ML20215E506
| ML20215E506 | |
| Person / Time | |
|---|---|
| Site: | Haddam Neck File:Connecticut Yankee Atomic Power Co icon.png |
| Issue date: | 09/18/1986 |
| From: | Delawrence J, Dimarzo J, Graves R, Michael Turner CONNECTICUT YANKEE ATOMIC POWER CO. |
| To: | Murley T NRC OFFICE OF INSPECTION & ENFORCEMENT (IE REGION I) |
| References | |
| NUDOCS 8610150342 | |
| Download: ML20215E506 (110) | |
Text
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e . Connecticut Yankee Atomic Power Company i Reactor Containment Building Integrated Leak Rate Test and Air Filtration System Test January 1986 to. July 1986 Rev. O Prepared by: _ u '/ 1 [6 J. T imarzo Date NUSCO Special Test Engineer Reviewed by: , b. / h '7//9/ff6
/
M. E. Turner Date CY ISI Engineer Reviewed by: a . M mg D b^
. L. DeLawrence Date C'1 ISI Engineering Supervisor 4
Approved by: J H. Ferguson Date CY Unit Superintendent C610150342 860918 PDR ADOCK 00000213 I P PDR A f
\
B r TABLE OF CONTENTS Section Title LIST OF ATTACHMENTS REFERENCES 1 PURPOSE 2
SUMMARY
2.1 Type A Test 2.1.1 Conclusion 2.7 Local Leakage Rate Tests (Types B and C) 3 TYPE A TEST 3.1 Edited Log of Events 3.2 General Test Description 3.2.1 Prerequisites 3.2.2 Equipment and Instrumentation 3.2.3 Data Acquisition System 3.2.4 Data Resolution System
& .O 3.3 Test Results 3.3.1 Presentation of Test Results 3.3.2 ILRT Results 3.3.2.1 Mass Point Analysis 3.3.2.2 Verification Test Results 3.3.2.3 Calculation of Superimposed Leakage Rate, Lo 3.3.2.4 LLRT Adjustment Penalties to ILRT L ,Results 3.3.2.5 Comparison of ILRT L ,Results to Test Acceptance Criteria 3.3.2.6-9 Comparison of ILRT L ,Results (Adjusted for "As-Left/As-Found" ILRT Penalties) to Test Acceptance Criteria 3.3.2.10 Test Result Summary and Discussion 3.3.2.11 Final Conclusion h
s .
'4 LOCAL LEAKAGE RATE TESTS (Types B and C) 4.0 Local Leakage Rate Test Data 4.1 Local Leakage Rate Test Corrective Action and July 1986 LLRT Results 5 ' Air Filtration System Test Results 6 Recirculation System Test Results 1
I
LIST OF ATTACHMENTS Attachment Title 3.2A Instrumentation 3.2B ILRT Temperature and Dew Cell Detector Locations - Profile View 3.3A ILRT Sensor Data 3.3B ILRT Average Sensor Data 3.3C ILRT Absolute Method - Mass Point Analysis Test Results 3.3D Verification Mass Point Method Data 3.3E Verification Mass Point Test Results 3.3F Graph 1 - Leakage Rate and UCL vs. Time, Mass Point Analysis 3.3G Graph 2 - Average Containment Air Temperature vs. Time 3.3H Graph 3 - Containment Air Pressure vs. Time 3.3I Graph 4 - Containment Vapor Pressure vs. Time 3.3J Graph 5 - Containment Air Mass vs. Time i.
- ,- o-REFERENCES
- 1. 10CFR50, Appendix J, Primary Reactor Containment Leakage Testing for Water-Cooled Power Reactors.
- 2. SUR 5.7-108, Rev. 2, Containment Integrated Leak Rate Test.
- 3. ANSI N45.4, American National Standard Leakage Rate Testing of Containment Structures for Nuclear Reactors, March 16, 1972.
- 4. ANSI /ANS-56.8, Containment System Leakage Testing Requirements, February 19,1981.
- 5. NEO 2.20,WRev. O.
'6. Reliability Engineering Branch Calculation No. 1301795, 007, RE, Rev. 0 (Sensor Volume Weight Calculation) .
l
- 7. Reliability Engineering Branch Calculation No. 1302120, 012, RE,
. Rev. 0 (24-Hour Lt , Calculation).~
l [ 8. CY Technical Specifications, Section 4.4. 4 9.- SUR 5.7-15,_Rev. 3, Individual Containment Penetration Test Calcu- ! lation and Documentation. l l
- 10. CY Calculation No. CY-XX-XXXX-001, Rev. O, Containment LLRT-1986 Refueling.
l ~ - ..- - _ .. .. - - _ . - -- . . . . - -.
SECTION 1 PURPOSE The purpose of this report is to present a description and analysis of the April 1986 Type A Reactor Containment Building Integrated Leakage Rate Test (ILRT), summary of the Types B and C Local Leakage Rate Tests (LLRTs), Air Filtration System Test Results, and Recirculation (RHR) System Tests conducted by the Connecticut Yankee Atomic Power Company and Northeast Utilities Service Company. A summary of CYAPCO's Corrective Action Plan for Types B and C penetrations is included. This report is submitted, as required, by 10CFR50, Appendix J Para-graph V.B. (Reference 1) and CY Technical Specifications.
SECTION 2
SUMMARY
2.1 Type A Test Pressurization for the ILRT was started approximately 2259 hours on April 2, 1986. The compressors were secured at approximately 0625 hours on April 3, 1986, with a peak pressure of 30.8 psia. At 1100 hours on April 3,1986, gross leakage (> 0.4 percent per day) was detected by the ILRT instrumentation. Investigation of penetration areas was conducted. By 1630 hours on April 3, 1986, penetrations P-3 (HPSI), P-81 (Auxiliary Feedwater), and P-65 (Air Monitoring System) were isolated and closed. A four-hour stabilization period following isolation of the valves commenced. During this time, leakage was monitored and trended. Computer analysis indicated no change in the leakage rate occurred. By 2013 hours on April 3, 1986,.the leakage was traced to an open service water vent valve in containment (going to containment fan cooler no. #2). Valve SW-V-266 was closed and then blank flanged. The measured leakage decreased significantly over the next few hours.
