 8.8888 INRCT e.eeee RVG 68. 3677 DEW CEI LS RHD 21 58.4217 RHD Z2 55. 3191 RHD Z2 49.9858 RHD Z3 54.4858 RHD Z3 52.9729 RHD Z3 52.5755 RHD Z4 53.4858 RHD Z4 54.7165 RHD Z5 52.4217 RHD Z5 51. 8968 INRCT 8.8888 INRCT 8.8888 I NFICT 8.8888 INRCT ee 8888 INRCT 8.8888 FIVG 52. 7888 FINBIENT PRESS 14.4888 VRPOR PRESSURE. .1972 DRY PRESSURE 55.4988 FLOWS 8.8888

( RECORD NUMBER 287 DRTE - 56 TINE 715 PRESSURES . 55.6998 55.6898 RVG 55.6948 RTD'S Zlrel 68. 4328 Z ir82 68.5488 Zir83 68.5228 Zire4 68. 3240 22rei 68.?748 Z2r82 68.5768 Z2r83 68 '848 22r84 68. 6128 22rBS 68.7388 Z2r86 68.5588 Z2re? 68 '948 Z3rel 68. 8828 Z3r82 68.9888 Z3r83 68.8648 Z3re4 68.8188 Z3r85 68. 8828 Z3re6 69. 1888 Z3r87 68.9368 Z3r88 68o9188 Z3re9 68. 9548 24rei 69.2688 Z4r82 69.8448 24r83 69.8888 Z4r84 6s. 9908 Z4r85 69. 1528 Z4r86 69.8888 Z4r87 68.8S28 Z4r88 68. 91SB Z4r89 69'1168 Z4r 1B 69. 1528 25rel 66.1828 25r82 66. 7588 Z5r83 66.7228 ZSr84 66.3988 25r85 67.1888 Z5r86 66. 4348 ZSr87 66.4888 Z5ree 66'.3448 ZSr89 66.8388 25r 1 8 68. 2348 I NFICT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 I NFICT 8.8888 INFICT 8.8888 INFICT 8.8888 INRCT 8.8888 INRCT 8.8888 INFICT e.eeee 8VG 68.3467 DEW CELLS RHD Zl 58.3863 RHD Z2 54e6524 RHD Z2 52.2886 RHD Z3 52. 6781 RHD. Z3 49. 3447 RHD Z3 49.8114 RHD Z4 52.7934 RHD Z4 51.5627 HD ZS 52. 5114 RHD Z5 51.4681 INRCT eieeee IN8CT 8.8808 NRCT 8.8888 INRCT 8.8888 INFICT 8.8888 RVG 51.6995 RNSIENT PRESS 14.4888 VFIPOR PRESSURE .1894 DRY PRESSURE 55.5846 FLOWS 8.8888 8.8888

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RECORD HUNBER - 28S DATE 56 TINE ?38 PRESSURES 55. 6968 55.6968 AVG 55.6916 RTD'S Zlrel 6S. 3968 Zlr82 69.5?68 Zir83 6S. 5848 Zir84 6S.3966 Z2rel 6S.?748 Z2r82 66.5768 22r83 6S. 9468 Z2r84 69.5766 Z2r85 6s. 73se Z2r86 66.5488 Z2r87 6S. 5588 Z3rei 6S ~ S646 Z3r82 66.6648 23r83 6S.SS28 23r84 6S. 7928 23r85 6S.S640 23r86 69.8628 Z3r87 66.91SB Z3res 6S. SS28 Z3r89 6S.9969 Z4rel 69.2868 Z4r82 69 '268 Z4r83 6S. 9548 Z4r84 6S.91SG 24r85 69.2428 Z4r86 69.8448 Z4r87 6S. SS28 Z4res 6S.9009 Z4r89 69.1528 Z4rle 69. 8968 Z5rel 66. 164e Z5r82 66.7499 25r83 66.?e4e Z5r84 66.3SGB Z5r85 67. 1888 Z5r86 66.3SGG Z5r87 66+4528 25res 66.38SG 25r89 66. 7948 Z5rle 6S.6999 INRCT 8.8880 INRCT 8.8886 INACT 8. 8888 INACT 8.9969 IHACT 8.8888 IHACT 8.8668 IHACT 8.8888 IHACT 8.6699 IHACT ee8888 INRCT 8.8888 AVG 6S.3242 DEW CE11 S RHD 21 52.8SS3 RHD Z2 47 '65S RHD Z2 52.3863 RHD Z3 51 7676

~

RHD Z3 58.5378 RHD Z3 51. 1811 RHD Z4 52.2558 RHD Z4 52.49SS RHD 25 52.267S RHD Z5 51. 3932 INACT 8.8888 INACT 8.8666 IHRCT 8.8889 INACT 8.8898 INACT 8.8888 AVG . 51. 4127 ANBIEHT PRESS 14.4888 VAPOR PRESSURE .1S?4 DRY PRESSURE 55.5836 FLOWS e.eeee e.eeee RECORD HUNBER - 289 DATE 56 TINE - 745 PRESSURES 55.6948 55+6848 'VG 55. 6998 RTD'S Zirel 6S.4146 Zir82 6S.5488 Zir83 69.4589 Zlr84 6se3240 Z2rel 69.7286 Z2r82 66.5228 Z2r83 6S.64SG 22r84 6S.55S0 Z2r85 6se?746 Z2r96 6S.5498 Z2r87 6S.55SG Z3rei 6S. S646 Z3r82 6S.6648 Z3r83 6S.S468 Z3r84 6S.Slee Z3r85 6S. S106 Z3r86 69.6448 Z3r87 66.9366 Z3res 6S.9649 Z3r89 6S. 9999 Z4rel 69.2248 Z4r82 69,88SB Z4r83 69.8449 Z4r84 6S.9369 Z4r65 69.27SG Z4r86 69.8SBG Z4r87 6S.SS28 Z4res 6S.S469 Z4r89 69.8SBG 24rle 69. 1348 Z5re1 66.12SG Z5r92 66.7640 Z5r83 66.66SB Z5r84 66.3446 Z5r85 6?.8648 Z5r96 66. 3626 Z5r87 66.4526 Z5res 66.3996 25r89 66.7948 25rl8 6S.1266 I NFICT 8.6689 IHRCT 8.8988 INACT Geeeee I NF}CT 8.6666 I HFICT 8~ 9699 INFICT 8.8888 IHRCT 8.8888 IHRCT 6.8600 IHRCT e.eeee INRcT e.eeee FIVG 6S ~ 311S DEW CELI S RHD Z 1 51. 3932 RHD Z2 58.7837 RHD Z2 53.6575 RHD 23 53. 2293 RHD Z3 52.6652 RHD Z3 49.2676 RMD Z4 53.3319 RHD Z4 51.?934 HD Z5 52. 1811 RHD Z5 51. 49SS I HFICT Gieeee IHACT 8. 6966 ACT 8. 8888 INACT .8. 8888 INACT 8+8888 VG 51. 9673 ANBIEHT PRESS 14 '888

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VAPOR PRESSURE .1913 DRY PRESSURE 55.4977 FLOWS 8>> 8888 e.eeee

RECORD NUttDER 218 DflTE 56 TINE - 888 PRESSURES 55'928 55. 6828 RVG 55 ~ 6878 RTD'S 2liel 68'.3868 Zir82 68.5848 Zlr83 68.4868 Zlr84 68. 2888 Z2iel 68. 6488 Z2i82 68.5588 Z2i83 68. 5228 22i84 68.5588 22ie5 68. 7748 22i86 68.5228 22re? 68.5588 Z3rel 68.8648 Z3i82 68.8468 23/83 68.8288 Z3r84 68.7748 Z3r85 68.8648 Z3r86 68.9988 Z3r87 68.9188 Z3~88 68,8648 Z3r89 68.9888 Z4ie1 69.1888 Z4~82 68.9728 Z4r83 69.8888 Z4i84 68.9368 Z4i85 69. 1888 Z4r86 68.9988 24re? 68.8288 24i88 68e8468 Z4/89 69. 1168 Z4r le 69.8888 25i81 66.1468 Z5r82 66 7228 Z5ie3 66.6868 25~84 66.3628 25i85 67. 8288 Z5i86 66.3888 Z5re? 66.4528 ZSr88 66. 3888 Z5r89 66. 8128 Z5r 1 8 68.8728 I t<flCT 8.8888 INFICT 8.8888 INflCT 8. 8888 INflCT Geeeee IN8CT 8.8888 INRCT 8.8888 INRCT 8. BBBB INRCT Geeeee INFICT 8.8888 INflCT 8.8888 flVG 68,2938 DEN CELLS RHD Zl 55.5378 RHD Z2 52.9986 RHD 22 58.3832 RHD Z3 51.8319 RHD Z3 58.8627 RHD 23 56.4858 RHD Z4 58.9986 RHD Z4 52.2837 RHD Z5 52. 1811 RHD Z5 51. 3319 INflCT 8.8888 INflCT Ge8888 I HFlCT 8.8888 INflCT 8.8888 INRCT 8.8888 flVG 52. 3788 flNB I Et3T PRESS 14.4888 VflPOR PRESSURE .1942 DRY PRESSURE 55.4928 FLOWS 8.8888 RECORD NUBBER - 211 DFITE - 56 TINE 815 PRESSURES 55.6898 55. 6888 flVG 55. 6845 RTD'S Zlrel 68+4148 Zli82 68. 5228 Z1 i83 68.4868 Zir84 68. 2888 22ie1 68.6128 Z2i82 68.5228 Z2ie3 68.6848 Z2re4 68. 5488 Z2r85 68. 6848 Z2i86 68.5228 Z2re? 68.5488 23rei 68. 8468 Z3r82 68.8468 Z3i83 68.8288 Z3r84 68.8188 Z3ie5 68. 8648 Z3i86 68,9548 Z3r'87 68.9888 Z3i88 68.8288 23r89 68. 8828 Z4r81 69. 1888 Z4i82 68. 9988 24i83 68.9548 Z4r84 68. 8468 24 85 69;2788 Z4r86 68.9728 24re? 68. 8288 Z4i88 68. 8288 Z4ie9 69.8268 24rie 69.8988 Z5rei 66' 188 Z5~82 66. 6688 Z5i83 66.6580 Z5r84 66.3888 Z5r85 67. 8188 Z5i86 66. 3268 z5/87 66.4168 Z5i08 66 '548 Z5~89 66,7588 Z5rie 67.9188 I NFICT G.GGGG INflCT 8.8888 INFICT 8.8888 INflCT G.GGGG INFICT 8.8888 INflCT 8.8888 INRCT 8.8888 INRCT 8. 8880 INflCT 8.8888 INRCT B.eeee flVG 68.2776 DEW CELLS RQD 21 55.2837 RHD Z2 47.9217 RHD Z2 58. 5114 RHD Z3 53.2558 RHD Z3 53. 1148 RHD Z3 53. 1524 RHD Z4 51.844? RHD Z4 49.1396 HD Z5 52o8883 RHD Z5 51. 3575 INRCT 8; 8888 INRCT 8.8880 flCT e.eeee INRCT eeeeee IN8CT 8. 8888 flVG 51. 7328 flNB I ENT PRESS 14 '888 VRPOR PRESSURE .1896 DRY PRESSURE 55.4949

, FLOWS Bo8888

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RECORD NUNBER - 212 DRTE 56 TINE - 838 PRESSURES 55.6878 55.6778 RVG 55. 6829 RTD'S Zlrei 68.2SSB Zir92 68.5949 Zir93 6S. 4589 Zir64 6S. 2349 Z2r81 68.6488 Z2r92 68.5948 22r83 68. 6488 Z2r84 68.5046 Z2r85 6S.?388 22r86 68.4588 22r87 6S. 5848 Z3rei 6S.8169 Z3r82 68.8189 Z3r83 68.8288 23r84 68. 7749 Z3r65 68.774e Z3r66 69. 1169 Z3r97 6S.8648 Z3reS 6S. 82SB Z3r69 6S.SS2e 24rel 69.1346 Z4r62 68.9728 24r83 6S. 9548 Z4r84 68.91SB Z4r85 69.1168 Z4r86 68.9968 Z4r97 6S. 7748 24reS 68.73S0 Z4r99 69. 8448 Z4r 19 69.8449 25rel 66. 8928 Z5r82 66.6506 Z5r83 66.6148 Z5r94 66.2969 Z5r65 66. 9928 ZSr96 66.36SG Z5re? 66.3989 Z5reS 66.2549 Z5r99 66.7488 ZSrle 68.9186 INRCT 8.'8998 INRCT 8.8698 IHFICT 8. 8888 INRCT 8.9996 INRCT 8.8998 IHRCT 8>>8898 INRCT 8.8888 IHRCT 9.8996 INRCT 8 '688 INRCT e.eeee RVG 68 '598 DEW CELLS RHD 2 1 51. 8755 RHD Z2 49. 1524 RHD Z2 RHD 23 4S. 5627 RHD 23 53.6652 RHD 23 51.8447 Z4 51. 3575 RHD Z4 52.1781 RHD Z5 52.2293 RHD Z5 51. 3575 INFICT'8.3832 RHD INFICT 8. 8868 INFICT 9.9999 INRCT 8.8888 INRCT 8.8888 8.8898 RVG 58.9791

'NBIENT PRESS 14.4888 VFIPOR PRESSURE .1843 DRY PRESSURE 55.4977 FLOWS e.eeoc RECORD NUNBER - 213 DRTE 56 TINE - 845 PRESSURES 55.6948 55.6758 RVG 55. 6795 RTD'S Zlrel 6S. 3429 Z ir82 68. 4148 2 ir83 68.4328 Zlr94 68.2349 22r61 68.5496 Z2r92 6S.S228 Z2r83 68.5946 Z2r84 68.4S69 22re5 68.6128 Z2r86 68.4688 22r67 68.5949 Z3r91 6S>>8196 Z3r92 68.7748 Z3r93 68.7928 Z3r84 68.73SG Z3r95 6S.7749 Z3r86 69.9448 Z3r97 6S.8468 Z3reS 68.7928 Z3r69 6S.S2SG Z4rei 69.1529 Z4r82 68.9369 Z4r63 68.9998 Z4r64 6S.S646 Z4r65 69."1346 24r86 68.9728 Z4r97 6S.8199 Z4rBS 6S.S2SG Z4r99 69.8269 Z4rie 69.8989 Z5rei 66.9748 Z5r82 66.6329 Z5r83 66.5969 25r84 66.2728 Z5reS 66.9748 ZSr66 66.2549 Z5r97 66>>3629 25reS 66.2188 Z5r69 66.7226 Z5rie 67.S926 I NFICT 9.9989 INRCT 8.8988 IHRCT 8.8996 IHRCT 9.6690 INRCT 6.8666 INRCT 8.8988 INRCT 9.9898 INRCT 9.9990 INRCT 8.8889 INRCT 8.8888 FIVG 68.2333 DEW CELLS RHD Zl 51. 9242 RHD 22 58>>BSS3 RHD Z2 51.2422 RHD 23 52. 6909 RHD Z3 51. 8969 RHD Z3 49>>3784 RHD 24 54>>9499 RHD Z4 52. 6396 HD Z5 51. 9729 RHD ZS 51. 1524 IHRCT 8.9999 INRCT G. 8699 RCT B.BBBB IHRCT 8>> 9888 INRCT 8.8889 VG 51. 5933 RMB IENT PRESS 14 '868 c VRPOR PRESSURE ~ 1886 DRY PRESSURE 55.4989 FI OWS 8.8898 e.eeee

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RECORD NUMBER - 214 DFITE - 56 TIME 988 PRESSURES 55. 6828 55.6739 RVG 55.6775 RTD'S Zlrel 68. 3868 Zir82 68. 4868 Zlr83 68. 3968 Z ir84 68. 2349 Z2rel 68. 6128 Z2r82 68.4868 Z2r83 68. 5768 Z2r84 68 4590 Z2r85 68.7828 Z2r86 68.4328 Z2r87 68. 4588 Z3rel 68.8198 23r82 68.?928 23r83 68.7748 Z3r84 68. 7288 23r85 68.?929 Z3r86 68.9548 Z3r87 68.8468 23r98 68.7928 Z3r89 68.8199 Z4rei 69. 1528 24r82 68.9548 Z4r83 68.9888 24re4 68.8469 Z4reS 69, 1528 Z4r86 69.8988 Z4r87 68.7928 Z4r88 6S.?929 Z4r89 69.8888 Z4rie 69.8268 Z5rei 66.8388 Z5re2 66o5969 Z5r83 66. 5788 ZSr84 66.2368 Z5r85 66 '748 Z5r86 66.2549 Z5r87 66.3628 ZSr88 66.2888 Z5r89 66e6868 Z5rle 67.8389 INRCT 8.8888 INFICT 8.8888 INRCT e.eeee IHFICT 8.9990 I HFICT 8.8888 IHFICT 8.8888 INRCT 8.8888 I NFICT 8.9898 I HRCT 8.8898 INRCT 8. 8888 FIVG 68.2224 DEW CELLS RHD Zl 58.9681 RHD Z2 55. 1781 RHD Z2 53.2558 RHD 23 52. 8968 RHD Z3 52.9888 RMD Z3 58.5755 RHD Z4 51. 6811 RHD Z4 52. 3794 RHD 25 51. 8784 RHD Z5 51. 3191 IHFICT 8.8888 INRCT 8.8999 INRCT 8. 8888 IHRCT 8.8888 INRCT 8.8888 RVG 52.2871 RMBIENT PRESS 14.4888 VRPOR PRESSURE ~ 1936 DRY PRESSURE 55.4839 FLOWS 8.8888 RECORD NUMBER 215 DRTE - 56 TIME 915 PRESSURES 55. 6888 55.6788 'VG 55. 6759 RTD'S Zirel 68.2?88 Zir82 68,4688 Zir83 68. 3968 Z1r94 68.1899 Z2rel 68.5768 Z2r82 68. 4149 Z2re3 68. 5228 Z2r84 68.4599 22rGS 68.5949 Z2r86 68.3968 22r87 68.4328 23rei 6S ~ ?740 Z3r82 68.7748 Z3r83 68.7389 Z3r84 68.6848 23r85 68.?e29 Z3r86 69e8448 Z3r87 68.8288 Z3r88 68.7748 Z3r89 ,

6S.8280 Z4rel 69. 1S28 Z4r82 68.9548 Z4r83 68.8828 24r84 6S.9900 24rGS 69.8898 24r86 68.9548 Z4r87 68.7749 24r98 68.7749 24r99 69.8888 24rie 68.9988 25rel 66.8289 ZSr82 66.5789 ZSr93 66.5788 Z5r84 66. 2188 Z5r85 66.9748 25r86 66.2549 25re? 66.3448 25r88 66. 1828 ZSr89 66.6869 Z5r1 8 67.8299 I NFICT 8.9888 IHRCT 8,9898 INRCT 8.9999 INRCT 8.9000 INRCT 8.8888 INFICT 8.8988 INRCT 8.8998 INRCT 8.9990 INRCT 8.8888 INRCT 8.8888 RVG 68.2882 DEW CELLS RHD Z 1 46. 9217 RHD 22 56.2886 RHD 22 51.3832 RMD 23 53.3319 RHD 23 59.9988 RHD Z3 53.4681 RHD Z4 51. 2558 RHD 24 53.0883 RHD Z5 51. 8319 RHD Z5 51. 3191 INRCT 8..8889 INFICT 8.8990 NRCT 8.8889 IHRCT 8.8988 IHRCT 8.8988 RVG 51 9582

~

RMBIEHT PRESS 14.4888 VRPOR PRESSURE ~ 1912 DRY PRESSURE 55.4838 FLOWS 8.8888

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RECORD NUMBER - 216 DATE 56 TINE - 938 PPESSURES 55. 6?88 55. 6688 FIV 6 55.6738 RTD'S Zlrei 68. 3868 Zir82 68.4328 Zir83 68.3788 Zir84 68.19SG Z2rel 68. 5588 22r82 68. 4148 Z2r83 68.5848 Z2r84 '8.432e Z2r85 68. 6388 Z2r86 68.3788 Z2r87 68.4328 Z3r81 68.7928 23r82 68.7928 Z3r83 68.7288 23r84 68.6848 Z3r85 68.?028 Z3r86 68 '888 Z3r87 68.7928 Z3r88 68.7568 Z3re9 68.7928 Z4rei 69. 1168 Z4r82 68.9888 Z4r83 68.8468 Z4re4 68.7928 Z4r85 69o8988 Z4re6 68.9548 24r87 68.7388 Z4r88 68.7569 Z4r89 69 F 8888 Z4rle 68.9988 Z5rel 66.8828 Z5re2 66.56GG Z5r83 66.5688 Z5r84 66.2888 Z5r85 66.9828 Z5r86 66.2548 Z5re7'NACT 66.3268 Z5r88 66.1648 25r89 66.6588 Z5rie 67.7848 Greece INACT B.BGBB INACT 8.8888 INACT 8 BBGG

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INACT 8.8888 INACT 8.8888 INACT 8 ~ 8888 INACT B.BBGG INACT 8.8888 INACT 8.8888 AVG 68 '817 DEW CELLS RHD Z1 51. 3575 RHD Z2 49.6811 RHD Z2 51. 9681 RHD Z3 58o8242 RHD Z3 49.2837 RHD Z3 58 '863 RHD Z4 51.3447 RHD 24 51.6811 RHD Z5 51. 9473 RHD Z5 58.9729 INACT 8. 8888 INACT B.BGGG INFICT 8.8888 INACT 8.8888 INACT e.eeee FIVG 58. 8646 AMBIENT PRESS 14.4eee VAPOR PRESSURE ~ 1835 DRY PRESSURE 55.4895 FLOWS e.eeee e.eeee RECORD NUMBER 217 DATE - 56 TINE - 945 PRESSURES 55.6758 55.6668 RVG 55.6785 RTD'S Zlrel 68. 2168 Z lre2 68.3688 Zlre3 68. 3428 2 lr84 68. 2340 Z2rel 68.6388 Z2r82 68 '588 Z2r83 68.4588 Z2r84 68.4588 Z2r85 68.6668 Z2r86 68.3968 Z2r87 68.4588 Z3rei 68.7280 Z3r82 68.7828 23r83 68.7828 Z3r84 68.6488 Z3r85 68.7288 Z3re6 69.8628 Z3re7 68.7928 Z3re8 68.7388 Z3r89 68.7928 Z4rel 69.8448 24r82 68.9188 Z4r83 68.8648 Z4r84 68.7928 Z4r85 69.8988 Z4r86 68.9188 24re? 68.7388 Z4rGS 68.6848 Z4r89 68.9988 Z4rle 69.8888 Z5rel 65.9848 Z5r82 66.5608 Z5r83 66.5248 25r84 66.2888 Z5r85 66.9288 ZSr86 66.2880 Z5r87 66.3888 Z5r88 66. 1468 Z5r89 66.6688 Z5rie 67.6768 I NFICT 8.8888 INACT 8. 8888 I NFICT 8.8888 INACT 8.8880 INACT 8.8888 INACT e.eeee INACT 8.8888 INACT 8.8888 INACT 8.8888 INACT B.GBBB AVG 68.1724 DEW CELLS RHD Zl 57.9858 RHD Z2 52.6268 RHD 22 52.2558 RHD Z3 49. 6268 RHD 23 58.5755 RHD 23 51 ~ 9345 RHD Z4 52.6268 RHD Z4 52. 2293 HD Z5 - 51. 9345 RHD Z5 51 o 1268 INACT 8 8888 INACT G.GGGG NACT 8.8888 INFICT 8. 8888 INACT 8. 8888 AVC 52o3821 RNB IENT PRESS 14.4888

( VAPOR PRESSURE .1937 DRY PRESSURE 55.4768 ~

FLOWS 8.8888 Gaeeee

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RECORD NUMBER 218 DRTE 56 T I ME 1888 PRESSURES 55. 6748 55.6648 RVG 55. 6699 RTD'S Zlr81 68.2528 Zir82 68.3968 2ir63 68.3248 Zlr84 68. 2169 Z2r81 68. 4148 Z2r82 68.3968 22r83 68.4868 Z2r84 68. 3786 Z2r85 68.5948 Z2r86 68.3786 Z2r87 68.3968 Z3r81 68. 7209 23r82 68.7828 Z3r83 68.7828 Z3r84 68.6488 Z3r65 68.6669 23re6 68.8828 Z3r87 68.7748 Z3r88 68.7288 23r89 68.7740 Z4r81 69.8888 Z4r82 68.8468 24r83 68.8648 Z4r84 .68. ?560 Z4r85 69.1888 24r86 68. 9368 24r87 68. 7748 Z4r88 68.7629 24r89 68.9366 Z4rlG 68.9969 Z5r81 65. 9486 Z5r82 66.5426 Z5r83 66.5248 Z5r84 66. 1648 Z5r85 66.8849 25r66 66.1469 Z5r87 66.2728 25r68 66.1188 Z5r69 66.5968 Z5r18 67.5686 INFICT 8.8888 INRCT Bo8886 INRCT 8.8888 INFICT 9.9660 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.9606 INRCT 8.8888 INRCT 8. 8888 RVG 68.1417 DEW CELLS RHD Zi 52.4729 RHD Z2 49. 1989 RHD Z2 52.2886 RHD Z3 51. 6114 RHD 23 58.3968 RHD Z3 51. 2558 RHD 24 51. 2559 RHD 24 56.7866 RHD Z5 51. 9729 RHD Z5 51. 1781 INRCT 8. 8888 INRCT 9.9009 INRCT 6.9669 INRCT 8.8888 INRCT 8. 8886 RVG 51.1978 AMBIENT PRESS 14.4888 VRPOR PRESSURE E1859 DRY PRESSURE 55.4831 FLOWS 8.8888 tt RECORD NUMBER 219 DRTE - 56 TIME - 1815 PRESSURES 55.6718 55.6628 AVG 55.6665 fi RTD'S Zlr81 68. 2888 Zir62 68. 3788 Z 1 r 83 68. 3248 Zlr64 68.1446 Z2r81 68.4688 Z2r82 68.3968 22r83 68. 5229 Z2r84 6S.3660 22r85 68.5949 Z2r86 68. 3966 Z2r97 68. 3968 23r61 6S. 7206 Z3r92 68.7268 Z3r83 68,6848 Z3r84 68. 6388 Z3r95 68.7920 Z3r66 68.8468 Z3r87 68.7566 Z3r88 68.7266 23r89 68. 7566 Z4r81 69.8628 Z4r82 68 8189

~ Z4r93 68.8188 Z4r64 68 '560 Z4r85 69. 1166 Z4r96 68.9369 24r87 68.7569 Z4rGS 68.?206 Z4r99 68.9888 Z4r18 68.9548 25r61 65o9488 Z5r82 66.5240 25r 83 66.4889 25r84 66. 1288 25r85 66.9926 Z5r86 66.1649 25r87 66.2728 Z5r88 66. 8928 Z5r89 66.5968 25rlG 67.5560 INACT 8.8886 INRCT 8~ 8688 INFICT 8.8968 I NFICT 9.6069 INRCT 8.8889 INRCT 8.8898 INRCT 8.8889 I NFICT 9.9990 INACT 8.8888 INRCT 8.8888 RVG 68.1373 DEW CELLS RHD Zi 53.8319 RKD Z2 53.6396 RHD Z2 48.3832 RHD Z3 50. 2165 RHD Z3 51.8499 RHD Z3 58.4888 RHD Z4 58+4858 RHD Z4 54.35?5 RHD Z5 5 1 ~ 6524 RHD Z5 51. 2678 INRCT 8, 8888 INRCT Go6999 NRCT 8.8888 INRCT 8. 8888 INRCT 8.8888 RVG 51.5356 AMBIENT PRESS ia.ae66 VRPOR PRESSURE ~ 1882 DRY PRESSURE 55. 4783 FLOWS Bo8888

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RECORD NUMBER - 228 DRTE - 56 TIME 1838 PRESSURES 55.6698 55. 6598 RVG 55.6648

(~ RTD'S Zlrei Z2rei

68. 1988 6S.5228 Zir82 Z2r82 6S.3688

68. 3788 Zlr83, Z2r83 6S. 2888 Zlr84

68. 3968 22r84 6S. loco 6S. 4328 Z2r85 6S.5768 Z2r86 68.3688 Z2r87 68. 3688 Z3rei 68. 6S48 Z3r82 6S.7828 Z3r83 68.6668 Z3r84 68.64SG Z3r85 6S ~ 64SG Z3re6 6S.8828 Z3r87 68.7568 23reS 68.7828 Z3r89 68. 7388 24rel 69.8268 Z4r82 68.8188 24r83 68.?928 Z4r84 6S. 82SG 24r85 69.1348 24r86 68.91SG Z4r87 68.7828 Z4reS 6S.6668 Z4r89 68.9988 24rle 68.9988 Z5rei 65.9388 Z5r82 66.4SSG 25r83 66.4788 Z5r84 66.1188 Z5r85 66.8388 Z5r86 66.1180 Z5re7 66.2548 Z5reS 66.8928 ZSre9 66.5968 Z5rle 67.4788 IHRCT Goeeee IHRCT 8.8888 IHRCT 8.8888 INRCT 8.8888 I HFICT 8.8888 IHRCT 8.8888 IHRCT 8.8888 IHRCT G.eeee IHRCT 8+8888 INRCT Geeeee RVG , 68. 1172 DEW CELLS RHD Zl 48.6989 PHD Z2 53.8447 RHD 22 52.7678 RHD Z3 49'811 RHD 23 58.9986 RHD Z3 52.3832 RHD 24 51. S191 RHD Z4 52. 9S58 RHD Z5 51 o 5114 RHD Z5 51. 1811 INFICT 8.8888 INRCT G.GGGG INRCT 8.8888 INFICT 8. 8888 INRCT 8.8888 RVG 51.5256 FIMB I EHT PRESS 14.4888 VRPOR PRESSURE .18S1 DRY PRESSURE 55.4759 FLOWS 8.8888 RECORD NUMBER 221 DFITE - 56 TIME - 1845 PRESSURES 55. 6668 55. 6578 FIVG 55.6615 RTD'S Zirel 6S. 2168 Z ir82 68.3428 Zir83 68.2888 Zire4 68.1628 22r01 6S.46ee Z2re2 6S.3428 Z2re3 68.3968 Z2re4 68.3608 Z2r85 6S.5768 Z2re6 68.3428 Z2r87 68.3688 Z3rel 68.6668 Z3re2 6S.6488 Z3r83 68.6668 Z3re4 68.6388 Z3r85 68.6660 Z3re6 6S.8468 Z3r87 68.7388 Z3reS 68.6668 Z3re9 68.7288 Z4r01 69.88SG Z4r82 68.8288 Z4r83 68.7928 24re4 6S.7568 Z4r85 69.GS00 Z4re6 68.9888 Z4re7 68.7388 Z4reS 68.6848 Z4re9 6S.9368 Z4rle 68.9728 Z5rei 65.9128 25r82 66.4788 Z5r83 66.4528 ZSr84 66.8928 ZSr85 66.S388 25r86 66.8928 Z5re7 66.2188 Z5reS 66.8388 Z5r89 66.5688 Z5rle 67.4428 IHRCT 8.8888 INRCT 8.8888 INRCT 8.8888 IHRCT 8.8888 I HFICT 8.8888 INRCT 8.8888 IHRCT 8.8888 IHRCT 8.8808 INRCT 8.8888 INRCT 8.8888 Fl VG 68.89S9 DEW CELLS RHD Z 1 52. 6781 RHD 22 53.4858 RHD 22 58.5499 RHD Z3 47. 7165 RHD 23 53.3863 RHD Z3 58.9729 RHD 24 52. 2165 RHD Z4 58.8863 D 25 51+5114 RHD Z5 51. 2165 IHRCT 8.8888 IHRCT 8.8808 RCT e.eeee INRCT 8. 8888 IHRCT 8.8888 FIVG 51. 4619 FIMB IENT PRESS 14.4888 VRPOR PRESSURE .1877 DRY PRESSURE 55.4738 FLOWS 8.8888

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RECORD HUNBER - 222 DFITE 56 TINE - 1188 PRESSURES 55. 6648 55.6558 RVG 55s6595 RTD'S Z1rel 68. 2528 Zir82 68.3688 Zlr83 68.2348 Zir84 68.1449 Z2rei 68.5489 Z2r82 68.3248 Z2r83 68.4688 Z2r84 68.3249 Z2r85 68.5948 Z2re6 68.3248 Z2r87 68.3428 Z3re1 68. 6399 Z3r92 68.6488 Z3r83 68.6388 23r84 68.5768 Z3r95 68 '489 23r86 68. 8828 23re7 68.6848 23r98 68.6668 Z3r99 68.?209 Z4rel 69.8889 Z4r82 68.7928 Z4r83 68.7928 Z4r94 68 8828 24r85 69. 1168 Z4r86 68.8829 Z4r87 68.6848 Z4r88 68.6489 Z4r89 68. 9188 24r 1 8 68.9888 Z5rei 65.8948 Z5r82 66.4529 25r83 66.4168 ZSre4 66.8748 Z5r85 66.8128 25r86 66.1199 25r87 66. 2188 Z5r88 66.8288 Z5r89 66.5428 ZSrle 67.3889 INRCT 8. 8898 IHRCT 8.8888 IHRCT 8. 8898 IHFICT 8 ~ 9000 I t<RCT 8.8989 INRCT 9.8888 INRCT 8. 8898 INRCT 8.9990 INRCT 8.8888 IHRCT 8.8888 RVG 68.8989 DEW CELLS RHD Z 1 51. 6148 RHD Z2 44. 8319 RHD Z2 54.5378 RHD ?3 49.8784 RHD Z3 52. 8114 RHD Z3 52. 1524 RHD Z4 59.6652 RHD 24 52.9988 RHD Z5 51. 4858 RHD Z5 58.8447 INRCT 8.8889 IHRCT 9.9999 I NFICT 8 ~ 8988 INRCT 8.8888 IHRCT 9.8888 RVG 51.8751 RNBIEt<T PRESS 14.4888 VRPOR PRESSURE . 1858 DRY PRESSURE 55. 4745 FLOWS 8.8888 RECORD NUNBER 223 DRTE - 56 TINE 1115 PRESSURES 55.6618 55.6528 RVG 55. 6565 RTD'S Z lrei 68. 1628 2 ir82 68 ~ 2888 Zir83 68. 2799 Zir94 68. 9729 Z2rei 68.4328 Z2r82 68.3868 Z2r83 68. 3969 Z2r84 68.3249 22rGS 68.5489 Z2r86 68.2888 Z2r87 68. 3249 Z3rel 68.6669 Z3r82 68.6390 Z3r83 68 '948 Z3r84 68.5948 Z3r95 68.5769 23r06 68.9549 Z3r97 68.6848 Z3r98 68.6489 Z3r99 68 '929 24rel 68.9998 24r82 68.8188 Z4r93 68.7568 Z4r84 6$ 82oe Z4re5 68.9988 Z4r86 68.8828 Z4r97 68.6489 Z4r98 68. 6309 Z4r89 68.9989 24rle 68.8468 Z5rei 65.8589 ZSr92 66.4349 Z5r93 66.3988 Z5r84 66.8568 Z5r85 66..7589 Z5r96 66.9929 ZSr87 66.2999 Z5r88 66.8288 ZSr89 66.5969 Z5rie 67.5149 INRCT 9.8989 IHRCT 8+8888 IHRCT 9.8899 INRCT 9.9099 INRCT 8.8998 IHRCT 8 ~ 8888 INRCT 8.8889 I NFICT 8.9999 IHRCT 8.8889 INRCT e.eeee RVG 68.8666 DEW CELLS RHD Zl 49 '575 RHD Z2 49.53?8 RHD Z2 53.8499 RHD Z3 53.8447 RHD 23 59. 1149 RHD Z3 53.8755 RHD Z4 59.8319 RHD 24 52.6268 RHD Z5 51. 5755 RHD Z5 58.8447 IHRCT 8;8899 INRCT 8.9099 RCT G. 8989 INRCT 8.8888 IHRCT 8.8888 VG 51. 4552 RNB I EN 7 PRESS 14.4888

( VRPOR PRESSURE- .1877 DRY PRESSURE 55.4688 FLOWS G.eeee

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RECORD NUNBER 224 DATE - 56 TINE - 1138 PRESSURES 55. 6598 55.6588 AYG 55.6545 RTD'S Zirel 68.1628 Zlr82 68. 3968 Z lr83 68. 2349 Zlre4 68.1989 22rei 68.4588 Z2r82 68.2?88 Z2r83 68.3248 Z2re4 68.3609 22r85 68.5228 22r86 68.3868 Z2r87 68.3248 Z3rel 68.6129 Z3r82 68.6128 Z3r83 68.5948 Z3r84 68.5948 Z3r85 68.7929 Z3r86 68.8288 Z3r87 68.6488 23re8 68.6388 Z3r89 68.6489 24rel 69.8888 Z4r82 68.7568 'Z4r83 68.7289 Z4r84 68.6669 24r85 69.8888 Z4r86 68.8648 Z4r87 68.6488 Z4r98 68.6480 Z4r89 68. 9188 Z4r 1 8 68.9888 Z5rel 65.8488 25r82 66.3989 ZSr83 66.3888 Z5r84 66.8288 25r95 66.7768 Z5r86 66.9569 Z5r97 66. 1828 Z5r88 65.9848 Z5r89 66.4888 Z5r 1 8 67.4969 INACT 8.8888 INACT 8.8888 IHFICT 8. 8888 IHFICT 8~ 9990 INACT 8.8888 INACT 8.8888 IHACT 8. 8888 I HFICT 8.9909 IHACT 8.8888 INRCT 8.8888 AYG. 68.8515 DEW CELLS RHD Zl 52.7934 RHD Z2 49.5242 RHD Z2 52. 8114 RHD 23 52.7550 RHD Z3 49o8378 RHD Z3 53.8114 RHD Z4 58.8968 RHD 24 51.4345 RHD Z5 51 ~ 4345 RHD Z5 58.?6?8 IHACT 8.8888 INFlCT 8.9999 INACT 8. 8888 INACT 8+8888 IHACT 8.8888 AVG 51.3534 ANBIEHT PRESS 14.4889 VAPOR PRESSURE .1869 DRY PRESSURE 55.4676 .