Wwf' At 2200 hours on April 3, 1986, ILRT instrumentation indicated that the containment air temperature was increasing significantly (> 0.85'F/HR) . This trend continued on into the early hours of April 4, 1986. Analysis indicated that the rise in temperature could potentially
" thermally mask" the actual integre.ted leakage rate. A methodical review of all systems and thermodynamic parameters, that could account for this effect, was conducted.
At 1445 hours on April 4, 1986, service water valve SW-V-264 (going to fan cooler no. #1) was cracked open. This action proved effective. By 1610 hours, the temperature rise was less than 0.2*F/ hour. Since the service water system operates under DBA LOCA conditions, it was determined that reintroduction of cooling flow to a fan cooler was acceptable (Reference 1). At this point, the test was restarted and a four-hour temperature stabilization period commenced. At 2036 hours on April 4, 1986, the 24-hour L measurement start-tm ed. On-line computer analysis trending indicated acceptable results and no further containment problems were encountered. The test equipment performed without problems during the Type A test. During the 24-hour L , measurement, no reweighting of ILRT instru-ments was required. I
_4_ At 2039 hours on April 5, 1986, the L , portion of the test was successfully completed. The LSF and 95 percent. upper confidence limit test results indicated that the containment leakage was essentially zero. A superimposed leakage verification test was successfully completed from 1009 hours to 1409 hours on April 6, 1986, and containment depressurization followed. 2.1.1 Conclusion The April 1986 CY ILRT Type A test is considered a successful test in that it demonstrated essentially zero leakage across the containment boundary. The measured leakage rates are well within the plant's maximum allowable leakage rate. 2.2 Local Leakage Rate Tests (Types B and C) The results of Local Leak Rate Tests (LLRTs) of containment isola-tion valves and other containment penetrations are documented per Reference 10. In accordance with 10CFR50, Appendix J, Paragraph V.B., data for the LLRTs are summarized.in Section 4 of this report.
-3_
SECTION 3 TYPE A TEST 3.1 Edited Log of Events This log was edited from the information contained in the Official Log of Events (per Reference 2). i April 2, 1986 1 0700 - Data acquisition system placed in operation. Functional i ) verification of test instrumentation field inputs com-menced. i 1744 - Test precautions completed and signed off. 1830 - Test prerequisites completed and signed off. 1830 - Containment Readiness Inspection commenced. 1 4 0400 - Containment inspection completed; no abnormalities observed. 4 2259 - Pressurization of containment commenced.
2355 - Containment smoke detector alarms. Operations prepares to make containment entry. April 3, 1986 0005 - Operations enters containment. Visual inspection indi-cates alarm false (no smoke or fire inside containment). Operations exits at 0040. 0043 - MCB containment high pressure alarm occurs at 4.4 psig. 0625 - Secured containment pressurization. A test pressure (P ) of 30.8 psia was attained. 0650 - Commenced containment temperature stabilization period. 1100 - Gross leakage (p=0.4 percent per day) detected by ILRT instrumentation. Commenced extensive investigations of all penetration areas. 1630 - Penetrations P-3 (HPSI), P-81 (Auxiliary Feedwater), and
?-65 (Air Monitoring System) isolated and closed. Test reinitialized and four-hour temperature stabilization period started.
t 0; '0 l-1730 - Computer analysis indicates no significant change in containment leak rate. Commenced reinspection of pene-tration areas. 2013 - Leakage traced to service water vent valve (to CAR fan cooler no. 2) SW-V-266. Valve closed. Residual leakage detected. 2200 - Blank flange installed on SW-V-266. -ILRT leakage begins to decrease. Commenced four-hour temperature stabiliza-tion period. 2231 - Computer trending indicates a rise in containment air temperature of 0.85 to 0.9'F/ hour. Trend continues into early morning hours of April 4, 1986. Computer analysis indicates the rise in air temperature could potentially
" thermally mask" the actual ILRT leakage rate. A method-ical engineering review of systems thermodynamic behavior (to account for this trend) is conducted.
April 4, 1986 1440 - It is determined that the original leak through CAR fan cooler no. 2 service water valve SW-V-266 had " depressed" the effect of the CAR fan motor heat output. When the leakage was terminated, so was the cooling flow through the cooler itself. It was determined that reintroduction l l j
, o of service' water (to a . fan cooler) would help control the rise'in temperature.
1445 - Service water flow to CAR fan cooler no. 1 initiated (by cracking open SW-V-264). Containment temperature rise began to decrease. 1610 - Temperature rise calculated to be 0.1 to 0.2*F/ hour. Test reinitialized and four-hour temperature stabiliza-tion period started. 2036 - Temperature stabilization completed. Start of 24-hour containment leak test. [ April 5, 1986 i i 2039 - Twenty-four hour L g measurement completed. Preparations started for verification test. Satisfied test acceptance criteria (Reference 2). I April 6, 1986 4 0122 - Volumetrics flow transmitter (S/N 8119-1) malfunctions. 0449 - Volumetrics flow transmitter (S/N 8119-2) placed into service. l i f
0608 - Four-hour temperature stabilization period commenced. 0614 - Superimposed leak rate of 3.62 SCFM through volumetrics flow transmitter (S/N 8119-2). 1009 - Start of verification test. 1021 - Temperature stabilization, Appendix F (Reference 2), signed off. 1409 - End of verification test. Appendix G (Reference 2) satisfied. - iF April 7, 1986 Plant began depressurization of containment. 3.2 General Test Description 3.2.1 Prerequisites i In accordance with the CYAPCO ILRT procedure, SUR 5.7-108 (Reference 2), the following is a listing of the perti-l l nent prerequisites that were completed and documented l prior to containment pressurization: I r. l
I
- a. All required Types B and C local leakage rate testing completed.
- b. All required system valve line-ups completed.
- c. Controlled access plan in effect,
- d. Temporary air compressors were checked out and available for pressurization.
- e. All equipment and instrumentation that could be damaged by test pressure, removed or protected.
- f. General inspection of the accessible interior and exterior surfaces of the containment structures and components completed,
- g. The Official Log of Events was established.
- h. All compressed gas cylinders removed from contain-ment.
- i. All test instrumentation calibrated and verified functional.
- j. The Data Acquisition and Analysis Computers were operational and programmed for ILRT functions.
1 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ 1
o .
- k. Containment water levels were taken prior to the start of the Type A test.
3.2.2 Equipment and Instrumentation Pressurization of the containment was achieved by the utilization of temporary air compressors. Air was piped through an after cooler and a refrigerated air dryer. The system included adequate instrumentation and valving to maintain proper monitoring and control of the compressed air quality throughout the pressurization sequence. The total rated capacity of the pressurization system as installed was 6,000 SCFM. The various containment parameters required to calculate containment leakage during the test were monitored using instrumentation which consisted of resistance temperature detectors (RTDs), dewpoint sensors (RTD type), and an absolute pressure quartz manometer. Pertinent data for the test instrumentation is listed in Attachment 3.2A and the general locations of the temperature and moisture sensors are shown in Attachment 3.2B. A mass flowmeter was used to perform the superimposed leakage verification test. All test instrumentation was monitored by Northeast Utilities' Data Acquisition System.
3.2.3 Data Acquisition System The data acquisition system used for the CYAPCO ILRT was provided by Northeast Utilities Service Company. The data acquisition system monitored the following instrumentation: y
])r ji Containment Temperature Detectors 20 Dewpoint Sensors 6 Quartz Manometers 2 Tyye PAB Mass Flow Meters 2 An HP 3497A was used to input the instantaneous instru-ment readings into the ILRT computer program every 15 minutes. The instantaneous instrument readings and averages were both recorded.
3.2.4 Data Resolution System After the appropriate data had been acquired, utilizing the HP 3497A, the parameters were input into Northeast
-a ?
*t r Utilities (HP 9836 and 9826) portable computers for leakage rate calculations.
For the CYAPC0 ILRT, the absolute method of mass point analysis was used to determine the leakage rate. Absolute Method of Mass Point Analysis The absolute method of mass point analysis consists of calculating the air mass within the containment struc-ture, over the test period, using pressure, temperature, and dewpoint measurements made during the ILRT. The air mass is computed, using the ideal gas law, as follows: M = 144V (P-Pv) (Eq. 1) RT where: M = air mass, lbm P = total pressure, psia l Pv = average vapor pressure, psia R = 53.339 ft-lbf/lbm *R (for air) T = average containment temperature, *R V = containment free volume, ft 1 1
1 1 The leakage rate is then determined by plotting the air mass as a function of time using a least-squares fit to determine the slope, A = dM/dT. The leakage rate is expressed as a percentage of the air mass lost in 24 hours or symbolically: Leakage Rate = (A/B) (-2400) (Eq. 2) Where A is the slope of the least-squares curve and B is the y-intercept, the sign convention is such that the leakage out of the containment is positive and the units are in percent / day. The air mass is calculated and the results are correlated as a function of time by means of a least-squares curve fit of the form: M = At + B (Eq. 3) The slope A and the y-intercept B are then used in Equation 2 to determine the leakage rate. A 95 percent confidence interval is calculated using a student's T distribution.
Plant Information General t
- a. Owner - Connecticut Yankee Atomic Power Company
- b. Plant - Haddam Neck
=
- c. Location - Haddam Neck, Connecticut
- d. Containment Type -' Reinforced concrete with an I
interior' steel liner
- e. Nuclear Steam System - Westinghouse PWR Technical Information l
! a. Containment Net Free - Air Volume 2,232,000 ft 8
- b. Design Pressure - 40 psig
- c. Design Temperature - 260*F
- d. Calculated Peak Accident Pressure Pa - 40 psig
- e. Containment ILRT Average Temperature Limits -
50-120*F
- f. Calculated. Peak Accident Temperature.- 260*F
- g. La .18 wt-% of air / day at 40 psig t
- h. P - 15 psig
- 1. L - 0.1102% per day
- j. 75 percent L = 0.08265% per day i
i I
, , . _ .,m.. - - _ - , _ _ , . _ _ . - _ _ . _ _ _ _ _ , , - . . _ . - - - , _ . . . . - - . _ , . . - - - . - . , - - - - _ _ _ , _ _ - ,.
,s. ..
Integrated Leakage Rate Measurement System Absolute Pressure a.. Readout 100,000 counts
- b. Accuracy - 0.010% of reading, plus two counts
- c. Resolution - 0.001% full scale ,
- d. Range 100 PSI
- e. Instruments (2):
- 1. Texas Instrument model 145-01, precision pressure instrument no. 2714 with bourdon capsule, serial number 5974.
- 2. Texas Instrument model 145-01 precision pres-sure instrument no. 2715 with Bourdon capsule, serial number 5975.
Drybulb Temperature (20 Sensors)
- a. Range 350*F
- b. Accuracy - .5*F
- c. Repeatability - 0.1% full scale
- d. Instruments (20):
-9 Resistance Temperature Detectors - Foxboro, Model DB-13-26W (permanent plant).
Resistance Temperature Detectors - Foxboro , , Model PR-13BBS-006 (ILRT test instrumentation). l Dewpoint Temperature (6 Sensors)
- a. Range 120*F
- b. Accuracy - 0.5'F y
- c. Repeatability - 0.1% full scale
- d. Instruments - Six Foxboro Model 2781-18-CG-Q (ILRT test instrumentation)
Verification Flow- (1 Channel)
-a. Range 13 SCFM
- b. Accuracy - i1% full scale I '
- c. Repeatability - 0.3% full scale 3
- d. Instrument - Volumetrics Flowmeter Model 1778 ~
(S/N 8119-2) 3.3 Test Results 3.3.1 Presentation of Test Results '~ The test data for the April 1986 ILRT is based on a 24-hour period starting at 2036 hours on April 4, 1986.
- The final test results were determined using Northeast Utilities' ILRT computer program. The reduced input
7 3
- Q'
' - 18 _
4 -,.. . . 4 data, mass point analysis test results, and representa-y tive graphs are contained in Attachments 3.3F through
. ,1 : 3.3J.
T- $ _*; r The mass point analysis test results for the ILRT sat-isfied the procedural acceptance criteria (Reference 2), f , I> The Type A test instrumentation was verified by the superimposed leakage verification test method. The mass
^- e.
point analysis test results for the superimposed-leakage
, _ _ verification-test satisfied the procedural acceptance criteria (Reference 2).
I 3.3.2 ILRT Results
~ The ILRT was conducted in accordance with CYAPCO station c
?
test procedure SUR 5.7-108 (Reference 2). The results
~ !" 2* for the ILRT and for the supplemental test are shown below.