FLOWS 8.8888

( RECORD HUNBER - 225 DATE - 56 TINE 1145 PRESSURES 55.6568 55.6488 AVG 55.6528 RTD'S Zirel 68.1888 Zlr92 68.3249 Zlr83 68. 2349 Zir94 68.1089 Z2rei 68.4SBB Z2r82 68.2889 Z2r83 68.3428 Z2r94 68.2709 Z2r95 68.5588 Z2r86 68.2528 Z2re? 68.3869 23rel 68.5949 Z3r82 68. 6128 Z3r83 68.5769 Z3r94 68.5489 Z3re5 68.5589 23r86 68.8468 Z3re? 68.6668 Z3r98 68.5949 23r99 68.6489 Z4rel 68.9548 Z4r92 68.7299 24r83 68. 7289 24r94 68.7928 Z4re5 69.8628 Z4r86 68.8288 Z4r87 68. 6128 Z4r88 68.5949 24re9 68. 9189 Z4r 18 68.8828 Z5rel 65. 8949 25r92 66. 3890 25r83 66.3628 Z5r84 66.8828 Z5r85 ee.?499 ZSree 66.9389 Z5r87 e6.164e ZSre8 65.9668 Z5r89 66.4799 25rle 6?.3700 INACT 8.8999 INACT 8.8888 INACT 8.9899 IHACT B.oooo I HFICT 8.8888 IHFICT 8.9999 INACT 8.9998 IHACT 9.9999 IHACT 9+8998 INACT 8.8888 AVG 68.8313 DEW CELLS RHD Zi 51. 8447 RHD Z2 52.4345 RHD Z2 59. 1989 RHD 23 59.3447 RHD Z3 51. 3784 RHD Z3 49.8755 RHD 24 51. 6396 RHD Z4 52. 7165 D 25 51.5755 RHD Z5 58.6652 IHACT 8.8888 IHACT 9. 9998 (ACT 8. 8888 INACT 8.9888 IHACT 8.8888 AVG 51.1925 At1B IENT PRESS 14.4888 VFIPOR PRESSURE ~ 1858 DRY PRESSURE 55. 4662 ~

FLOWS 8+8888

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RECORD NUNBER - 226 DATE - 56 TINE - 1288 PRESSURES 55.6548 55.6458 AVG 55. 6495 R TD'S Zlre1 6S. 18SG Zlr82 6S. 2SSG Z1r83 6S. 2168 Zlr84 6S. 8728 Z2rei 6S.37SG Z2r82 6S.2528 Z2r83 6S. 4328 Z2r84 6S.2528 Z2r85 6S.46SG Z2r86 6S.2348 Z2re? 6S. 2SSB Z3rel 6S.5768 Z3re2 6S.6128 Z3r83 6S.55SG Z3r84 68.5228 Z3r85 68.55SG Z3r86 6S.7928 Z3r87 6S.6388 Z3rGS 6S.5948 Z3r89 6S.6388 Z4rel 6S.9728 Z4r82 6S.7568 Z4r83 6s.?e2e Z4r84 68.5948 Z4reS 6S.9548 Z4r86 6S.S2SG Z4r87 6s.63ee Z4reS 6S 5948 Z4r89 6S. Slee 24rie 6S.S468 25rel 65.S848 Z5r82 66.3448 Z5r83 66.3268 Z5r84 65.9668 Z5r85 66.7488 Z5r86 66.8388 Z5r87 66. 1468 Z5reS 65.9388 Z5r89 66.4788 Z5rle 6?e29SG INACT 8. 8888 INACT 8.8888 INACT 8.8888 I NFICT G.GGGG INACT 8.8888 INACT 8 ~ 8888 INACT B. 8888 INACT G.GGGG I NFICT e.eeee INACT'S.BBS2

8. 8888 FIVG DEW CELLS RHD Zi 54. 17S1 RHD Z2 52. 4S5S RHD 22 58.49S6 RHD 23 53. 3S32 RHD Z3 49.98SS RHD Z3 48 ~ 5SS3 RHD Z4 51. 7558 RHD Z4 52e4729 RHD Z5 51. 5499 RHD Z5 58+8447 INFICT G. 8888 I NFICT 8.8808 INACT 8 8888 F INFICT 8.8888 INACT 8. 8888 AVG 51.56SS AMBIENT PRESS 14.4888 YAPOR PRESSURE .1SS5 DRY PRESSURE 55.4618 FLOWS 8.8888 8.8888 RECORD NUNBER 227 DATE 56 TINE 1215 PRESSURES 55.6518 55.6428 AVG 55. 6465 RTD'S Zlrel 6S. 1448 2ire2 68.2528 Zlr83 6S.2168 Zlr84 6S. 8188 Z2rel 6S.37SG Z2r82 6S.2528 Z2r83 6S.3868 Z2re4 68. 2348 Z2r85 6S.5848 22r86 68.2348 22r87 6So2788 Z3rel 6S. 55SG Z3re2 6S.55SG Z3r83 6S.5488 23re4 6S.5848 Z3r85 6S.5220 Z3r86 6S.S648 23re7 6Ss 6128 Z3reS 68.55SG Z3r89 6S.6128 Z4rel 6S.9368 Z4re2 6S.7828 Z4r83 6S.7288 Z4r84 6S.7208 Z4r85 6S.9548 24r86 6S.Slee Z4r87 6S.612e Z4reS 6S.5488 24r89 6S.S2SG Z4rle 6SoS188 Z5rel 65.7588 25r82 66.3268 Z5re3 66.3GSG Z5r84 65.94SG 25re5 66.66SG Z5r86 65.9668 Z5r87 66.8928 Z5res 65.9128 Z5r89 66. 4168 Z5r 1 8 67.3168 I NFICT 8 8888 I NFICT

~ eoeeee INFICT G. 8888 I NFICT 8.8808 INACT 8.8888 INACT 8.8888 INACT 8. 8888 I NFICT G.GGGG INACT 8.8888 INACT 8.8888 AVG 67.9S94 DEW CELLS RHD 21 54.48SS RHD Z2 49.5499 RHD Z2 52.267S RHD Z3 52. 6781 RKD Z3 51. S447 RHD Z3 52.2934 RHD 24 58.4S5S RHD Z4 52.3191 HD 25 51. 4473 RHD Z5 58. 6148 I NACT 8.8888 INACT 8.8808 NACT e. eeee INFICT 8. 8888 INACT 8.8888

. AVG 51.75S4

( ANB I ENT PRESS 14e4888 YAPOR PRESSURE .189S DRY PRESSURE 55.4567 FLOWS e.eeee

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RECORD HUNBER 228 DFITE <<56 TINE - 1236 PRESSURES 55. 6498 55.6488 RYG 55.6445 RTD'S Zlrei 68.8366 Zlr82 68.2346 Zlr63 68.2168 Zlr84 67. 9826 Z2rei 68.3688 Z2r82 68.2168 Z2r63 68.3428 Z2r64 68.2766 Z2r85 68.4328 Z2r86 ..68. 1988 Z2r67 68.2528 Z3rel 68.5760 Z3r82 68.5768 Z3r83 68.5486 Z3r84 68.4868 Z3rGS 68.5040 Z3r86 68.8288 Z3r87 68.5948 Z3r88 68 '768 Z3r69 68.5946 Z4rei 68. 9188 Z4r82 68.7828 24r63 68.7828 Z4r84 68.6840 Z4r85 68.9668 Z4r86 68.8186 Z4r67 68.6128 Z4r88 68.5400 Z4r89 68.7928 Z4rle 68.7748 Z5rel 65.?328 Z5r82 66.3260 Z5r83 66.2728 Z5r84 65.9388 Z5r85 66. 7848 Z5r86 66.6620 Z5r67 66.8748 Z5r88 65.8948 Z5r89 66. 3888 Zsrle 67.2860 INRCT 8~ 8888 INRCT 8.8888 INFICT 8. 8888 INACT 6.6606 IHRCT 8.8888 IHRCT 8.8888 IHRCT 8. 8886 INRCT 8.6600 IHRCT 8 ~ 8888 INFICT 8.8868 AVG 67.9744 DEW CEI LS RHD 21 55.8832 RHD 22 58. 1396 RHD Z2 58.7422 RHD 23 51.6396 RHD 23 52.2866 RHD 23 52.8447 RHD 24 58.7293 RHD Z4 49.8663 RHD Z5 51. 1652 RHD Z5 58.7837 INRCT 8.8888 INRCT 6.6800 INRCT 8. 8868 INRCT 8.8688 INRCT 8.6888 FIYG 51.5782 RNBIEHT PRESS 14.4866 VRPOR PRESSURE .1885 DRY PRESSURE 55.4568 FLOWS 8.8886 RECORD NUNBER 229 DATE - 56 TINE - 1245 PRESSURES 55. 6478 55.6388 RVG 55.6425 RTD'S Zlrel 68. 8366 21r82 68. 1268 21r63 68. 1268 Zir64 67. 9820 22rei 68. 1986 Z2r82 68. 2166 Z2r83 68. 3668 22r64 68. 2520 Z2r85 68.4326 Z2r66 68.2168 22re? 68. 1888 Z3rel 68.5406 Z3r82 68.5586 23r83 68.5228 23r84 68.4868 Z3r85 '68.S586 Z3r66 68. 6848 Z3re? 68.5948 Z3r88 68.5228 Z3r89 68.5940 Z4rel 68. 9188 Z4r62 68.6848 Z4r83 68.6668 Z4r84 68.7206 Z4r85 68. 9728 Z4re6 68.7568 24re? 68.6488 Z4r68 68.5580 24r89 68. 8288 24rle 68.7928 Z5rel 65.7146 Z5r62 66.3080 25r83 66.2548 Z5r64 65.9128 Z5r65 66.6688 Z5r66 65.9366 Z5r87 66.8388 25r88 65.8588 25r89 66.3626 25rle 67.1726 INRCT Goeeee INRCT 8.8688 INRCT 8.8686 IHRCT 6.6660 IHRCT 8. 8866 IHRCT 8.8888 INFICT 8.8888 I HFICT 8.6666 IHRCT 8.8888 INRCT 8.8888 RYG 67.9498 DEW CELLS RHD 21 48.5755 RHD Z2 52.9986 RHD 22 53.9858 RHD 23 51.8319 RHD Z3 seo8663 RHD 23 58.7293 RHD 24 58 8883 RHD Z4 56 '934 HD Z5 51 4217

~ RHD 25 51 ~ 2165 I NRCT 8.8868 IHRCT 6.6606 NRCT e.eeee IHRCT 8.8888 IHRCT 8. 8888 RVG 51 ~ 2211

( RNBIEHT PRESS 14. 4888 VRPOR PRESSURE .1868 DRY PRESSURE SS.4S6S FLOWS 8 8888

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RECORD NUI1BER 230 DATE 56 TINE - 1309 PRESSURES 55.6440 55. 6350 RVG 55. 6395 RTD'S 21rei 68o0540 Zir82 68.1620 Zlr03 68. 1260 Zir84 67. 9199 Z2rei 68.2888 Z2r82 68. 1980 Z2r03 68.2880 22r84 68.1899 Z2r05 68. 4140 Z2r06 68. 1800 Z2r07 68. 1980 Z3rei 68.5940 Z3r02 68. 5048 Z3r03 68. 5040 Z3r04 68.4500 Z3r05 68.5229 Z3r06 68.7200 Z3r87 68.5760 Z3r88 68.5480 Z3r09 68.5949 24rei 68.8460 24r92 68.?828 Z4r03 68.6380 Z4r04 68.7290 Z4r05 68.9360 24r86 68.7740 Z4r07 68 '948 Z4r88 68.5400 Z4r09 68. 7920 24rie 68.7560 ZSrei 65.6968 25r82 66.2729 Z5r03 66.2369 ZSr84 65.8940 Z5r95 '66.6680 Z5r86 65.9669 Z5re? 66.0380 Z5r08 65.8408 Z5r09 66.3440 Z5rie 6?.2629 I NFICT 8.0008 INFICT Gseeee INRCT 8.0000 INRCT 8.9999 INRCT 0.0000 INRCT 8.0900 INRCT 0.8000 INRCT 0.0990 INRCT 0.0080 INRCT 0.8080 FIVG 67. 9378 DEW CELLS RMD Zl Seo9345 RHD 22 50.4473 RHD Z2 50.9858 RHD 23 49.0370 RHD 23 49.4345 RHD 23 52.4729 RMD 24 51. 9601 RHD Z4 52; 6524 RHD 25 51. 3832 RHD 25 50. 921 7 I NRCT 0. 0000 I NFICT 0. 0090 INRCT Geeeee INRCT 0. 0000 INACT 8. 0800 FIVG 51. 0258 AflBI ENT PRESS 14. 4000 VRPOR PRESSURE ~ 1847 DRY PRESSURE 55. 4548 FLOWS e. eeee RECORD NUNBER 231 DATE - 56 TINE 1315 PRESSURES 55.6420 55.6330 RVG 55.6375 RTD'S Zirel 68 0009 Zir02

~ 68. 1888 Z ir03 68. 1268 Zir84 67. 8929 Z2rel 68. 3240 Z2r02 68. 1980 Z2r 03 68.3240 Z2r04 68.1440 Z2r05 68. 4680 Z2r06 68. 1889 Z2r87 68.1980 Z3rel 68.5220 23r02 68.4680 Z3r03 68.4868 23r04 68.4509 Z3r05 68.4869 23r06 68.7299 Z3r87 68.5580 Z3r98 68.5949 Z3r99 68.5769 24rel 68.8460 Z4r82 68.6669 Z4r03 68.6120 Z4r04 68.5940 24r05 68.8820 Z4r06 68.7388 Z4r07 68.5400 24r08 68.594e Z4r09 68.8100 Z4rie 68.7389 Z5rel 65.6680 Z5r92 66.2360 Z5r03 66.2180 Z5r04 6S.8580 Z5r85 66'140 ZSr96 65.9399 Z5r07 66.0209 25r08 65.8228 Z5r89 66.3268 ZSrle 67.2620 I NFICT 0.0000 INRCT 0.0800 INRCT ~

8.9009 INRCT 0.9999 INRCT 0.0009 INRCT 0.0808 INRCT 0.0099 INRCT 9.9999 INRCT 0. 0000 INRCT 8.0888 RVG 67. 9208 DEW CELLS RHD Zi 52. 3191 RHD 22 47.5499 RHD Z2 49.2837 RHD 23 49.1268 RHD 23 50.7934 RHD 23 52+2550 RHD Z4 51. 2037 RHD Z4 49.1268 HD 25 51. 3575 RHD 25 50.5242 INRCT 0.0080 INRCT 9.9990 NACT 8.0000 INRCT 0.0000 INRCT 0.0000 RVG 50.3502 FlNB I ENT PRESS 14.4000 VRPOR PRESSURE .18ee DRY PRESSURE 55.4575 FLOWS 8.8000

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- - 4j RECOPD NUMBER -.232 DFITE 56 TIME 1338 5 ~

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PRESSURES 55.6398 55. 6318 RYG 55. 6358 RTD'S Zlrel 6S. 9548 2lr82 68.1628 Zir83 68. 1268 Zir84 67. 91'0<'8.

Z2rel 68.2348 Z2r82 68 1898 Z2r83 F 68. 3248 Z2r84 1/29 .

Z2r85 68.4328 Z2r86 68.1988 Z2r87 68.1888 Z3rel 68.5g49 Z3r82 68.4868 Z3r83 68.4688 Z3r84 68.4328 Z3r85 4890

'8.

Z3r86 68.6668 Z3r87 68.5228 Z3r88 68.4868 Z3r89 68. 5465 Z4rel 68.8288 Z4r82 68.6488 Z4r83 68.6388 Z4r84 68.55se.'.

Z4r85 68.9548 Z4r86 68,7568 Z4r87 68.5488 Z4ree 68.486+:: ',

Z4r89 68.7388 Z4rle 68.7388 Z5rel 65.6428 25r82 66. 2189ji Z5r83 66. 1828 25r84 65.8488 Z5r95 66.5968 Z5r96 65 9120~

~

25r97 65.9848 Z5ree 65.8848 Z5r89 66.3888 25r1 8 67. 2269 ".

IHRCT 8.8888 INFICT eeeeeo IHFICT 8.8888 INRCT e. eotIO".;

IHRCT Goeoee IHFICT 8.8988 INRCT 8.8888 IHRCT INFICT 8.8888 IHRCT 8.8888 f, RYG 67.9854 DEW CEI LS RHD Zl 53.3863 RHD Z2 51.3319 RHD 22 47.3863 RMD 23 Si 6268~

~

RHD Z3 49.9729 RHD Z3 58. 1396 RHD Z4 52.3575 RHD 24 59o7165g RHD Z5 51.3447 RMD Z5 58.4729 INRCT 8.8889 INRCT e.Gobe.;.

INRCT 8. 8888 INRCT 8.8888 INRCT 8.8888 RVG 58.8589 RMB IEHT PRESS 14.4889 VRPOR PRESSURE ,.1835 DRY PRESSURE 55. 4515 FLOWS 8. 8888 i (IRECORD NUMBER 233 DRTE - 56 .TIME - 1345 PRESSURES 55.6368 55.6288 RVG 55.6328 ~

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RTD'S W~

Zlrei 68.8369 Zlr82 68.1448 2lr83 6e. e9eo Zlre4 67. 87&

Z2rol 68.2529 Z2r92 68. 1448 Z2r83 68.2349 Z2r94 68. 25M !

Z2r85 68.3788 22r86 68. 1888 Z2r97 68.1449 23rel 68.4868-.,

Z3r92 68.4689 23r93 68.4329 23r94 68.3969 Z3r85 68.3969 L, Z3r96 6S.64SG 23r87 68.5489 Z3ree 68.4688 23r89 68.5940:..

Z4rel 68.7928 Z4r92 68o6489 Z4r93 6S.5949 24r94 6e.6669 24r95 68.8649 24r86 68.7289 24r97 68.5499 Z4rGS ~

.'8.4680 Z4re9 68e7828 Z4rle 68.7828 Z5rei 65.6249 Z5r92 66.1829 p~

Z5r83 66. 1648 ZSr84 65.8949 25r85 66.5690 25r96 65.8580 <:

Z5r87 65.9668 Z5reS 65 '868 Z5r89 66.2990 ZSrle 67.1720 '

IHRCT 8.9998 INFICT 8.8889 INRCT 9.8989 INFICT 9.9098 IHFICT 9.8888 INRCT 9.8888 INFICT 8.8998 INRCT 8.8900 - .

INRCT 8.8889 IHRCT 8.8888 RVG 67.8799 1>.

DEW CELLS 'Ig RHD Zl 47.6989 RHD Z2 58.8378 RHD Z2 51.6148 RHD Z3 947~ '1.

7934

1.

RHD 23 52.7293 RHD Z3 52.7896 RHD 24 59.8863 RHD Z4 HD Z5 51. 3191 'RHD Z5 58.6652 INRCT 8:9988 IHRCT G. 8909

<RCT 8. 8998 INRCT 8.8888 INRCT 8.8888 RVG 51 ~ 1816 8NBIENT PRESS 14.4eee

( YRPOR PRESSURE ~ 1852 DRY PRESSURE 55.4468 FLOWS 8.8888

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RECORD NUNBER 234 DRTE - 56 TINE 1488 PRESSURES 55. 6349 55. 6258 RVG 55.6295 RTD'S Zlr91 68.8368 Zlr82 '8. 1448 Zlr83 68.9548 Zlr94 67 '199 Z2r81 68.2888 Z2r82 68 ~ 14'48 Z2r83 68.2348 Z2r84 68.1269 Z2r85 68.3868 Z2r86 68. 1888 Z2r87 68.1888 Z3r81 68 '689 Z3r82 68.4588 Z3r83 68.4148 Z3r84 68.3968 Z3r85 6e.3969 Z3r86 68.6668 23r87 68.5848 Z3r88 68.4688 Z3r89 68.5649 Z4r81 68.8288 Z4r82 68.6128 Z4r83 68.6128 Z4r84 68.5229 Z4r85 68. 9368 Z4r86 68. 7298 Z4r87 68.4868 Z4r88 68.3960 Z4r89 68. 6668 Z4r18 68. 6848 Z5r81 65.6868 ZSr82 66. 1640 Z5r83 66. 1288 Z5r84 65. 7868 Z5r85 66.5788 Z5r86 65.eseG Z5r97 65.9488 25r88 65. 7588 25r89 66.2728 Z5riB '67.1729 INRCT Be8898 IHRCT 8.8898 IHRCT 8.9888 INRCT 8.9808 INRCT 8.8898 INRCT 8.8888 INFICT 8.8888 IHRCT 8. 9909 INRCT 8.8888 IHRCT 8.8888 RVG 67.8642 DEW CELI S RHD 21 53.3832 RHD Z2 53.8968 RHD Z2 52.3863 RHD Z3 51.3863 RHD Z3 52.8499 RHD Z3 49.9986 RHD Z4 ~

52.7678 RHD Z4 58.4088 RHD ZS 51.3784 RHD Z5 58.8784 INRCT 8.8898 INFICT 8.8989 IHRCT 8. 8888 I NFICT 8.8888 IHRCT 8.8888 RVG 51. 8375 FINB IENT PRESS 14.4888 VRPOR PRESSURE +1984 DRY PRESSURE 55.4391 FLOWS 8.8888

( RECORD NUNBER - 235 DRTE - 56 TINE 1415 PRESSURES 55. 6318 55.6238 RVG 55.6279 RTD'S Zlr81 67.9648 Zlr82 68.1888 Zlr83 68.8368 Zir94 67. 8569 22r81 68.3868 Z2r82 68.8998 Z2r83 68. 1268 Z2r84 68.1449 22r95 68.3248 Z2r86 68.8988 Z2r87 68.1888 Z3r81 68.4140 23r82 68e4148 Z3r83 68.3788 Z3r94 68.3698 Z3r95 68.3960 Z3r86 68.7748 23r87 68.4688 Z3r98 68.4328 Z3r89 68.4680 Z4r81 68.7929 Z4r82 68.5588 Z4r93 68.5588 Z4r84 68.5229 24r95 68.7748 24r86 68.6669 24r87 68.4869 Z4r88 68.4149 Z4r89 68.7829 Z4r18 68.6849 Z5r81 65. 5788 Z5r82 66.1289 ZSr83 66.1188 ZSr84 65.7328 Z5rBS 66.5249 ZSr86 65.8589 25r87 65.9399 ZSr98 65.7328 25r89 66.2369 Z5r18 6 1549 IHRCT 8.9898 IHRCT 8.8888 IHRCT 8.8880 IHFICT 8.8990 INRCT 8.8988 IHFICT 8.8988 IHRCT 8.8889 IHRCT 9.9089 INRCT 8.8888 INRCT 8.8888 RVG 67.8386 DEW CELLS RHD Zl 52.9217 RHD Z2 54.7837 RHD Z2 58.2837 RHD Z3 52.9370 RHD Z3 51.9888 RHD Z3 49.7558 RHD 24 58.9986 RHD Z4 53.1524 HD Z5 51. 3784 RHD Z5 59.5242 IHRCT 9.8888 INRCT 9.9999 NRCT 8.8888 IHRCT 8+8888 INRCT 8.8888 RVG 51.7433

(

FINB IEHT PRESS 14 '888 VRPOR PRESSURE ~ 1897 DRY PRESSURE 55. 4373 FI OWS 8.8888

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RECORD HUNBER 236 DRTE - 56 TINE - 1438 PRESSURES 55. 6288 55.6288 RVG 55>>6248 RTD'S

(

Zlrel 67.9188 Zlr82 68. 8988 21r83 67. 9828 Zire4 6?.8928 Z2rel 68.2348 22r82 68.8728 Z2r83 68. 1888 Z2r84 68 1268 Z2r85 68.2788 Z2r86 68.8548 22r87 6s. 89ee Z3rel 68.3788 Z3r82 68 4 1 48 Z3r83

~ 68.3968 Z3r84 68. 3428 Z3r85 68.4eSG Z3r86 68.6128 Z3r87 68.4588 Z3r88 68.4148 Z3r89 68.4S6e Z4re 1 68.7748 Z4r82 68.5488 Z4r83 68.6128 Z4r84 68.5948 Z4re5 68.8468 Z4r86 68.6488 Z4r87 68.5848 Z4res 68>>3968 Z4r89 68>> 6488 Z4r1 8 68.6388 Z5rel 65.5348 ZSr82 66>>1288 Z5r83 66.8928 Z5r84 65.7328 ZSre5 66.5868 25r86 65.8220 ZSre7 65.9388 Z5res 65>> 7148 ZSr89 66.2368 ZSrle 67.8828 IHRCT 8.8888 IHflCT 8.8888 INRCT 8.8888 IHRCT 0.8808 INRCT 8.8888 INRCT 8.8888 INFICT 8.8888 IHRCT G.GGGG IHRCT 8.8888 INFICT 8. 8888 RVG 67.8212 DEW CELLS RHD Zl 54.8784 RHD 22 52. 8191 RHD 22 52. 6781 RHD 23 49.9986 RHD Z3 58.9681 RHD Z3 58.5883 RHD Z4 49. 1989 RHD Z4 58.9681 RHD ZS 51. 2558 RHD Z5 58.7422 INACT 8 ~ 8888 INflCT 8>>GGGG INRCT 8. 8888 I NFICT G.eeee IHRCT 8.8888 RVG 51 ~ 4342 ANBIEHT PRESS 14 '888 VFIPOR PRESSURE .1875 DRY PRESSURE 55.4365 FLOWS 8.8888 8.8888

( RECORD NUNBER 237 DRTE 56 TINE 1445 PRESSURES 55.6268 55.6188 RVG 55. 6228 RTD'S Zirel 67>>8928 21r82 68,1888 Zir83 68. 8888 Zir84 67.82GG Z2rel 68.1988 Z2r82 68.8988 Z2re3 68.1888 22re4 68.8900 Z2re5 68.2528 Z2r86 68.8988 22r87 68.8728 Z3rel 68.4148 Z3r82 68.3688 Z3r83 68.3?88 Z3r84 68.3428 Z3r85 68.3?SG Z3r86 68.6848 Z3r87 68.4688 Z3res 68.3968 Z3r89 68.4508 24rel 68,.7568 Z4r82 68.5588 Z4r83 68.5228 24re4 68.6128 Z4re5 68.8188 24re6 68.6128 Z4re7 68.45GG Z4res 68.3248 Z4r89 68.5?68 Z4rie 68.6488 Z5rei 6s.5528 25re2 66.11GG Z5r83 66.8748 ZSre4 65.6968 Z5r85 66.4788 25re6 6S.75GG 25r87 65.8768 Z5res 65.6788 Z5r89 66.1828 25rle 67.1180 INRCT 8.8888 INRCT 8.8888 IHRCT G.eeee INRCT G.GGOG I HRCT 8.8888 INRCT 8.8888 INRCT B.eeee IHRCT G.GGGG IHACT 8.8888 INRCT B.BGGG flVG 67.8853 DEW CELLS RHD 21 46. 1524 RHD 22 47.2293 RHD Z2 49. 1268 RHD Z3 46. 2934 RHD Z3 58.9888 RHD Z3 48>>4217 RHD Z4 51. 8575 RHD 24 52.1396 HD Z5 51. 2678 RHD Z5 58. 7165 INRCT 8;8888 IHRCT G.GGOO RCT 8.8888 IHRCT 8>>8888 INRCT 8.8888

.RVG 49>> 4428 FINB IENT PRESS 14.4888

( VRPOR PRESSURE ~ 1748 DRY PRESSURE 55. 4488 FLOWS 8.8888 8.8888

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RECORD NUNBER - 238 DRTE - 56 TINE 1588 PRESSURES 55.6238 55. 6168 FIVG 55.6195 RTD'S 2lrel 67.9288 Zlr82 68.'8989 Zlr83 68. 8188 Zlr94 67. 8926 Z2r81 68. 1448 Z2r82 68. 8726 Z2r8.3 68.1988 Z2r84 ee. Gs49 Z2r85 68.2528 22ree 68. 9368 Z2r87 68.8728 Z3rei 68. 3786 23r82 68.3688 23r83 68. 3689 Z3r84 68.3428 Z3r85 68.3786 23r86 68.4588 Z3r87 68. 4329 Z3r88 68.3788 Z3r89 ee.4566 Z4rel 68.?568 Z4r82 68. 5588 24r83 68.4688 Z4r84 68.4326 Z4r85 68. 8188 Z4r86 68.6399 24r87 68.4588 24r88 6S.3966 24re9 68.5948 Z4rle 6S.6668 25re1 65.4988 25r82 66.6746 Zsr83 66.eSee ZSre4 65.6788 25r85 66.5868 Z5r86 65.?566 25r87 65.8588 Zsr88 65.6689 25r99 66.1648 Z5rle 67.64oO INRCT 8.9889 INRCT 9.9988 IHRCT 8.8888 INRCT 6.6666 I t(FICT 8.8888 IHFICT eeeeee INRCT 8.8888 INRCT 6.6066 I HFICT B.BBBG INRCT 9.8868 RVG 67 '848 DEW CELLS RHD Zl 49 '293 RHD Z2 47.7165 RHD Z2 52. 8114 RHD Z3 49. 1?81 RHD Z3 49. 5378 RHD Z3 58.3447 RHD 24 56.3863 RHD Z4 51. 9499 RHD Z5 51. 3863 RHD Z5 58.5242 INFICT 8.8899 INRCT 9.9669 INFICT 8. 8988 IHFICT 8.9888 IHFICT 8.6989 RVG See1962 RHBIENT PRESS 14.4888 VFIPOR PRESSURE . 1?98 DRY PRESSURE 55. 4485 FLOWS 8. 8888 5. 8888 I

RECORD NUMBER - 239 DATE - 56 TINE 1515 PRESSURES 55. 6268 55. 6138 FIVG 55. 6165 RTD'S Zlrei 67.8568 Zir82 68. 8368 Zlr83 67.9649 21r64 67. 7666 Z2rel 68. 1628 Z2r82 68. 8369 Z2r83 68. 1869 Z2r94 68. 9906 Z2r85 68.2?89 Z2r86 67.9828 Z2r87 68. 9189 Z3rel 68. 3666 Z3r82 68.3689 Z3r83 68. 3429 Z3r84 68.2889 23r65 6S.3246 Z3r96 68.?389 Z3r97 68. 4148 23r88 68.3426 Z3r99 68.3966 Z4rel 68.7288 24r82 68. 5498 24r93 68.5226 Z4r94 es.4686 Z4r85 68.6849 24r86 68.5589 24r87 68.3969 24r68 68.3660 Z4r69 68.5768 24rle 68.5768 25rel 65.4986 Z5r02 66.05oO Z5r83 66.8288 Zsr84 es.eeee Zsr95 66.4889 Zsr96 65.7506 Z5r87 65.8588 Zsree 65.6428 Z5r89 66. 1469 Z5r10 67.1366 I NFICT 8.8988 INRCT 9.8688 I NFICT 8.8968 INRCT 6.0600 I t<FIC T 9.8886 INFICT 8.8668 IHRCT 8.9906 IHFICT 0.6600 INRCT 8.8888 INRCT 8.8888 RVG 67.7685 DEW CELLS RHD Zi 47.4986 RHD 22 48+5627 RHD Z2 51. 8863 RHD Z3 56. 6268 RHD 23 52.2678 RHD Z3 51. 2937 RHD Z4 52.5376 RHD Z4 49.2165 RHD ZS 51.1396 RHD ZS 58.9217 IHRCT 8.9888 INRCT 9.9660 IHRCT 8. 8888 I NFICT 8+8988 IHRCT 8.8888 RVG 58.5697 8NBIEHT PRESS 14.4888

( VFIPOR PRESSURE .1815 DRY PRESSURE 55.4358 FLOWS 8.8888 5.8888

P

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RECORD NUMBEP. - 249 DATE 56 T I ME 1538 PRESSURES 55. 6178 55. 6188 AVG 55.6135 RTD'S Zirel 67.874e Zlr92 68.8998 Zir83 68. 8888 Zlr94 67. 7660 Z2rel 6S. 1448 Z2r82 68.8988 22r83 68.8988 Z2r84 68.8189 Z2r85 68.2528 22r86 67. 9829 'Z2r87 68.9368 Z3rel 68.3690 Z3r92 68.3868 23r83 68.3248 Z3r84 68.2888 Z3r85 68.3249

.Z3r86 68.5228 Z3r97 68.3968 Z3r88 68.3248 Z3r99 68.3969 Z4rel 68.7828 Z4r82 68.5228 24r93 68.4868 Z4r84 68 5760

~

Z4r85 68.64SG 24r96 68.5488 Z4re? 68 '788 Z4r88 6S 3249

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24r89 68.5768 Z4rle 68.6128 Z5rel 65.4888 Z5r82 66.8389 Z5r83 66.9828 Z5r84 65.6428 Z5r85 66.4168 ZSr86 65.7509 Z5re? 65.8228 Z5r88 65.6248 25r89 66.1288 ZSrle 67.1900 I NFICT 8.8998 INFlCT 8.8898 INACT 8.8889 INACT 8.9099 INACT 8.8989 INACT 8.8988 INACT 8.8888 INFICT 8.8909 INACT 8.8888 INFICT 8.8988 AVG 67 '472 DEW CELLS RHD Zl 49'781 RHD Z2 51. 8378 RHD Z2 59. 1989 RHD Z3 48.1781 RHD Z3 49 '396 RHD 23 51.7837 RHD 24 5io7806 RHD 24 50.8704 RHD Z5 51. 8499 RHD Z5 58. 8114 I NACT 8.8888 INACT 8~ 8999*

INACT 8. 8888 INACT 8. 8888 INACT 8. 9998 AVG 59.3788 AMBIENT PRESS 14.4888 VAPOR PRESSURE .1882 DRY PRESSURE 55.4333 FLOWS e.eeee 5.8122 RECORD NUMBER 241 DATE - 56 TIME - 1545 PRESSURES 55.6148 55. 6978 AVG 55.6185 RTD'S Zlrei 67. 8389 2 lr82 68.8188 Zlr83 67. 9649 Zir84 67.7489 22rel 68.8989 Z2r92 68.8088 Z2r83 68.1880 Z2r94 68.9998 Z2r95 68.2348 Z2r96 67.9468 Z2r97 68.8888 Z3rei 68.3429 Z3r82 68 '869 Z3r83 68.2888 Z3r84 68.2789 Z3r85 68,3960 Z3r96 68.4868 Z3r97 68.3788 Z3r88 68.3428 Z3r99 68.3789 Z4rel 68.6669 Z4r92 68.5948 Z4r93 68.4588 Z4r84 68.3789 Z4r 05 68.7389 Z4r86 68.5588 24re? 68 '968 Z4r98 68.3429 Z4r99 68.5499 Z4rle 68 '948 Z5rel 65.4448 Z5r82 G. 99 Z r93 65.9848 Z5r84 65.6868 Z5r85 66.4349 Z5r86 65. 7329 Z5r97 65'?868 Z5r98 65.5889 Z5r89 66.1189 25r10 66.9560 INACT 8.9999 INACT 8.8999 INACT 8.9999 INACT 9.0900 INACT 8.9898 INACT 8.8888 INACT 8.8988 INACT 9.9999 INACT 8.9888 INFICT 8.8888 RVG 6?e7251 DEW CELLS RHD Zl 53.6524 RHD Z2 52.7165 RHD 22 58. 8114 RHD Z3 49.1781 RHD 23 52.2558 RHD Z3 51. 9888 RKD 24 5'G. 8447 RHD Z4 50.7937 HD Z5 51 ~ 8378 RHD Z5 49.98S8 INACT 8; 8888 INFICT 8.9099 NACT 8.8888 INACT 8.8888 INACT 8. 8888 AVG 51.2871 AMBIENT PRESS 14+ 4888 VAPOR PRESSURE . 1859 DRY PRESSURE 55. 4246 FLOWS 8.8888 5. 8122

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RECORD NUMBER -. 242 DATE - 56 TIME 1688 PRESSURES 55. 6198 5S.6838 RVG 55.6865 RTD'S Zlrel 6?.8568 Zir82 68.8888 Zir83 67. 9468 Zlr94 67. 7309 Z2rel 68. 1448 Z2r82 67.9468 22r83 68. 8548 Z2r94 67. 9829 22r85 68.2788 22r06 67.9468 Z2r07 67. 9828 Z3rei 68. 3420 Z3r02 68.2888 Z3r83 68.3860 Z3r04 68. 2168 Z3r85 68. 2529 23re6 68.5949 Z3r87 68.3428 Z3r88 68. 3248 Z3r89 68.3429 Z4rei 68.6488 24r82 68.4688 24r83 68.4508 Z4r84 68.4149 24r85 68.7388 24r86 68.5588 Z4re? 68.3428 Z4re8 68.2880 Z4r89 68. 5588 Z4rie 68.5040 Z5r81 65.4088 ZSr82 65.9849 25r83 65.9488 Z5r84 65.5888 Z5r85 66.4168 Z5r96 65.7149 Z5r87 65.7688 Z5res 65.5528 Z5r99 66.8748 25rle 66.9929 IHRCT 8.8888 IHACT 0.0890 IHRCT 8.0088 IHRCT 8.8909 INACT 8.8888 INRCT 8.8888 IHRCT 8.8888 INRCT 9.9909 INRCT e.eeee INRCT 8. 8880 AVG 67.7884 DEW CELLS RHD Zi 59.4601 RHD Z2 48. 6148 RHD Z2 58.5242 RHD Z3 51. 2559 RHD Z3 58. 1S24 RHD Z3 49.3447 RHD Z4 51. 4986 RHD Z4 51. 3575 RKD Z5 51 ~ 8114 RHD 25 58.2896 IHRCT 8.8899 IHRCT 8. 9099 INRCT 8.8889 IHRCT 8.8888 INRCT 8.8989 RVG 58.4451 FINBIEHT PRESS 14.4088 VFIPOR PRESSURE .1887 DRY PRESSURE 55.4258 FLOWS 8.0880 5. 8122 RECORD NUMBER - 243 DRTE - 56 TIME " 1615 PRESSURES 55.6878 55.6088 RVG 55. 6835 RTD'S 21rel 6?e8388 21r82 67.9820 Zir03 67. 87 49 2 1 r84 67.6949 Z2rei 68.8888 Z2r82 68.0988 22r83 68.9988 Z2r84 6r.9289 Z2r05 68. 1988 Z2r86 67.8928 Z2r97 68.9999 Z3rei 68.2799 Z3r02 68. 2788 23r83 68.2528 23r84 68.2168 Z3r95 68.2880 Z3r96 68.4328 23r07 68.3248 23res 68.3869 23r99 68. 3249 24r01 68.6129 Z4r02 68.4588 Z4r03 68.4328 Z4r84 68 3680

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Z4r95 68.7569 Z4r86 68.5229 24re? 68.324e Z4rGS 68.2709 Z4r89 68.5229 Z4rle 68.5948 ZSrel 65.3729 25r92 65.9480 Z5r83 65'128 Z5r84 65.5348 25r95 66.3628 Z5r96 65.6969 ZSr87 65.7329 25res 6S.5349 ZSr89 66.9389 Z5rle 66. 9749 IHRCT 0.9998 INRCT 8.0989 IHRCT 8.8009 IHFICT G. 9909 INRCT 8.8899 INRCT 8.8888 INACT 8.8888 IHRCT G. 9999 IHRCT 0.8888 IHRCT 8.8888 AVG 67.6794 DEW CELLS RKD Z 1 51. 7886 RHD 22 46.7558 RHD Z2 51. 4681 RHD Z3 46. 8314 RHD Z3 58. 4217 RHD Z3 48.8499 RHD Z4 51. 9345 RHD Z4 49. 921?