3.3.2.1 Mass Point Analysis V Item Percent / Day 1
- a. L , (LSF) leakage rate (1) -5.20 X 10 ~3 a
1
, . - - , - - - - - - - , , - ,n , -v., g-- .,.-m ,- , - - - - ,. , -
- b. L , (UCL) 95%
confidence level leakage rate ( } -1.5 X 10
-3 Results were within the acceptable (Reference 2) limit of 0.0827 (75 percent L )
percent per day. Notes 1, 2: -Results are for the 24-hour interval starting April 4, 1986 at 2036 hours to April 5, 1986 at 2039 hours. SUR 5.7-108 (Reference 2), Subsection 9.3,
" Total Leakage Rate," lists results from April 4, 1986 at 2036 hours to April 5, 1986 at 2024 hours: L LSF =
-3
-5.10 X 10 and L g UCL =
-3
-1.38 X 10 percent per day.
The dif'rvence is due to cuaI; /in : an additional 13 minutes of ILRT data. The difference (s) is negligible. w , , --- .. -
3.3.2.2 Supplemental Test Results The supplemental verification test was performed using the superimposed leakage verification test method in accordance with station test procedure SUR 5.7-108. The results for the superimposed leakage verification test are shown below. The superimposed leakage verification test is acceptable provided L falls within the follow-c ing range: (L tm +L o - 0.25Lt ) f' L c (b tm +b o + 0.25Lt ) where: L = Type A calculated leakage (computer) at 2024 hours (Lg LSF = -0.0051) L 9
= Superimposed leakage rate from Reference 2, Appendix G (L = 0.1147)
L = Maximum allowable leakage rate at P (0.18 percent per day at 40 psig) l L = Composite leakage (computer)4 at l 1409 hours (L = 0.110)
The Mass Point Verification: (L + L, - 0.25 L t c tm
+
o + 0.25 L ) (-0.0051 + 0.1147 - 0.0276 h 0.110 b -0.0051 + 0.1147 + 0.0276) 0.0821 b 0.1100 b .1372 0 Note 3: Per References 1 and 2, L =L A\ Where L = .18 percent per day, L = A 0.1102 percent per day at P > 15 psig. P = 15 psig and P = 40 psig. l Note 4: L = Mass point gross LSF date. column (Attachment 3.3E at 1409 hours). 3.3.2.3 Calculation of the Superimposed Leakage Rate, Lo from SUR 5.7-108 (Reference 2), Appendix G: L, (% per day) = [ ] [1440( )] [0.075( )] [100%)
= volumetric flow meter setpoint =
Q 3.67 SCFM.
e M = c ntainment ILRT air mass at end of A 24-hour L ,= 345473 LBM. L, = (3f;f773) x (1440) (0.075) (100%) = 0.1147 % per day. L = 0.1147% per day. 9 3.3.2.4 LLRT "As-Left and "As-Found" Adjustment Penalties to ILRT L _ Results 3.3.2.4.1 From Reference 2, the following penetrations were not tested during the ILRT: Leak Rate @ 15 psig Penetration (percent per day P-28 +0.000902 P-29 +0.0 P-63 +0.0 , P-70 +0.000008 P-80 +0.000225 P-81 +0.000039 Total +0.0012 3.3.2.4.2 From Reference 2, the following penetrations were isolated during the
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Type A test and leakage rate measured:
"As-Left" Leak Rate Penetration (percent per day)
P-3 +0.0 P-81 +0.000039 (5) P-65 +0.000228 Total (5) +0.0002 i Note 5: Total does not include leakage from P-81 as it is included in Section 3.3.2.4.1. 3.3.2.4.2.1 From Reference 10, the following penetrations "as-found" LLRT leakage, prior to the Type A test:
~ ~
"As-Found" Leak Rate Penetration (percent per day)
P-65 +0.00228 P-3 +1.0057 P-13 +0.000121 P-28 +0.000902 P-70 +0.000008 P-80 +0.000225 P-81 +0.000039 Total +1.0093 l 3.3.2.4.2 Total "As-Left" Penalty l From Sections 3.3.2.4.1 and 3.3.2.4.2, the total LLRT add-on penalty to ILRT L ,results is: 0.0012
+ 0.0002 Total "as-left" Leakage is: +0.0014 (%/ day) 3.3.2.4.2.1 Total "As-Found" LLRT Penalty From Section
l 3.3.2.4.2.1, the total add-on "as-found" LLRT penalty to the ILRT L ,results is: Total "as-found" leakage is +1.0093 (%/ day). 3.3.2.5 Comparison of ILRT L ,results to acceptance criteria (from Section 3.3.2) (6) i t Test Results: L tm LSF = -0.0052 % per day @ 2039 hours
~
L tm UCL = -0.0015 % per day @ 2039 hours SUR 5.7-108 (Reference 2) ILRT L___ E ME Acceptance 4 Criteria: L : 0.75 L tm
- L , 3
- 0.0827 % per day Note 6: L , not adjusted for LLRT add-on penalty.
l 4 3.3.2.5.1 Comparison (L LSF to 0.75 L ): Lg,LSF 6 0.0827 % per day
-0.0052 { 0.0827
Conclusion:
The L LSF (-0.0052) satisfies the test acceptance inequality and is within the acceptance criteria's maximum allowable leakage rate. 3.3.2.5.2 Comparison (L UCL to 0.75 L ): L UCL d 0.0827 % per day
-0.0015 ( 0.0827
Conclusion:
The L tm UCL (-0.0015) satisfies the test acceptance inequality and is within the acceptance criteria's maximum allowable leakage rate.
-, . - . . - - - - - . _ - . _ , , _ _ _ . , _ . . . ._ ..__,-------.-x--., . . , . - - , - _ - - ~ . . - - - . _ _ . . . . . , - - . - _ . - - _ _
;. . +
3.3.2.6 Comparison of ILRT L results (adjusted for "as-left" LLRT penalties) to test acceptance. criteria: Test Results: L LSF = -0.0052 % per day @ 2039 hours Lg,UCL = -0.0015 % per day O.2039 hours "As-Left" Adjusted L Results: From Section 3.3.2.4.3, the total "as-left" LLRT penalty to be added to L is: +0.0014
% per day.
"As-lef t'.' adjusted L tm LSF + 0.0014 = -0.0038
% per day.
"As-lef t" adjusted L UCL + 0.0014 = -0.0001
% per day.
3.3.2.6.1 "As-Lef t" Comparison (Adjusted L LSF to 0.75 L; ):
"As-lef t" adjusted L LSF db 0.75 L t
(from Reference 2)
"As-lef t" adjusted L LSF S 0.0827
% per day
-0.0038 ( 0.0827
Conclusion:
The adjusted "as-left" L LSF (-0.0038) satisfies the test acceptance inequality and is within the acceptance criteria's maximum allowable leakage rate. 3.3.2.7 "As-Left" Test Result Summary and Discussion 3.3.2.7.1 Summary of "As-Left" ILRT Test Results: The following table summarizes the CY' "as-left" ILRT test results. ILRT L LLRT Add-On Penalty ILRT Adjusted L tm 0.75 L t (% per day) (% per day) (as-left) (% per day) (as-lef t) % per day L LSF = -0.0052 0.0014 -0.0038 0.0827 L UCL = -0.0015 0.0014 -0.0001 0.0827
g ,... 1-3.3.2.7.1.1 The "as-lef t" adjusted ILRT test results satinfy the acceptance s ia requirements ol lant technical specifications end 10CFR50, Appendix J. The test results demonstrate the leak tightness of the CY containment. I CY passed the "as-left" Type A test. 3.3.2.8 Comparison of ILRT LTM Results (Adjusted for "As-Found" LLRT Penalties) to Test Acceptance f Criteria i Test Results: Lg,LSF = -0.0052 % per day 0 2039 hours L ,UCL = -0.0015 % per day @ 2039 hours
"As-Found" Adjusted L Results:
l l From Section 3.3.2.4.2.1, the total "as-found" LLRT penalty to be added to L tm is +1.0093
% per day.
"As-found" adjusted L g,LSF + 1.0093 = +1.0041
% per day.
"As-found" adjusted L UCL + 1.0093 = +1.0078
% per day, s
3.3.2.8.1 "As-Found" Comparison (Adjusted L _ ! LSF to 0.75 L ) b {
"As-found" adjusted L LSF A 0.75 L t (from Reference 2).
"As-found" adjusted L LSF i 0.0827
% per day.
+1.0041 ( 0.0827
Conclusion:
The adjusted "as-found" L LSF tm (+1.0041) exceeds the acceptance
criteria's maximum allowable leakage , rate. 3.3.2.8.2 "As-Found" Comparison (Adjusted L UCL to 0.75 L )
"As-found" adjusted L UCL d- 0.75 L t (from Reference 2).
"As-found" adjusted L UCL 6 0.0827
% per day.
+1.0078 4 0.0827
Conclusion:
The adjusted "as-found" L UCL (+1.0078) exceeds the acceptance criteria's maximum allowable 1e.akage rate. 3.3.2.9 "As-Found" Test Result Summary and Discussion 3.3.2.9.1 Summary of "As-Found" ILRT Test Results: The following table summarizes the CY "as-found" ILRT test results.
ILRT L 'LLRT Add-On Penalty ILRT Adjusted L tm 0.75 L t (% per day) (% per day) (as-found) (% per day) (as-found) % per-day Lg,LSF = -0.0052 +1.0093 ,
+1.0041 0.0827 Lg,UCL = -0.0015 +1.0093 +1.0078 0.0827 3.3.2.9.1.1 The "as-found" adjusted ILRT test results do not satisfy the acceptance criteria requirements of plant specifications and 10CFR50, Appendix J.
Section 4 and Attach-ment 4A documents the plant's corrective action and retest efforts to reduce Type B and C leakage rates. CY did not pass the "as-found" Type A test.
*~
3.3.2.10 Discussion of Test Results The results listed in Section 3.3.2.7.1 demon-strate the "as-left" leak tightness of the CY containment boundary. The ILRT measured leakage rates (L tm LSF and UCL) satisfied all test (Reference 2) acceptance criteria. The results listed in Section 3.3.2.9.1 show that the "as-found" condition of the CY con-tainment did not meet the requirements of the test acceptance criteria (Reference 2) due to leakage through Type C penetrations. Rework and retest efforts decreased the Type C leakage significantly, as indicated in Section 4 of this report. Graph 1 (Attachment 3.3F) trends the ILRT leakage rate over time (24 hours). The L tm curves (LSF and UCL) fall under the test acceptance criteria (0.0827 % per day). Graph 2 (Attachment 3.3G) trends the average containment air temperature over time (24 hours). The temperature curve is stable
and increasing at a very low rate ( 4 0.15*F per hour). Graph 3 (Attachment 3.3H) trends the contain-ment air pressure over time (24 hours). The pressure curve is stable and increasing at a very low rate ( 6 0.0087 psia per hour). The increase in pressure is due to the effect of the temperature rise, in accordance with the ideal gas law. Graph 4 (Attachment 3.31) trends the containment vapor pressure over time (24 hours). The vapor pressure behavior is acceptable. Review of dewpoint temperature listed in Attachment 3.3B indicates trending is satisfactory. Finally, Graph 5 (Attachment 3.3J) trends the containment air mass over time (24 hours). The curve indicates a nearly constant air mass (approximately between 345,400 to 345,500 LBM) was present during the ILRT. The slope depicted in Graph I (Attachment 3.3F) also indicates a nearly constant air mass was present. The mass plot is satisfactory.
3.3.2.11 Final Conclusion The April 1986 CY "as-left" ILRT was successful and demonstrated the leak tightness of the containment building's boundaries. The plant passed the requirements of a Type A test (References 1 and 2).
-... i*
SECTIONS 4 THROUGH 6 Section 4.0 summarizes the local leakage rate tests (LLRTs) data that was established to support the overall containment leakage testing program. These LLRTs were performed per the requirements of the CY LLRT surveillance program. The acceptance criteria for Types B and C testing is in accordance with 10CFR50, Appendix J, as amended by existing exemptions. Individual penetration leakage rates for all containment isolation valves and Icakage barriers subject to Types B and C tests are listed in Section 4.0. Section 4.1 lists corrective action performed by CYAPCO. Section 4.1.2 lists additional LLRT testing on selected isolation valves during the
' July 1986 Steam Generator Outage.
Section 5.0 lists Air Filtration System Test results. Section 6.0 lists Recirculation System Test results.