RHD Z5 58.8832 RHD 25 58.3447 INRCT Go 8988 INRCT 9.9909 NFIC7 8.8888 INRCT 8.8988 INRCT 8.0988 RVG 49 ~ 8764 RMB IENT PRESS 14+4988

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~ RHD Z4 52.6 6e RHD Z5 58.6989 RHD Z5 58.2422 INRCT 8.8888 INRCT 8 GGGG

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INRCT 8. 8888 I NFlCT 8.8888 INRCT 8.8888 RVG 51.8758 AMBIENT PRESS 14 '888 VFlPOR PRESSURE ei858 DRY PRESSURE 55.4155 FLOWS 8.8888 5.8122 RECORD NUNBER 245 DRTE 56 TINE 1645 PRESSURES sso6888 55. 5938 RVG 55. 5965 RTD'S Zlrei 67.7848 Zlr82 67. 9288 Zir83 67.8288 Zir84 67.6588 22rel 68 8548 Z2r82 F 67. 9188 Z2r83 68.8188 Z2r84 67.9188 22r85 68.8988 22r86 67.8928 Z2r87 6?.9288 Z3rel 68.2528 Z3r82 68.2348 Z3r83 68.1988 23re4 68.1888 Z3r85 6S.1988 Z3r86 68.5588 Z3r87 68.2888 Z3r88 68.2520 Z3r89 68.3860 24rei 68. 6128 Z4r82 68.4328 Z4r83 68.3428 Z4r84 68.4868 Z4r85 68.7828 Z4r86 68.5228 24r87 68.3068 Z4re8 68.2160 Z4r89 68.4328 Z4rie 68.4588 Zsrel 65.3888 Z5r82 65.8768 Z5r83 65.8588 Z5r84 65.4888 Z5r85 66.3628 Z5r86 65. 6600 Z5r87 65.6688 Zsre8 65.4888 Z5r89 65.9668 ZSrie 66.9740 I tlFICT 8.8880 INRCT 8.8888 I NFI CT 8.8888 INRCT 8.0000 I t<FICT 8.8888 INFlCT 8.8888 INRCT 8.8888 I NFICT G.GGGG INRCT 8.8888 INRCT 8.8888 FlVG 67e6429 DEW CELLS RHD Z 1 51+ 8627 PHD Z2 51. 3447 RHD Z2 47.8447 RHD Z3 51. 3968 RHD'3 48.6268 RHD Z3 49.7422 RHD Z4 49.6396 RHD Z4 58.1268 RHD 25 58.7558 RHD Z5 see 7165 INRCT 8.8888 INRCT 8.8808 NRCT Goeeee INFtCT G. 8888 INRCT 8.8888 RVG, 58.1492 RNBIEHT PRESS 14. 4888 VFlPOR PRESSURE . 1787 DRY PRESSURE 55.4178 FLOWS eoeeee 5.8122

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RECORD NUI'1BER - 246 DRTE - 56 T I NE - 1789 PRESSURES 55. 5968 55 '988 RVG 55. 5939 RTD'S 2lrei 67+ 7488 Zlr82 67. 8928 Zlr83 67.8388 2ir84 67. 6499 22re 1 67. 9648 Z2r82 67. 9188 22r83 67.9648 22r84 67 8929 Z2r85 68. 8548 22re6 67. 8748 Z2r87 67. 9288 Z3rel 68.2349 Z3r92 68. 1898 Z3r83 68. 1888 Z3r84 68.1988 Z3r85 6S,2799 Z3r86 68. 4688 Z3r87 68. 2528 23r88 68.2348 23r89 68. 3069 24rei 68. 5948 Z4r82 68. 3428 Z4r83 68.3248 24r84 68. 3969 24r95 68. 5768 Z4r96 68.4328 Z4r87 68.3968 Z4reS 68. 2340 Z4r89 68. 4328 Z4rie 68.4868 Z5rei 65.2828 Z5r82 65. 8589 Z5r83 65'848 Z5r84 65.4448 Z5r85 66. 3888 25r86 65. 6429 Z5r87 65. 6969 25r88 65.4448 Z5r89 65. 9388 Z5rie 66. 9560 IHRCT 0.8889 INRCT eoeeee IHRCT 8. 8888 I NRCT 9.9909 I HFICT 8.8998 !NRCT 8.8988 INRCT 8. 8888 INRCT 9.8999 IHRCT Be9889 INRCT ee 8988 RVG 67 '171 DEW CELLS RKD Zl 51 ~ 1811 RHD Z2 52+ 8114 RHD Z2 48.3863 RHD Z3 52. 2165 48.5242 58.8242 RHD 23 RHD Z5 I HFICT 58.8863 8.8888 RHD RHD INRCT Z5, 23 52e8447 RHD Z4

58. 1524 INRCT 8.8888 INRCT 8.9889

8. 9888 RHD 24 IHRCT 48 81'91

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0.9909 RVG 58. 4764 RNB IENT PRESS 14. 4888 VFIPOR PRESSURE ~ 1889 DRY PRESSURE 55. 4121 FLOWS 8.8888 5. 8185 RECORD HUNBER 247 DRTE 56 TINE - 1715 PRESSURES 55.5939 55.5868 AVG 55. 5895 RTD'S Zlrel 6?.7488 Zlr82 67.8569 2ir93 67. 8388 Zir84 67.6849 Z2re 1 68.9188 Z2r82 67.8568 Z2r83 68. e549 22r84 67.9289 22r95 68. 1448 22r86 6708748 Z2r87 67+ 8928 Z3rei 68.1988 23r82 68. 2168 Z3r93 68.1988 23r84 68.1449 Z3r85 68.2349 Z3r96 68.4599 Z3r97 68. 2349 Z3r88 68.2168 Z3r99 '8.2889 24rel 68.5760 24r82 68. 3788 Z4r83 68.3689 Z4r84 68. 2SSG 24r85 68.6389 Z4r86 68. 4688 Z4r87 68.2528 24r88 6S. 1809 24r99 68.4149 Z4rle 68. 4328 Z5rel 65.2468 Z5r'82 65. 8220 25r93 65.7688 25r84 65. 4888 Z5r85 66.3448 Z5r96 65. 6249 Z5r87 65.5888 25r88 65. 4268 25r89 65.8948 25r10 66. SS40 IHRCT Geeeee IHFICT e.eeee IHRCT 8. 8899 INRCT 9. 9999 IHACT Geeeee INRCT 8.8998 IHRCT 8. 9989 INRCT 8. 0809 IHRCT 8.8988 INRCT 8.8888 RVG 6?.6855 DEW CELLS RHD 21 58.7293 RHD 22 46.5627 RHD Z2 49. 1989 RHD Z3 52. 2422 RHD Z3 48.9681 RHD Z3 48.9858 RHD 24 51. 5627 RHD 24 49o9473 HD Z5 59.7422 RHD Z5 58.8447 INFICT G.eeee INACT 9.9909 NRCT 8.8888 INRCT 8.8888 INRCT 9.8888 RVG 49.9822 FIMBIEHT PRESS 14.4888 VAPOR PRESSURE .1776 DRY PRESSURE 55. 4119 FLOWS 8. 8888 5 ~ 8185

RECORD NUMBER - 248 DRTE - 56 TINE - 1738 PRESSURES 55. 5988 55.5838 AVG 55.5865 RTD'S Zirei 67.7849 21r82 67.8928 Zlr83 6?. 8928 Zir84 67. 6229 Z2rei 68. 8188 Z2r82 67. 8388 Z2r83 67. 9288 Z2r84 67.8569 Z2r85 68. 1268 Z2r86 67.8288 Z2r87 67.8748 Z3rei 68 '169 Z3r82 68. 1988 Z3r83 68. 1628 23r84 68.1888 23r95 68.1449 Z3r96 68o5228 23r87 68.2348 Z3ree 68.1888 23r89 68.2529

'24r81 68o5488 Z4r82 68.3788 24r83 68.3428 Z4r84 68.2169 Z4r85 68,6128 24re6 68.4328 Z4r87 68.2168 Z4ree 6e.1440 Z4r89 68.3789 Z4rie 68.4328 Z5rei 65.2188 Z5r82 65.?689 25r83 65.7588 25r84 65. 3989 25r85 66.3888 Z5r96 65.6249 Z5re? 65.5528 25r88 65.3989 Z5r89 65.8588 Z5rie 66.9380 INRCT 8.8898 INRCT eeeeee INRCT 9.8888 INRCT 9.9909 INRCT 8.8888 INRCT 8,8898 INFICT e.eeee INRCT 8.8990 INRCT 8.8888 INRCT 8.8888 RVG 67 '825 DEW CELLS RHD Zi 58.8755 RHD Z2 52.8447 RHD Z2 58.9729 RHD Z3 52.8832 RHD 23 49.4888 RHD 23 53.2422 RHD 24 48.7293 RHD Z4 49.844?

RHD 25 58.6268 RHD 25 58.3447 INRCT 8.8888 INRCT 8.9009 I NFICT 8.8888 INRCT 8.8888 INFICT 8.8898 RYG 58.8874 RNBIENT PRESS 14.4888 VRPOR PRESSURE .183?

DRY PRESSURE 55.4828 FLOWS 8.8888 5.8185 RECORD NUNBER 249 DRTE 56 TINE 1745 PRESSURES 55.5878 55.5888 FIYG 55.5835 RTD'S Zirei 67e 7398 Zir82 67.8748 Zir83 67.7848 Zir84 67.6400 Z2rei 67.9468 Z2r92 67.8749 22r83 67.9288 Z2r94 67.8209 Z2r85 68. 8728 Z2r86 67.8288 Z2r87 67.8748 Z3rei 68.1899 Z3r82 68.1628 23r83 68.1628 23r84 68.1'889 Z3r85 68.1449 23r96 68.3968 23r97 68.2168 Z3ree 68.1898 Z3r89 68.2529 24rei 68.5588 Z4r82 68.3788 24r83 68.3429 Z4r84 6S.2169 24r85 68o6489 Z4re6 68.3789 Z4r87 68.1898 Z4r88 6S.1440 24r89 68.3968 Z4rie 68.4149 ZSr81 65.1929 Z5r82 65.7500 Z5r93 65.7148 Z5r84 65.3549 Z5r85 66.2989 Z5r96 65.5?00 Z5r97 65.5168 25ree 65.3548 Z5r89 65.8228 Z5rie 66.9389 INRCT 8.8880 INRCT 8 9889

~ INRCT 9.9089 INRCT 8.8909 I NRCT 8.8988 INRCT 8.8888 INACT 8.8899 INRCT 8.9009 INRCT 8.8888 INRCT 8.8898 RVG 6?e5631 DEW CELLS RHD Zi 49.3575 RHD 22 48.3784 RHD Z2 52.4986 RHD Z3 51. 6652 RHD Z3 58.421? RHD Z3 51. 4729 RHD Z4 48.8784 RHD 24 49.4088 RHD Z5 58+6989 RHD Z5 49. 8575 INRCT et.eeee INRCT 9.9090 NRCT eoeeee INFICT 8.8888 INRCT 8.8888 FIVG 58. 2557 AMBIENT PRESS 14.4888

( VRPOR PRESSURE . 1794 DRY PRESSURE 55.4e41 FLOWS 8.8888 5.8185

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RECORD HUttBER - 259 DRTE <<56 TINE - 1888 PRESSURES 55. 5849 55.5778 RVG,- 55.5865 RTD'S Zlz91 67.6949 Zli62 67.9288 21<83 67.7848 Zlr94 67. 5590 22i81 67. 9468 22i82 67. 8388 22i83 67.9188 22r64 67.8299 22r05 68.8899 22r86 67. 8388 22i87 67.8568 23r81 68. 1446 23>'92 68.1448 23r83 68. 1448 23i84 68. 8988 23iGS 68o2349 23r86 68.3966 23r87 68. 2348 23i88 68. 1628 23i69 68.1986 24i81 68.5498 24/82 68.3248 24r83 68.3249 24r64 68.2166 24r85 68.6128 24r86 68.3968 24r87 68.2348 24r98 68.1890 24i89 68. 4146 24iiG 68.4569 25r81 65.1568 25r82 65.7566 25r93 65.6968 25r64 65.3368 25r85 66.2548 25r86 65.5340 25r87 65.4449 25r88 65.3188 ZSr89 65.8488 ZSriG 66.7946 I HFICT 8.8899 INFICT 8.8698 INRCT 8.8888 INRCT 6.9666 IHRCT 6.8898 INRCT 8.8888 INRCT 8.8886 'INRCT 0.6960 I ttFICT 8.8888 IHFICT 8.8988 RVG 67. 5479 DEW CELLS RHD Zi '9o53?8 PHD Z2 51.9858 RHD 22 47.3832 RHD 23 49.9729 RHD 23 52.8242 RHD Z3 49.4888 RHD 24 56.4729 RHD Z4 52.9345 RHD ZS 59.5499 RHD 25 58. 3191. INRCT 8.8889 INRCT 9.0999 I thFICT 8.8988 I NRCT 8;8888 IHRCT 8. 8988 RVG 58. 4481 RHBIEHT PRESS 14e4888 YFIPOR PRESSURE .1886 DRY PRESSURE 55.3999 FLOWS 8.8898 5.8185 RECORD NUMBER - 251 DRTE 56 TINE 1815 PRESSURES 55.5818 55.5748 RVG 55. 5775 RTD'S Zli91 67. 6768 2 lr82 67.8749 Zir93 67. 7849 2ii94 67. 5860 22r91 68. 8886 22i82 67.8926 22r63 67. 9198 22i94 67. 8200 22iGS 68.8669 22i66 67.7848 22i97 67.8389 23i81 68.1440 23i92 68. 1268 23i63 68.1448 23r94 68.8999 23i65 68.1080 23i96 68.2799 23r67 68.1889 23r88 68.1888 23r89 68.1626 24r91 68. 4868 24i62 68.3428 24r83 68.2528 24i64 68.1989 24r65 68.6489 24r86 68.3968 24r97 68.1886 24i88 68.1266 24i89 68.3696 24/19 68.3968 25r61 65.1269 ZS/82 65 '960 25r83 65.,6696 25i84 65.3888 ZSr85 66.2548 ZS/86 65.5346 25i97 65. 4448 ZSi88 65.2828 25~89 65.7686 25r19 66.8489 INRCT 8. 6996 I t<RCT Ge9686 IHRCT 9.8969 I HFICT 9.9960 I t<RCT 8.6989 INRCT 8.8988 INFICT 8.6099 IHRCT 9.9669 INFICT 8.8889 INRCT 8.9989 FIVG 67. 5219 DEW CELLS RHD 21 48.6781 RHD Z2 53.8832 RHD Z2 46.6781 RHD Z3 47. 8663 RHD Z3 58.3784 RHD 23 58.4988 RHD Z4 49.6989 RHD Z4 51 ~ 4345 HD 25 56.4888 RHD 25 58.3832 INRCT Gi 8886 IHRCT 8.6660 RCT 8.8888 INRCT 8.8898 INRCT 8.8888 RVG 49.9989 'I RNB I ENT PRESS 14'888 YRPOR PRESSURE o 1776 DRY PRESSURE 55.3999 FLOWS Go8868 5.8185

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RECORD NUMBER -. 252 DRTE - 56 TIME 1838 PRESSURES 55.57SG 55.5788 RVG 55. 5748 RTD'S Zirel 67. 6588 2 ir82 67. 8568 Zire3 67. 7668 Zir84 67. 5140 Z2rel 67. 9188 Z2r82 67. 8828 Z2r83 67. 9828 Z2re4 67. 7848 Z2r85 68.8368 Z2r86 67. 7388 Z2r87 67. 8288 Z3rel 63. 1440 Z3r82 68.1888 Z3r83 68.8988 Z3r84 68. 8548 Z3re5 68. 1888 Z3r86 68.3968 Z3r87 68.1628 Z3r88 68. 1448 Z3r89 68. 1 eee Z4rei 6S.4868 Z4r82 68.2528 Z4r83 6S. 2528 Z4re4 6e.2528 Z4r85 68o5768 24r86 68.3788 Z4r87 68. 1988 Z4re8 68 1888 Z4r89 68.3428 Z4rle 68. 3428 Z5rel 65. 1828 25r82 65.67SG Z5r83 65.6248 25r84 65. 2648 Z5re5 66. 2888 ZSre6 65.5168 ZSre7 65.3988. Zsree 65. 2468 Zsr89 6s.7see Z5rle 66.8840 INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8000 INRCT 8.8888 INRCT 8.8888 INRCT 8. 8888 I NFICT G. 8000 INRCT 8.8888 INRCT 8.8888 RVG 67.5883 DEW CELLS RHD Zl 53+8832 RKD Z2 46.4729 RHD Z2 49.4473 RHD Z3 53 '627 RHD Z3 48.5114 RHD Z3 52.7837 RHD Z4 49.8863 RHD Z4 SG.3832 RKD Zs 58+3784 RHD Zs 49.8575 INRCT 8.8888 INRGT 8 ~ Geee INRCT 8. 8888 INRCT 8.8888 INRCT 8.8888 RVG 58. 4591 RMBIENT PRESS 14.4888 VRPOR PRESSURE o1888 DRY PRESSURE 55.3932 FLOWS 8.8888 5.8185 RECORD NUMBER - 253 DRTE 56 TIME 1845 PRESSURES 55.5748 55.5678 RVG 55.5785 RTD S Zirel 67.6588 Zlr82 67. 7848 Z lre3 67'488 Zir84 67. 4968 22re1 67.8928 22r82 67.7848 Z2re3 67. 8568 Z2r84 67. 7480 Z2r85 68.8548 Z2r86 67.7488 Z2re7 67. 8288 Z3rei 68.87 28 Z3r82 68.8988 Z3r83 68.8988 Z3r84 68.8548 23r85 68. 8720 Z3r86 68.4688 Z3r87 68.1448 23r88 68 1888 Z3re9

~ 68.1620 24rel 6S.4588 24r82 68.2788 Z4re3 68. 1988 24re4 68.28$ 0 Z4r'85 6S.5848 Z4r86 68.3428 24re7 68.1888 Z4ree 6S.lOS0 Z4re9 68.3868 Z4rie 68.3868 25rel 65.8668 Z5re2 65.6428 25r83 65.5888 Z5re4 65.2288 Zsres 66.1828 25r86 65.4988 25r87 65.3980 Zsree 65.2288 25r89 65.7148 Z5rle 66.S488 INRCT 8.8808 INRCT 8.8888 INRCT 8.8888 INRCT G.eeee INRCT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 8.8000 INRCT 8.8888 INRCT 8.8888 RVG 67.4864 DEW CELLS RHD Zi Seo8832 PHD Z2 48.3784 RHD 22 49.7837 RHD Z3 se.si14 RHD Z3 49.5755 RHD Z3 49.3832 RHD Z4 51. 4681 RHD Z4 45.5627 HD Z5 58.3784 RHD Z5 58. 8114 INRCT 8; Geee INRCT 8.0088 NRCT e.eeee INRCT 8 F 8888 INRCT Goeeee RVG 49.6869 RMBIENT PRESS 14. 4888 VRPOR PRESSURE . 1751 DRY PRESSURE 55. 3954 FLOWS 8. 8888 5.8185

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RECORD NUNBER - 254 DATE 56 TINE - 1988 PRESSURES 55.5718 55.5648 RVG 55.5675 RTD'S zirei 67. 6588 Zir82 67.7389 Zlr83 67.6588 Zlr84 67. 4969 Z2r81 67.9188 Z2r82 67.7848 Z2r83 67.7668 22r64 67. 8269 Z2r85 67.9288 Z2r86 67. 7488 Z2r87 67.7848 Z3r81 68.9999 23r82 68.8728 Z3r83 68. 6368 Z3r84 68.8188 23r85 68.1686 Z3r86 68.28SG 23r87 68. 1448 Z3reS 68.8728 Z3r89 68. 1446 Z4r81 68+4588 Z4r82 68.2168 Z4r83 68.2169 Z4r84 68.2?99 Z4r85 6S.5589 Z4r86 68.'248 Z4r87 68.1989 zw res 68o9990 24r89 68.3428 Z4riG 68. 3428 Z5rel 65.8389 Z5r82 65.6246 Z5r83 65.5888 Z5r94 65. 2288 ZSr85 66.1648 Z5r86 65.4446 ZSr87 65.3548 Z5r88 65.2188 Z5r89 65.6968 ZSrl6 66.7949 IHFICT 8.9868 INRCT 8.8899 INRCT 8.9889 INRCT 8.9960 INACT 8.8888 INRCT 8.8888 IHRCT 8.9888 INRCT 8.9990 I NFICT 8.8888 INRCT 8.8888 RVG 67.4644 DEW CELLS RHD Zl 47. 8191 PHD Z2 48.9888 RHD Z2 58.5755 RHD 23 48.8114 RHD Z3 49.4888 RHD Z3 52. 3319 RHD Z4 49.6396 RHD Z4 Sl.ieii RHD 25 58.4729 RHD 25 49. 7165 I NRCT 8.9896 INRCT 6.9866 IHRCT 8.8888 INRCT 8. 8888 INRCT 8.8888 RVG 49.7988 RNB IEHT PRESS 14.4888 VAPOR PRESSURE ~ 1763 DRY PRESSURE 55.3912 FLOWS 8.8888 5.8185

( RECORD NUMBER 255 DFITE 56 TINE 1915 PRESSURES 55.5698 55 561 8

~ Fl VG 55. 5658 RTD'S Zir81 67.5866 Zire2 67.?486 Zlr93 67.6589 Zir84 67.4966 Z2rei 67.8388 Z2r82 67. 7398 Z2r83 67.8388 Z2r84 67.7489 22rGS 67.9288 Z2r86 67.?398 22r87 67.7489 Z3rel 68.9969 Z3r82 68.9728 Z3r83 68.8368 Z3r84 68.8188 Z3r85 68.1269 23r66 68.2526 Z3r87 68.1268 23r88 68.9729 23r89 68.1986 Z4rel 68.4329 Z4r82 68.2348 Z4r63 68. 1448 Z4r94 68.1266 Z4r85 68.5766 Z4r86 68e2888 Z4re? 68.1889 Z4r88 6s.e909 24r89 68.3429 Z4r18 68.3248 ZSrei 64o9948 Z5r92 65.'5886 Z5r83 65.5?86 25r94 65.1929 Z5r85 66. 1649 ZSr96 65.4448 ZSr87 65.3369 Z5reS 65.1568 ZSr69 65.6786 25rle 66. 8129 INRCT 8.8998 IHRCT 8.8986 IHRCT 8.9899 IHRCT 9.9969 IHRCT Ge8888 INRCT 8.8889 INFICT 8.8989 INRCT 8.8096 IHRCT 8.8888 INRCT e.eeee RVG 6?s4446 DEW CELLS RHD Zl 52:7837 RHD Z2 49. 4345 RHD Z2 51. 7886 RHD Z3 51. 3447 RHD Z3 58.6268 RHD 23 52.6652 RMD Z4 51.9986 RHD Z4 53.4601 HD Z5 S8.5755 RHD ZS See 2165 INRCT G.eeee INRCT 8.9906 NRCT 8.8898 IHFICT Ge8898 INRCT 8.8888 FIVG 51. 4288 FINBIENT PRESS 14 ~ 4898 VAPOR PRESSURE ~ 1875 DRY PRESSURE 55. 3775 FLOWS Bo8988 So8185

1 FF

RECORD NUMBER 256 DFITE - 56 T IME - 1930 PRESSURES 55. 5660 55.5590 RVG 55.5625 RTD'S Zlr61 67.5560 Zlr02 67. 7120 Zir03 67.6760 Zir04 67 4786 Z2r01 67.7480 Z2r02 67. 7300 Z2r03 67.8748 Z2r04 67. 7366 Z2r85 68.0000 Z2r06 67.7308 Z2r07 67.7660 Z3r01 68 '728 Z3r02 68.8720 Z3r03 68.0360 Z3r04 68.0180 Z3r05 68.6726 Z3r86 68. 2160 Z3r07 68.0720 Z3r08 68.0360 Z3r09 68.0966 24r01 68.3788 24r02 68.1980 24r03 68.1620 Z4r04 68. 6726 Z4r05 6'8.5400 24r06 68.2880 24r07 68.0900 Z4r08 68.0546 Z4r09 68.3420 Z4ri0 68.3248 Z5r01 64.9760 ZSr02 65.5766 ZSr03 65.5340 Z5r04 65.1560 Z5r85 66.1280 Z5r06 65.4266 25r07 65.3000 25r08 65.1280 Z5r09 65.6420 25r10 66.7946 INRCT 0,0000 INRCT 0.0000 INRCT 8.0000 IHRCT 0.0600 INRCT 0.0080 INRCT 0.0000 INRCT '8.0000 INRCT 0.0666 INRCT 0+0000 INRCT 8.6000 RVG 67.4260 DEN CELLS RHD Zl 48.8704 RHD Z2 48.7678 RHD 22 47.9729 RHD Z3 50.6268 RHD Z3 48.011.4 RHD 23 54.1140 RHD Z4 49.8832 RHD Z4 51.3575 RHD 25 ,

50.5370 RHD Z5 49.7293 INRCT 0.0008 IHRCT 0.0600 INRCT 0.8000 INRCT 0.0800 INRCT 8 ~ 0000 RVG 49. 9574 RMB IEHT PRESS 14.4000 VRPOR PRESSURE ~ 1774 DRY PRESSURE 55. 3851 FLOWS 8 ~ 0000 5 '185

( RECORD NUMBER - 257 DATE - 56 TIME - 1945 PRESSURES 55. 5630 55.5560 AVG 55.5595 RTD'S Zlr01 67.5500 Zlr02 67.7128 Zir03 67. 6940 Zir04 67. 4246 22r01 67.8380 22r02 67.7308 Z2r03 67.8020 Z2r04 67.7120 Z2r05 67.9286 Z2r06 67.7120 Z2r07 67+7480 Z3r01 68.0360 23r02 68.0180 Z3r03 68'188 23r04 67.9820 Z3r05 68.8540 Z3r06 68. 1800 Z3r07 68.1080 23r08 68.0540 Z3r09 68.1086 Z4r01 68.3960 24r02 68 '168 Z4r03 68.1440 Z4r84 68. 2160 24r05 68.4500 Zar06 68.2700 Z4r07 68.0900 Z4r08 68. 0606 Z4r09 68.2528 Z4r10 68 '708 Z5r01 64.9586 ZSr02 65 55 25r03 65.5160 ZSr04 65.1388 Z5r05 66.1106 25r06 65.4266 25r07 65.2820 Z5r68 65 '020 Z5r69 65.6066 Z5r16 66.?946 I HFICT 0.0000 INRCT 0.0800 INRCT 0.0600 INRCT 0.0066 I NFICT 8.0080 INRCT 8.0088 IHRCT 0.0008 INRCT 0.0666 I NFICT 0.0000 INRCT 8.0000 RVG 67.4116 DEW CELLS RHD Zl 45.2422 RHD Z2 49 '883 RHD 22 52'165 RHD 23 49'191 RHD 23 49+6524 RHD 23 50. 8319 RHD 24 50.0499 RHD Z4 51.4661 HD Z5 50 ~ 3704 RHD 25 49. 3704 INRCT 0.0000 IHFICT 0. 0066 HRCT 0.0000 INRCT 0 ~ 8800 INRCT 0.0800 RVG 49 ~ 7515 RMB IEHT PRESS 14.4800 VRPOR PRESSURE .1768 DRY PRESSURE 55.3835 FLOWS 0 ~ 0000 5.8185

RECORD HUNBER - 258 DATE - 56 TINE - 2889 PRESSURES 55.5618 55.5538 AVG 55.5576 RTD'S Zlr81 67.5868 Zlr82 67.6768 Zir83 67. 6228 2 1r84 67.4666 Z2r81 67.8829 22r82 67.7388 Z2r83 67 ~ 8288 22r84 67.6589 Z2r85 67.9468 Z2r86 67.6948 Z2r87 67.6948 Z3r81 68.9186

,'3r82 68.8188 Z3r83 68. 8188 Z3r84 67.9648 Z3r85 68.6996 Z3r86 68.2168 Z3r87 68.8728 Z3r98 68.8548 Z3r69 68.6540 Z4r81 68,3248 Z4r92 68.1628 Z4r83 68.1988 Z4r84 68.6906 Z4r85 68.5768 Z4r86 68.2888 Z4r87 68.1268 Z4rGS 68.6189 Z4r89 68.2788 Z4riG 68.2529 ZSr81 64.9228 Z5r82 65.5340 Z5r83 65.4888 Z5r84 65.1288 Z5r85 66.8748 Z5r86 ,65.3996 ZSr8? 65.2648 ZSr68 65.8668 Z5r99 65.5788 25r18 66.7409 INACT 8.8889 IHACT 8.8888 IHACT 8. 8888 INACT 0.6908 IHACT 8.8888 IHRCT 8.8896 IHACT 8. 8888 IHACT 6.9600 IHFICT 8.8688 IHACT 8.8888 AVG 67 '938 DEW CELLS

.RHD 21 48.7678 RHD Z2 48.4888 RHD Z2 47.6811 RHD Z3 49.4691 RHD 23 49. 8319 RHD Z3 51. 5242 RHD Z4 58o5114 RHD Z4 59.4661 RHD Z5 58.3863 RHD Z5 49.7934 INFICT 8.8886 INFICT 8.6996 INACT 8.8868 INACT . 8.8888 IHACT 8. 8888 AVG 49.6488 ANBIEHT PRESS 14+4888 VAPOR PRESSURE .1753 DRY PRESSURE 55.3817 FLOWS 8.8888 5.8185 RECORD NUNBER 259 DATE - 56 TINE - 2815 PRESSURES 5S. 5578 55. 5588 55. 5535 RTD'S Z ir81 67.5328 Zir82 67.6588 Zlr83 67. 6468 2ir84 67.4969 Z2r81 67.8746 22r82 67.6948 Z2r83 67. 7388 Z2r64 67.6766 Z2r85 67.9469 Z2r86 67. 6488 Z2r97 67. 6768 Z3r81 68.6999 Z3r82 68.8889 Z3r83 67.9648 Z3r64 67. 9828 Z3r65 68.9699 Z3r86 68.8968 Z3r87 68.8728 Z3r98 68. 8188 Z3r89 68 '980 Z4r81 68.3689 Z4r82 68.1449 Z4r83 68. 1888 Z4r94 6e.2346 Z4r85 68.3699 24r86 68.2166 Z4r67 68. 8368 Z4r88 67.9646 Z4r89 68. 1989 24r18 68.2168 Z5r61 64.9648 Z5r62 65.49SG ZSr63 65.4868 Z5r84 65.1826 Z5r85 66.8568 Z5r96 65.3996 ZSr67 65.2466 ZSr98 65.8488 Z5r69 65.5526 Z5r19 66.6129 INACT 9.6966 IHACT 8.8968 INFlCT 8.8669 INACT 8.6900 I NFICT 8.8960 IHRCT 8.6688 IHACT 6. 6866 INACT 8.9600 IHACT 8.8688 IHACT 8.8886 AVG 67+3733 DEN CELLS RHD Zl 52. 1148 RHD Z2 52 '345 RHD Z2 52. 1781 RHD Z3 51.4986 RHD 23 49.4345 RHD Z3 51. 4986 RHD Z4 52.8499 RHD Z4 51 o 1146 RHD 25 58.4858 RHD Z5 49. 8319 I HACT 8.8888 IHFICT 8. 9990 HACT 8 ~ 6888 INACT 8.8888 INFICT 8.8888 AVG 51.2915 ANBIEHT PRESS 14'888 VFIPOR PRESSURE ef865 DRY PRESSURE 55.3678 Fl OMS Be8888 5.8185

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RECORD HUttBER " 268 DRTE - 56 TINE 2838 PRESSURES 55. 5558 55'478 RVG 55. 5518 RTD'S Zlr81 67. 4968 Z lr92 67.7128 Zlr83 67.6488 2ir94 67.4240 Z2r81 67. 8748 Z2r82 67.6?68 Z2r83 67.8568 Z2r94 67.6949 Z2r95 67.8748 Z2r86 67.6768 22r87 67.7128 23r81 67.9469 Z3r82 67.9468 Z3r83 67.9468 Z3r84 67.9189 Z3r85 67.9829 Z3r86 68.8988 Z3rB? 68.8368 Z3r88 67.9829 Z3r89 6S.9549 Z4r81 68.3688 Z4r82 68. 1888 24r83 68. 1888 Z4r84 68.9720 Z4r85 68.3788 Z4r86 68.1988 Z4r87 68. 8368 Z4rGS 67.9S29 Z4r99 68.1988 Z4rlG 68.2348 25r91 64.9848 Z5r82 65.4899 25r83 65.4448 ZSr94 65.8848 Z5r85 66.8288 25r86 65.3728 Z5rG? 65.2188 Z5r88 65.8388 ZSr89 65.5348 25riB 66.7499 I NFICT 8.8888 INRCT Go8889 INRCT 8.8888 INRCT 8.9909 INRCT 8.8888 INRCT 8.8988 INRCT 8.8888 IHRCT 8.8999 I NFICT 8.8899 IHRCT 8.8888 AVG 67.3593 DEN CELLS I RHD 21 49.9986 RHD Z2 46.7678 RHD Z2 58. 1781 RHD Z3 49.3794 RHD 23 51. 9345 RHD 23 58.2678 RHD Z4 52.5755 RHD Z4 49.8963 RHD Z5 59.3784 RHD 25 49.5627 INRCT 8.8889 INACT 8.9099 I NFICT 8.8888 INRCT 8.8888 INFICT 8.8888 RVG 58.8586 ANBIENT PRESS 14.4888 VAPOR PRESSURE ~ 1788 DRY PRESSURE 55. 3738 FLONS 8+8888 5 '185 RECORD NUNBER 261 DRTE 56 TINE 2845 PRESSURES 55.5528 55e5458 RVG 55.5485 RTD'S I 2l r81 6?o4789 2ir82 67. 6948 Zi r93 67. 6229 Zir84 67.4249 Z2r91 67.7128 22r82 67.6588 Z2r83 67. 7388 Z2r84 67.6589 Z2r95 67.8388 Z2r96 67.6588 22r87 67.6948 Z3r91 67.9649 23r82 67.9289 23r83 67.9468 Z3r84 67.9288 Z3r85 68.9549 Z3r96 68.1898 Z3r97 68. 8189 Z3r98 67.9828 Z3r99 68.0009 Z4r91 68.3249 Z4r82 68.1448 24r83 68.1889 24r84 68. 9729 Z4r95 68.5849 Z4r96 68.2529 24re? 68.8360 24r88 67.9469 24r99 68.1629 Z4r18 68.2168 Z5r81 64.8868 Z5r82 65.4629 25r83 65.4269 Z5r84 65.8488 25r85 66.8288 Z5r86 65.3189 Z5r87 65.1929 Z5r88 65. 8128 Z5r09 65. 5168 Z5r18 66.7940 IHRCT 8.8899 IHRCT Go 9888 IHFICT 9.8889 INRCT 9.9098 IHRCT 8.9889 I HFICT 8. 8888 I NFICT 8.8888 INRCT 8. 9909 INRCT 8.8888 INRCT 8. 8888 RVG 6?.3442 DEW CELLS RHD Zl 52 '345 RHD Z2 52.5883 RHD Z2 52.9883 RHD 23 58. 8191 RHD Z3 48.6989 RHD 23 51. 2678 RHD Z4 48.3832 RHD 24 48. 2678 RHD 25 58. 1989 RHD ZS 58. 2165 INFICT 8 8988 IHACT 8. 8900 HRCT 8.8898 I NFICT 8. 8889 IHRCT 8 '888 RVG 58.5739 RNBIEHT PRESS 14.4888 VRPOR PRESSURE .1816 DRY PRESSURE 55 '669 FLOWS 8.8888 5o 8185