SECTION 4.0 LOCAL LEAKAGE RATE TEST DATA
4.0
SUMMARY
OF TYPE B AND C LEAK RATE RESULTS (1986) Pene- (1) As-Found As-Left tration Test Test Test Leak Test Leak No. Description Type Method Date Rate (2) Date Rate (2) Notes 3 Safety Injection C LC 1/13 0 4/20 0 3 4 Pressurizer Relief Tank Vent C PD 1/11 .00001 1/11 .00001 6 Post-Accident Sampling System C PD 1/12 .00001 1/12 .00001 7 RCP Seal Water Return C LC 1/21 .07011 3/28 .00062 3 9 Post-Accident Sampling System C PD 1/12 .00001 1/12 .00001 10 Reactor Coolant Letdown C LC 1/15 1.25030 4/2 0 3 11 Liquid Sample Lines C LC 1/3 .00025 4/25 .00023 12A Valve Stem Leakoff C LC 1/14 0 3/27 .00005 12B Neutron Shield Tank Sample C PD 1/9 0 1/9 0 13 Sump Pump Discharge C PD 1/18 .00012 1/18 .00012 14/78 Vapor Seal Head Tank Drain / C PD 1/14 .00026 3/27 .00020 Pressurizer Relief Tank Drain 15-18 Steam Cencrator Blowdown Nos. 1-4 C LC 1/2 .00020 1/2 .00020 20 Pressurizer Relief Tank Nitrogen C PD 1/10 .00193 3/1 .00022 3 Supply 22 Space Heating Condensate Return C PD 1/18 .00453 3/27 .00007 3 23A Containment Leak Detection Open C PD 1/12 .00048 1/12 .00048 Bulb System 23B Containment Leak Detection C PD 1/9 .00018 1/9 .00018 Closed Bulb System 23C Dead Weight Tester (Seal Welded) C PD 1/9 .00001 1/9 .00001 23D Air Monitor Purge C PD 1/12 .00021 1/12 .00021 24 Safety Injection Recirculation C LC 1/13 .00061 1/13 .00061 Lines 28 Component Cooling to RCP Oil C LC 1/8 .00093 1/8 .00093 Coolers 29 Component Cooling from RCP Oil C PD 1/8 0 3/30 .00006 Coolers
30 Containment Space Heating Supply C LC 1/22 .20419 4/1 0 3 33 Refueling Cavity Purification C PD 3/28 .00007 3/28 .00007 34 Component Cooling from RCP C LC 1/14 .00013 4/30 .00011 3 Thermal Barrier 38 Component Cooling to RCP Thermal C LC 1/14 .37491 5/2 .00022 3 Barrier 39 Containment Purge Air: Exhaust C PD 12/27 .04391 3/30 .00031 40 Containment Purge Air: Supply C PD 12/19 0 12/19 0 41 Loop Drain Header C PD 1/18 .00042 3/31 .00042 50 Fuel Transfer Tube C PD 1/13 0 3/31 0 60 Component Cooling to Neutron C LC 1/15 2.3110 5/3 .00016 3 Shield Tank Cooler 61 Component Cooling From Neutron C LC 1/9 0 3/27 .00024 Shield 62 Service Air C PD 3/25 .00032 3/25 .00032 63 Neutron Shield Tank Fill Line C LC 1/9 0 3/28 0 64 Air Monitor Sample From C PD 1/17 .108 1/24 .00030 3, 6 Containment 65 Air Monitor Sample to Containment C PD 1/16 .00189 2/19 0 3 66 Component Cooling to Drain Cooler C PD 1/10 .00041 5/1 .00038 67 Component Cooling from Drain C LC 1/10 .00007 5/1 .00006 Cooler
- 68 Primary Water to Containment C LC 2/4 .00060 2/4 .00060 69 Loop Fill C LC 1/3 .00001 1/3 .00001 70 Instrument Air Supply to B PD 1/3 .00001 1/3 .00001 Containment 71 Primary Vent Header C PD 2/4 .108 3/5 .00001 3, 6 80 Auxiliary Containment Spray C LC 1/18 .00017 4/26 .00038 from Fire System 81 Steam Cencrator Auxiliary C LC 1/4 .00004 1/4 .00004 Feedwater Supply
A Personnel Hatch B PD 1/1 0 5/3- 0 4 B Electrical B PD 2/10 .00016 2/10 .00016 C Equipment Hatch B .PD 3/22 .00001 3/22 .00001
.D Dome Vent Flange (Top) B PD 1/12 .00001 4/2 -.00001 E Dome Penetration Flange (Side) B PD 1/12 .00001 1/12 .00001 F Equipment Hatch Penetrations B PD N/A N/A 3/30 0 5
, (P-F-AEB) 74 No. 4 RCP Seal Water Supply C LC 3/19 .00115 3/19 .00115 75 No. 3 RCP Seal Water Supply C LC 3/19 .00871 3/30 0 3 76 No. 2 RCP Seal Water Supply C LC 3/19 .00074 3"/19 .00074 77 No. 1 RCP Seal Water Supply C LC 3/19 .00115 3/19 .00115 NOTES: 1. Test Method: LC-Liquid Collection; PD-Pressure Decay
- 2. Leak Rate is in %/ day at 40 psig.
- 3. Retest After Maintenance.
- 4. As-Found Leak Rate - Last test prior to shutdown.
As-Left Leak Rate - Leak test prior to start-up. ] 5. Two penetrations were installed on the equipment hatch during the 1986 refueling
- outage. The as-found test is not applicable.
- 6. A leak rate could not be obtained. It is assumed that the leak rate exceeded
.6 La (.108%/ day).
Acceptance Criteria: The combined local leak rate of all containment penetrations subjected to local leak testing shall not exceed .6 La (.108%/ day at 40 psig). As-Found Combined Local Leak Rate:
4.28024%/ day at 40 psig, plus two penetrations with leak rates greater than .108%/ day at 40 psig. As-Left Combined Local Leak Rate:
.01109%/ day at 40 psig.
4.1 LOCAL LEAKAGE RATE TEST CORRECTIVE ACTION PLAN AND JULY 1986 LLRT RESULTS The following is a summary of the corrective action performed on the containment penetrations with significant as-found leak rates. Leak rates in excess of .02200%/ day at 40 psig are considered significant with respect to the combined local leak rate. The corrective action for containment penetrations with significant leak rates was reviewed for additional action. The additional action consisted of mid-cycle testing and modification. Mid-cycle testing was considered if it was not felt that the failure mechanism was corrected. Modifications are planned for penetrations that had repetitive failure rates. During July 1986, the plant was shut down for steam generator repairs. Many of the penetrations considered for mid-cycle testing were tested at this time. The details are provided under each penetration. The plant had been operating for approximately two months from the latest refueling outage. The results of the mid-cycle tests are attached. P-3 High Pressure Safety Injection The penetration has four check valves in parallel for containment isolation. The initial as-found leak test was satisfactory. Leakage was detected past SI-CV-862B during the
ILRT. SI-CV-862B was not seating properly due to hinge wear. The hinge was built up with_ weld metal and the seating' angle redrilled. The retest was satisfactory. No additional action was warranted. P-7 Reactor Coolant Pump Seal Water Return
'The penetration has three containment isolation valves in parallel. The total as-found leak rate of the penetration was
.07011%/ day, which consists of .03249%/ day for CH-TV-334,
.03722%/ day for CH-RV-332, and .00040%/ day for CH-CV-262.
Abrasive wear was found on the seating surface of CH-TV-334. The seat and plug were repaired. It is felt that the seat wear was related to the deterioration of the seal water return filter. This could not be confirmed. A mid-cycle leak test conducted during July shutdown indicated that CH-TV-334 was performing satisfactorily (.00006%/ day). No additional action was warranted. The initial leakage of CH-RV-332 was reported as.04955%'/ day. A bench test of the relief valve indicated that there was no valve leakage. A review of the test procedure showed that there were several test boundary valves whose leakage would be attributed to CH-RV-332. The procedure was revised to ensure that there was no leakage from the test boundaries. A retest with CH-RV-332 reinstalled was satisfactory. A mid-cycle test
=
.i .'
during the July shutdown was also satisfactory. No additional action was warranted. P-10 Reactor Coolant System Letdown The containment isolation boundary has three containment isolation valves in parallel. Due to the piping configuration, the valves are leak tested simultaneously. The seating surfaces of LD-A0V-202, 203, and 204 had eroded. 'The cause of the erosion was an increased differential pressure across the valve due to wear of the letdown orifice (lo'cated immediately upstream of each valve). The orifices were replaced and the valves repaired, with one valve peing replaced. A retest was satisfactory. P-10 was reviewed for mid-cycle testing. Due to the large as-found leak rate, it was felt an additional test was desirable. However, since the failure mechanism was addressed, mid-cycle testing was only recommended if the plant was shut down for other reasons and plant conditions permitted testing. The penetration was not tested during July due to the short outage duration and manpower constraints. P-30 Containment Space Heating Steam Supply The containment penetration has two check valves in series. The leakage past HS-CV-295A was .20419%/ day. Signs of disc
.+ .
drift and rust particles were found on the valve seat. The redundant valve, HS-CV-295, had a leak rate of .06381%/ day. The threads on the end caps that hold the disc pins in place were stripped. This allowed the discoto drift on the valve seat. The identified problems were corrected and a retest was satisfactory. Mid-cycle test during the July shutdown measured leak rates of
.02909%/ day past HS-CV-295 and .00002%/ day past HS-CV-295A.
The leakage past HS-CV-295 was between the valve body and the seat ring. The seat ring is threaded into the valve body. The threads were cleaned and a bevel was put cn the top of the seat ring threads to improve the surface contact. The retest was satisfactory. P-30 has been selected for modification during the 1987 refueling outage. The specific cause of the valve leakage has always been identified and corrected. However, the valves have begun to show an increasing trend in leakage over the past three refueling outages. It is believed that the root cause of the leakage is valve age and valve design. The modification will address these concerns. P-38 Component Cooling Water to Reactor Coolant Pump Thermal Barrier
P-60 Component Cooling Water to Neutron Shield Tank Cooler These two penetrations are addressed together as they have similar configurations and failure causes. Each penetration has a single check valve for containment isolation purposes. The check valves have a history of repetitively high leak rates. Previous action consisted of changing the valves from swing checks to lift checks during and before the 1980 outage. A slip stream filter was installed in the component cooling water system between the 1983 and 1984 outages. The filter was installed to remove sand from the system. Disassembly of the check valve _showed that sand and silt was causing the piston to stick open. The valve internals were cleaned. A new slip stream filter, with a greater capacity to remove sand and silt, was installed in the component cooling system. A series of leak tests were conducted after the filter was placed in service. The check valves were not seating. The isolation valves for the RCP thermal barrier
, loop and neutron-shield tank cooler loop were cycled in an l attempt to remove residual sand. A subsequent series of leak tests indicated that CC-CV-721 (P-38) was functioning properly and CC-CV-885 (P-60) was sticking open.
CC-CV-885 (P-60) was replaced with a horizontal lif t check valve. It was concluded that wear of the valve internals l r
allowed system flow to cock the piston of the angle lift check valve. A subsequent series of tests indicated that the new valve was functioning properly. It was concluded that the slip stream filter was removing suspended solids from the component cooling water. However, P mid-cycle testing was considered important for P-38 and P-60. The penetrations have had repetitive leakage problems in the past. However, the corrective action addressed the root cause of the leakage. The mid-cycle tests would provide confidence in the long-term effectiveness of the corrective action. P-38 and P-60 were mid-cycle tested during the July outage. P-38 had a leak rate of .00001%/ day and P-60 had a leak rate of .00020%/ day. Initially, a large leak' rate was reported for P-38. The large leak rate was due to leakage past a test boundary valve. In addition, CC-CV-721 (P-38) was disassembled for inspection. The valve internals and seating surfaces were clean. The seating surfaces were wiped with a clean white rag. No sand or silt was on the seating surfaces. This testing provides assurance that the containment isolation valves for P-38 and P-60 will remain operable for the existing cycle.
.= ,
The long-term corrective action planned for P-38 and P~60 is to modify the containment penetrations. An additional modification will minimize any sand that enters the component cooling system from the service water system cross-connection. This work is scheduled for the 1987 refueling outage. i. P-39 Containment Purge, Exhaust The penetration has a 42-inch butterfly valve, and 8-inch manual valve, and a 6-inch blind flange which are in parallel. Initially, a leak rate of .04391%/ day was measured. A blind flange is attached to the piping to form a test boundary for the leak test. The primary leak path was across the blind flange installed for a test boundary. The blind flange was reinstalled. The subsequent leak test was satisfactory. The containment boundaries in this penetration have a good history of being leak tight. 4.1.1 conclusion The corrective and preventive maintenance identified for each penetration provide adequate assurance that the containment isolation valves will function properly. Containment , penetrations with high Icak rates will be reviewed for mid-cycle testing and modifications to ensure containment integrity is maintained.