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RECORD NUI'1BER " 262 DATE - 56 TINE - 2188 PRESSURES 55. 5498 55.5418 AVG 55.5459 RTD'S Zirei 67. 5148 Zlr82 67. 7128 21r83 67.5668 Zlr94 67.3700 Z2rel 67.7648 Z2r82 67 ~ 6228 Z2re3 '7.7646 Z2r64 67.6SSO Z2r85 67.63SG Z2r86 67.5668 Z2r87 67.6488 Z3rei 67.9466 Z3r82 67.92SG Z3r83 67.9188 Z3r84 67.6928 23r65 67.9196 Z3r86 6S. 1968 Z3r87 66.8368 23reS 67.9628 Z3r89 6S.8600 24rei 66.3248 Z4r82 66.1628 Z4r83 66.8988 Z4r84 6S.9720 Z4re5 66.4668 Z4r86 6S.1628 Z4r87 6S.GBGG 24reS 67. 9640

'24r89 6S. 1628 Z4r1 8 66.2168 25rel 64.6588 25r82 65.4266 Z5r83 65.48SG 25r84 65.8388 25r85 65.9668 Z5r86 65.31SO Z5r67 65.1740. Z5reS 65.8128 25r89 65.49SG Z5rie 66.7229 INFICT 8.8988 IHACT 8. 8868 IHACT 8. 8888 IHACT 0.9990 IHACT 8.8888 INACT 8. 8986 INACT 8.8888 IHACT 8.6860 INACT 8.8688 IHRCT 8. 8888 AVG 67.3297 DEW CELLS RHD 21 51. 6447 RHD Z2 47.7934 RHD Z2 51.1652 RHD 23 56.4217 RHD Z3 49.6652 RHD Z3 49.5755 RHD 24 51.46SS RHD 24 4S.767S RHD Zs 58.8378 RHD 25 49.3S32 INFICT GIGGGG IHACT 6.6996 INACT 8.8898 IHACT 8.8868 INRCT 8.8686 AVG 49.996S AMBIENT PRESS 14.4889 VAPOR PRESSURE .1777 DRY'RESSURE 55.3673 FLOWS 8.8888 soS1SS i RECORD NUI1BER 263 DATE - 56 TINE 2115 PRESSURES 55.5478 55.5398 AVG 55.5439 RTD'S Zirei 67. 4666 2ir62 67.6488 Zlr83 67. 5588 Zlr94 67. 3520 Z2rel 67.74SG Z2r82 67.6948 Z2r93 67.7126 Z2r94 67.6229 22r85 67.63SG Z2r86 67.5589 Z2r87 67.6228 Z3rel 67.9469 Z3r92 67. 92SG Z3r83 67.9188 Z3r84 67.6568 23r95 67.S929 Z3re6 6S. 1448 23r87 67.9648 Z3reS 67.9468 23r89 67.9S26 24rei 6S.3666 Z4r82 66.6986 Z4re3 6S.6549 Z4r64 67.9S20 Z4r85 66.4148 Z4r66 6S. 19SG Z4r87 6S,GGGG Z4rGS 67.6929 Z4r89 66.1628 24rle 6S. 1628 25re1 64.6146 Zsr82 65.4269 Z5r63 651 3988 25r64 65.8128 25r85 65.94SG Z5r66 65.2646 ZSre7 65.1568 25reS 64.9948 Z5r89 65o4SGG 25rle 66.7949 INACT 8.8888 IHACT 8.8888 INACT 9.8696 INACT 6.6600 INACT 8.6898 IHFICT eoeeee IHFICT 8.8888 INRCT 9.6099 I NFICT 8.8888 INACT e.eeee AVG 67.2996 DEW CELLS RHD 21 51. 6148 RHD Z2 49.2293 RHD Z2 51.9345 RHD Z3 4S ~ 1524 RHD Z3 47.6378 RHD Z3 49.9217 RHD Z4 47 '447 RHD Z4 49. GSS3 RHD Z5 58.2293 RHD Zs 49. 3191 INFICT, . e. 8868 INACT G. 6906 I HFIC T 8. 8868 IHACT 8. 8688 IHFICT e. 8888 AVG 49+4664 AMBIENT PRESS 14. 4888

( VAPOR PRESSURE ~ 1743 DRY PRESSURE 55. 3667 FLOWS 6.8888 5.61S5

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RECORD NUHBER - 264 DRTE 56 TINE - 2138 PRESSURES 55. 5448 55e5368 RVG 55. 5489 RTD'S Zlrel 67. 4868 Z lr82 67. 5328 Zir83 67. 5328 Zlr84 67.3?99 Z2rei 67. 7668 Z2r82 6?e 6228 Z2r83 67. 7668 Z2r94 67.5689 22r85 67.8298 22r86 67.5588 Z2r87 6?. 6848 Z3rel 67.9199 Z3r82 67. 9188 Z3r83 67 '188 Z3r84 67. 8568 Z3r85 67.9289 Z3r86 68. 1888 Z3r87 67.9648 Z3r98 67.9188 23r89 6?.9649 24r81 68.2788 Z4r82 68.8368 Z4r83 68.8368 Z4r84 67.9829 Z4r85 68.4328 Z4r86 68.2168 24r87 67.9828 Z4r88 67.8749 Z4r89 68.1888 Z4rle 68.1448 25rel 64.7968 Z5r82 65 '999 ZSr83 65.3548 25r84 64.9948 25r85 65.9388 Z5r86 65.2649 Z5r87 65. 1389 Z5r88 64.9588 Z5r89 65..4628 Z5rle 66.7049 I NFICT 8.8888 INRCT 8.8888 INRCT 8.8888 INRCT 9.9900 INRCT 8.8888 INRCT 8.8898 INRCT 8.8888 INRCT 8.9999 INRCT 8.8888 INRCT 8.8888 RVG 67 '856 DEW CELLS RHD Zl 47.3832 RHD Z2 47.8963 RHD 22 49.5242 RHD 23 59.2934 RHD Z3 58. 3191 RHD 23 58. 6811 RHD 24 48.9888 RHD 24 59.2165 RHD Z5 58.3832 RHD Z5 49.6148 INRCT 8.8888 INRCT Geoeoe INRCT . 8.8888 INRCT 8.8888 INRCT e.eeee FIVG 49.4965 FINBIENT PRESS 14.4889 YFIPOR PRESSURE .1743 DRY PRESSURE 55.365?

FLOWS Goeeee .5.8185 RECORD NUMBER 265 DRTE - 56 TINE 2145 PRESSURES 55.5418 55.5338 RVG 55. 5378 RTD'S Zlrel 67.4429 Zlr82 67.6489 Zlr83 67.5589 2ir84 67 3169

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22roi 67.7668 Z2r82 67.5588 22r83 67.7488 Z2r84 67. 5869 Z2r85 67.8828 Z2r86 67.5868 22r97 67.5688 Z3rel 67. 8929 23r82 67.8928 Z3r83 67.8568 Z3r84 67.8389 Z3r85 67. 9469 Z3r86 68.8898 Z3r87 67.9468 Z3r88 67;8748 23r89 67 9469

~

Z4rel 68.2528 Z4r82 68.8728 Z4r83 68.9188 Z4r84 67. 9289 24r85 68.3968 Z4r86 68.8988 Z4r87 67.8928 24r88 67. 8569 Z4r89 68.8728 Z4rie 68.1888 25rea 64.7789 25r82 65. 3729 25r83 65.3368 Z5r84 64.9768 25r85 65.9388 Z5r86 65 2460

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Z5r87 65.1288 25r98 64.9499 Z5r89 65.4888 25r 1 8 66. 7229 INRCT 8.8889 INRCT 8.8888 INRCT 8.8988 INRCT G. 8999 INRCT 8.9888 I NFICT 8.8888 INRCT 8.9998 INRCT 8. 8990 INRCT e.eeee INRCT B.BBBB RVG 67.2648 DEW CELLS RHD 21 47.5755 RHD 22 58. 1268 RHD 22 58. 7165 RHD Z3 48.8832 RHD Z3 58.2837 RHD 23 58o6268 RHD Z4 48.6268 RHD Z4 49. 6396 RHD Z5 58+8755 RHD 25 49 '934 INFICT 8.8889 INRCT G. 8999 NRCT e.csee INRCT 8.8988 INRCT 8.8888 RVG 49.6391 RNBIENT PRESS 14. 4898

( VRPOR PRESSURE .1753 DRY PRESSURE 55.3617 FLOWS 8. 8888 5. 8185

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RECORD NUMBER - 266 DFITE 56 TINE - 2288 PRESSURES 55'388 55 '318 RVG 55 5345

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RTD'S Zirei 67. 4960 Z 1 r82 67.5688 Zlr93 67. 5148 Z lr84 67.289e Z2rel 67.7488 Z2r82 6?e5588 Z2r83 67. 7128 Z2r84 67.55ee Z2r95 67.8828 Z2r86 67.6228 Z2r87 67 '688 Z3rel 67.8749 23re2 67.8748 Z3r83 67.856e Z3r84 6?.8828 Z3r85 67.8929 Z3r86 68.8368 Z3r97 67.9468 23r88 67.8928 Z3r89 67.9649 Z4rel 68. 2168 Z4r82 68.8988 Z4r83 67.9648 24r84 67. 9649 Z4r85 68. 3429 24r86 68.8988 24r87 67.9468 Z4r88 67. 9189 Z4r89 68.1448 Z4r,ie 68. 1268 25r81 64.7788 25r82 65.3728

~ Z5r83 65.3369 Z5r84 64. 9588 Z5r85 65.,8768 Z5r86 65.1569

'25r87 65. 1828 25r88 64. 9488 Z5r89 65.4888 Z5rle 66.6688 I NFICT 8.8989 INRCT 8. 8888 INRCT 8.8888 INFICT 8. 9999 IHRCT 8.8898 INRCT 8. 8888 INRCT 8 '888 INRCT 8. 9909 INRCT 8.8888 INRCT 8. 8888 RVG 67.2537 DEW CELLS RHD Zl 52.8755 RHD Z2 44. 9858 RHD 22 45.8575 RHD Z3 49.9988 RHD Z3 48.8499 RHD Z3 49.2422 RHD Z4 49o8378 RHD Z4 47.3863 RHD Z5 59. 2165 RHD Z5 58. 1396 IHRCT 8.8888 IHRCT 8.9999 IHRCT 8.8988 INRCT 8.8888 INRCT B.eeee RVG 48.7121 RNBIEHT PRESS 14.48ee VAPOR PRESSURE .1692 DRY PRESSURE 55.3653 FLOWS 8.8888 5.8185 RECOPD NUMBER - 267 DRTE - 56 TIME - 2215 PRESSURES 55.5368 55.'5298 RVG 55.5325 RTD'S Zlrel 67. 3789 Zlr82 67. 5598 Zlr83 67.5148 Zir84 67.2628 Z2rei 67.?128 Z2r82 67.5589'2r83 67.6768 Z2r84 67.56se Z2r85 67.7848 Z2r86 67.4968 Z2r87 67.5688 23rel 67.8389 Z3r92 67.8389 Z3r83 67.8389 Z3r84 67.8388 Z3r85 67.8299 Z3r96 68.8988 Z3r87 67.9188 Z3r88 67.8568 Z3r89 67.9199 Z4rel 68.2348 Z4r82 68.8188 Z4r83 67.9648 Z4r84 68.8360 Z4r95 68.3869 24r86 68. 1888 Z4r87 67.9188 Z4rBS 67.8560 Z4r89 68.9999 Z4rle 68.8988 Z5rei 64.7688 Z5r82 65.3369 ZSr83 65.3188 25r84 64.9588 Z5r85 65.8589 Z5r86 65.2198 Z5r87 65. 1928 Z5r88 64.9488 Z5r89 65.3989 25rle 66.6599 INRCT Greece IHRCT Boeeee INFICT 8.9888 I NFICT 8.9009 IHRCT 8.9999 IHRCT 8.8888 INRCT 8.8888 IHRCT G.eeee IHRCT 8.8888 IHRCT 8.8888 RVG 6?.2358 DEW CELLS RHD Zl 48. 1989 RHD Z2 46.8755 RHD Z2 48.5378 RHD Z3 52. 2934 RHD Z3 58. 1811 RHD Z3 Seoe?55 RHD Z4 51. 4888 RHD 24 49.1149 RHD Z5 49+9681 RHD 25 49.8447 INRCT 8. 8888 INRCT 8.8999 NRCT 8.8888 INRCT Be8888 INFICT 8.8888 RVG 49.5259 FIMB IENT PRESS 14e4888 VFIPOR PRESSURE ~ 1745 DRY PRESSURE 55.3588 FLOWS 8.8888 5.8198

pL s>

i j'i'r I

I E.

f ll

RECORD HUNBER - 26S DATE - 56 TINE - 2238 PRESSURES 55. 5348 55.5268 AVG 55'369 RTD'S Zir91 67,3788 Zlr82 67. 4688 Zir83 67. 4788 Z ir84 67. 3528 22r81 67,5148 22r82 67 '328 Z2r83 67 6488 Z2r84 6? o 6649 Z2r85 67.6948 Z2r86 67.5588 22r87 67. 5588 Z3r91 67.6566 Z3r92 67.8928 Z3r83 67 '568 Z3r84 67.9828 Z3r85 6?o8569 Z3r86 68. 1888 Z3r87 67.9188 Z3r88 67.6568 Z3r89 67.6929 Z4r81 68.2528 Z4r82 6e.eiSB Z4r83 67. 9828 Z4r64 67.9169 Z4r85 68.3428 Z4r96 68.1268 Z4r87 67.92SB Z4ree 67.83$ 6

~ 24r99 68.8988 Z4r18 68 '988 ZSr81 64.?688 Z5r92 65.3368 ZSr63 65.3868 Z5r84 64.9488 25r85 65.8768 Z5r86 65.1566 ZSr67 65.8668 25rBS 64.9848 Z5r89 65.4888 Z5r18 66.5966 IHACT 8.8886 IHACT 8.8898 INACT 8.8888 INRCT 8.8966 I HFICT 8.8888 IHACT 8.8888 INACT 8.8888 INACT 9. 9909 INACT B.BBBB IHFICT 8. 8888 FIVG 67 '264 DEN CELLS RHD Zl 49.4858 RHD Z2 47.6989 RHD Z2 49.1781 RHD Z3 51. 1611 RHD 23 48 '678 RHD Z3 51.3784 RHD Z4 46.6999 RHD Z4 49. 2559 RHD Z5 58.2556 RHD ZS 49.5883 IHACT 9.8998 INFICT 6.8966 IHACT 8.8888 INACT 8 8888 INACT F 8.8898 AYG 49.4878 ANBIENT PRESS 14.4888 YAPOR PRESSURE .1743 DRY PRESSURE 55.3557 FLOWS 8.8988 5. 8198 RECORD HUNBER 269 DATE >> 56 TINE - 2245 PRESSURES 55. 5318 55.5248 AVG 55. 5275 RTD'S Zlr91 67,3789 Zlr92 67.5598 Zlr83 67. 4428 Zlr94 67.2626 Z2r81 67.6488 Z2r82 67.5328 Z2r93 67. 5966 Z2r84 67.5329 22r95 67.7489 22r96 67.5148 Z2r67 67. 5149 Z3r91 67.8389 Z3r82 67.8298 Z3r83 67.9268 Z3r94 67. 9626 Z3r85 67.S3SB Z3r86 68.8729 23r97 67.8928 23rBS 67. 6269 Z3r69 67.S746 Z4r81 69.1.9SB Z4r92 6Se8988 24r83 67. 9469 Z4r84 6S.6906 Z4r85 69.3696 Z4r86 66.1268 Z4r97 67. 9199 Z4rBS 6?.S929 Z4r89 66.8989 Z4r18 68.8728 'Z5r81 64.7248 25r82 65.3186 Z5r93 65.2928 Z5r84 64.9229 Z5rBS 65.9486 Z5r66 65.1266 Z5r87 65.64SB ZSrBS 64.9848 ZSr89 65.3728 25r18 66.6140 IHACT 9.8966 IHACT 8.9988 INACT 6.9668 INACT 9.6009 INACT 9.6888 IHACT 8.8888 INACT 8.8988 INACT 9.8990 IHACT 8.8888 IHACT 8.9899 AVG 67 ~ 2891 DEW CELLS RHD Zl 49.9681 RHD Z2 49.4729 RHD Z2 51.9319 RHD 23 51.6SS3 ROD Z3 51 e 3447 RHD Z3 49.9755 RHD Z4 51.8114 RHD Z4 51. 9217 RHD Z5 49. 9217 RHD Z5 49o6524 INACT 9. 6888 INACT 6.9669 HACT 8.8896 IHACT 8.8969 INACT 8;6969 YG 58. 4955 ANB IENT PRESS 14.4996 YFIPOR PRESSURE ~ 1818 DRY PRESSURE 55e3465 FLOWS 9.8886. 5.8198

gh~

E p

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RECORD NUMBER 278 DATE - 56 TIME - 2386 PRESSURES 5S.5298 55. 5218 FIVG 55. 5258 RTD'S 2lr81 67.3888 Zlr82 67. 4688 2 lr83 67.3788 21r84 67. 2446 Z2r81 67.6588 Z2r82 67.4968 Z2r83 67.5588 Z2r84 67. 5599 Z2r85 67.7488 22r86 67.4788 Z2r87 67.5148 23r81 67. 8389 23r82 67.8288 Z3r83 67.8828 Z3r84 67.7668 Z3r85 67.7666 Z3r86 68. 1688 Z3r87 67.8748 Z3r88 67.8288 23r89 67.8566 24r81 68. 1988 Z4r82 68. 8188 Z4r83 6?.9468 Z4r84 67.8929 24r85 68. 3248 Z4r86 68.8548 Z4r87 67 '928 Z4r88 67.8299 24r89 68. 8188 Z4ri 9 68.8548 Z5r81 64.7428 25r82 65.3666 25r83 65.2648 Z5r84 64.9848 Z5r85 65.8848 ZSr86 65.1626 25r87 65.8668 25r88 64.8868 25r89 65.3728 Z5r18 66.S429 I NRCT 8.8888 INRCT 8.8888 INFICT 8.8888 INFICT 8.6960 INRCT 8.8888 INRCT 8.8868 INRCT 9.9668 INRCT 8.6960 INRCT 8.8888 INRCT 8.8888 RVG 67'899 DEW CELLS RHD 21 58.7559 RHD 22 49.7678 RHD 22 58.2422 RHD 23 51.5755 RHD Z3 48.9691 RHD 23 48.7422 RHD 24 46.6268 RHD Z4 49.3863 RHD Z5 58.8114 RHD 25 49. 6148 INRCT 8.8889 INFICT 8.8669 INRCT 8. 8888 INRCT 8.8888 INRCT 8.8868 RVG 49 ~ 5841 AMBIENT PRESS 14.4888 VAPOR PRESSURE .1749 DRY PRESSURE 55.3591 FLOWS 8.8888 5 ~ 8198 RECORD NUMBER - 271 DRTE 56 TIME' 2315 PRESSURES 55. 5278 55. 5198 RVG 55.5238 RTD'S 2lr61 67. 3168 Z ir82 67. 4968 2ir83 67.4688 Zlr84 67. 2268 Z2r61 67.6768 22r82 67.5148 22r83 67.5689 22r84 67. 4789 Z2r85 67.7128 22r86 67.4?88 Z2r87 67.4968 Z3r81 67. 8209 Z3r82 67.7848 23r83 67.8928 Z3r84 67.7668 Z3r85 6?.7486 Z3r86 68.8189 Z3r87 6?.8568 Z3r88 67.8286 Z3r89 67.8926 24r81 68. 1886 24r82 67.9288 Z4r83 67.9648 Z4r84 67.9466 Z4r85 68.2526 Z4r86 68.8368 Z4r87 67.8568 24ros 6?o7848 24r69 68.8728 Z4riG 68.8368 25r81 64.7868 Z5r62 65 '829 25r83 65.2468 Z5r84 64o9848 25r85 65.7868 Z5r86 65.6669 Z5r87 65.8488 ZSr88 64.8868 2Sr89 65.3546 Z5r19 66.5966 INFICT 8.8886 INRCT 8 '988 INFICT 8.8886 INFICT 8.6699 INRCT 8,8898 INFICT 6.8688 INRCT 9.8899 INRCT 9.9966 INRCT 8.8888 INRCT 8.8969 RVG 67.1787 DEW RHD Zi CELLS 48.7293 RHD Z2 52. 3447 RHD '2 48.4858 RHD Z3 49 ~ 5242 RHD 23 49.3968 RHD 23 51. 7837 RHD 24 58.5627 RHD Z4 48'242 RHD Z5 49.9858 RHD ZS 49. 3784 INFICT 8..8888 INRCT G. 6069 NRCT 8.8986 INRCT 8. 8888 INRCT 8.8888 RVG 49.8556 AMBIENT PRESS 14.4889 PRESSURE 'APOR

.1767 DRY PRESSURE 55e3463 FLOWS 8.8888 5. 8198

ff

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RECORD NUNBER - 272 DATE - 56 TINE - 2330 PRESSURES 55. 5258 55.5178 AVG 55.5218 RTD'S Zirei 67.3520 Zire2 67. 4788 Zir83 67.4680 Zir84 67. 2448 22rei 67.4428 Z2r82 67.4968 22r03 67.4780 Z2r84 67.5328 Z2r85 67.6400 22r06 67 '688 Z2r87 67.5328 Z3rei 67.8288 Z3r82 67.7840 Z3r03 67.7840 Z3r04 67.7480 Z3r85 67.7668 Z3r06 67.9648 Z3r87 67.8388 Z3r08 67.8020 Z3r89 67.8748

~ Z4rei 68. 1440 Z4r82 68.8888 Z4r03 67 '460 Z4r84 67.8568 Z4r05 68.3420 Z4r86 68.0728 Z4r87 67.8928. Z4r88 67.7848 Z4r89 68.0360 Z4rie 68.0720 Z5rei 64.7240 Z5r82 65 '888 ZSr03 65.2640 Z5r04 64.8860 25r05 65.8040 Z5r86 65. 8668 Z5r87 65.8120 Z5reS 64.8320 ZSr09 65.3360 25rie 66 4528

~

INACT 8.0800'NACT 8.0880 INACT 8 '000 INACT 8.8088 INACT 0.8080 INACT e.eeee INACT '8.0080 INACT 8.8888 INACT 8.8008 INACT 8.0888 AVG 67 ~ 1629 DEW CEI LS RHD Z 1 49. 1524 RHD Z2 51.5627 RHD Z2 49o2550 RHD 23 58.5378 RHD Z3 58.3447 RHD Z3 51.2886 RHD 24 52.6268 RHD Z4 46.8863 RKD Z5 49 '934 RHD Z5 49.5755 INACT 8.8888 INFICT 0.8888 INACT 8 ~ 0800 INACT B.eeee INACT 8.8888 FIVG 50.8732 RI'1B I ENT PRESS 14.4eee VAPOR PRESSURE .1782 DRY PRESSURE 55.3428

.FLOWS 8.8080 5.8198

0

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EN V I RONNE N T LISTING +++++++++++++++++ ++++++++++

JUL IRN DRTE 55 TINE - 1445 REC DRTE T j NE TEMP VRPOR CONTRINNENT RELRTIVE 'IR PSIR Ut1 PRESSURE PRESSURE HUMIDITY DENSITY VRRIRNCE 141 55 1445 529. 288 . 2838 55. 6455 56. 71 ~ 2838 8.88888 142 ss 15ee 529.179 ~ 2818 55. 6437 56. 42 ~ 2838 -.88.183 143 SS 151S 529. 151 ~ 2812 55.6488 56. 31 ~ 2838 -oee298 144 55 1538 529. 125 ~ 2845 55.6335 57. 38 ~ 2838 -+88?36 145 55 1545 529. 892 ~ 1998 55.6368 55. 88 e2838 .88256 146 55 1688 529.878 ~ 1947 55.6373 54 ~ 63 .2838 ~ 88129 147 55 1615 529.861 .2885 55.6285 56. 38 .2838 -.88883 148 55 1638 529.825 .1967 55.6298 55. 28 .2838 .88135 149 55 1645 529.888 .1992 55.6248 56. 81 e2838 -.88497 ise 55 1 r 88 528.988 ~ 1996 55.6289 56. 28 ~ 2838 -.88396 151 55 ir 15 528.972 .1992 55.6188 56. 88 .2838 -.88285 152 55 1738 528.944 .2813 55.6142 56. 73 .2838 -.88461 153 55 1 r 45 528.929 ~ 1982 55.6153 55. 88 ~ 2838 .88112 154 55 1888 528e988 e 2827 55.6878 570 21 .2838 -.88757 155 55 1815 528 '79 ~ 1996 56'8 .2838 .88814 156 157 55 55 1838 1845 528.868 528.835

.1954

.1962 55.6879'5.6896 5S.6858 55 '2 sso58

.2838

~ 2838

.88172

-.88388 158 55 1988 528.825 .1989 ss.eeee 56. 28 .2838 -.88528 159 55 1915 528.888 .1989 55.5976 56. 34 .2838 -.88382 lee 55 1938 528.791 .2824 55.5921 5?. 34 .2838 -.88558 161 55 1945 528.769 .1992 55.5928 56. 48 .2838 .88878 162 55 2888 S28.?S1 .1938 55.5957 S4. 99 .2838 .88289 163 55 2815 528.729 ~ 2838 55.5837 57. 87 .2838 -.81281 164 55 2838 528. 713 .1966 ssi5889 55. 84 .2838 .88525 65 55 2845 528. 684 .1975 55.5858 56. 18 .2838 -.88399 6 55 2188 528. 6?9 ~ 1912 55.5893 54. 37 ~ 2838 .88438 67 55 2115 528. 657 .1936 55.5849 55. 11 .2838 -.88443 168 55 2138 528. 647 1981 55.5784 56. 48 .2838 -.88648 169 55 2)45 528.626 .1962 55,5783 55.98 .2838 -.88818 178 55 2288 528.613 ~ 2888 55.5717 5?.24 .2838 -.eeee2 171 55 2215 528.682 .1978 55.5732 56.48 .2838 e88152 172 55 2238 528.578 1947 55.5733 55.57 .2838 .88889 173 174 55 55 2245 2388 528.564 528.541

~

~ 1995

.1984 55.5678 55.5656 56 '5

56. 78

~

2838 2838

-.88625

- ~ 88145 175 SS 2315 528.522 .1954 55.5671 55. 88 .2838 .88149 176 55 2338 528.516 .1936 55.5669 55. 37 .2838 -.88817 177 55 2345 528.499 .1974 55.5616 56 ~ 49 .2838 -+88532 178 56 8888 528.484 ~ 1991 55.5569 57. 81 ~ 2837 .88478 179 56 8815 528.466 ~ 1978 55.5567 56. 68 .2838 -.88823 188 56 8838 528.468 .1978 55.5547 56. 67 .2838 -.88194 181 56 8845 528.444 e2818 SS.SS88 57. 63 .2837 .88473 182 56 8188 528.432 .1952 55.5538 56. 88 .2838 .88375 183 56 8115 528. 489 .1967 55.5498 56. 45 .2838 -.88392 184 56 8138 528. 394 e1988 55.5478 56. 86 .2837 -.88288 185 56 8145 528. 379 ~ 1979 55.5446 56. 87 ~ 2837 .88245 186 56 8288 528. 367 ~ 1962 55.5438 56. 48 ~ 2837 -.88878 187 56 8215 528.346 .1969 55.5411 56. 65 .2837 -.88274 188 56 8238 528.332 ~ 1957 55.5413 56. .2838 .88825 528.327 55.543? 2838 .88239 32'so 189 56 8245 ~ 1913 87 ~

8 56 8388 528.385 ef974 55.5351 .56. 86 .2837 -.88858 i 56 8315 528.283 ~ 1949 55 '351 56. 19 .2837 .88883

ENVIRONMENT LISTING +++++a++++++++++++yyy++++yy JUL IRN DFITE 55 TINE - 1445 EC DFlTE T) ME TEMP VRPOR CONTR IHNENT RELFlT I VE Fl IR PS IR UN PRESSURE PRESSURE HUNI DITY DENSITY VFlRIRNCE 192 193 56 8338 56 8345 528.275 528.257

.'889

.1968 55.5391 5S.5292 54 '7

56. 78

.2838

~ 2837 -

~

88499 89987 194 s6 ei'88 528.244 ~ 1918 55.5332 55. 37 .2838 .88396 19S Gc. 1 5 528.221 .1998 55.5312 55 ~ 12 .2838 -.88197 196 56 Gc 38 528.286 .1981 55.5299 54. 94 ~ 2838 -o88139 197 56 8445 528.194 .1873 55 '297 54. 16 ~ 2838 -I88822 198 56 8588 528.176 .1938 55.5228 SS. 85 ~ 2837 -o89779 199 56 8'ris 528.145 .1952 55 '168 56'4 ~ 2837 -e88528 288 56 8538 528.139 . 1989 55.5288 55. 94 .2837 .88323 281 56 8545 528. 132 .1972 55. 5188 57 ~ 14 *

.2837 -.88921 282 56 8688 528. 182 ~ 1989 55.5151 55 ~ 38 ~ 2837 .88429 283 56 8615 528. 886 ~ 1969 55 '871 57. 16 ~ 2837 -.ee892

.284 56 8638 528. 872 .1876 55.5134 54. 47 .2837 ".89635 28S 56 8645 528. 849 ~ 1991 55.4999 57. 87 .2837 -.81356 286 S6 er'ee 528. 838 ~ 1972 55 '988 5?. 32 ~ 2837 -o88184 287 56 8715 528. 817 ~ 1894 55.5846 55. 18 .2837 .88579 288 56 9 r'38 527. 994 ~ 1874 55.5836 54 ~ 55 .2837 -.88898 289 56 9 r'45 527. 982 e 1913 55.4977 55. 72 .2837 -.88592 218 56 8888 527. 964 ~ 1942 55.4928 56. 68 .2837 -.88498 211 56 8815 527. 948 .1896 55.4949 55. 38 .2837 .88287 212 56 8838 527.929 e 1843 55 '977 53'8 +2837 .8827?

.89679 213 56 8845 527.983 . 1886 55.4989 55. 18 ~ 2837 214 56 8988 527 '92 ~ 1936 55.4839 56. 56 I2837 - ~ 88695 15 6 8915 527.878 .1912 55.4838 55. 91 ~ 2837 -.88814 6 56 8938 527.852 ~ 1835 55 '895 53. ?1 ~ 2837 ~ 88567 56 8945 527.842 ~ 1937 55.4768 56. 69 .2837 -<<81263 218 56 1888 527.812 ~ 1859 55.4831 54. 46 ~ 2837 .98633 219 56 1815 527.887 ~ 1882 55.4?83 55. 16 ~ 2837 -.88486 228 56 1838 527.787 .1881 55.4759 55. 18 ~ 2837 -. 88243 221 56 1845 527.769 ~ 1877 55.4738 55. 88 .2837 -.88285 222 56 1188 527.769 ~ 1858 55.4745 54. 38 ~ 283? .88878 223 56 1115 527.737 .187? 55+4688 55. 13 ~ 2837 -e89565 224 225 56 56 1138 1145 527.721 527.781

.1869

~ 1858 55 '676 55.4662 54 '5

54. 65

~ 2837

.2837

-.89129

-e88138 226 56 1288 527.678 ~ 1885 55.4618 55. 47 o2837 -.ees14 227 56 1215 527 '59 .1898 55.4567 55. 98 ~ 2837

- ~ 88434 228 56 1238 527.644 ~ 1885 55.4568 55. 54 .2837 .88967 229 56 1245 527o628 ~ 1868 55.4565 54. 87 ~ 2837 .98845 238 56 1388 527.687 ~ 1847 55.4548 54. 49 .2837 -+89164 231 56 1315 527.591 ei889 55.4575 53. 15 .2837 .88262 232 56 1338 527.575 .1835 55.4515 54. 19 .2837 -. 89592 233 56 1345 527.558 ~ 1852 55.4468 54. 75 .2837 -. 88473 234 56 1488 527.534 .1984 55.4391 56. 31 ~ 2837 -.88767 235 56 1415 527 '89 ~ 1897 S5.4373 56.16 . .2837 -.88183 236 56 1438 527e491 01875 55.4365 55.55 .2837 -+88982 237 56 1~45 527.475 .1748 55.4489 51.57 ~ 283? o 81152

It" 4

I

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I

++++++++++++ MFlSS LOSS CRLCULRTION RESULTS JULIFIN DRTE - 55 TINE - 1445 REC T I l'lE CONT NRSS NRSS NRSS NUN (DELTFl RIR . LOSS LOSS LOSS HOURS) NRSS INCR (1 HR) (x 24) 141 88 643129.1 8~8 8.8 8.8 142 ~ ~ 5 643134.1 5.8 8.8 8.8 143 ~ 58 643134. 6 .5 8.8 8.8 144 643888.7 -53 9 ~ 8.8 8.8 145 1. 88 643158.4 69 7~ -21 ~ 3 -511.1 146 1 ~ 25 643183.1 32. 7 -49. 8 -1175.4 147 1 ~ 58 643181.3 -81. 8 33 ' 888.4 148 1 ~ r5 643168.7 59. 5 -88.8 -1928 9 ~

149 2. 88 643123c5 -37 ~ 2 26. 9 644. 6 158 2~c 5 643112.6 -18. 9 78. 5 1691 ~ 5 151 2. 58 643898.6 -14.8 2~7 64.1 152 2. 75 6438?9.2 -19 ' 81 ~ 5 1957.2 153 3. 88 643118.5 31 ' 13. 8 312.7 154 3 ~ 25 643847.7 -62.8 64 ~ 9 1557.4 155 3. 'i8 643884.7 37.8 13. 9 333.5 156 3. 75 643127.6 42.9 -48. 4 -1161c 8 157 4. 88 643113. 8 -13.8 -3 3 .-88 8

~

158 4 ~ 25 643866.5 -47. 3 -18. 8 -458. 6 159 4 ~ 58 643862.3 -4.1 22. 3 536. 3 168 4 ~ r5 643889c4 -52. 9 iiee2 2835.8 161 5. 88 643843c9 34.5 69. 9 1678. 4 162 5. 25 643899.2 55. 3 32 ~ 7 ~ 4 '784 163 5;58 642987.7'43867.6

-111 5 ~ 74.7 1791 ~ 6

5. 75 79 ' -58.2 -1396. 6

6. 88 643856.5 -11. 1 -12.7 -384cB

6. 25 643113.6 57 ~ 1 -14 ' -347.5 167 6. 58 643888 ' -24 ~ 8 -181ci -2427. 6 168 6. r5 643825.6 -63. 2 42.8 1887. 8 169 7. 88 643858c5 24. 9 6.8 144 4

~

1?8 7. 25 642989.9 -68c 7 123c 8 2978.5 171 7. 8 64382811 38.2 68. 7 1649.6 172 7. rS 643858.4 38. 3 -24c 7 -593. 9 173 8. 88 642995.2 -55.2 55.3 1327c8 174 B. 25 643886c3 11. 1 -16c4 -393. 3 175 8. 'i8 643846.3 48 8~ -26.2 -628. 3 1?6 B.r5 643852.5 6.2 -2.1 -51.2 177 9. 88 643811.5 -41cB -16. 3 -392.4 178 9 ~ 25 64297S.i -36.4 31.1 746c9 179 9. 58 642993.9 18. 8 52.3 1256.4 188 9 75

~ 642979.8 -15. 8 73 ' 1764.4 181 18.88 642943.7 -35. 2 67. 8 1627.6 182 18.25 643881. 6 57.9 -26. 5 -635.8 183 18 .'.i8 642985.1 -16c 6 8.9 213.1 184 18 r'5

~ 642978.9 -14 ' 8.1 194. 8 185 11. 88 642968.7 -18. 2 -17. 8 -488' 186 1 1 c c.'5 642966c4 5.7 35. 2 845+ 7 187 11. 58 642959.8 -6c 6 25. 3 686. 3 188 11. r5 642988.3 28. 5 -9. 4 -224. 8

12. 88 643813.5 33 3~ -52. 8 -1266c5

12. 25 642941.3 -72 ~ 2 25. 1 682.4 12 58~ 642967.7 26. 4 -?.9 -188.?

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~

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++++++++++++ NFISS LOSS CRLCULRTION RESULTS JULIFIN DRTE 55 TINE 1445 REC T I I'IE CONT NRSS NFISS NRSS NUN (DELTR RIR LOSS LOSS LOSS HOURS) NRSS INCR (1 HR) (x 24) 192 12. r5 643822.9 55. 2 -42. 6 -1822. 5 193 13. 88 642938.7 -.92. 1 82. 8 1986>>7 194 13>> c!5 642992.4 61>>6 -51 1 ~ -1225.4 195 13 58 642998.5 6~2 -38. 9 -741 '

196 13.r5 643888.8 2~3 22. 1 529.2 197 14.88 643813.8 13. 8 -83. 1 -1993.2 198 14.25 642946.3 -67. 5 46. 1 1185'5 199 14 ~ 58 642923.4 -22 ' 75. 2 1883.6 288 14. r5 642967.7 44 ' 33. 1 793.8 281 15. 88 642878.2 -97 ' 143. 6 3445.2 282 15. 25 642955.9 85. 7 -9. 7 -231. 6 283 15>> 58 642882.8 -73>> 2 48. 6 974. 7 284 15.r5 642973>>7 Sl ~ 8 -6. 8 -144. 1 285 16. 88 642844.8 -129.7 26. 2 629. 8 286 16. 25 642846.8 1 ~ 9 118>>8 2639. 5 287 16 '>>8 642938.6 92. 7 -55>> 8 -1348. 3 288 16.?5 642954.6 15. 9 19. 2 468>>4 289 17. 88 642981.2 -53. 4 -57. 1 -1371.8 218 17. 25 642866.3 -34. 9 -28. 3 -488.1

, 211 17. 58 642918. 8 43. 7 28. 6 686.1 212 17.?5 642964.7 54>> 7 -18. 1 -243. 6 213 18. 88 642917 ~ 4 -47. 3 -16. 2 -389. 5

18. 25 642858.2 -67. 2 16. 1 386. 2 l 215 18 58 642875.5 25. 3 34. 5 828. 8 216 18. r'5 642963.8 88. 3 ~ 9 '21. 9 217 19. 88 642828.6 -135. 2 88>> 7 2129. 7 218 1S ~ c!5 642939.3 118>>7 -89 ~ 1 -2138.?

219 19 58 642888.3 -51 ~ 8 -12. 8 -388>>2 228 19. 75 642884.7 -3. 6 79 ~ 1897>> 8 221 222

28. 88 642883.2 -i. 5 -54.

1 6 -1389>> 7

28. c.'5 642982.1 18. 9 3?. 2 893 5~

223 58 642865.2 -36. 9 23. 2 555. 7 224 28.?5 642868.6 3.5 16. 1 385. 7 225 21. 88 642877>>3 8.6 5.9 142. 2 226 21. 25 642845.9 -31 4 ~ 56. 2 1348. 2 227 21. 58 642818. 5 -27. 5 1121. 4 228 21.?5 642829.1 18. 6 39. 6 949 ~ 7 229 22. 88 642864.2 35. 1 13. 1 314.4 238 22. c.'5 642868>>7 -3. 5 -14 ~ 8 -354.7 231 22. 58 642918.8 58 1 ~ -92>> 4 -2216.4 232 22. r'5 642861>>8 -49. 9 -31 ~ 9 -765.2 233 23. 88 642837.2 -23>> 7 26>> 9 646. 5 234 23 ~ c 5 642767.5 -69 8 ~ 93. 2 2237 ~ 1 235 236 237 23 '5 23 58 24.88 642777.4 642789.1 642942.8 9.9 11 ~ 7 153. 8 133. 4 71 ~ 9

-184. 8 3282. 2 1?25. 3

-2514>>8

APPBNDIX D TYPB A CALCULATIONS Mass Point Analysis Total Time Analysis

I 5,'c F~

C,/

14 "f

VC 4

++++++++++++i+++++ NRSS POINT CRLCULRT ION RESULTS JULIRN DRTE 55 TINE 1445 CONT CONT LSF UPPER VAPOR DEW RIR RIR LEFIK CONF INE TEI'IP PRESS PT PRESS NRSS RFITE LEVEL 1445 529. 288 ee2838 53. 562 55 646

~ 643129.86 e. eeeee 8 88888

~

1588 529. 179 8.2818 53.486 55 644

~ 643134.11 8 ~ 88888 Ge 88888 1515 529. 151 8.2812 53.326 55e641 643134.68 .84131 8. 88888 1538 529. 125 8.2845 53.773 55.633 643888.71 . 21588 .65338 1545 529. 892 ee1998 53.829 55. 636 643158.36 ~ 81612 e35457 1688 529; 878 8.1947 52.443 55. 637 643183.88 -.11388 ei4293 1615 529e 861 ee2885 53.237 55. 628 643181. 25 -.81614 . 18878 1638 529ee25 8.1967 52.715 55. 638 643168.75 .84844 .18319 1645 529.888 8.1992 53.851 55.625 643123.58 .82323 e89456 1788 528.988 8.1996 53.114 55. 621 643112. 68 -.eee24 e89523 1715 528.972 8.1992 53.853 55. 619 643898.58 ~ 82182 .18213 1738 528.944 Ge2813 53.337 55. 614 643879.28 .84483 ei151S 1745 528.929 8.1982 52. 916 55.615 643118.47 .84187 .18884 1888 528.988 8.2827 53. 531 55.688 643847.71 .86558 ~ 12132 1815 528.879 8.1996 53. 118 55.688 643884.68 .86556 e 11352 1838 528.868 8.1954 52. 534 55.618 643127.57 .84997 . 89468 1845 528.835 8.1962 52. 644 55.686 643113. 88 .84233 e 88226 1988 528.825 8 ~ 1989 53. 813 55.681 643866.48 e84861 . 88451 1915 528.888 Be 1989 53. 815 55.598 643862.34 .85332 e 88566 1938 528. r'91 8. 2824 53.485 55.592 643889.42 .86727 ~ 89946 1945 528.r'69 8.1992 53 '56 55.593 643843.87 .87885 .89922 2888 528. r'51 8.1938 52.318 55. 596 643899.16 .86152 .88929 2815 528 r'29

~ 8.2838 53.675 55. 584 642987.69 .87244 .89997 2838 528. r 13 8.1966 52.698 55. 589 643867.61 .86828 .89372 845 528.684 8.1975 52.833 55. 585 643856.54 .86588 .88935 188 528.679 8.1912 51 ~ 951 55. 589 643113.64 ~ 85686 .87988 115 528.657 8 ~ 1936 52. 298 55.585 643888.84 .85882 .87336 2138 528e647 8. 1981 52.985 55.578 643825.62 ~ 85323 .87426 2145 528.626 8.1962 52e647 55.578 643858.52 .85224 .87182 2288 528eC13 8.2888 53.274 55. 572 642989.87 .85694 e87576 221S 528 C82

~ 8.1978 52.865 55. 573 643828.18 ~ 85771 .87531 2238 528.578 8 ~ 1947 52.442 55. 573 643858.36 .85545 .87288 22'45 528.564 8.1995 53.892 55.567 642995.28 .85769 .87345 2388 528.541 8.1984 52.958 55.566 643886.26 .85843 .87326 2315 2338 528e522 8.1954 52 '48 55.567 643846.28 .85593 .87811 528e 516 8.1936 52.287 55. 567 643852.58 .85315 .86681 2345 528. 499 8.1974 52.813 55. 562 643811.54 .85318 .86689 8888 528e484 8.1991 53e843 55. 557 642975.14 .85519 .86757 8815 S28e466 8 ~ 1978 52.878 55. 557 642993.93 .85562 .86735 8838 528.468 8.1978 52.862 55. 555 642978.98 .85659 .86778 8845 528.444 8.2818 53.299 55. 558 642943.73 .85987 .86997 8188 528 '32 8.1952 52.517 55. 554 643881.63 .85814 .86856 8115 528.489 8. 1967 52.712 55. 558 642985.85 .85794 .8678?

8138 528.394 Ge 1988 52e898 55. 547 642978.98 .85823 .86778 8145 528. l?9 8.1979 52.882 55. 545 642968.74 .85875 .86781 8288 528. 367 8. 1962 52.647 55. 544 642966.48 .85881 .86747 8215 528.346 8. 1969 52e 748 55. 541 642959.79 '85897 e86726 8238 528. "32 8.1957 52. 577 55. 541 642988.26 .85818 .86616 8245, 528. 327 8.1913 51e 967 55. 544 643813e51 .85612 ~ 86483 8388 528.385 8.1974 52. 887 55. 535 642941.38 .85671 .86431 528.283 8.1949 52. 469 55. 535 642967.65 .85621 e86353

i Vt

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A'I t,i t

C

= 'I v~~

'(

t L

ft 0

MFISS POINT CRLCULFITION RESULTS JULIRN DRTE 55 TINE 1445 CONT CONT LSF UPPER YRPOR DEW RIR RIR LEFIK CONF I I'1E TEI'IP PRESS PT PRESS NRSS RRTE LEVEL 8338 528 c'.75

~ 8. 1889 51. 631 55. 539 643822.86 ~ 85385 .86125 8345 528>> c'.57 8. 1968 52.727 55. 529 642938.73 .85451 .86166 8408 528 c'.44

~ 8. 1918 52.841 55. 533 642992.35 .85314 .86815 8415 528 ~ c'.21 8.1988 51.896 55. 531 642998.54 <<85163 >>85854 8438 528 '86 8.1981 51.798 55. 538 643888.81 .85811 <<85693 8445 528.194 8.1873 51.483 55.538 643813.78 .84831 .85511 8588 528. 176 8.1938 52.287 55.522 642946.29 ~ 84837 .85493 8515 52S. 145 8 ~ 1952 52.511 55.517 642923.39 .84892 .85528 8538 528. 139 8.1988 51.782 55.528 642967.74 .84825 .85443 8545 528>> 132 8.1972 52.782 55.511 642878.23 ~ 84987 .85686 8688 528 l 82

~ 8.1989 51. 912 55.515 642955.94 .84931 <<85531 8615 528. 886 8>>1969 52 747

~ 55.587 642882.?8 .85834 .85624 8638 528. 872 8.1876 51. 442 55.513 642973.74 .84926 <<85586 8645 528.849 8.1991 53.847 55.588 642844.83 .85898 .85675 8788 528.838 8.1972 52.781 55.499 642845.96 .85238 .85812 8715 52S.817 8>>1894 51>>788 55.585 642938.62 .85168 .85736 8738 527.994 8>>1874 51.413 55. 584 642954>>56 .85875 .85633 8745 527 '82 8<<1913 51. 967 55.498 642981 <<15 .85882 .85624 8888 527.964 8.1942 52. 371 55.493 642866.38 .85145 .85675 8815 527.c<48 8.1896 51.732 55.495 642918.84 .85121 .85636 8838 527 '<29 8<<1843 58.979 55<<498 642964.71 .84999 .85514 8845 52?.983 8.1886 51.593 55.491 642917.38 .84968 .85462 8908. 527.892 527.878 8.1936 8 ~ 1912 52.28?

51.958 55.484 642858 55.484 642875.58

'1 .85827

.85844

.85528

.85524 527.852 8. 1835 58.865 55.489 642963.79 .84919 .85481 527.842 8.1937 52.382 55.477 642828.64 <<85881 .85477 1888 527.812 8 ~ 1859 51.198 55.483 642939.32 .84918 .85382 1815 527 '87 8 1882

~ 51. 536 55.478 642888.35 .84894 .85354 1838 527 8? 8 ~ 1881 51. 526 55.4?6 642884.72 .84879 .85328 1845 527.?69 8. 1877 51.462 55.474 642883.21 .84864 .85381 1188 527.r68 8.1858 51.875 55.474- 642982.89 .84828 >>85249 1115 527<<?37 8.1877 51 '55 55.469 642865.19 .84822 .85241 1138 52? r'21

~ 8.1869 51 ~ 353 55.468 642868.65 .84816 .85225 1145 527>> r'8l 8.1858 51.192 55.466 642877.29 .84796 .85196 1288 527. 678 8<<1885 51.569 55.461 642845.92 >>84811 .85281 1215 527. 659 8.1898 51.758 55.457 642818.47 .84853 .85237 1238 52?. 644 8.1885 51>>578 55.456 642829.88 .84877 .85252 1245 527 628

~

8. 1868 51.221 55.456 642864. 19 >>84856 .85223 1388 527. 687 8<<1847 51.826 55.455 642868.78 .84836 <<85196 1315 527, 'i91 8.1888 58.358 55.457 642918.82 .84761 .85121 1338 527 ~ '.i 75 8.1835 58.851 55.452 642868.96 .84748 .85892 1345 52?. 558 8.1852 51.182 55.447 64283?.25 ~ 84741 .85085 1488 527. ci34 8.1984 51.837 55.439 642767.48 .84888 .85152 1415 527. 589 8. 1897 51.743 55.437 642777.39 .84859 .85198 1438 527. c'9 l 8. 1875 51.434 55.436 642789.87 .84892 .85226 1445 527.~75 8. 1748 49.443 55.448 642942.83 .84776 .85121 MFIX RLLOWFIBLE LERK RRTE

~ 1 75r OF NR)l RLLOWFIBLE LERK RRTE

.875 EPRI EQURTION 06 IS NOT SRTISFIED.

EPR I EQURT I ON 07 IS SFITI SF I ED

I'~

P f

."g sfi 1 1 wi g

Ap Ik

~ e rg>>

ACl its

++++%+++++++++++++ TOTAL TINE CALCULATION RESULTS JUL I AN DFITE - 55 T I ME 1445 CONT LSF UPPER MEASURED VAPOR DEN AIR LEAK CONF LEAK TINE TENP PRESS PT PRESS RATE LEVEL RATE 1445 529. 288 8.2838 53.562 55. 646 8. 8888 8. 88888 8. 88888 1588 529.179 8.2818 53.486 55. 644 8. 8888 B<<88888 .87524 1515 529.151 8.2812 53.326 55. 641 -. 8413 8.88888 -<<84131 1538 529.$ 25 8.2845 53.773 55. 633 .1993 .86847 <<24868 1545 529.892 8.1998 53.829 55. 636 .8515 ~ 64334 .87947 1688 529.878 8.1947 52.443 55.63? -.8654 <<34674 -<<16126 1615 529.861 8.2885 53.237 55.628 .8849 .31858 .86928 1638 529.825 8.196? 52.715 55. 638 -.8333 ~ 21716 . 86756 1645 529.888 8.1992 53.851 55. 625 -.8184 .18997 .81838 1788 528.988 8 ~ 1996 53.114 55. 621 -. 8821 <<17695 .82731 1715 528.9?2 8. 1992 53<<853 55. 619 . 8154 ~ 17277 .84558 1738 528.944 8. 2813 53. 337 55. 614 .8349 ~ 17565 .86767 1745 528,cr29 8. 1982 52.916 55. 615 .8359 .16269 .82313 1888 528.988 8. 2827 53.531 55. 688 .8558 .17211 .89342 1815 528.879 8.1996 53. 118 55.688 .8598 ~ 16584 .84732 1838 528.868 8 '954 52. 534 55.618 .8584 ~ 15837 .88148 1845 528.835 8.1962 52.644 55.686 .8462 .13967 .81424 1988 528.825 8.1989 53.813 55.681 .8515 .13881 .85495 1915 528 888 F 8.1989 53.815 55.598 .8558 .13774 .85533 1938 528.791 8.2824 53. 485 55. 592 .8668 .14428 <<89488 1945 528.r'69 8.1992 53. 856 55. 593 .8?83 .14349 .86358 2888 528<<r 51 8.1938 52.318 55. 596 .8656 .13568 .82125 2815 528 r'29

~ 8.2838 53. 675 55 '84 .8?42 .14898 .89592 528. r 13 8.1966 52. 698 55.589 ~ 8723 .13631 .83989 528.684 8.1975 52. 833 55.585 .8715 <<13279 <<84511 528.679 8.1912 51. 951 55.589 ~ 86S3 .12481 . 88921 2115 528<<657 8.1936 52. 298 55. 585 <<8618 .11938 .82318 2138 528.647 8.1981 52.985 55. 578 <<8635 .11874 .85719 2145 528.626 8.1962 52. 647 55. 578 .8629 <<11613 .84187 2288 528.613 8.2888 53. 274 55. 572 <<8662 .11751 .87165 2215 528.682 8.1978 52.865 55. 573 .8669 .11643 .85422 2238 528,578 8'947 52.442 SS. S?3 <<8655 <<11348 .83798 2245 528<<564 8. 1995 53. 892 55. 56? <<8671 .11352 .86245 2388 528<<541 8<<1984 52. 958 55. 566 .867? ~ 11278 .85555 2315 528.522 8 '954 52.548 55. 56? .8661 .18985 .83634 2338 528.516 8<<1936 52 '87 55.567 ~ 8642 <<18683 .83266 2345 528.499 8 '974 52<<813 55 562

~ .8642 .18568 .84873 8888 528.~84 8.1991 53.843 55<<55? .8655 .18577 .86218 881S 528. 4'66 8.1978 52.878 55.557 <<8658 .18498 .85388 8838 528.~68 8<<1978 52<<862 55 '55 .Bees .18461 .85744 8845 528. 4'44 8.2818 53. 299 55.558 .8682 .18535 .86916 8188 528.~32 8 ~ 1952 52. 517 55.554 <<8676 .18398 .84648 8115 528.~89 8, 1967 52. 712 55.558 .8675 .18293 <<85118 8138 528.394 8.1988 52. 898 55.54? .8677 .18232 .85491 8145 528.379 8.1979 52. 882 55.545 ~ 8681 <<18198 .85718 8288 528.367 8.1962 52. 647 55.544 .8682 .18121 .85396 8215 528<<346 8.1969 52. 748 55.541 <<8683 <<18862 .85493 8238 528.332 8.1957 52. 577 55.541 .8678 . 89944 .84726 8245 528<<327 8.1913 51<<967 55<<544 <<8664 .89746 .83593 388 528.385 8.1974 52.887 55.535 .8667 .89717 .85728 315 528 '83 8.1949 52.469 55. 535 .8664 .89628 ,

.84819

4 lent R

A4 "k

~r

,l

~d'f r.

C" 4

a<

TOTAL TINE CRLCULRTION RESULTS +++++++++++++++++++

JUL IRN DRTE 55 TINE 1445 CONT LSF UPPER NERSURED YRPOR DEW RIR LERK CONF LERK T I NE TENP PRESS PT PRESS RATE LEYEL RRTE 8338 528.275 B. 1889 51. 631 55. 539 . 8647 .17589 .83188 8345 528. c.'57 Bci968 52. 727 55. 529 . 8651 .17425 .85693 8488 528 '44 Bc1918 52.841 55. 533 . 8648 ci7231 .83858 8415 528. ct21 8.1988 51.896 55. 531 . 8629 c17831 c83688 8438 528. 286 8.1981 Sin?98 55. 538 . 8617 ~ 16831 .83481 8445'588 528c 194 8.1873 51.483 55. 538 . 8684 .16619 .83873 528.176 8 ~ 1938 52.287 55. 522 .8682 .16584 .84786 8515 528.145 8.1952 52.511 55.517 .8684 .16423 <<85293 8538 528.139 8 ~ 1988 51.782 55.528 .8598 ~ 16275 .84882 8545 528.132 Bci972 52.782 55.511 .868B ~ 16273 .86439 8688 528 '82 8 ~ 1989 51.912 55. 515 .8682 .16138 .84236 8615 528.886 8. 1969 52.747 55. 587 8688 ~ 16182 .85938 8638 528.872 8.1876 51.442 55. 513 .8688 .15946 c83688 8645 528.849 8. 1991 53. 847 55. 588 .8618 .15958 c86648 8788 528.838 8.1972 52. 781 55. 499 ~ 8618 .15958 c86581 8715 528.817 8.1894 Sf.?88 55. 585 .8613 c15836 .84387 8738 527.994 8.1874 51c 413 55. 584 .8686 .15699 .83888 8745 527.982 8 '913 51. 967 55.498 c8685 .15618 .85883 8888 527.964 8.1942 52c371 551 493 .8689 c15574 .85684 8815 527.948 8.1896 51.732 55.495 .8686 c15479 .84671 8838 527.929 8.1843 58e979 55.49S c8597 .15335 c83455 8845 527.983 8.1886 51.593 55.491 .8593 c15234 .84389 8988 527.892 8. 1936 52.28? 55.484 .8597 .15199 .85782 8915 527.878 8. 1912 51.958 55.484 .8597 ~ 15134 .85115 8938 527.852 8.1835 58c865 55.489 F 8588 .14994 .83289 527.842 8.1937 52.382 55.477 .8592 .14972 .85981 527.812 8.1859 51.198 55.483 .8585 ~ 14852 .83678 1815 527.887 8.1882 51c536 55.478 .8583 .14772 .84687 1838 527.787 8. 1881 51 '26 55.476 .8581 .14694 .84617 1845 527cr69 8. 1877 51.462 55c474 .8579 c14616 .84587 1188 527.r68 8.1858 51.875 55 '74 .8575 .14524 .84183 1115 527.737 8.1877 51.455 55.469 .85?4 .14468 e84883 1138 527.r21 8.1869 51.353 55.468 .8573 cl4391 .84683 1145 527.r81 8.1858 51 ~ 192 55.466 .8571 .14315 .84474 1288 52?.678 8.1885 51. 569 55.461 .8571 .14262 c84972 1215 527.659 8.1898 51. 758 55c457 .8572 c14227 .85391 1238 527.644 8.1885 51. 578 55.456 .8573 .14181 .85147 1245 527.628 8.1868 51. 221 55.456 .85?1 .14111 .84493 1388 527.687 8.1847 51. 826 55.455 .8569 . 14842 .84581 1315 527, 591 8.1888 58.358 55.457 .8563 .13944 .83628 1338 527. >75 8.1835 58. 851 55.452 .8561 .13874 .84398 1345 527 558

~ 8 '852 51.182 55.447 .GS68 . 13819 .84735 1488 527 c534 8. 1984 51c837 55.439 .8563 e13888 c85884 1415 527c589 8 ~ 1897 51.743 55.437 .8566 .13787 .85585 1438 527.491 8.1875 51.434 55.436 .8568 .13756 . 85342 1445 527.475 8.1748 49.443 55 '48 .8559 cB?189 .82988 CRLCULRTED LE RK RATE USING TOTAL TINE) .8559 THE NERN TOTR L TINE R RTE OF .8463 IS LESS THRN THE RLLO NABLE NRKINUN LEAK RATE OF .288

APPENDIX B VERIFICATION TEST CALCULATIONS Mass Point Analysis

4, Z

"~

A 3

%J re I

~ I

+ ++ MASS POINT 0ITH VER IF I CRT ION JUL IFIN DATE 56 TIME - 1588 MFISS POINT VERIF I CRT ION GROSS GROSS NET NET IME MFISS LSF 95'CL SCFM LSF 95~ UCI 1588 642888.9 8. 8888 8.8888 5. 881 .8975 -o 8975 1515 642835.7 8. 8888 8.8888 5. 881 .8975 -.8975 1538 642e42.6 .2859 8.8888 5. 812 .1883 ~ 8976 1545 642768.8 o4954 .9588 5 ~ 812 . 3978 .e684 1688 642882.8 .3344 .6484 5. 812 . 2368 .5427 1615 64284?.7 .1447 .4484 5. 812 .8471 ~ 3427 1638 642739.2 .2352 .4598 5 ~ 812 .1375 ~ 3614 1645 642789.8 .1982 .3589 5. 812 ~ 8926 ~ 2612 1788 642755.1 .1912 .3185 5. 819 ~ 8934 ~ 2288 1715 642767.3 ~ 1713 ~ 2733 5. 819 .8735 +1?55, 1738 642689.1 .2857 .2955 5. 819 ~ 1879 .1977 1745 642728.8 .1953 .2788 5. 819 .8975 e1722 1888 642697.2 .1977 .2683 5. 819 +1888 ~ 1625 1815 642729.2 .1888 .2362 5. 819 .8822 .1384 1838 642668.6 .1866 .2354 5. 819 e8888 .1376 1845 642728.9 .1696 .2155 ,5. 819 -8718 .11??

1988 642698.3 .1613 .2824 5.819 .8635 .1846 1915 642564.3 .1877 .2328 5. 819 .8899 ..1 358 1938 642674.8 .1776 o2191 5. 819 .8799 ~ 1213 1945 642673.4 .1688 .2864 5. 819 .8783 .1887 2888 642674.8 -

~ 1586 ~ 1945 5 ~ 819 .8688 .896?

2815 642528.9 . 1754 .2119 5. 819 .8776 .1141 838 642615.3 ~ 1722 .2856 5. 819 .8744 .1879 45 642563.7 .1757 .2865 5. 819 .8779 .1887

( 88 642586.1 .1738 .2821 5. 819 .8768 .1843 2115 642638.8 ~ 1648 ~ 1918 5. 819 .8662 ..8941 2138 642628.3 .1572 . 1838 5. 819 .8594 . 8868 2145 642599.9 .1528 . 1?78 5. 819 .8558 . GSGG 2288 642654.5 .1425 . 1679 5. 819 .8448 . 8781 2215 642592.? .1393 .1631 5e 828 .8415 . 8653 2238 642577.1 .1372 .1595 5. 828 .8393 .8617 2245 642498 ' ~ 1419 ~ 1634 5. 828 .8441 . 8656 2388 642556.2 .1399 .1682 5. 828 .8421 . 8624 2315 642525+7 .1399 .1589 5. 828 .8428 . 8611 2338 642584.9 .1486 +1586 5. 828 ;8428 . 8687

hPPBNDIX F TYPB A PLOTS Temperature vs Time Pressure vs Time Dew Point vs Time Containment Mass vs Time Mass Point Leakage Rate vs Time Total Time Leakage Rate vs Time

S RTG Zli8l 55: 3445 TO 6: 1445 74 72 8 32 16 DELTR TINE (IN HOURS)

I c

er I

RTO 2 li82 55: 1445 TO 56: 1445 73 8 ]2 16 DELTR TIME (1N HOUR5)

RTQ Zli83 55: l445 TO 56: 1445 74 8 l2 16 DELTR TINE (IN HOURS)

RTO 2 l/84 55'445 TO 56: 1445 74 8 )2 16 DELTR TINE (IN HOURS)

RTO ZZi81 55: j 445 TO 56: 1445 8 )2 16 DELTA TINE (IN HOURS)

RTQ Z2i82 55'445 TO 56: 1445 8 )2 16 DELTR TINE (IN HOURS)

RTO Z2i83 55: 1445 TO 56: 1445 74 73 72 4 8 )2 16 DELTR T2NE (ZN HOURS)

RTO Z2i84 55: 1445 TO 56: 1445 74 73 72 71

. B 8 l2 16 DELTR TIME (IN HOURS)

RTO Zc! i85 55: l 44 5 TO 56: 144 5 74 73 72 8 l2 16 24 DELTR TINE (ZN HOURS)

RTQ Z2i86 55: 1445 TO 5R: 1445 8 ]2 16 DELTR TINE (IN HOURS)

aqf g c',$

RTD Z2i8'7 55: i445 0 56: 1445 8 ]2 l6 DELTR TINE (IN HOURS)

Y P

ad%'

RTD Z3i81 55: ]445 TO 56) 1445 74 73 72 8 }Z 16 DELTR TEt1E (XN HOURS)

gee S

r4 4,

RTO Z3i82 55'445 TO 5S: 1445 74

?3 8 12 16 DELTR TINE (IN MOURS)

AOz 4p S

'I I

RTO Z3i83 55 ! 1445 TO 56: 1445 74 8 }2 16 DELTR TINE (IN HOUR53

f RTD Z3i84 55: j 445 TO 56: 1445

?3 72 8 J2 16 24 DELTR TENE (XN HOURS)

'V RTQ Z3r'85 55t ]445 TO 56) 1445

?4 73 72 8,

DELTR TIME

]2 (IN HOURS) 16

/,

dr'.

RTO Z3i86 55 t ) 445 TO 56: 1445 74 73 72 71 8 )2 16 DELTR T2NE (lN HOURS)

ff ~

8 1

RTD Z3i87 55: 1445 TO 56: 1445 74 73 8 12 16 DELTR TINE (IN HOURS)

gi ~

>t

RTO Z3r'88 55> 1445 'To SG: 1445 I

CA LJ La>

K CO LLI 8 )2 16 DELTR TIME (XN HOURS)

RTO Z3i89 55: ]445 TO 56: 1445 74 72 7l 8 12 16 DELTR TINE (IN HOURS)

RTQ Z4i81 55 t ] 445 TO 56: 1445 74 72 B 32 16 DELTR TINE (IN HOURS)

8 RTG Z4i82 55: ] 445 TO 56: 1445 74 72 8 ]2 16 DELTR TINE (IN HOUR5)

4 RTO Z4i83 55:1445 TO 56) 1445 72 71 8 )2 - 16 DELTA TINE (XN HOURS)

RTO Z4i84 55: 1445 TO 56: 1445 72 8 ]2 16 24 DELTA TINE (IN HOURS)

S RTQ Z4r85 55: j445 TO 56:1445 72 8 12 16 DELTR T2 NE ( XN HOURS)

P,

s j

iq s~i'

RTO 24/86 55'445 TO 56! 1445 74 73 72 8 l2 16 DELTR TIME (IN HOURS)

RTQ Z4i8? 55'445 TO 56: 1445 74 73 72 71 8 12 16 DELTR TINE (IN HOURS)

k S

~i 1

W '1 q

tJ

RTO Z4i88 55: j445 TO 56: 1445 74

?3

?1 8 l2 l6 DELTR TINE (IN HOURS)

i RTO Z4/89 55 i ] 445 TO 56: 1445 74 73 72 71 8 )2 16 24 DELTR T1tlE (IN HOURS)

RTO Z4i l8 55: ] 445 TO 56: 1445 74

?3 8 ]2 16 24 DELTR TINE (XN HOURS)

RTQ ZSi81 55 ) 1445 TO 56 t 1445 74 72 71 8 )2 16 DELTA TINE (IN MOURB)

I' RTO ZSi82 55: 1445 TO 56: 1445 74

?3 72 8 ]2 16 DELTA TIME (IN HOURS)

RTO Z5i83 55! j 445 TO 56: 1445 74

?3 8 ]2 l6 DELTR TINE (IN HOURS)

RTO Z5i84 55: j445 TO 56'445 74

?3 72 8 )2 l6 DELTR TINE (IN HOURS)

RTO Z5r'85 55: ]445 TO 56: 1445 74 72 8 12 16 24 DELTA TINE (IN HOURS)

RTO 25i86 55'445 TO 56: 1445 73 72 8 )2 lb 74 DELTR TiNE (IN HOLlRS)

Y S

RTD ZS/87 55: 1445 TO 56: 1445 74 71 LI.

M 4J LJ K

LIJ R

8 12 16 24 DELTR TIME (IN HOURS)

~

RTQ ZS/88 SG: 1445 TO 56: 144S 74 73 71 8 12 16 24 DELTR T151E (TN HOURS)

RTO Z5i89 55: ]445 TO 56s 1445 74 72 8 )2 16 DELTR TINE (IN HOURS)

RTD Z5~l8 55'445 TO 56:1445 74 72 8 '2 DELTR TIME (IN HOURS) 16

RTO RYG ~ 55: 1445 TO 56: 1445 74 71 L.

U) ld LIJ CL Ld 8 l2 16 DELTR T2NE tIN HOURS)

4 0

PRESS NO ~ 1 55: 1445 TO 56: 1445 55.

73 5o 83 12 24 DELTR TIME (XN HOURS)

p 0

PRESS NO. 2 55! 1445 TO 56! 1445 55.'.

72 5 ~ 82 DELTA TIME (IN HOURS)

CONT PRESSURE 55:]445 TO 56)j445 55.

'e T2 24 DELTR TIME (IN HOURS)

DRY PRESSURE 55: 1445 TO 56: 1445 8 f2 24 DELTR TINE (IN HOURS)

I RHO Z liR 55: 1445 70 56: 1445 7B 75 UJ LJ LLJ 5

LLJ Cl 24 DEf.TR TINE (VN HOURS)

RHO Z2iR 55: 1445 TO 56: 1445

?8 75 24 DEETR TIME (VN HOURS)

RHO Z2iB 55: ] 445 TO 56: 1445 re M

LJ LJ C9 o

LLI DEETR TIME (Vhl HOURS) 24

RHO Z3iR 55:1445 TO 56:1445 24 DISTR TIME (fN HOURS)

RHO Z3iB 55: 1445 TO 56: 1445 7B 75 72 DEETR TINE (%l HOURS)

RHQ Z3r'C SG: ]445 'TO 56: 1445 DEETR TINE (VN HOURS)

RHO Z4zR 55: 1445 TO 56: 1445 7B 75 72 24 DEETR TIME (6l HOURS)

4' RHQ Z4iB 55: j445 TO 56: 1445 re 75 4.

N 3" LLj W

W O

24 DEf.TR TIME (VN MOURS)

RHO ZSrR 55: ] 445 TO 56: 1445

?B 75 72 24 DEfTR TIME (Vtl HOURS)

4 0

8 ~ I RHO ZSiB 55: 1445 TO 56: 1445

?e 75 72 DEETR TINE (Vtl HOURS)

RHO RVG 55: ]445 TO 56: 1445 75 72 DEETR TIME (VH HOURS)

gE f~

VR R PRESBURL 5:1445 TO 56'445 f2 16 24 DELTR TINE lIN HOURS)

hit>,

A

MP MERSURED 55: 1445 TO SB: 1445 8 12 16 DELTR TIME ( IN HOURS)

4 g

NRSS POINT ( lr'DRY) 55: 1445 TO 56: 1445 LSF

.787 S5rUCL

.75LR

.687 87 f7 87 --'N ~-v-~

. 113 8 12 16 DELTR TINE (IN HOURS)

TOTRL TIME (iiDRY) 55: 1445 TO 56: 1445 LSF 85rUCL

.75LR 24 DELTR Tx. i~ (IN HOURS)

APPENDIX G VERIFICATION TEST PLOTS Average Temperature vs Time Average Pressure vs Time Average Dew Point vs Time Containment Mass vs Time Mass Point Leakage Rate vs Time

RTD RVG 56: 1588 TO 56: 2338 3 5 DELTR TIME (IN HOVRS)

I COMT PRESSURE 56: 1588 TO 56:2338 3 5 DELTR TIME (ZN HOLIRB)

~ l RHD RYG 56'. 1588 TO 56:2338 DELTR TIME ( IN HOURS)

NP NERSURED 56:1588 TO 56:2338 DELTR TINE (IN HOURS)

f' MFjSS POINT (iiIlRY) 6: 1588 TO LSF 85iuCL j

.a ji i

l i

(

j 3 5 DELTR TIME (IN HOURS) .

APPENDIX H SCHEMATIC FOR LEAKAGE RATE MEASURING SYSTEM

S's ea IC t

l

~ Ot<<AAM We f%IT t)OSCAR NP (0 Cote) Me ~ ~I ALIMOI LI1 5

( W lt TC EIL

~ Ct Lelll>>C AIE &40&safe Nc M ~ 0<<M ~ C E IIAwaf<<W

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SYSTEM BLOCK DIAGRAM ve ~ ~ I frCTAIL (

04<<0 Is&wc tw weeeea<<M rval tt far es re 1 .w f'

(Continued)

TABLE 3.2.1-1 CLASS IF I CATION OF STRUCTURES SYSTEMS AND COMPONENTS Deslnn and Construction and Operations Remarks Quality Quality Safety Code Seismic Quality Class Assurance S stems and Components ~

Class (1) Code Class ~Csts or (2) Assurance (3) (23) (24)

Safet In ection S stem (Continued) b) Required for t I Injection In I Ia 2 ASME I I I or long term recirculation of sump xater for emergency core cooling c) Normally or automatically NNS ANSI 831 '

isolated from parts of system covered by a, b I22 Instrumentation (in part) IE See Note (15)

Operators for Safety-Related IE See Note (31)

Active Valves Residual Heat Removal S stem I

Residual Heat Removal (Lox Head 2 ASME III Safety Injection) Pumps RHR Pump Motors IE Residual Heat Exchanger (tube side)- 2 ASME III 8 Q (shell side) 3 ASME III B Q

%OP)>>

System Piping and Valves 2 /~

pcs a) Part of RCPB 1 ASME III A Q b) Required for residual heat 2 ASME III A Q removal

lt I 7 'pv, lg

~l t

La.yl SHNPP FSAR I

TABLE 3.9.2-1 (Cont'd)

METHOD OF UALIFICATION FOR NSSS E UIPMENT Seismic

~Com onent Desi n (1)

Emer enc Core Coolin S stem Accumulators Boron Injection Tank (BIT) 27 Hydro Test Pump Residual Heat Removal S stem Residual Heat Removal Pump Residual Heat Exchanger (tube side)

(shell side)

Boron Rec cle S stem Recycle Evap. Feed pump Recycle Evap. Feed Demineralizer Recycle Evap. Feed Filter Recycle Evap. Concentrate Filter e

Recycle Evap. Condensate Demineralizer Reactor Makeup Water Pump Recycle Evap. Reagent Tank Recycle Holdup Tank Vent Ejector Recycle Evaporator Package

1. Feed Preheater

a. Feed Side b) Steam Side 3.9.2-12 Amendment No. 27

P . /~qv I

1

'1 1

z DATA c z T I ME cnW

~I Ill m C

rz ncn mm PERIOD NUMBER ELAPSED (Sec.) (')

TEMP

~~o~~ ~o 2.5 220 z~a7 0z oz I 2 9.0 321 m~

I REPRESENTATIVE PERIOD SHORN IN TABLE 3 30.0 360 O 4 60 ' 380 Cn cn~ r 5 70.0 350 00

~ Cn 6 80.0 300 m

O 400 7 2000.0 260 8 6000.0 240 9 10000 ' 200 10 5X 180 Qz 0

10'X O, 11 1(t 160 CD 11 12 1.0 X 10 1 44.

m m'

300 0 0 13 14 1.6 1.6 X 10 X 10 130 120 z Qi 0

O O+.

~OC -:"

OKm K 200

'gzmm Z %l 0 -0 Cp l DQ 0~ K 00

~~cn c ~z c- cn p

'-Oll n, Cll m' 100 zI O

Q 'll m,

m OI z 0 Q 'l IT1 10 100 1000. 104 105 106 Zl i

\ 1.6 X 1P I '" TIME (SECONDS).

'll A Z, 0,'i Cll

yf 4 I

L I

i

-U at t.a 1

z DATA I zC TIME CO CI PERIOD m ~

O rx O

mm CO

/i NUMBER ELAPSED (Se c ~ )

TEMP

('-")

-I

~ "o mO I

-REPRESFPlTATIVE PERIOD SHOWN IN TABLE 2.5 220 z ~oz 1CO 0 2 9.0 321 0 00 I Aoo O

m~ 3 30.0 360 CO Cl ~ 4 60.0 CO

~ CO 380 m ~D z 5 70 ' 350 O

0 Qs 6

7 80.0 400.0 300 260 300 8 6oo.n U

O 0 00 9 10 1000.0 2000.0 250 230 210 0Zl m ill lL Qo 11 3600.0 170 CI D

Z 200 ',

( Q C

1 K 011 0z CI Ill~ ~ I-zZ Il rPmr CO Q I 100 O z=

CO' 0Ill O OI Cli z Z,','00 oz 0 2!'TI1 Z 10 100 1000 10000 o'I TIME (SECONDS)

Zl CA) 4p,

4 t'

I l i

h

/

f~~'~*

rt

~

SHNPP FSAR 3.11.5 ESTIMATED CHEMICAL AND RA'DIATION ENVIRONMENT 3.11.5.1 Chemical Environment Safety Related Systems are designed to perform their safety-related functions in the temperature, pressure, and humidity conditions discussed in Section 3.11.1 and in Section 6.2. In addition, components of ESF systems inside the Containment are designed to perform their safety-related functions in a long-term contact with boric acid and sodium hydroxide solutions, recirculated through the Safety Injection System (SIS) and Containment Spray System (CSS).

The pH time history of the water both in the containment spray and in the containment sump, as well as the boron concentration in the Reactor Coolant System', is discussed in Section 6.5.2.

The containment atmosphere is maintained below 4 volume percent hydrogen consistent with the recommendations of Regulatory Guide 1.7. The extent to which this and other recommendations of Regulatory Guide 1.7 are followed are discussed in FSAR Section 6.2.5.

The CVCS, SIS, and CSS are designed for both the maximum and long-term boric 27 acid concentration of 2000-2200 ppm at a pH of 8.5 to 11.0.

3.11.5.2 Radiation Environment Safety related systems and components are designed to perform their safety related functions after the normal 40-year operational exposure plus one accident exposure. The normal operational exposure is based on the design source terms presented in Section 11.1 and Section 12.2.1. Post accident system and component radiation exposures are dependent on equipment location. Source terms and other accident parameters are presented in Section 12.2.1 and in Chapter 15. For safety related systems, normal operational exposure and post accident radiation exposures are listed in Appendix 3.11B.

The degree to which the recommendations of Regulatory Guide 1.4, "Assumptions Used for Evaluating the Potential Radiological Consequences of a Loss of Coolant Accident for Pressurized Water Reactors," has been u'sed in determining the source terms used in evaluating radiation exposure is detailed in Section 1.8.

The design radiation exposures are based on gamma and beta radiationo The effects of beta radiation are effectively attenuated by small amounts of shielding, such as conduits for cable and casings for equipments Organic materials which are located inside the Containment are identified in Section 6.1.2.

3.11.5-1 Amendment No. 27

I k

k II k

. It I~

'll Z REPRESENTATIVE PERIOD SHOWN IN TABLE DATA r

cn cl Z

C PERIOD TIME ELAPSED RESSUR o

rx cn NUMBER (Sec.) PSIA

~g m~

-I

~~o~~

mm

>b Q 2.5 29.0 r~ mO 50 2 1

9.0 43.0 Z ~< OZ oroc "7 ~x m~

3 30 ' 52.0 XI 4 60.0 49.0 cn cn~ r

~ cn Qs 5 6

70.0 80 '

49.0 49.0 m ~

0 7 2000.0 54.0 40 8 6000.0 42.0 9 10000.0 28.0 10 5X 10'X10 23.0 11 21.0 12 1.0 X 10 19.0 1

13 1 ' X 10 17.5 Tl ~l a- 30 14 1.6 X 107 17.0 m'n ill

,1m Z C, CC I

m D c/l IO Cl ~

co 0Z 0, Lll mOr r ll K Cl Q11 Q

ZOm 20 ~ 14

"> ~ <cn.Z.

Cn .

I Dmm rO C~

8Z.

o I2 10 I ~

0Z m, Z 1 I

Z.

OI 1 Ill Z 10 '02; 10

" 1O" '1O5 .106 )

I.G X 10 Z TIME (SECONDSj A

C 0,' I Cb,*

fll

'l'8 ~ e' I I< pt V%I" "1

I F,'let"ted&' ~ S'

~, J

Tl z DATA I zC TIME CO CI O PERIOD ELAPSED RESSURE m ~

cz mm CIT NUMBER (Sec.) PSIA

-I 50

~ "o 2 2 c mO 1 2.5 22.0 z 3 oz 0 2 9.0 34.0 C

CIT CIT m

'Tl 0

OCII 0

3

'T~

TTl

~2

~

~ Cil z 40 I p~

Op Qo 3

4 5

6 30.0 60.0 70.0 80 ~ 0 40.0 43.0 42.0 40.0 7 400.0 54.0

.e 600.0 50.0 9 1000.0 40 '

30 QII 10 2000.0 35. 0 0 fll 11 3600.0 37 '

Cll m C D Z Il m QI 0z 0 20

~

zgc m

TTl pcz Cil C

o m I+~

8z 10 2 -t I'0 o

0z zm ITI Z

0 0 1 100 1000 10000 ITI Z TIME (SECONDS)

'll CA)

A Z CT)

C 0 tO m

sr i r.>>>

rtS I h il t 1

SHNPP FSAR The following legend, examples and notes apply to the environmental parameter zone maps contained in this appendix.

Buildin Plant Locations These consist of alpha-numeric designations (CB11, etc.) identifying the various plant areas. Refer to Table 3.11B-l for a description and list of figures which identify these areas.

Parameter Le end (Units)

Temperature ('F)

Pressure (psig/psia)

H = Relative Humidity (%)

Boron concentration in the Chemical Spray Solution (parts per million-ppm). 'Applicable inside containment only.

27 pH = Negative logarithm of Hydrogen Concentration in the Chemical Spray Solution. Applicable inside containment only.

S = Maximum flood level (Ft)

~Exam le l CBll, CB21 Normal Accident 120'F FSAR Fig. 3.11.4-1, 2 ATM FSAR Fig. 3.11.6-1, 2 H 40% 100%

NA 2000-2200 ppm pH NA 8e5 - ll S NA 228.3'he above chart (example 1) lists the environmental parameters applicable to containment building plant location areas CBll and CB21. Refer to Table 3.11B-1 for a description of the plant areas covered by CB11 and CB21.

All equipment located in areas CB11 and CB21 is exposed to the environmental conditions indicated in the above chart.

The column designated normal lists environmental parameters existing during the normal 40-year plant life.

3.118-3 Amendment No. 27

'p i

l~, dj

)v ...i I I

SHNPP FSAR designated accident lists the environmental parameters resu tang

~ ~ ~ ~

The column design basis accident such as a LOCA or MSLB.

~

from a ~

T: The maximum dail y tern p erature durin g the 40- y ear p lant

~ ~ ~

life is a maxi mum 120'F. The design basis accident temperature conditions are time dependent and are shown in the applicable FSAR figure indicated on the CES. In general it will be FSAR Figure F 11.4-1 which is the DBA, Temperature Profile Inside Containment based on a combined LOCA/MSLB condition (worst case inside containment).

P ~

The normal pressure during the 40-year plant life is atmospheric. The design basis accident pressure conditions inside containment are time dependent and are shown in the applicable FSAR figure indicated on the CES. In general, it will be FSAR Figure F 11.6-1 which is the DBA Pressure Profile Inside Containment based on a combined LOCA/MSLB (worst case inside containment). 'ondition H: The normal daily humidity during the 40-year plant life is 40%o The humidity subsequent to a design basis accident is 100X.

B: This is the Boron concentration in the chemical spray solution. During normal operation of the plant this parameter is not applicable.

Subsequent to a design. basis accident inside containment, the boron concentration will vary between 2000 - 2200 parts per million (ppm). )

22 pH: This parameter is also associated with the chemical spray solution, and is only applicable inside containment following a design basis accident. It may vary between 8.5 and 11.

S: Submergence level is only applicable subsequent to a design basis accident. The maximum flood level will be at the 228.3 ft elevation inside containment.

~Exam le 2 Zone Time Gamma Beta R3 1DA 8.2(+3) 2.0(+4) DBA Radiation Dose for time period indicated AB11 1.5(+4) 3.7(+4) 1YA 3.3(+4) 7.2(+4) 40YN 1.0(+3) Negligible Normal gamma radiation dose over 40 years.

Beta radiation dose

( ) Power of Ten during this time period Environmental zone 6 Plant area is negligible location 3.11B-4 Amendment No. 27

m f c ~

V

,I 1

1

SHNPP FSAR in Section 5.2.3 for Westingho'use supplied insulation

~ ~

and in Section 1.~

all other insulation. ~

~

of aluminum and zinc will be minimized in the Containment. An aluminum

~ ~ ~ ~ ~ ~ ~

Use and zinc inventory in the Containment is given in Table 6 '.1-2.

6.1.1.2 Com osition, Com atibilit and Stabilit of Containment and I Core S ra Coolants The pH of the containment spray will be adjusted during the injection mode by the addition of a 28-30 weight-percent sodium hydroxide (NaOH) solution to provide a minimum pH of 8.5. A discussion of the NaOH addition .,design basis is provided in Section 6.5.2.3.3. In no case will the solution pH fall outside the range of 8.5 to 11.0.

The refueling water storage tank is the source of borated cooling water during injection. The boron concentration, as boric acid, is 2,000 2,200 ppm. The tank is maintained above 40F, thus ensuring that the boric acid remains soluble.

In order to ensure materials compatibility during storage, the sodium hydroxide chemical additive is contained in a stainless steel tank. r The spray additive solution is not corrosive to the stainless 'steel components of the system with which it comes into contact. The spray and sump solutions will tend to severeLy cor'rode aluminum alloys, but will not attack stainless steel or copper-nickel alloys.

H y drogen release within the C ontainment due to corrosion of materials by the sprays and cooling water in the event of a LOCA is controlled as descibed in Section 6.2.5. The use of aluminum within the Containment is minimized to the greatest extent practicaL, thereby precluding concern over excessive hydrogen generation due to the corrosion of aluminum.

The vessels used for storing engineered safety features coolant include the accumulators, the boron'njection tank, and the refueling water storage tank (RWST).

The accumulators are carbon steel clad with austenitic stainless steel and the boron injection tank is austenitic stainless steel. Because of the corrosion resistance of these materials, significant corrosive attack of the storage vessels is not expected.

The accumulators are vessels filled with borated water and pressurized with nitrogen gas. The boron concentration, as boric acid, is 2000 ppm.

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Samples of the solution in the accumulators are taken periodically for checks of boron concentration. Principal design parameters of the accumulators are listed in Table 6.3.2-1.

27 6.1.1-3 Amendment No. 27

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SIiNPP FSAR 27 Principal design parameters of the boron injection tank are listed in Table 6.3.2-1.

6.1.l-4 Amendment No. 27

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ip }) '~ pr SHNPP FSAR The containment analyses for the MSLBs have been performed using all the containment initial conditions, heat sinks and methodology assumed for the LOCA analyses except for the following:

a) For the MSIV and MFIV failure cases, both containment heat removal trains (four fan coolers and two spray pumps) are assumed to operate. For the cases of one heat removal system train failure, two fan coolers and one spray pump areiassumed to operate. Also for all the full double-ended rupture cases, one of the operating fan coolers is assumed to be failed due to the possible steam jet impingement on the fan cooler.

b) The mass and energy release rates for the most severe MSLB Containment transient are calculated with the assumption of the availability of the 27 offsite power, as further described in Section 6.2.1.4.8. The Containment Isolation Actuation Signal (CIAS) (T), HI-1(4.5 psig), is reached within 2 seconds after the postulated ruptures for both the most severe temperature and the most severe pressure cases. The fan coolers are assumed in full operation 27 seconds after the CIAS. The containment spray systems are assumed to start the spray in 49 seconds after the CIAS and to reach full flow 3.67 seconds later (HI-1) also assuming HI-3 and the containment spray pumps start.

c) The mass diffusion calculation of the CONTEMPT-LT computer code for the containment vapor-sump heat and mass transfer was conservatively omitted for all MSLB analyses.

For all MSLBs analyzed following blowdown of the ruptured steam generator unit, the RCS decay heat is transferred to the intact units which, in turn, vent to the atmosphere when their safety relief valves open. Therefore, there is no physical mechanism for the release of significant amounts of mass or energy to the Containment after the end of blowdown. Main feedwater line breaks (MFWLB) are not analyzed since such breaks result in a blowdown less limiting than the MSLB because the pipe break mass flow for the MFWLB is limited by the steam generator internals design. Fluid enthalpy for the MFWLB is also less than the enthalpy of the fluid in the MSLB.

A discussion of the computer codes, and the assumptions, including all assumed single active failures, used in deriving the MSLB mass and energy releases are discussed in Section 6.2.1.4.

Accident chronologies for the most severe secondary system break are provided in Table 6.2.1-9. It is assumed that time equals zero at the start of the accident. A detailed energy distribution at several key points of time for these cases is provided in Table 6.2.1-10. These tables show the distribution of energy prior to the accident, at the time of peak pressure, and at the end of blowdown.

The instrumentation provided to monitor and record the post accident containment pressure and temperature is discussed in Section 7.5 ~ This instrumentation is designed and qualified for the SSE and the environmental conditions discussed in Section 3.11

'.2.1-12 Amendment No. 27

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SHNPP FSAR TABLE 6.2.1-2 CALCULATED VALUES FOR CONTAINMENT PARAMETERS Parameter Desi n Basis Accident Calculated Value I

Peak Containment Atmosphere DEHLG with minimum 36.7 psxg Pressure (LOCA) safety injection Peak Pressure (MSLB) 30K Power full DE 39.1 psig+

Rupture MFIV Failure Peak Containment Atmosphere Temperature DEHLG with minimum 257F (LOCA) safety injection Peak Temperature (MSLB) 30X Power Full DE 379F Rupture MSIV Failure Peak Subcompartment Differential Pressure Reactor Cavity 150 in. CLG 29.8 psid Steam Generator (Loop 1) DEHLG 22.2 psid Steam Generator (Loop 2) and Pressurizer DESLG 22.4 psid Steam Generator (Loop 3) DECLG 29 ' psid External Differential Pressure Containment Inadvertent Operation 1.93 psid of the Containment Heat Removal System Minimum Pressure See Section 6.2.1.5

"' containment sensitivity analysis was performed for an initial containment

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27 pressure of 1.9 psig with a resulting peak pressure of 40.91 psig. This

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SIiHPP FSAR ~s TABLE 6.2.1-3 PRINCIPAL CONTAINMENT DESIGN PARAMETERS Parameter ~Desi e Mar in(1)

Containment Internal design pressure, psig (LOCA) 45.0 22.6X (MSLB) 45.0 15.1X External design pressure, psid 2.0 3.6X Net free volume, 10 ft. 2.266 Not Applicable Design leak rate, percent free volume 0.1 Not Applicable per day at 45.0 psig Subcompartments Reactor cavity design wall loading, psid 64.0 115%%d

.Steam generator compartment design wall loading, psid Loop 1 38 71%%d Loop 2 (Including pressurizer compartment) 38 70X Loop 3 38 28X Notes'.

(1) Margin (X) = 100 Desi n value eak calculated value peak calculated value Actual margin, i.e., the margin between design values and peak calculated values when using realistic or mediam parameter values would be much larger.

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SUMMARY

OF CALCULATED CONTAINMENT PRESSURE AND TEMPERATURE 3 ft. Pump DESLG DESLG 0.6 x DESLG Suction Split DEHLG DECLG (Max.SI) (Min.SI) (Min.SI) (Min.SI) (Min.SI) (Min. SI)

A. LOCA Peak Pressure, psig 34.7 34.7 34 34.4 36.7 34.5 Peak Temperature, F 253.5 253 251. 5 252.1 257.1 252.4 Time of Peak Pressure, sec. 19 18 19 31 18.5 16 Time to End of Blowdown, sec. 21.0 21.0 22.2 36.4 19.6 18.8 Energy Release to Containment at End oj Blowdown 244.73 244.73 242.19 252.28 254.06 246.83 Btu x 10 B~ MSLB - COOLING TRAIN FAILURE Percent Power 102 70 30 MSLB Break Size, Full .6 .645 Full .5 .681 Full 4 .7065 Full .1 ft 2 DE DE Split DE DE Split DE

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DE Split DE DE Peak Pressure, 31.7 26.3 27.3 33.5 27.0 28.3 30.9 27.2 30.5 29.6 17.3 Ps1g Peak Temperature, 378 330 343 377 313 349 376 306 351 367 289 F

Time of Peak 154 258 212 178 336 222 207 480 250 240 1810 702 27 Pressure, sec.

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TABLE 6.2.1-4 (continued)

SUMMARY

OF CALCULATED CONTAINMENT PRESSURE AND TEMPERATURE 3 ft. Pump DESLG . DESLG 0.6 x DESLG Suction Split DEHLG DECLG (Max.SI) (Min.SI) (Min.SI) (Min.SI) (Min.SI) (Min.SI)

B. MSLB COOLING TRAIN FAILURE (cont'd)

Time of End 154 258 212 178 336 222 207 480 250 240 1810 702 of Blowdown, sec.

C. MSLB MAIN FEEDWATER ISOLATION VALVE FAILURE Percent Power 102 70 30 MSLB Break Size, Full .6 .645 Full 5 .681 Full .4 .7065 Full .1 .3

~ 8 ft. DE DE Split DE

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DE Split DE DE Split DE DE Split Peak Pressure, 34.4 28.3 29.5 36.1 28.5 30.6 38.7 29.3 33.2 psig 39 1 13'8 24'7 ~l 22 Peak Temperature, 378 319 343 377 313 349 378 307 351 366 291 311 ) 27 F

Time of Peak 190 314 256 217 402 274 249 563. 301 289 2114 845 Pressure, sec.

Time of End 190 314 256 217 402 274 249 563 301 289 2114 845 of Blowdown, I 22 sec.

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SUMMARY

OF CALCULATED CONTAINMENT PRESSURE AND TEMPERATURE 3 ft. Pump DESLG DESLG 0.6 x DESLG Suction Split DEHLG DECLG (Max.SI) (Min.SI) (Min.SI) (Min.SI) (Min.SI) (Min.SI)

D. MSLB MAIN STEAM ISOLATION VALVE FAILURE Percent Power 102 70 30 MSLB Break Size, Full .6 .645 Full .5 .681 Full .4 .7065 Full .1 3 ft 2 ~

DE DE Split DE DE Split DE DE ~ Split DE DE

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Split Peak Pressure, 31.3 26.2 27.4 33.3 27.3 28.5 35.8 27.3 30.9 35.4 13.3 23.1 pslg Peak Temperature, 379 332 343 379 314 350 379 305 350 368 291 310 F I I

Time of Peak 154 258 223 178 336 236 207 480, 264 240 1810 737 Pressure, sec.

Time to End 154 258 223 178 336 236 207 480 264 240 '810 737 of Blowdown, sec.

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SHNPP FSAR TABLE 6.2.1-5 INITIAL CONDITIONS FOR LOCA CONTAINMENT PEAK PRESSURE-TEMPERATURE ANALYSIS Parameter Value Reactor Coolant System and Secondary Sys'em Reactor power level, Mwt 2968.2 Core Inlet Temperature, F 559.2 Steam Pressure, psia 964 Containment Pressure, psia 14.84 Normal operating range, in wg -1 to 4 Temperature, F 120

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Normal operating range, F 80 to 120 Relative humidity,

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%%d Normal operating range, X 5 to 100 Component cooling water temperature, F 145 Refueling water storage tank temperature, F 125 Net free volume (minimum), x 10 ft. 2.266 Stored Water Minimum RWST volume available for Safety Injection, 266,863 /z~

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TABLE 6.2.1~9 (continued)

B. Worst Case Suction Le Break (DESLG)

Assuming Max. SI Assuming Min. SI Time Time (Seconds) (Seconds) Event N/A 2150.0 50 percent of containment design pressure (22.5 psig) reached N/A 2900.0 50 percent of containment peak calculated pressure (18.3 psig) reached C. Worst Case Cold Le Break (DECLG)

Time (Seconds) Event 0.0 Break occurs 16.0 Peak containment pressure during blowdown 18.8 End of blowdown Start of pumped injection 28.0 Start of containment fan coolers 64.24 Start containment spray injection 64.24 Containment spray reaches full flow N/A Peak containment pressure subsequent to end of blowdown 281.5 End of core reflood N/A End of steam generator energy release for post-reflood phase (Froth period)

D. Worst Pressure Case MSLB (Full DEB, MFIV Failure, 0/ Power) 0.0 Break occurs 0.8 Main Steam Isolation Signal 27 0.8 Main Feedwater Isolation Signal 2.0 Containment Isolation Actuation Signal (CIAS) 6.2.1-49 Amendment No. 27

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D. Worst Pressure Case MSLB (continued)

Time (Seconds) Event 2.8 MFIV's start to close 2.8 MSIV's start to close 27 7.8 MFIV's closed 7.8 MSIV's closed 29.0 Start of Containment fan coolers 51.0 Start Containment spray injection 54.67 Containment spray reaches full flow 27 289.0 Peak Containment Pressure 289.0 End of blowdown E. Worst Tem erature Case MSLB (Full DEB, MSIV Failure, 30X Power)

Break occurs Main Steam Isolation Signal Main Feedwater Isolation Signal 27 2.00 CIAS Signal 3.0 MFIV's start to close 3;0 MSIV's start to close 8.0 MFIV's closed 8.0 MSIV's closed 29.0 Start of containment fan coolers 51.0 Start of containment spray injection 51.0 Peak containment temperature 27 54.67 Containment spray reaches full flow 207.6 End of blowdown 6.2.1-50 Amendment No. 27

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SiPHPP FSAR Ii 'Qarmm TABLE 6.2.1-10 (continued)

D. MSLB MSIV Failure at 30X (Full DEB)

(DBA Temperature)

Energy (10 Btu)

At Peak Prior Pressure Ener Descri tion to MSLB (207 sec.)

Energy content of containment atmosphere 0.621 208.105 Energy content ~f containment and internal 0.0 68.792 27.

structures Energy content of recirculation intake water 0.0 16.833 (containment sump)

Energy content of RWST (125 F) 224.77 217.85 Energy removed by shutdown heat exchangers 0.0 0.0 Energy removed by containment fan coolers 0.0 8.37 lgy E. MSLB - MSIV Failure at 30X (Full DEB)

(Worst Pressure)

Energy (10 Btu)

At Peak Prior Pressure Ener Descri tion to MSLB (289.2 sec.)

Energy content of containment atmosphere 0.621 228.919 27 Energy conten( ~f containment and internal 0.0 84.268 structures Energy content of recirculation intake water (sump) 0.0 23.401 Energy content of RWST (125 F) 224.71 214.18 Energy removed by shutdown heat exchangers 0.0 0.0 Energy removed by containment fan coolers 0.0 12.288 /gy 6.2.1-55 Amendment No. 27

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REACTOR CONTAINMENT BUILDING ENERGY DISTRIBUTION NOTES:

(1) The datum temperature is 32 F unless otherwise noted.

(2) Atmospheric constituent datums are 120 F for air and 32 F for water.

(3) Datum for energy content of Containment Building and internal structures is 120 F.

(4) At 15.0 seconds (5) At 19.5 seconds (6) At 20.0 seconds (7) At 189 seconds (8) At 180 seconds (9) At 700 seconds (10) At 90000 seconds (ll) At 19 seconds (12) At 21 seconds (13) At 280 seconds 27 6.2.1-56 Amendment No. 27

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SIINPP FSAR TABLE 6.'2.1-58A Full Double Ended Rupture at 30 Percent Power 1.4 ft. Double Ended Rupture at 30 Percent Power FORWARD FLOW REVERSE FLOW"c Time Flow Enthalpy Pressure Time Flow Enthalpy sec. lb./sec. Btu/lb. PSIA sec. lb./sec. Btu/lb.

0.00 3314.8 1136.48 Tl + 0.00 6629.6 1187.55 1.00 3165.97 1191.28 1043.97 Tl + 1.00 6331.94 1191.28 2.00 2908.14 1194.20 964.92 Tl + 2.00 5816.30 1194.20 3.00 2680.93 1196.69 890.82 Tl + 3.00 5361.92 1196.69 4.00 2464.55 1198.77 822.10 Tl + 4.00 4929.56 1198.76 5.00 2276.46 1200.34 763.88 Tl + 5.00 4554.53 1200.33 27 6.00 2126.48 1201.42 719.22 Tl + 6.00 4258.42 1201.38 7.00 2005.64 1202.24 680.91 Tl + 7.00 4023.65 1202 F 19 8.00 1901.75 1202.88 647.60 Tl + 8.00 3823.25 1202.81 9.00 1810.89 1203.38 618.10 Tl + 9.00 3649.10 1203 '0 10.00 1729.84 1203.78 591.47 Tl + 10.00 3494.53 1203.68 11.00 1655.83 1204.09 567.06 Tl + 11.00 3353.66 1203.99 12.00 1588.16 1204.29 548.85 Tl + 12.00 0 F 00 1203.79 13.00 1549.26 1204.42 535.14 Tl + 13.00 0.00 1203.53 14.00 1509.50 1204.53 521.25 Tl + 14.00 0 F 00 1203.30 15.00 1469.59 1204.63 507.40 Tl + 15.00 0.00 1203.08 17.50 1373.18 1204.77 474.25 Tl + 17.50 0.00 1202.61 20.00 1285.05 1204.78 444.14 Tl + 20.00 0.00 1202.30 22.50 1208.27 1204.70 418.04 Tl + 22.50 0.00 1202.11 25.00 1142.70 1204.56 395.73 Tl + 25.00 0.00 1201.98 27.50 1086.56 1204.37 376.57 Tl + 27.50 0.00 1201.88 30.00 1038.40 1204.15 360.20 Tl + 30.00 0.00 1201.81 35.00 963.10 1203.71 334.44 Tl + 35.00 0.00 1201 '0 40.00 907.01 1203.28 315.17 Tl + 40.00 0 F 00 1201.64 45.00 864.12 1202.90 300 '1 Tl + 45.00 0 F 00 1201.59 50.00 831.26 1202.56 289.10 Tl + 50.00 0 F 00 1201.56 60.00 786.56 1202.04 273.69 Tl + 60.00 0.00 1201.51 70.00 759.78 1201.70 264.45 Tl + 70.00 0.00 1201.49 80.00 744.19 1201.48 259.08 Tl Tl

+ 80.00 0.00 1201 '7 90.00 735.22 1201.35 256.00 + 90 F 00 0.00 ~

1201.46 100.00 730.24 1201.28 254.28 Tl + 100.00 0.00 1201.44 120.00 725.87 1201.21 252.76 Tl + 120 F 00 0.00 1201.42 140.00 724.07 1201.19 252.14 Tl + 140.00 0.00 1201.39 160.00 720.93 1201.14 250.97 Tl + 160.00 0.00 1201.37 180.00 716.15 1201.06 249.27 Tl + 180.00 0.00 1201.35 200.00 710.67 1200.97 247.32 Tl + 200.00 0.00 1201.34 220.00 704.38 1200.87 245.08 Tl + 220 F 00 0 F 00 1201.34 240.00 697.27 1200.75 242.54 Tl + 240.00 0.00 1201.35 260.00 657.77 1199.96 . 226.76 Tl + 260.00 0.00 1201.37 280.00 537.57 1197.22 184.57 Tl + 280.00 0.00 1201.41 300.00 477.02 1195.43 163.54 Tl + 300.00 0.00 1201.47 Note: (1) The time that piping blowdown ends and reverse flow from steam generators begins.

(2) The mass flowrate during steam piping blowdown in ibm/sec.

+Total Reverse Flow 6.2.1-163 Amendment No. 27

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P+y SIPNPP FSAR TABLE 6.2.1-58B Q>> Full Double Ended Rupture at 0 Percent Power 1.4 ft. Double Ended Rupture at 0 Percent Power FORWARD FLOW REVERSE FLOW" Time Flow Enthalpy Pressure Time Flow Enthalpy sec. lb. /sec. Btu/lb. PSIA sec ~ lb./sec. Btu/lb.

0.00 3221.3 1188.01 1106.08 Tl + 0.00 8442.5 1188.81 1.00 3087.34 1192.00 1025.03 Tl + 1.00 6174.67 1192,00 2.00 2885.37 1194.24 963.62 Tl + 2.00 5770.48 1194.16 3.00 2712.88 1196.54 895.54 Tl + 3.00 5435.19 1196.47 4.00 2457.53 1199.08 810.97 Tl + 4.00 4928.48 1199.02 5.00 2215.56 1201.08 733.66 Tl + 5.00 4445.68 1201.01 27 6.00 2005.14 1202.51 667;50 Tl + 6.00 4029.26 1202.43 7.00 1828.22 1203.48 611.69 Tl + 7.00 3682.43 1203.40 8.00 1679.09 1204.12 564.33 Tl + 8.00 3392.85 1204.04 9.00 1552.74 1204.51 523.60 Tl + 9.00 3146.73 1204.45 10.00 1443.54 1204.72 488.01 Tl + 10.00 2934.87 1204.68 11.'00 1347.81 1204.79 456.50 Tl + 11.00 0.00 1204 '6 12.00 1262.61 1204.78 438.41 Tl + 12.00 0.00 1204.74 13.00 1241.39 1204.75 430.46 Tl + . 13.00 '.00 1204.68 14.00 1217.46 1204.72 421.72 Tl + 14.00 0 F 00 1204.62 15.00 1191.78 1204.67 412.50 Tl + 15.00 0.00 1204.55 17.50 1124.73 1204.50 388.94 Tl + 17.50 0.00 1204.44 20.00 1060.97 1204.25 367.01 Tl + 20.00 0.00 1204.37 22.50 1005.50 1203.96 348.08 Tl + 22.50 0.00 1204.33 25.00 958.25 1203.66 331.92 Tl + 25.00 0.00 1204.29 27.50 917.49 1203.35 317.92 Tl + 27.50 0.00 1204.25 30.00 882.01 1203.04 305.73 Tl + 30.00 0.00 1204.23 35.00 824.83 1202.47 286.13 Tl + 35.00 0.00 1204.19 40.00 783.42 1201.98 271.96 Tl + 40.00 0.00 1204.15 45.00 753.66 1201.59 261.76 Tl + 45.00 0.00 1204.10 50.00 732.07 1201.28 254.36 Tl + 50.00 0.00 1204.04 60.00 705.37 1200.88 245.22 Tl + 60.00 0.00 1203.93, 70 F 00 691.63 1200.66 240.51 Tl + 70.00 0.00 1203.80 80.00 684.78- 1200.54 238.17 Tl + 80.00 0.00 1203.67 90.00 681.66 1200.49 237.11 Tl + 90.00 0.00 1203.55 100.00 680.54 1200.47 236.74 Tl + 100.00 0.00 1203.44 120.00 680.98 1200.48 236.93 Tl + 120.00 0.00 1203 '4 140.00 682.32 1200.50 237.40 Tl + 140.00 0.00 1203.08 160.00 683.35 1200.52 237.76 Tl + 160.00 0.00 1202.95 180.00 683.72 1200.53 237.88 Tl + 180.00 0.00 1202.85 200.00 683.27 1200.52 237.70 Tl + 200.00 0.00 1202 78 220.00 679.85 1200.46 236.42 Tl + 220.00 0.00 1202.74 240.00 674.31 1200.36 234.44 Tl + 240.00 0.00 1202.72 260.00 667.83 1200.24 232 '3 Tl + 260.00 0.00 1202.73 280.00 660.49 1200.10 229.52 Tl + 280.00 0.00 1202.75 300.00 652.35 1199.95 226.62 Tl + 300.00 0.00 1202.79 Note: (1) The time that piping blowdown ends and reverse flow from steam generators begins.

(2) The mass flowrate during steam piping blowdown in ibm/sec'Total Reverse Flow Amendment No. 27 6.2.1-163a

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SHNPP FSAR 6.2.2 CONTAINMENT HEAT REMOVAL SYSTEM The purpose of the Containment Heat Removal System (CHRS), is to rapidly reduce the containment pressure and temperature following a reactor or steam generator energy release and to maintain them at acceptably low levels. The CHRS also serves to limit offsite radiation levels by reducing the pressure differential between the containment atmosphere and the external environment, thereby decreasing the driving force for fission product leakage across the Containment. In addition, airborne iodine following a loss-of-coolant accident (LOCA) is removed by spraying borated sodium hydroxide solution into the Containment. The fission product removal function is carried out by the Iodine Removal System (IRS) as discussed in Section 6.5.2.

The systems provided for containment heat removal include the Containment Cooling System (CCS) and Containment Spray System (CSS). The Containment Cooling System is designed to operate during both normal plant operations and under LOCA or main steam line break (MSLB) conditions. The operations of the CCS are discussed in Section 6.2.2.2.1. The CSS is designed to operate during accident conditions only. The operation of the CSS is discussed in Section 6.2.2.2.2.

The CCS and the CSS are designed to remove heat from the containment atmosphere following a LOCA accident or a secondary system rupture inside Containment, as required by General Design Criteria 38. The CCS also provides a supply of cooling air to the annular clearance between the reactor vessel and primary shield wall, the reactor vessel supports and the annular space between the reactor coolant legs and the concrete wall.

a) The sources and amounts of energy released to the Containment as a function of time which were used as the basis for sizing the Containment Heat Removal System are given in Sections 6.2.1.3 and 6.2.1.4. The CCS and CSS are each designed to remove 240x10 Btu/hr. under LOCA post accident steam-air mixture conditions of 258 F, 36.7 psig and 100 percent relative humidity while the essential portions of the Service Water System (SWS) is providing cooling water to the CCS at 95 F. A description of the SWS is presented in Section 9.2.1.

b) The heat removal capacity of either the CCS'r the CSS is sufficient to keep the containment temperature and pressure below design conditions for any size break up to and including a double ended break of the largest reactor coolant pipe. The system is also designed to mitigate the consequences of any size break in the secondary systems, up to and including' double ended break of the largest main steam line inside Containment.

c) The CCS and CSS each consist of two redundant loops and are designed such that failure of any single active or passive component will not prevent adequate post-accident cooling of the containment atmosphere.

d) The safety related portions of the CCS and CSS are designed to Safety Class 2, Seismic Category I requirements.

6.2 '-1 Amendment No. 27

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SHNPP FSAR Upon receipt of the CSAS the containment spray pumps are started and borated water from the RWST is discharged into the Containment through the containment spray headers. The CSAS starts the two containment spray pumps and opens the motor operated containment spray isolation valves. Upon initiation of the containment spray pumps, water will reach the nozzles and start spraying within 32 seconds. The spray headers are located to maximize heat removal.

Each train of the CSS has two headers which conform to the shape of the Containment and contain a total of 106 spray nozzles per train. The number of spray nozzles in the system provides 100 percent redundancy for effective heat removal and iodine removal. Figure 6.2.2-2 provides the location of spray piping and nozzles and the resulting spray pattern. Refer to Section 6.5.2 for a discussion of Containment sprayed and unsprayed volumes.

A flow element is installed in each containment spray pump s discharge line.

Low flow alarm will be provided to monitor the system operation.

The spray nozzles, which are of open throat design, without any moving parts (minimum inside diameter of approximately 0.375 in.), break the flow into small droplets, which increases the cooling effectiveness on the containment atmosphere. As these droplets fall through the containment atmosphere they absorb heat until they reach the temperature of the containment air-steam mixture. The spray nozzles are protected from clogging by the following means:

There are two independent sumps which serve as reservoirs and provide suction to the ECCS and CSS plumps during the recirculation mode of operation. Each sump is covered with a removable checker plate steel cover which is fastened to the support steel by stainless steel screws. In addition, the sump wall openings are provided with two-stage stainless steel screens composed of:

a) A stainless steel coarse outer screen with openings having an area of approximately 2.25 square inches.

b) A stainless steel fine inner screen with openings no larger than 0.125 inch in diameter.

Figure 6.2.2-19 shows the containment building recirculation sump screens.

A curb approximately 18 in. high and located 2 ft. in front of the screen structure is provided to prevent heavy debris from impingement: upon the screens. The floor outside of the curb slopes away from the sump'o minimize debris from entering the sump.

The containment recirculation sumps have been designed and constructed to ensure the functional capability of the sumps to provide an adequate supply of water during the recirculation mode of operation for the Containment Spray System and the Residual Heat Removal System. In addition, the containment recirculation sumps have been evaluated against the guidelines provided in NUREG-0869, Revision 1 "Unresolved Safety Issue A-43 Regulatory Analysis" (Reference 6.2.2-2). This evaluation concluded that post-LOCA insulation debris will not degrade either the performance of the containment sumps or that of the RHR pumps and the CS pumps.

6.2.2-7 Amendment No. 27

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.L b) The tank must provide a quantity of water requir l

Refueling Cavity, the Fuel Transfer Tube and the Fuel, Transfer Canal, during refueling.

The RWST is designed for a 469,812 gallon capacity with a minimum water inventory of 433,285 gallons maintained during all'normal modes. This minimum inventory will only be removed from the RWST during unit refueling after shutdown and will always be maintained for post-accident recirculation mode I 27 operation and system testing.

The two RWST vent lines are protected from freezing by redundant ambient sensing heat tracing on each vent line. The power supply for the heat tracing on each vent line is supplied by separate trains.

The water in the RWST will be maintained't a temperature of not less than 40 F utilizing heaters, the minimum temperature for injection of borated water during emergency core cooling as indicated in Section 6.3. The freezing point of 2000 ppm boron solution, 1.14 weight percent boric acid, is below the normal freezing point of water, therefore a 40 F minimum temperature precludes freezing. In addition, the solubility temperature for a 2000-2200 ppm boron, 1.14 - 1.26 weight percent boric acid solution is below 40 F.

The refueling water storage tank is a Seismic Category I field-fabricated tank of stainless steel construction. It is designed, fabricated, erected, and tested in accordance with the requirements of ASHE Boiler and Pressure Vessel Code Section III, Winter Addenda 1971, Class 2.

The RWST is designed for the horizontal and vertical seismic loads for both the Design and Operating Basis Earthquakes. The RWST would not be required for plant shutdown following a tornado. The tank is therefore not designed for tornado winds or pressure drops.

The major design parameters for the refueling water storage tank are indicated in Table 6.2.2-9.

6.2.2.3.2.4 Primary Shield and Reactor Supports Cooling System The Primary Shield and Reactor Support Cooling Systems are safety related and designed to Safety Class 3 and Seismic Cateogry I requirements.

Each system is provided with redundant fans to assure continuity and reliability of operation. "Each fan is supplied with onsite emergency power from the diesel generators, in the event of loss of offsite power.

6.2.2.4 Testin and Ins ection 6.2.2.4.1 Containment Cooling System CCS The CCS undergoes preoperational startup tests as described in Section 14.2.12. Periodic tests are required as described in the Technical Specifications. Inservice inspection requirements are described in Section 6.6 and pump and valve testing requirements of Section 3.9.6 will apply.

Factory tests verify cooling coil and motor performance.

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SHNPP FSAR TABLE 6.2.2-1 CONTAINMENT COOLING SYSTEM COMPONENTS NOTE: All air quantities are actual cfm.

CONTAINMENT FAN COOLER SAFETY CLASS 2 UNITS Normal Design Basis Operating Accident Conditions Conditions No. of Units 2 fans per 1 fan per unit unit and half speed, 4 2 units units starting operating and 2 units operating Fan Cooler 125,000 31,250 Unit Operating Capacity ACFM Actual Air Mixture 62,500 31,250 Flow (ACFM) at Fan Inlet Design Ambient 0 45.0/39.1 (1) 27

Pressure, e psig Ambient Temp, F 120 258 Total Pressure, in. WG 7.9 5.1 Fan RPM 1770 870 Outlet Velocity, FPM 5800 2560 Brake HP 101.2 32.8 Motor HP 125 62.5 Cooling Water 1500 1500 Flow GPM Entering Water 95 95 Temp. F NOTE:~ (1) 39.1 psig steam line break pressure 45.0 psig

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TABLE 6.2.2-9 CONTAINMENT SPRAY SYSTEM COMPONENT PARAMET Containment ~S>~ra ~Pum s Number of Pumps 2 Type of Bump Centrifugal Design Flow, gpm 2275 Design Head, ft 425 27 Driver Electric Motor Driver horsepower (approximate) 350 Material (casing) SA-182 Type F 304 Code ASME III, Safety Class 2

~Refuelin Mater ~Stars e Tank Quantity 1 Material Stainless Steel Type 304 Maximum Volume, gal 469,812 Minimum Volume, (solution) gal ~ 433,285 27, A Normal Pressure, psig Atmospheric Operating Temperature, F 40-125 27

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Design Pressure, psig Atmospheric Design Temperature, F 200 Boric Acid (as ppm B) 2000-2200 ppm I

27 Code ASME III, Code Class 2

~Cavitatin Venturi Quantity (per train) 1 Size, inches 8 Design Flow, gpm 2770 Material 316 SS Code ASME III, Class 2 Containment ~S r~a Nozzles Quantity (per train) 106 Nozzle size, inches '/8 Design Flow, gpm 15.2 Material ASME A-351 GrCF8 Code ASME III, Class 2 Motor ~0 crated Isolation Valves Quantity, (per train) 1 Size, inches 8 Type Gate Design, Pressure, psig 300 Design Temperature, F 300 Material 304 SS Code ASME III, Class 2 Operator Motor 6.2.2-28 Amendment No. 27

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4 SHNPP FSAR 6.3 EMERGENCY CORE COOLING SYSTEM 6.3.1 DESIGN BASES The Emergency Core Cooling System (ECCS) is designed to cool the reactor core and provide shutdown capability following initiation of the following accident conditions:

a) Loss-of-coolant accident (LOCA) including a pipe break or a spurious relief or safety valve opening in the Reactor Coolant System (RCS) which would result in a discharge larger than that which could be made up by the normal makeup system.

b) Rupture of a control rod drive mechanism causing a rod cluster control assembly ejection accident.

c) Steam or feedwater system break accident including a pipe break or a spurious power operated relief or safety valve opening in the secondary steam system which would result -in an uncontrolled steam release or a loss of feedwater.

d) A steam generator tube failure.

The primary function of the ECCS is to remove the stored and fission product decay heat from the reactor core during accident conditions.

The ECCS provides shutdown capability for the accidents above by means of boron injection. The system is designed to tolerate a single active failure (injection'hase), or a single active or passive failure (recirculation phase). Table 6.3.1-1 provides a failure modes and effects analysis which demonstrates the capability of the ECCS to perform following a single active failure. This analysis also shows that single failures occurring during ECCS operation 'do not compromise the ability to prevent or mitigate accidents. The capabilities are accomplished by a combination of suitable redundancy, instrumentation for indication and/or alarm of abnormal conditions, and relief valves to protect piping and components against malfunctions. The ECCS can meet its minimum required performance level with onsite or offsite electrical power.

The ECCS consists of the centrifugal charging pumps, residual heat removal pumps, accumulators, a boron injection tank, residual heat removal heat exchangers, the hydro test pump, a refueling water storage tank, along with

'I associated piping, valves, instrumentation and other related equipment.

See Section 1.3.1 for comparison of the SHNPP ECCS with similar facility designs.

The design bases for" selecting the functional requirements of the ECCS are derived from data which is consistent with 10CFR50 Appendix K limits following any of the above accidents as delinated in 10CFR50.'46. The subsystem functional parameters are integrated such that the Appendix K requirements are met over the range of anticipaed accidents and single failure assumptions.

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EMERGENCY CORE COOLING SYSTFM FAILURE MODES AND EFFECTS ANALYSIS n

Failure Detqqtion Component Failure Mode Function Effect on System Method Remarks operation. Alternate isolation'valve 1-8803B (1-8803A) opens to provide backup flow path to BIT.

8. Motor Fails to Provides isolation Failure reduces redun- Same as in item g2.

operated open on of fluid discharge dancy of providing gate valve demand. from the BIT to fluid flow from BIT 1-8801A (1- high head injection to high head injection 8801B header connected to header feeding the analogous) the cold legs of cold legs of RCS loops.

RCS coolant loops. Negligible effect on system operation.

Alternate isolation valve 1-8801B (1-8801A) opens to provide backup flow path to header.

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EMERGENCY CORE COOLING SYSTEM FAILURE MODES AND EFFECTS ANALYSIS Failure Detection Component Failure Mode Function Effect on System Method Remarks 27 11 'otor Falls Provides regulation Failure reduces working Same as item SI ~ Valves are regulated operated opens of fluid flow through fluid delivered to RCS In addition, pump by signals from flow globe miniflow bypass line from LHSI/RHR pump 1 discharge header transmitter located valve 1- to suction of (pump 2), Minimum flow, pressure and flow in each pump dis-FCV-602A LHSI/RHR pump I requirements will be met indication at MCB. charge header, The (I-FCV-6028 (pump 2) to protect by LHSI/RHR pump 2 control valves open analogous) against overheating (pump 1) delivering when a LHSI/RHR pump of the pump and loss working fluid to RGB discharge flow is of suction flow to less than 500 gpm and the pumps close when the flow exceeds 1000 gpm,

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TABLE 6.3.1-1 (Continued)

EMERGENCY CORE COOLING SYSTEM FAILURE MODES AND EFFECTS ANALYSIS List of acrongms and abbreviation MCB Main control board 27 BIT Boron injection tank RCS - Reactor Coolant System 27 RHR Residual heat removal CHG Charging RWST Refueling water storage tank HHSI High head safety injection SIAS safety injection actuation signal LHSI Low head safety injection SIS Safety Injection System LOCA Loss-of-coolant accident SSPS Solid state protection system VCT Volume control tank

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~ ~ SYSTEM DESIGN The ECCS components are designed such that a minimum of two accumulators, one charging pump and one residual heat removal pump together with their associated valves and piping will assure adequate core cooling in the event of a design basis LOCA. The redundant onsite standby diesel generators assure adequate emergency power to at least one train of electrically operated components in the event that a loss of offsite power occurs simultaneously with a LOCA.

6.3.2.1 Schematic Pi in and Instrumentation Dia rams Flow diagrams of the ECCS are shown in Figures 6.3.2-1 through 6.3.2-3.

Pertinent design and operating parameters for the components of the ECCS are given in Table 6.3.2-1. The codes and standards to which the individual components of the ECCS are designed are listed in Table 3.2.1-1.

The component interlocks used in different modes of system operation are listed below.')

The safety injection signal, "S", is interlocked with the following components and initiates the indicated action.')

Centrifugal charging pumps start on "S" signals

2) Refueling water storage tank suction valves to charging pumps open on "S" signal ~

3) Boron injection tank suction and discharge parallel isolation valves open on "S" signal.

4) Normal charging path valves close on "S" signal.

5) Normal charging pump miniflow valves close on "S" signal.

6) Alternate miniflow path valves open on "S" signal.

7) Residual heat removal pumps start on "S" signal.

27

8) Any closed accumulator isolation valves open on "S" signal.

9) Uolume control tank outlet isolation valves close on "S" signal.

b) Switchover from injection mode to recirculation involves the following interlocks:

1) 'he suction valves from the containment sump open when two out of four low level transmitters indicate a low-low level in the RWST in conjunction with an "S" signal.

2) The charging pump suction (recirculation line) isolation

~alve from the RHR pump discharge line cannot be opened unless one of the RHR suction isolation valves from the RCS hot legs is closed.

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3) The recirculation flow paths from the RHR pumps discharge to the charging pump suction is interlocked such that the isolation valves in these lines cannot be opened unless the alternate miniflow paths are isolated.

6.3.2.2 E ui ment and Com onent Descri tions I

The component design and operating conditions are specified as the most severe conditions to which each respective component is exposed during either normal plant operation or during operation of the ECCS. .For each component, these conditions are considered in relation to the code to which it is designed. By designing the components in accordance with applicable codes, and with due consideration for the design and operating conditions, the fundamental assurance of structural integrity of the ECCS components is maintained.

Components of the ECCS are designed to withstand the appropriate seismic loadings in accordance with their safety class as given in Table 3.2 1.

The discussion of each maj or mechanical component of the ECCS follows below.

6.3.2.2.1 Accumulators The accumulators are pressure vessels partially filled with borated water and pressurized with nitrogen gas. During normal operation each accumulator is isolated from the RCS by two check valves in series. Should the reactor coolant system pressure fall below the accumulator pressure, the check valves open and borated water is forced into the RCS. One accumulator is attached to each of the cold legs of the RCS. Mechanical operation of the swing disc check valves is the only action required to open the injection path from the accumulators to the core via the cold leg.

Connections are provided for remotely adjusting the level and boron concentration of the borated water in each accumulator during normal plant operation as required. Accumulator water level may be adjusted either by draining to the refueling water storage tank or by pumping borated water from the refueling water storage tank to the accumulator. Samples of the solution in the accumulators are taken periodically for checks of boron concentration.

Accumulator pressure is provided by a supply of nitrogen gas, and can be adjusted as required during normal plant operation', however, the normally isolated from this nitrogen supply. Gas relief accumulators're valves on the accumulators protect them from pressures in excess of design pressure.

The accumulators are located within the Containment, but outside of the secondary shield wall which protects them from missiles'ccumulator gas pressure is monitored by indicators and alarms'he operator can take action as required to maintain plant operation within the requirements of the Technical Specification covering accumulator operability.

6.3.2.2.2 Boron Injection Tank The boron injection tank is connected to the discharge of the centrifugal

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SHNPP FSAR pumps provide the pressure to inject the boric acid solution into the RCS when the isolation valves associated with the boron injection tank open automatically.

In the accide nt analysis (Section 15.5) the system was analyzed assuming the BIT boron concentration as boric acid was 0 ppm. This assumption provides the most limiting case for analyses; however, the BIT may contain a boron concentration as boric acid within the range of 0 2200 ppm.

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7 SHNPP FSAR The changeover from the injection mode to recirculation mo'de is initiated automatically and completed manually by operator action from the Control Room.

The design of the Refueling Water St or age Ta nk ( RWST ) at Shearon Harris Nuclear Plant includes allowances to account for working and transfer water allowance, instrument error, single failure and the unusable volume of water present in the bottom of the tank. Consideration has been given to the amount of water required for core reflood and cooling and the pH requirements for water entrained in the containment sump. Additionally, the positioning of the inst'rument (alarm) levels permits sufficient time for appropriate operator action required for ECCS switchover to recirculation. The. shortest times available for ECCS injection and switchover are as follows.

a) In ection Mode Allowance The safety injection mode of ECCS operation consists of the ECCS pumps (charging pumps and residual heat removal pumps) and the containment spray pumps taking suction from the refueling water storage tank (RWST) and delivering to the reactor coolant system (RCS) and containment, respectively. In order to analyze the shortest time available for injection mode operation, the following conservative bases are established:

1) The RMRT volume available for injection mode operation is 266,863 J 27 gallons.

2) Containment and RCS pressures are conservatively assumed to be 0 psig to maximize flow out of the RWST.

3) Flow out of the RWST during the injection mode includes conservative allowances for two pumps of each type operating at the following flow rates: J Charging pump 650 gpm per pump RHR pump 3750 gpm per pump Spray pump 2130 gpm per pump 27 Total RWST outflow during injection mode operation is 13,060 gpm.

Based on the above minimum available RWST volume for injection mode operation and the maximum total flow rate out of the RWST, the shortest injection mode operation time is approximately 20 minutes. '27 b) Transfer Allowance - During the safety injection mode of ECCS operation, the operator monitors the RWST level and containment recirculation sump level in anticipation of switchover. During this time, the operator is required to open the component cooling water inlet isolation valves to the residual heat removal (RHR) heat exchanger.

s The ECCS switchover from safety injection to cold leg recirculation is initiated automatically upon receipt of the RWST low-low level signal in conjunction with the safety injection signal and is completed via timely operator action at the main control board.

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SHNPP FSAR Switchover is initiated via automatic opening of the containment recirculatio sump isolation valves (8811 A/B and 8812 A/B). This automatic action aligns the suction of the RHR pumps to the containment recirculation sump to ensure continued availability of a suction source The low-low RWST level signal, which initiated the automatic opening of the containment sump valves, also provides an alarm to inform the operator that he must initiate the manual actions required to complete switchover.

Manual actions 1 through 5 of Table 6.3.2-6 must be performed following switchover initiation prior to loss of the RWST transfer allowance to ensure that all ECCS pumps are protected with suction flow available from the containment sump. The manual actions required to complete ECCS switchover are shown as actions 6 through 7 of Table 6.3.2-6. The ECCS switchover procedure is structured so that the operator simultaneously switches both trains of the ECCS from injection to recirculation, repositioning functionally similar switches as part of the same procedural steps.

The time available for switchover is dependent on the flow rate out of the RWST as the switchover manual actions are performed. As ECCS valves are repositioned, the flow rate out of the RWST is reduced in magnitude. In order to analyze the shortest time available for switchover, the following conservative bases are established:

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1) The RWST minimum transfer allowance available is 59,271 gallons.

2) The RWST volume available for switchover does not take credit for the additional 46,100 gallons below the minimum submergence level but above the bottom of the RWST outlet nozzle.

3) Containment'and RCS pressures for large break conditions are conservatively assumed to be 0 psig. Thus, no credit is taken for the reduction in RWST outflow that will result with higher containment and RCS pressures following a large break.

The same conservative assumption is made for the small break conditions (except that RCS pressure is assumed to be greater than RHR pump shutoff head resulting in no RHR pump flow to the RCS for small break conditions).

4) Flow out of the RWST during switchover includes allowances for both pumped flow to the RCS and containment and backflow to the containment sump based on the 0 psig containment pressure assumption.

Average flow rates are assumed during switchover and include the following conservative flow rate allowances assuming two pumps of each type are operating:

Charging pump 650 gpm per pump 27 RHR pump 3750 gpm per pump Spray pump 2130 gpm per pump Backflow to the containment sump may occur during ECCS switchover based on the 0 psig containment pressure assumption and ECCS operating conditions. Backflow, if it occurs, will vary as the switchover proceeds depending on ECCS alignment.

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5) Flow rate out of the RWST for the worst ECCS single failure condition is determined assuming one of the RWST/RHR isolation valves (8809A or 8809B) fails to close on demand. This single failure maximizes RWST outflow during switchover. Flow rates out of the RWST assume no operator corrective action to mitigate the single failure (i.e., stop the affected RHR pump and close the appropriate sump isolation valves).

I Based on the criteria, the calculated flow rates out of the RWST as a function of switchover manual action are itemized in Table 6.3.2-9 for Large breaks.

The large break with single failure constitutes the condition where RWST outflow is the greatest. Flow rate data for small breaks is less than for large breaks and is not included in Table 6.3.2-9. Table 6.3.2-9 also identifies the operator action time assumed per switchover step and shows the change in RWST volume per switchover step. Analyzing the flow rate out of the RWST for large LOCA with single failure indicates that 56,559 gallons are )27 consumed in performing switchover manual actions 1 through 5. This volume is less than the transfer allowance of 59,271 gallons, which ensures that the )27 switchover steps necessary to protect all ECCS pumps can be accomplished before the transfer allowance is depleted.

Protection Logic is provided to automatically open the ECCS recirculation containment sump isolation valves when two out of four refueling water storage tank leveL channels indicate a refueling water storage tank level less than a low-low level setpoint in conjunction with the initiation of the safety injection actuation signal ("S" signal). This automatic action aligns the two RHR pumps to take suction directly from the containment sump.

The charging pumps will continue to take suction from the RWST, following the above automatic action, until manual operator action is taken to align these pumps in series with the RHR pumps. The low-low RWST level signal, which initiated the automatic opening of the containment sump valves, also provides an alarm to inform the operator that he must initiate the manual actions required to realign the RHR and charging pumps for the recirculation phase.

The manual switchover sequence are delineated in Tables 6.3.2-6, 6.3.2-9, and 6.3.2-10. The RHR pumps would continue to operate during this changeover from injection mode to recirculation mode. Following the automatic and manual switchover sequence, the two RHR pumps would take suction from the containment sump and deliver borated water directly to the RCS cold legs. The RHR pump discharge flow would be used to provide suction to the two charging pumps which would also deliver directly to the RCS cold legs.

After approximately 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months following a LOCA, the hot leg recirculation phase would be initiated. Both the RHR pumps and the charging pumps would be aligned to deliver flow only to the RCS hot legs'he refueling water storage tank level protection logic consists of four level channels with each level channel assigned to a separate process control protection set. Four refueling water storage tank level transmitters provide level signals to corresponding normally deenergized level channel bistables.

Each level channel bistable would be energized on receipt of a refueling water storage tank level signal less than the low-1'ow level setpoint.

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TABLE 6.3.2-1 L EMERGENCY CORE COOLING SYSTEM COMPONENT PARAMETERS Accumulators Number Design pressure (psig) internal 700 external 60 Design temperature (F) 300 Operating temperature (F) 120 Normal pressure (psig) 665 27 Minimum operating pressure (psig) 585 Total volume (ft. ) 1450 each Normal operating water volume (ft..) 925 each Volume N2 gas (ft. 3 ) 525 Boron concentration, (ppm) 2000 2200 Centrifu al Char in Pum s Number Design pressure (psig) 2800 Design temperature (F) 300 Design flow (gpm) 150 Design head (ft.) 5800 Maximum flow (gpm) 650 Head at maximum flow (ft.) 3100 Motor rating (hp) 900 Residual Heat Removal Pum s Number 2 Design pressure (psig) 600 6.3.2-14 Amendment No. 27

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SHNPP FSAR TABLE 6.3.2-1 (Continued)

Residu'al Heat Removal Pum s (Continued)

Design temperature (F) 400 Design flow (gpm) 3750 I

Design head (ft.) 240 NPSH required Q 4500 gpm (ft.) 18 Available NPSH 20 Motor Rating (HP) 300

< Provisions are made to install orifices in the safety injection headers, to limit runout flow to a maximum of approximately 4500 gpm.

Residual Heat Exchan ers (See Section 5.4.7 for Design Parameters)

H drostatic Test Pum Number Design pressure (psig) 3300 Design temperature (F) 300 Normal operating temperature ambient Design flow rate (gpm) 24.5 Developed head (ft) at design flow 7000 Boron In ection Tank Number Total volume (gal.) 900 Boron concentration (ppm) 0 - 2,200 Design pressure 2735 (psig)'perating pressure ATMo Design temperature (F) 300 Operating temperature (F) 120 27 I

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Motor 0 crated Valves Maximum 0 enin or Fast 3" and 4" 15008 valves 10 sec (")

6" 12" valves 15 sec.

20 sec.

Slow Up to and including 8 in. 12 in./min./in. of nominal valve size Over 8 in. 2 min.

NOTES:

(a) Includes 60 gpm allowance for miniflow (b) Stroke times of the following valves are < 15 seconds. 'LC V115 B/D, 8130 A/B, 8131 A/B, 8888 A/B, 8889, and 8706 A/B. Stroke times of the following valves are < 20 seconds. '8808 A/B/C, 8811 A/B, and 8812 A/B.

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TABLE 6 3.2-2 EMERGENCY CORE COOLING SYSTEM RELIEF VALVE DATA Fluid Inlet Set Backpressure Maximum Total Fluid Temperature Pressure Constant Backpressure Description (~a(schar sd Normal ~(ps< ) ~(as i (psI ) ~caaacit N2 supply to accumulators 120 700 0 0 1500 scfm 27 Residual heat removal pump safety injection M

I ine Water 120 600 50 20 gpm a4 I

Accumulator co to Containment N2 gas 120 700 0 0 1500 scfm Hydrostatic Test

~ Pump Discharge Water 120 0 0 30 gpm 0

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SUNPP FSAR TABLE 6.3.2-4 MATERIALS EMPLOYED FOR EMERGENCY CORE COOLING SYSTEM COMPONEN

~Com oncet Material Accumulators Carbon steel clad with austenitic stainless steel Boron Injection Tank Austenitic stainless steel 27 Pumps Centrifugal charging Austenitic stainless steel Residual heat removal Austenitic stainless steel Hydrotest Austenitic stainless steel 27 Residual heat exchangers Shell Carbon steel Shell end cap Carbon steel Tubes Austenitic stainless steel Channel Austenitic stainless steel Channel cover Austenitic stainless steel Tube sheet Austenitic stainless steel Valves Motor operated valves containing radioactive fluids Pressure containing Austenitic stainless steel parts or equivalent (Refer to Table 6.1.1-1).

Body-to-bonnet Low alloy steel Bolting and nuts Seating surfaces Stellite Stems Austenitic stainless steel or 17-4 pH stainless Motor operated valves containing nonradioactive, boron-free fluids Body, bonnet Carbon steel and flange Stems Corrosion resistance steel Amendment No. 27 6.3.2-22

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4 TABLE 6.3.2-8 NORMAL OPERATING STATUS OF EMERGENCY CORE COOLING SYSTEM COMPONENTS FOR CORE COOLING Number of charging pumps operable I

Number of residual heat removal pumps operable Number of residual heat exchangers operable Refueling water storage tank minimum volume (gal.) 433,285 Boron concentration in refueling water 'storage tanks, minimum (ppm) 2,000 Boron concentration in accumulator, minimum (ppm) 2,000 Number of accumulators Minimum accumulator pressure (psig) 585 Nominal accumulator water volume (ft. ) 925 System valves, interlocks, and piping required for the above components which are operable All 6.3.2-28 Amendment No. 27

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TABLE 6 ' '-9 RWST OUTFLOW LARGE BREAK NO FAILURES TIME REQHIljED PR TOTAL ELAPSED RWST FLOW RAT] PER STEP CHANGE IN RWST TOTAL RWST STEP STEP (SEC) TIME (SEC) (GPM)(2)< )L7J VOL. PER STEP (GAL) VOL. CHANGE (GAL) 0 17.1 17.1 18,183 5,182 5,182 1 47.1 64.2 13,186 10,351 . 15,533 2 42.2 106.4 13,245 9,316 24,849 27 3 40 146.4 6,716 4,477 29,326 4(8) 40 186.4 1,152 768 30,094 5 40 226.4 0 0 30,094 NOTES'1)

See Table 6.3.2-6 for a description of the steps.

(2) Flow rates are based on pump flows as follows'. CQ RHR pump = 3750 gpm per pump CCHG pump = 650 gpm per pump 27 CS pump = 2130 gpm per pump (3) Valve operating times are maximum operating times.

(4) Time for valves 8811A/B and 8812A/B to automatically open.

(5) Time required to complete the required action includes a conservative 30 seconds for operator response time for each manual procedure.

(6) The flow rate in this column represents an average value during the entire time interval for its respective step.

(7) Flow out of the RWST during switchover includes allowances for both pumped flow to the RCS and containment and backflow to the containment sump.

(8) Following the completion of this step RHR, Charging, and Containment Spray pumps are aligned with suction flow capability from the containment sump.

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RWST OUTFLOW LARGE BREAK WORST SINGLE FAILURE TIME REgUIlgf PR TOTAL ELAPSED RWST FLOW +'g PEg STEP CHANGE IN RWST TOTAL RWST STEP(') STEP (SEC) TIME (SEC) (GPM)(2JR )C7S VOL. PER STEP (GAL) VOL. CHANGE (GAL) 0 17.1(4) 17.1 18,183 5,182 5,182 1 47 ' 64.2 19,243 15,106 20,288 2 42.2 106.4 20,645 14,520 34,808 3 40 146.4 16,676 11,117 45,925 27 4(8) 40 186.4 8,551 5,701 51,626 5 40 226.4 7,400 4,933 56,559 NOTES'1)

See Table 6.3.2-6 for a description of the steps.

(2) Flow rates are based on pump flows as follows:

RHR pump = 3750 gpm per pump CCHG pump = 650 gpm per pump 27 ~

CS pump = 2130 gpm per pump (3) Valve operating times are maximum operating times.

(4) Time for valves 8811A/B and 8812A/B to automatically open.

(5) Time required to complete the required action includes a conservative 30 seconds for operator response time for each manual procedure.

(6) The flow rate in this column represents an average value during the entire time interval for its respective step.

This is conservative since valve repositioning may reduce the flow rate during the time interval.

(7) Flow out of the RWST during switchover includes allowances for both pumped flow to the RCS and containment and backflow to the containment sump.

(8) Following the completion of this step all ECCS and containment spray pumps are aligned with suction flow from the containment sump with the exception of one residual heat removal pump due to the single failure.

(9) Based on Large Break LOCA in conjunction a single failure of one of the RWST to residual heat removal pump isolation valves (8812A or 8812B fails to close on demand.)

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~ PERFORMANCE EVALUATION Accidents which require

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a) Inadvertent opening of a steam generator power operated relief or safety valve (see Section 15.1.4).

b) Small break LOCA (see Section 15.6.5).

c) Large break LOCA (see Section 15.6.5).

d) Major secondary system pipe failure (see Section 15.1.5).

I e) Steam generator tube failure (see Section 15.6.3).

6.3.3.1 Inadvertent 0 enin of a Steam Generator Relief of Safet Valve The most severe core conditions resulting from an accidental depressurization of the Main Steam Supply System are associated with an inadvertent opening of a single steam dump, power operated relief or safety valve.

C Safety injection system actuation from any of the following.')

Low pressurizer pressure signal.

b) Low steam line pressure.

c) Hi-1 containment pressure.

d) Manual actuation.

A safety injection signal will rapidly trip the main turbine, close all feedwater control valves, trip the main feedwater pumps, and close the feedwater isolation discharge valves.-

Following the actuation signal, the suction of the centrifugal charging pumps is diverted from the volume control tank to the refueling water storage tank. Simultaneously, the valves isolating the boron injection tank from the charging pumps and the valves 'isolating the boron injection tank from the injection header automatically open. The charging pumps then force boric acid solution from the boron injection tank, through the header and injection line and into the cold legs of each loop. The passive injection system (accumulators) and the low head system provide no flow at normal reactor coolant system pressure.

The assumed steam release is typical of the capacity of any single steam dump relief or safety valve. The boron solution provides sufficient negative reactivity to maintain the reactor well below criticality. The cooldown for this case is more rapid than the actual case of steam release from all steam 6.3.3-1 Amendment No. 27

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b) The amount of fuel element cladding that reacts chem 'ca&1'ivi th~df em-'gJ or steam does not exceed 1 percent of the total amount of Zircaloy in the reactor.

c) The clad temperature transient is terminated at a time when the core geometry is still amenable to cooling. The cladding oxidation limits of 17 percent are not exceeded during or after quenching.

d) The core temperature is reduced and decay heat is removed for an extended period of time, as required by the long-lived radioactivity remaining in the core.

6.3.3.4 Ma'or Secondar S stem Pi e Failure The steam release arising from a rupture of a main steam pipe would result in energy removal from the RCS causing a reduction of coolant temperature and pressure. In the presence of a negative moderator temperature coefficient, the cooldown results in a reduction of core shutdown margin. There is an increased possibility that the core will become critical and return to power. A return to power following a steam pipe rupture is a potential problem. The core is ultimately shut down by the boric acid injection delivered by the Safety Injection System.

For the cases where offsite power is assumed, the sequence of events in the safety injection system is the following. After the generation of the safety injection signal (appropriate delays for instrumentation, logic, and signal transport included), the appropriate valves begin to operate and the high head 27 ) safety injection (charging) pumps start. In 12 seconds, the valves are assumed to be in their final position and the pumps are assumed to be at full 27 speed. The volume containing the low concentration borated water is swept.

This delay, described above, is inherently included in the modeling.

In cases where offsite power is not available, an additional 10 second delay is assumed to start the diesel generators and to load the necessary safety injection equipment.

The analysis has shown that even assuming a stuck rod cluster control assembly with or without offsite power, and assuming a single failure in the engineered safeguards the core remains in place and intact. Radiation doses will not exceed 10CFR100 guidelines.

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1) One acumulator for each loop which discharges borated water into its respective cold leg of the reactor coolant loop piping. (

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One boron injection tank.

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3) Associated piping, valves and instrumentation.

b) Components which also have a normal operating function axe as follows:

1) Residual heat removal pumps and the residual heat exchangers These components are normally used during the latter stages of normal reactor cooldown and when the reactor is held at cold shutdown for core decay heat removal or for, flooding the refueling cavity. However, during all other plant operating periods, they are 'aligned to perform the low head injection function.

2) Centrifugal charging pumps - These pumps are normally .aligned for charging service. As a part of the Chemical and Volume Control System, the normal operation of these pumps is discussed in Section 9.3.4.

During safety injection conditions, however, they are aligned with the RWST to perform the high head injection function.

3) Refueling water storage tank This tank is used to the refueling canal for refueLing operations and to provide makeup fill to the spent fuel pool. However, during all other plant operating periods it is aligned to the suction of the charging pumps, and the residual heat removal pumps. The charging pumps are automatically aligned to the suction of the refueling water storage tank upon receipt of the safety injection signals or volume control tank low level alarm.

During normal operation they take suction from the volume contxol tank.

c) Positive Displacement Hydrostatic Test Pump - Normally this pump takes suctions from the RWST. It serves two functions, neither of which is safety related. By temporary connections at the discharge of the pump to the Chemical and Volume Control System, this pump is used for hydrotesting the high pressure parts of the Reactor Coolant System. Permanent connections to the accumulators provide for using the hydrostatic test pump in supplying borated water to the accumulators.

-An evaluation of all components required for operation of the ECCS demonstrates that either:

a) The component is not shared with other systems, or 6.3.3-7 Amendment No. 27

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SHVPP FSAR b) If the component is shared with other systems, it is cather ala.gned during normal plant operation to perform its accident function or if not aligned to its accident function, two valves in parallel are provided to align the system for injection. These valves are automatically actuated by the safety injection signal.

Table 6.3.2-7 indicates the alignment of components during normal operation, and the realignment required to perform the accident function.

In all cases of component operation, safety injection has the priority usage such that an "S" signal will override all other signals and start or align systems for injection.

6.3.3.8 Limits on S stem Parameters The analyses show that the design basis performance characteristic of the ECCS is adequate to meet the requirements for core cooling following a LOCA with the minimum engineered safety features equipment operating.

In order to ensure this capability in the event of the simultaneous failure of any single active component to operate, Technical Specifications are establ'ished for reactor operation.

Normal operating, status of

~V ECCS components is given in Table 6.3.2-8.

The ECCS, components are available whenever the coolant energy is high and the reactor is critical. During low temperature physics tests, there is a negligible amount of stored energy in the coolant and low decay heat; therefore, an accident comparable in severity to accidents occurring at operating conditions is not possible and ECCS components are not required.

The principal system parameters and the number of components which may be out of operation in test, quantities and concentrations of coolant available, and allowable time in a degraded status are specified in the Technical Specifications. If efforts to repair the faulty component are not successful the plant is placed into a lower operational status.

6.3.3.9 Time Se uence for the 0 eration of the ECCS Com onents The following action times for ECCS were assumed in Chapter 1S non-LOCA analysis.

2 second delay Logic delay 10 second delay - This delay only used for loss of offsite power cases. This delay simulates the time required to start diesel generators and loading of SI pumps.

I 10 second ramp- SI flow is brought up to full flow over a 10 second ramp.

this simulates bringing SI pumps to full speed and aligning valves.

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SIL'HAPP FSAR 6.3.4 TEST AND INSPECTIONS (~<Qff rIj j~$,

I 6.3.4.1 ECCS Performance Tests 6.3.4.1.1 Preoperational Test Program at Ambient Conditions Preliminary operational testing of the ECCS is conducted during the hot-functional testing of the RCS following flushing and hydrostatic testing, with the system cold and the reactor 'vessel head removed. Provision will be made for excess water to drain into the reactor cavity. The ECCS must be aligned for normal power operation with the boron injection tank filled with 27 refueling water. Simultaneously,.the safety injection block switch is reset and the breakers on the lines supplying offsite power are trapped manually so that operation of the standby diesel generators is tested in conjunction with the safety injection system. This test will provide information including the following facets:

a) Satisfactory safety injection signal generation and transmission.

b) Proper operation of the standby diesel generators, including sequential load pickup.

c) Valve operating times.

d) Pump starting times.

e) Pump delivery rates at

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ECCS design'lows (one point on the operating curve). ~

Recirculation tests of the ECCS are performed under the requirements of Reg.

Guide 1.79 with exceptions/clarifications as noted in Section 14.2.7(g) ~

Testing of the containment recirculation sumps, to demonstrate vortex control and acceptable pressure drops across screening and suction lines and valves, is provided in Section 14.2.12.1.66.

6.3.4.1.2 Components a) ~porn s Separate flow tests of the pumps in the ECCS are conducted during the operational startup testing (with the reactor vessel head off) to check capability for sustained operation. The centrifugal charging, and residual heat removal pumps will discharge into the reactor vessel through the injection lines, the overflow from the reactor vessel passing into the reactor cavity. Each pump will be tested separately with water drawn from the refueling water storage tank. Data will be taken to determine pump head and flow at this time. Pumps will then be run on miniflow circuits and data taken to determine a second point on the head flow characteristic curve.

b) Accumulators Each accumulator is filled with water from the refueling water storage tank and pressurized with the motor operated valve on the discharge line closed. .Then the valve is'pened and the accumulator allowed to discharge into the reactor vessel as part of the operational startup testing with the reactor cold and the vessel head off.

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A B C D E F G Valve Normal Injection Injection Cold Leg Cold Leg Recir- Hot Leg Hot Leg Recir-No, Standby Maximum Hlnimum Recirculation culation Mini- Recirculation culation Mini-Safeguards Safeguards Haximum mum Safeguards Maximum mum Safeguards (Train A Only) Safeguards (Train A Only) Safeguards (Train A Only) 15A 0 0 0 0 0 0 0 15B 0 0 0 0 0 0 0 16A 0 0 0 0 0 0 0 16B 0 0 0 0 0 0 0 17A 0 0 0 C 0 C 0 17B 0 0 0 C 0 C 0 18A 0 0 0 C 0 C 0 18B 0 0 0 C 0 C 0 19A 0 C 0 C 0 C 0 19B 0 C 0 C 0 C 0 19C 0 C 0 C 0 C 0 20 0 C C C C C C 2IA 0 C C C C C C 21B 0 C 0 C 0 C 0 22A C 0 0 0 0 C C 22B C 0 C 0 C C C 23A C 0 0 0 0 C C.

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Pressure Temperature Flow Location Fluid (OS iCli (F) (cCpm) 27 49 Rufueling Water 70 600 j 50A Refueling Water 0 27 50B Refueling Water 1000 70 600 51A Refueling Water 0 52A Refueling Water 0 53A Refueling Water 0 518 Refueling Water 100 70 200 27 52B Refueling Water 100 70 200 53B Refueling Water 100 70 200 54A Refueling Water 0 55A Refueling Water 0 548 Refueling Water 0 55B Refueling Water 0 56 Refueling Water 0 57A Refueling Water 0 578 Refueling Water 0 60 Nitrogen 0 120 0 61 Nitrogen 0 120 0 62 Nitrogen 0 120 0 70 Refueling Water 0 70 0 27 71 Refueling Water 0 70 0 72 Refueling Water 0 70 0 73 Refueling Water 0 70 0 74A Refueling Water 0 70 0 74B Refueling Water 0 70 0 75 Refueling Water 0 70 0 Amendment No. 27

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Pressure Temperature Flow Location Fluid ~(na l (F) ~(pm) 51A Recirculating Water 0 52A Recirculating Water 0 53A Recirculating Water 0 518 Recirculating Water 100 145 200 528 Recirculating Water 100 145 200 538 Recirculating Water 100 145 200 54A Refueling Water 0 55A Refueling Water 0 548 Refueling Water 0 558 Refueling Water 0 56 Refueling Water 0 57A Refueling Water 0 578 Refueling Water 0 60 Nitrogen 0 120 0 61 Nitrogen 0 120 0 62 Nitrogen 0 120 0 70 Recirculating Water 0 145 0 71 Recirculating Water 0 145 0 72 Recirculating Water 0 27 145 0 73 Recirculating Water 0 145 0 74A Recirculating Water 0 145 0 748 Recirculating Water 0 145 0 75 Recirculating Water 0 145 0 Amendment No. 27

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Pressure Temperature Flow Location F lui d ~(used ) (F) (cCpm) 5IA Recirculating Water 0 52A Recirculating Water 0 53A Recirculating Water 0 518 Recirculating Water 0 528 Recirculating Water 0 538 Recirculating Water 0 54A Recirculating Water 100 125 200 55A Recirculating Water 100 125 200 548 Recirculating Water 0 558 Recirculating Water 0 56 Recirculating Water 0 125 200 57A Recirculating Water 1125 125 600 578 Recirculating Water 0 60 Nitrogen 0 120 0 61 Nitrogen 0 120 0 62 Nitrogen 0 120 0 70 Recirculating Water 0 125 0 71 Recirculating Mater 0 125 0 72 Recirculating Water 0 125 0 73 Recirculating Water 0 125 0 27 74A Recirculating Water 0 125 0 748 Recirculating Water 0 125 0 75 Recirculating Water 0 125 0 Amendment No. 27

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COOL i SS SHEARON HARRIS NUCLEAR POWER PLANT Carolina Power ()I Light Company FINALSAFETY ANALYSIS REPORT EMERGENCY CORE COOLING SYSTEM PROCESS F LOW 0(AGRAM SHEET 2 FIGURE 6 3 2 5

SHNPP FSAR h) To provide system materials which are compatible with fluid chemistry and applied codes and standards. System component design data parameters are given in Table 6.5.2-1 ~

The system flow diagram is shown on Figure 6.2.2-1. System component design data parameters are given in Table 6.5.2-1.

A discussion of the spray header design including a description of the number of nozzles per header, nozzle spacing, and nozzle is contained in Section 6.2.2.

System operation is automatically initiated by a HI-3 signal. The signal starts the two spray pumps and the motor operated spray isolation valves.

Within 55 seconds, water will reach the nozzles and start spraying (see Section 6.2.2). The motor operated NaOH isolation valves will be opened automatically by the HI-3 signal.

After the opening of the NaOH Isolation valve, the kinetic energy in the eductor will create a negative pressure to draw the Sodium Hydroxide solution (NaOH) from the containment spray additive tank NaOH solution will be injected into the Containment Spray System (CSS) lines just up stream of,thh'S pump suction at a rate sufficient to provide the required range of pH 8.5-11 for the containment spray. Turbulence in the fluid passing through the pump is sufficient to assure complete and uniform mixing of the fluid. The operator will manually close the NaOH Isolation valves when the NaOH is spent as indicated by low NaOH tank level. Additional NaOH can be added to the tank or through an emergency NaOH addition line outside the Tank Building. If necessary, the operator may reopen these NaOH isolation valves at any later time. The containment spray pumps initially take suction from the refueling water storage tank (RWST). The minimum operating capacity of the RWST (see Section 6.2.2) is more than adequate to supply enough water for the injection mode of operation. When low-low level tank water level is reached in the RWST, pump suction is transferred to containment recirculating sump automatically by opening the recirculation line valves and closing the valves at the outlet of the RWST.

The Containment Spray System can provide one year of operation if required.

The layout of the containment spray system headers and nozzle orientation (see Section 6.2.2) provides a minimum spray coverage of 92.6 percent of the containment free volume and 95 percent of the surface area of the operating floor (Elevation 286 ft.) with only one spray train in operation. This includes the volume beneath the grating in the operating floor. The specified grating has 80 percent free area. The drop size spectrum is discussed in Section 6.2.2.

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above the actual containment pressure.

Parsley (Reference 6.5.2-5), reported that using the assumption of uniform drop size at the surface-average diameter leads to conservative results. He also reported that coalescence of the spray droplets causes the removal time constant to be reduced by 10 to 20 percent. Using an average value, coalescence correction factor is therefore taken as 0.15.

The overall correction factor is calculated as the square root of the sum of the squares of the individual correction factors. This number is 0.292. The correct'ed removal coefficient is then.'1.0-CF).

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= 26.4 .708) = 18.6 hr

= uncorrected removal coefficient CF = overall correction factor The associated half-life of the molecular iodine in the containment atmosphere during spraying is 134 seconds. With the complete system operating (both pumps), the removal constant becomes 37.2 hr 6.5.2.3.3 Injection of Spray Solution The Containment Spray System is designed to deliver a spray to the Containment with a minimum pH of 8.5 and a maximum pH of 11 under all conditions'his pH range is maintained by the controlled addition of sodium hydroxide to the spray solution.

27 The containment spray eductors are sized to deliver sodium hydroxide into each of the two containment spray loops as discussed in Section 6.5.2.2.

Figures 6.5.2-2 and 6.5.2-3 show the pH time history of the water both in the containment spray and in the containment sump for the following cases:

a) Case I- Minimum pH, longest time 27 b) Case II Maximum pH, shortest time 6.5.2-6 Amendment No. 27

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SHNPP FSAR Wn' 27 The time history curves assume total mixing in the sump for the minimum and maximum RWST volumes.

The figures indicate that the containment spray in all cases has a pH within the range of 8.5 11.0 (see Figures 6.5.2-2 and 6.5.2-3). It was assumed for Case II that NaOH is added until the tank=is empty, h'owever, this is optional and the operator may stop NaOH addition when the minimum volume has been added. 27 A pH of 10.8 represents the upper limit for the containment spray in Case II during recirculation mode, when NaOH addition is completed. Uninterrupted inadvertent containment spray would have to continue for at Least 110 minutes for a pH value of 10.5 to be reached. Administrative action for terminating the inadvertent containment spray will be taken within this time.

Fission products and sump pH may be monitored, via the sumps. connected to the Safety Injection System, from samples taken at the discharge of the RHR heat exchangers (see Sections 5.4.7, 6.3, and 9.3.2).

The pH of the water in the sump during recirculation and after the contents of the spray additive tank have been introduced into the Containment can be determined by using known volumes and chemical compositions of the Reactor Coolant System, refueling water storage tank, accumulators, and spray additive tank. If necessary, additional sodium hydroxide may be added to the Containment and recirculated sump fluid.

If additional sodium hydroxide must be added to the recirculated water in excess of the amount injected from the spray additive tank, this can be accomplished by utilizing the emergency sodium hydroxide addition connections (see Figure 6.2.2-1).

The emergency addition connections are fitted with a hose connector. If it is determined (by sampling and pH measurement, in conjunction with trend monitoring of the recirculation fluid) that additional sodium hydroxide will be required, a tank truck of sodium hydroxide will be obtained from a local supplier. A hose will be run from the truck unloading area to an emergency addition connection. After the hose connection is made, the sodium hydroxide will be added to the system utilizing the tank truck pump.

A 30 weight percent NaOH solution has a freezing point of approximately 32 F>

and a boiling point of 240 F at atmospheric pressure. The NaOH is stored in the containment spray additive tank in the RAB, thus, no special provisions for temperature control are installed on the tank. An N2 'blanket is I

6.5.2-7 Amendment No. 27 1

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SHNPP FSAR TABLE 6.5.2-1 IODINE REMOVAL SYSTEM COMPONENTS A Containment S ra Additive Tank Volume, gallons 7098 Minimum Liquid Volume in tank, gallons 2736 Design Temperature, F 200 Design Pressure, psig 15 Operating Temperature, F 100 Operating Pressure, psig 2 Fluid 2 8-30X by weight sodium hydroxide Solution with nitrogen (N2) cover gas Material 304 Ss Code ASME III, Code Class 3 B Motor 0 crated Valves Quantity 2 Size, Inches 2 Type Globe Design Pressure, psig 50 Design Temperature, F 200 End Connection SW Pipe Schedule 40S Material 304 Ss Fluid 28-30X by weight sodium hydroxide Solution Operator Motor Code ASME III, Code Class 3 C Eductor Quantity 2 Design Pressure, psig 300 Design Temperature, F 300 Material 304 ss Code ASME III, Code Class 2 D All other Valves Material 304 ss Code ASME III Code Class 2 and 3 Amendment No. 27 6.5 '-10

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NOTE 2 RCP MOTOR OI L PUMP MOTOR Ol SCONNECTEO, NOTE 3 TURBINE GENERATOR BEARING OIL PUMP DISCONNECTED NOTE 4 RHR PUMP CONNECTED FOR LONG-TERM COOL INGo AMENDMENT NO. 27 SHEARON HARRIS FIGURE NUCLEAR POWER PLANT Carolina DIESEL GENERATOR LOADING PROF I LE IA-SA B.3 '-12 Power 5 Light Company FINAL SAFETY ANALYSIS REPORT

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NOTE 2: RCP MOTOR OIL PUMP MOTOR DISCONNECTED NOTE 3: TURBINE GENERATOR BEARING OIL PUMP DISCONNECTED, NOTE 4: RHR PUMP CONNECTED FORI LONG-TERM COOLING SHEARON HARRIS FIGURE NUCLEAR POWER PLANT Carolina DIESEL GENERATOR LOADING PROFILE 1B-SB 8.3.1-13 Power 5 Light Company FINAL SAFETY ANALYSIS REPORT

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TABLE 7 ~ -5 (Continued)

ESF ACTUATION SYSTEMS-SAFETY INJECTION SIGNAL(S)

EQJ IPMENT ACTUATION REFERENCE SCHE MATI C/LOG I C" IDENT IF I CATION SERVICE CHANNEL ACTION F IGURE NUMBER NUMBER

/ n 2CS-L523SA-1 2CS-L522SB-I 2CS-L520SA-I RWST RWST to Charging to Charging Volume Control Tank Pumps Pumps Outlet Isolation Open Open Close

',3,4-3 9,3,4-3 9.3,4-3 NSSS NSSS NSSS I-LCV-1158 I-LCV-115D I<<LCV-115C 2CS-L521SB-1 Volume Control Tank Outlet Isolation Close 9,3.4-3 NSSS - I-LCV-115E 3CC-L ISA-I CCW to Failed Fuel Detector Isolation Close 9.2.2-4 NSSS - I-LCV670 3CC-L2SB-I CCW to Failed Fuel Detector Isolation Close 9,2,2-4 NSSS I-LCV676 3CC-D547SA-I Sample Coolers CCW Isolation Close 9.2 2-4 3CC&54SB-I Sample Coolers CCW Isolation Close 9,2,2-4 AH-I (IA-SB) Safety Related Containment Fan Cooler Start Note I, 4 6.2.2-3 CAR-2166-8-430-SH31 64 AH-I (18-SB) Safety Related Containment Fan Cooler Start Note I, 4 6,2,2-3 CAR-2166-8-430-SH31,64 27 AH-2 (IA-SA) Safety Related Containment Fan Cooler Start Note I, 4 6,2,2-3 CAR-2166-8-430-SH31,64 AH-2 (18-SA) Safety Related Containment Fan Cooler Start Note I, 4 6,2,2-3 CAR-2166-8-430-SH31,64 AH-3 (IA-SA) Safety Related Containment Fan Cooler Start Note I, 4 6.2.2-3 CAR-2166"8-430-SH31,64 AH-3 (18-SA) Safety Related Containment Fan Cooler Start Note I, 4 6,2,2-3 CAR-2166-8-430-SH31,64 AH"4 (IA-SB) Safety Related Containment Fan Cooler Start Note I, 4 6,2,2-3 CAR-2166-8-430-SH31,64 AH-4 (18-SB) Safety Related Containment Fan Cooler Start Note I, 4 6.2.2-3 CAR-2166-8-430-SH31 64 28D-P6SB-1 Steam Generator IA Slowdown Isolation Valve Close 10,1,0-6 CAR-2166-8-430-SH23,8 28D-V2SB-I Steam Generator IA Blowdown Isolation Valve Close 10,1.0-6 CAR-2166-8-430-SH23,8 280-VIISA-I Steam Generator IA Blowdown Isolation Valve Close 10,1,0-6 CAR-2166-8-430-SH23,8 28D-P7SB-1 Steam Generator 18 Blowdown Isolation Valve Close 10,1,0-6 CAR-2166-8-430-SH23 9 28D-V5SB-1 Steam Generator 18 Blowdown Isolation Valve Close 10,1,0-6 CAR-2166-8-430-SH23 9 28D-V15SA-1 Steam Generator 18 Blowdown Isolation Valve A Close 10 '.0-6 CAR-2166-8-430-SH23 9 28D-PBSB-I Steam Generator IC Blowdown Isolation Valve 8 Close 10,1,0-6 CAR-2166-8-430-SH23 F 10 27 280-VBSB-I Steam Generator IC Blowdown Isolation Valve 8 Close 10 ~ 1,0-6 CAR-2166-8-430-SH23 F 10 2BD-V19SA-1 Steam Generator IC Blowdown Isolation Valve Close 10,1,0-6 CAR-2166-8-430-SH23 F 10 id j

2SI-V570SB-I Cnmt Sump to RHRP-8 Isol Valve Open Note 5 NSSS - 1-88118 2SI-V571SA-I Cnmt Sump to RHRP-8 Isol Valve Open Note 5 NSSS - 1-88 I 1A 2SI-V572SB-I Cnmt Sump to RHRP-8 Isol Valve Open Note 5 NSSS - 1-88128 2SI-V573SA-I Cnmt Sump to RHRP-8 Isol Valve Open Note 5 NSSS I-8812A

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5) Initiate each of the following signals and assure hero operation occurs'.

(a) Containment Phase "A" Isolation.

(b) Containment Spray Actuation.

(c) RWST Lo-Lo Level (Containment spray switchover to recirculation mode of Operation).

d) Acceptance Criteria

1) Containment spray pumps operate in accordance with the specific pump performance curves contained in the Containment Spray Pump Technical Manual, Ingersoll-Rand.

2) The Containment Spray chemical addition tank will operate, at Containment Spray Pump design flow, in accordance with Section 6.5.2, SHNPP FSAR.

3) Spray nozzles are free of obstructions.

4) Pumps and valves operate on specific signals and spray commences with a time delay consistent with the Technical Specifications after 27 Conta'inment Spray Actuation.

14.2.12.1.31 Chemical and Volume Control Cold Test Summary a) Test Objectives

1) To verify the automatic makeup mode function in accordance with design.

2) To verify volume control'tank level and pressure alarms and controls operate properly.

3) To demonstrate the operation of the charging/safety injection pumps on minimum flow.

b) Prerequisites

1) Reactor Makeup Water is available to support operation of the automatic makeup.

2) Service water is available to the charging/safety injection pump coolers.

3) The applicable general prerequisites are met.

c) Test Method

1) Operate or simulate operation of the system to verify that all controls, interlocks, and alarms function as designed.

2) Operate the Charging/Safety Injection Pumps on minimum flow and record baseline data.

14.2.12-33 Amendment No. 27

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SHNPP FSAR 15.1.4

~ ~ INADVERTENT OPENING OF A STEAM GENERATOR RELI SESTET VALVE 15.1.4.1 Identification of Causes and Accident Descri tion The most severe core conditions resulting from an accidental depressurization of the Main Steam System are associated with an inadvertent opening of a single steam dump, power operated relief or safety valve. The analyses performed, assuming a rupture of a main steam line, are given in Section 15.1.5.

The steam release as a consequence of this accident results in an initial increase in steam flow which decreases during the accident as the steam pressure falls. The energy removal from the RCS causes a reduction of reactor coolant temperature and pressure. In the presence of a negative moderator temperature coefficient,'he cooldown results in an insertion of positive reactivity.

The analysis is performed to demonstrate that the following criterion is satisfied:

Assuming a stuck rod cluster control assembly, with offsite power available, and assuming a single failure in the Engineered Safety Features System there will be no consequential fuel damage after reactor trip for a steam release equivalent to the spurious opening, with failure to close, of the largest of any single steam dump, power operated, relief, or safety valve.- Accidental depressurxzation of the secondary system xs classxfxed as an ANS Condition II event. See Section 15.0.1 for a discussion of Conditi on II events.

The following systems provide the necessary protection against an accidental depressurization of the Main Steam Supply System.

a) Safety Injection System actuation from any of the following'.

1) Two out of three pressurizer pressure signals.

2) Two out of three High-1 containment pressure signals.

3) Two out of three low steamline pressure signals in any one main steam line.

b) The overpower reactor trips (neutron flux and AT), low pressurizer pressure reactor trip, and the reactor trip occurring in conjunction with receipt of the safety injection signal.

c) Redundant isolation of the main feedwater lines.

Sustained high feedwater flow would cause additional cooldown. Therefore, in addition to the normal control action which will close the main feedwater valves following reactor trip, a safety injection signal will rapidly close all feedwater control valves and back up feedwater This criteria .is verified by verifying the DNB design criteria is met. 27 15.1.4-1 Amendment No. 27

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SIDIPP FSAR isolation valves, trip the main feedwater pumps, and clos (e pump discharge valves.

d) Trip of the fast-acting main steam line isolation valves (designed to close in less than 5 seconds) on:

1) High-2 containment pressure.

2) Safety injection system actuation derived from two out of three low steam line pressure signal in any one main steam line (above Permissive P-11) ~

3) High negative steam pressure rate indication from two out of three signals in any one main steam line (below Permissive P-11) ~

Plant systems and equipment which are available to mitigate the effects of the accident are also discussed in Section 15.0.8 and listed in Table 15.0.8-1.

15.1.4.2 Anal sis of Effects and Conse uences Method of Anal sis The following analyses of a secondary system steam release are performed for this section.

a) A full plant digital computer simulation using the LOFTRAN Code (Reference 15.1.2-1) to determine RCS temperature and pressure during co oldown, and the effect of safety injection.

I The Analyses to determine that there following conditions are is no consequential to exist at the time of fuel damage.

assumed a secondary steam system release:

a) End-of-life shutdown margin at no-load, equilibrium xenon conditions, and with the most reactive rod cluster control assembly stuck in its fully withdrawn position. Operation of rod cluster control assembly banks during core burnup in accordance with Technical Specifications will ensure that the addition of positive reactivity in a secondary system steam release accident will not lead to a more adverse condition than the case analyzed.

b) A negative moderator coefficient corresponding to the end-of-life rodded core with the most reactive rod cluster control assembly in the fully withdrawn position. The variation of the coefficient with temperature and pressure is included. The keff versus temperature at 1000 psi corresponding to the negative moderator temperature coefficient used is shown in Figure 15.1.4-1.

c) Minimum capability for injection of high concentration boric acid solution corresponding to the most restrictive single failure in the Safety Injection System. This corresponds to the flow delivered by one charging pump delivering its full contents to the cold leg header. Low concentration boric acid must be swept from the safety injection 15.1.4-2 Amendment No. 27

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-.. 4' 4 4 4ss SIL'HAPP FSAR 4 lines downsteam of the Refueling Water Storage Tank prx.or to the defxvery of 27 high concentration boric acid (2,000 parts per million (ppm)) to the reactor coolant loops. This effect has been accounted for in the analysis.

d) The case studied is a steam flow of 268 pounds per second at 1200 pounds per square inch absolute (psia) with offsite power available.

This is the maximum capacity of any single steam dump, power operated relief, or safety valve. Initial hot shutdown conditions at time zero are assumed since this represents the most conservative initial condition.

Should the reactor be just critical or operating at power at the time of a steam release, the reactor will be tripped by the normal overpower protection when power level reaches a trip point. Following a trip at power, the RCS contains more stored energy than at no-load, the average coolant temperature is, higher than at no-load and there is appreciable energy stored in the fuel.

Thus, the additional stored energy is removed via the cooldown caused by the steam release before the no-load conditions of RCS temperature and shutdown margin assumed in the analyses are reached. After the additional stored energy has been removed, the cooldown and reactivity insertions proceed in the same manner as in the analysis which assumes no-load conditon at time zero.

Since the initial steam generator water inventory is greatest at no-load, the magnitude and duration of the RCS cooldown are less for steam line release occurring at power.

In computin'g the steam flow, the Moody Curve (Reference 15.1.4-1) 4 e) for fh/0 = 0 is used and thereby conservatively eliminates frictional losses. (fy f) Perfect moisture separation in the steam generator is assumed.

g) Relief valve acceptance criteria pressurizer of 15.636 ft /sec (455,000 lbs/hr at 2575 psia). This is in excess of the rated flow rate for one pressurizer safety valve (Crosby 6M6, 420,000 lbs/hr at setpoint plus 3 percent accumulation).

Per ASME Code requirements (certified) capacity (Section III, Article NB-7000), the rated must be less than the maximum capacity for the valve. The flow valve assumed in the safety analysis is consistent with the maximum demonstrated flow rate for the Crosby safety valve (see data from EPRI test report in EPRI/CE Safety Valve Test Report, July 1982) and is well in excess of that demonstrated for the power-operated relief valve, (Copes-Vulcan D-100-160) (see data in EPRI test report NP-2670-LD, Volume 8 entitled "EPRI/Wyle Power-Operated Relief Phase III Test Report," October 1982).

Relief or Safety Valve" accident is an ANS Condition II steamline break event The Condition II criterion that must be met for this event is that the DNB criteria, as discussed in FSAR Section 4.4, is not violated. That is, the minimum calculated DNBR must be greater than or equal to the 95 x 95 DNBR limit (> 1.30). This analysis was based on a steam flow of 268 pounds per second at 1200 psia.

15.1.4-3 Amendment No. 27

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k$ z The most limiting steamline break event is the double, a main steamline, FSAR Section 15.1.5, which is an NS Condition IV event. Even though this is a Condition IV event, the analysis performed shows that the Condition II acceptance criteria, given above, is met (DNBR > 1.30).

Since the double-ended steamline rupture is more than an order of magnitude larger than any secondary side relief valve and since the Condition IV event meets the Condition II criteria, flow in excess of the assumed maximum secondary relief valve flowrate will not result in violating the Condition II DNB criteria for the "Inadvertent Opening of a Steam Generator Relief or Safety Valve" event.

Thus, should the actual secondary relief valve capacity be in excess of that assumed in the accident analysis, no safety concern would exist.

Results The calculated time sequence of events for this accident is listed in Table 15.1.4-1.

The results presented are a conservative indication of the events which wo4.d occur assuming a secondary system steam release since it is postulated that all of the conditions described above occur simultaneously.

Figures 15.1.4-2 and 15.1.4-3 show the transient results for a steam flow of 268 lb./sec. at 1200 psia.

The assumed steam release is typical of. the capacity of any single steam dump, power operated relief, or safety valve. Safety injection is initiated automatically by low pressurizer pressure. Operation of one centrifugal 27 charging pump is assumed. Boron enters the RCS providing sufficient negative reactivity to prevent core damage. The transient is quite conservative with respect to cooldown, since no credit is taken for the energy stored in the system metal other than that of the fuel elements and steam generator tubes.

Since the transient occurs over a period of about 5 minutes, the neglected stored energy is likely to have a significant effect in slowing the cooldown.

Figure 15.1.4-4 shows the upper head void volume as a function of time for incidents in which the pressuriz'er is emptied during the inadvertant opening of a steam generator relief or safety valve. Since the reactor coolant in the coolant loops remains subcooled, this voiding has no effect on the safety of the plant and causes no problem in recovery.

15.1.4.3 Conclusions The analysis shows that the criteria stated earlier in this section are satisfied. A DNBR less than 1.30 does not exist.

15.1.4-4 Amendment No. 27

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er erYg SIINPP FSAR TABLE 15.1.4-1 TIME SE UENCE OF EVENTS FOR INADVERTENT OPENING OF A STEAM GENERATOR RELIEF OF SAFETY VALVE INCIDENTS Time Event (seconds)

Inadvertent opening of 0.0 one main steam safety or relief valve Pressurizer empties 166 27 Boron reaches 225 core 15.1.4-5 Amendment No. 27

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$ C~S 3 i'j"vwH b) The thermal and hydraulic behavior of the core folLowing m'~ste'am'"Line A detailed thermal and hydraulic digital-computer code, THING, (see ~"'reak.

Chapter 4) has been used to determine if DNB occurs for the core conditions computed in Item (a) above.

The following conditions were assumed to exist at the time of a main steam line break accident:

a) End-of-life shut down margin at no-load, equilibrium xenon conditions, and the most 'reactive RCCA stuck in its fully withdrawn position. Operation of the control rod banks during core burnup is restricted in such a way that addition of positive reactivity in a steam line break accident will not lead to a more adverse condition than the case analyzed.

b) A negative moderator. coefficient corresponding to the end-of-life rodded core with the most reactive RCCA in the fully withdrawn position. The variation of the coefficient with temperature and pressure has been included.

The Keff versus temperature at 1000 psi corresponding to the negative moderator temperature coefficient used is shown in Figure 15.1.4-1. The effect of power generation in the core on overall reactivity is shown in Figure 15.1.5-1.

The core properties associated with the sector nearest the affected steam generator and those associated with the remaining sector were conservatively combined to obtain average core properties for reactivity feedback calculations. Further, it was conservatively assumed that the core power distribution was uniform. These two conditions cause underprediction of the reactivity feedback in the high power region near the stuck rod. To verify the conservatism of this method, the reactivity as well as the power distribution was checked for the limiting statepoints for the cases analyzed.

This core analysis considered the Doppler reactivity from the high fuel temperature near the stuck RCCA, moderator feedback from the high ~ater enthalpy near the stuck RCCA, power redistribution and nonuniform core inlet temperature effects. For cases in which steam generation occurs in the high flux regions of the core, the effect of void formation was also included. It was determined that the reativity employed in the kinetics analysis was always larger than-the reactivity calculated including the above local effects for the statepoints. These results verify conservatism', i.e., underprediction of negative reactivity feedback from power generation.

c) Minimum capability for injection of high concentration boric acid (2,000 ppm) solution corresponding to the most restrictive single failure in the Safety Injection System. The Emergency Core Cooling System consists of three systems: 1) the passive accumulators, 2) the Residual Heat Removal System, and 3) the Safety Injection System. Only the Safety Injection System is modeled for the steam line break accident analysis.

The actual modeling of the Safety Injection System in LOFTRAN is described in Reference 15.1.2-1 ~ The flow corresponds to that delivered by one charging pump delivering its full flow to the cold leg header. No credit has been taken for the low concentration borated water, which must be swept from the lines downstream of the refueling water storage tank prior to the delivery of high concentration boric acid to the reactor coolant loops. For the cases 15.1.5-3 Amendment No. 27

~

SliNPP, FSAR where offsite power is assumed, the sequence of events in th 't System is the following. After the generation of the safety injection signal (appropriate delays for instrumentation, logic, and signal transport included), the appropriate valves begin to -operate and the high head safety injection pump starts. In 12 seconds, the valves are assumed to be in their final position and the pump is assumed to be at full speed. The volume containing the low concentration borated water is swept before the 2,000 ppm reaches the core. This delay, described above, is inherently included in the modeling.

In cases where offsite power is not available, an additional 10-second delay is assumed to start the diesel generators and to load the necessary safety injection equipment onto them.

d) Design value of the steam generator heat transfer coefficient including allowance for fouling factor.

e) Since the steam generators are provided with integral flow restrictors with a 1.4 sq. ft. throat area, any rupture with a break area greater than 1.4 sq. ft., regardless of location, would have the same effect on the NSSS as the 1.4 sq. ft. break. The following cases have been considered in determining the core power and RCS transients:

e

1) Complete severance o'f a pipe, with the plant initially at no-load conditions, full reactor coolant flow with offsite power available.

2) Case (1) with loss of offsite power simultaneous with the steam line break and initiation of the safety injection signal. Loss of offsite power results in reactor coolant pump coastdown.

f) Power peaking factors corresponding to one stuck RCCA and nonuniform core inlet coolant temperatures are determined at end of core life. The coldest core inlet temperatures are assumed to occur in the sector with. the stuck rod. The power peaking factors account for the effect of the local void in the region, of the stuck control assembly during the return to power phase following the steam line break. This void in conjunction with the large negative moderator coefficient partially offsets the effect of the stuck assembly. The power peaking factors depend upon the core power, temperature, pressure, and flow, and thus, are different for each case studied.

The core parameters used for each of the two cases correspond to values determined from the respective transient analysis.

Both cases above assume initial hot standby conditions at time zero since this represents the most pessimistic initial condition.- Should the reactor be just critical or operating at power at the time of a steam line break, the reactor will be tripped by the normal over-power protection system when power level reaches a trip point. Following a trip at power, the RCS contains more stored energy than at no-load, the average reactor coolant temperature is higher than at no-load and there is appreciable energy stored in the fuel. Thus, the additional stored energy is removed via the cooldown caused by the steam line break before the no-load conditions of RCS temperature and shutdown margin assumed in the analysis are reached. After the additional stored energy has

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SUNPP FSAR been removed, the cooldown and reactivity insertions proceed in the same manner as the analysis which assumed no-load condition at time zero.

g) In computing the steam flow during a steam line break, the Hoody Curve (Reference 15.1.4-1) for fL/D 0 is used and thereby conservatively eliminates frictional losses.

h) A maximum value of 1520 gpm of auxiliary feedwater flow is assumed for the steamline rupture analysis, with 100 percent of this flow going to the broken loop. The enthalpy of the auxiliary feedwater is 50 BTU/1bm and the flow is assumed to start at the beginning of the transient. These three assumptions, maximum flow, minimum enthalpy, and no delay in delivery of flow are conservative because they maximize the cooldown of the primary coolant.

Further information can be found in Reference 15.1.5-1.

The only operator action assumed is terminating auxiliary feedwater flow after 10 minutes. Some of the alarms and indications the operator would see from protection systems include; hi negative steamline pressure rate, SG hi-hi 27 level, steamline lo pressure, pressurizer low pressure, and hi containment pressure.

Results The calculated sequence of events for both cases analyzed is shown on Table 15.1.5-2.

The results presented are a conservative indication of the events which would occur assuming a steam line rupture since it is postulated that all of the conditions described above occur simultaneously.

Core Power and Reactor Coolant System Transient Figures 15.1.5-2 through 15.1.5-4 show the RCS transient and core heat flux following a main steam line rupture (complete severance of a pipe) at initial no-load condition.

Offsite power is assumed available so that full reactor coolant flow exists.

The transient shown assumes an uncontrolled steam release from only one steam generator. Should the core be critical at near zero power when the rupture occurs the initiation of safety injection by low steam line pressure will trip the reactor. Steam release from more than one steam generator will be prevented by automatic trip of the fast acting isolation valves in the steam lines by high containment pressure signals, by low steam line pressure signals or by high negative steam pressurization rate signals. Even with the failure of one valve, release is limited by isolation valve closure for the other steam generators, while the one generator blows down. The steam line stop valves are designed to be fully closed in less than five seconds from receipt of a closure signal.

As shown in Figure 15.1.5-3, the core attains criticality with the RCCAs )27 inserted (with the design shutdown assuming one stuck RCCA) before boron solution at 2,000 ppm enters the RCS. A peak core power significantly lower than the nominal, full power value is attained.

15.1.5-5 Amendment No. 27

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SIINPP FSAR TABLE 15.1.5-2 TIME SE UENCE OF EVENTS FOR STEAM SYSTEM PIPING FAILURE INCIDENTS Time Event (Seconds)

Case 1 Offsite Power Available Steam line rupture 0 Pressurizer empties 15 Criticality attained 25 27 Boron reaches core 42 Case 2 Offsite Power Not Available Steam line ruptures 0 Pressurizer empties 27 Criticality attained 30 Boron reaches core 48 15.1.5-9 Amendment No. 27

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SHEARON HARRIS FIGURE NUCLEAR POWER PLANT 1.4 FT STEAMLINE RUPTURE. OFFSITE POWER Carolina AVAILABLE 15.1.5-3 Power 5. Light Company FINAL SAFETY ANALYSIS REPORT

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SHEARON HARRIS FIGURE NUCLEAR POWER PLANT 1.4 FT STEAMLINE RUPTURE,OFFSITE POWER CaroIina AVAILABLE .q5 q 5g Power 8 Light Company FINAL SAFETY ANALYSIS REPORT

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SHEARON HARRIS FIGURE NUCLEAR POWER PLANT 1.4 FT STEAMLINE RUPTURE, OFFSITE POWER 15.1,5-5 Carolina Power fk Light Company NOT AVAILA8 LE FINAL SAFETY ANALYSIS REPORT

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SHEARON HARRIS FIGURE NUCLEAR POWER PLANT Carolina 1.4 FT STEAMLINE RUPTURE, OFFSITE POWER 16.].5-6 Power & Light Company NOT AVAILABLE FINAL SAFETY ANALYSIS REPORT

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SHEARON HARRIS FIGURE NUCLEAR POWER PLANT 1.4 FT STEAMLINE RUPTURE, OFFSITE POWER Carolina 15.1.5-7 NOT AVAI LABLE Power 5 Light Company FINAL SAFETY ANALYSIS REPORT

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ML18019B042

Contents

Text

1.0 INTRODUCTION

SUMMARY

5.0 REFERENCES

SUMMARY

SUMMARY

1.0 INTRODUCTION

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

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ML18019B042

Text

1.0 INTRODUCTION

SUMMARY

5.0 REFERENCES

SUMMARY

SUMMARY

1.0 INTRODUCTION

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

SUMMARY

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