.,s . ,
7
. 4.1.2 . JULY 1986 LLRT RESULTS Pane- (1) As-Found As-Left tration Test Test- Test Leak - Test Leak Nn. Description Type Method Date Rate (2) Date Rate (2) Notes i.
i' 7 .RCP Seal Water Return C LC 7/19 . 05684 - 7/21 .00006 3 23A Containment Leak Detection C PD 7/18- . 00018- 7/18 .00018 Open Bulb System , . 30 Containment Space Heating Supply C LC 7/18 . 02909 -7/20 .00010 4' I 38 Component Cooling to RCP Thermal C LC 7/19 . 60286 7/20 .00010 5 Barrier 4
- 60. Component Cooling to Neutron C LC 7/19 . 00020 7/19' .00020- ;
Shield Tank Cooler - 66 Component Cooling to Drain Cooler C LC 7/20 0 7/20 0 67 Component Cooling from Drain C LC 7/20 0 7/20 0 Cooler ' 68 Primary Water to Containment C LC 7/20 0 . 7/20 0 71 Primary Vent Header C PD 7/21 .00017 7/21 .00017
' NOTES: 1. Test Method: LC-Liquid Collection; PD-Pressure Decay l 2. Leak Rate is in %/ day at 40 psig.
- 3. The majority of the as-found leakage was f rom the test of CH-RV-332. A retest j performed after improving the isolation of test boundary valves verified that CH-RV-332 was not leaking. -
- 4. . The as-found leakage was through HS-CV-295. Details are provided in the correc-tive action plan. The redundant isolation valve, HS-CV-295A, had an as-found
{ 1eak rate of .00002%/ day, which is satisfactory.
- 5. The high as-found leak rate was due to leakage past a test boundary valve. A retest and disassembly verified that the containment isolation valve was opera-ble.
i 4 e e - - - - . . y , . - % v. , , - . . -m, , , , -
5.0 AIR FILTRATION SYSTEM TEST RESULTS The te at requirements for the Air Filtration System are in Technical Specifications, Section 4.4, " Containment Testing." The Air Filtration System includes four Containment Air Recirculation (CAR) Fans. The CAR Fans are located inside the containment building. The CAR Fans are Trane Model SPE0 centrifugal fans, powered by Westinghouse Model 65F13098 motors. The test results
~
are tabulaced below: Acceptance CAR CAR CAR CAR Test Criteria Fan #1 Fan #2 Fan #3 Fan #4_ HEPA DOP Removal Eff. (%) 199.5 99.92 99.8 99.99 99.6 Freon Removal Eff. (%) 2 99.0 99.9 99.9 99.99 99.88 Flow Rate (cfm) 50,000[0% 57,490(1) 50,938 51,772 51,442 Combined HEPA/ Charcoal Press. Drop (in W.G.) 46.0 2.25 1.75 1.8 3.5 Methyl Iodide Removal Eff. (%) > 90.0 98.12 97.95 96.77 98.19 Elementa1' Iodine Removal Eff. (%)99.9 99.97 99.96 99.96 99.96 Visual Inspection No damage OK OK OK OK Date Tested N/A 2-14-86 2-12-86 4-1-86 2-13-86 Notes: (1) #1 CAR fan flow was reduced to 52,136 cfm on 4-1-86. i k
a
- s .
6.0 Recirculation System Tests The recirculation system test is a visual inspection for leakage of the accessible portions of the Residual Heat Removal (RHR) System located
- outside of containment. The inspection is conducted daily, at-least once per shift, during plant operation. Included in the inspection are pumps, heat exchangers, valves and piping. The total leak rate must be less than 3 liters per hour (50 cc per minute).
The inspection interval included in this report is from November 1984 through December 1985. Portions of the Chemical and Volume Control System (CVCS) used for high pressure recirculation were added to the recirculation system test in August 1985. A summary of the measurable leakage detected is provided below. Recirculation System Leakage Date Leakage Comment July 1985 .6 cc/ min A RHR Pump
.2 cc/ min B RHR Pump August 1985 .01 cc/ min RH-RV-715 20 cc/ min FI-103 (CVCS) 5 cc/ min FI-104A (CVCS)
September 1985 1 cc/ min CH-V-283 November 1985 .33 cc/ min B-Charging Pump December 1985 1 cc/ min B-Charging Pump
-wom - w..- -
v.. ,. .--
ATTACHMENT 3.2A INSTRUMENTATION The following instrumentation was calibrated within six months of the test and functionally verified prior to the performance of this test. Note 1: RTDs 1-9 are permanent plant instrumentation. RTDs 9-20 are temporary ILRT test equipment. 2: Dew cells 1-6 are temporary ILRT test equipment. 3: Texas Instrument precision pressure gauges, model 145-01 are temporary test instrumentation. 4: Volumetrics flow transmitters are temporary test instrumentation. i
.+ .
A. Temperature Weight Instrument Factor Channel Range Elevation Acc~uracy RTD1 0.048 1 0-350*F 85' O.5*F RTD2 0.048 2 0-350*F 85' 20.5'F l RTD3 0.048 3 0-350*F 85' O.5*F RTD4 0.048 4 0-350*F 85' O.5'F RTD5 0.042 5 0-350*F 25' O.5'F RTD6 0.042 6 0-350*F 25' O.5*F RTD7 0.027 7 0-350*F 25' O.5'F RTD8 0.027 8 0-350*F 25' 10,5"F RTD9 0.020 9 0-350*F 35' O.5'F RTD10 0.089 10 0-350*F 128' O.5'F RTD11 0.071 11 0-350*F 174' O.5'F RTD12 0.'071 12 0-350*F 152' O.5*F RTD13 0.059 13 0-350*F 140' !0.5*F RTD14 0.097 14 0-350*F 113.5' 0.5'F RTD15 0.044 15 0-350*F 53' O.5'F RTD16 0.044 16 0-350*F 53' !0.5*F RTD17 0.044 17 0-350*F 53' !0.5'F RTD18 0.044 18 0-350*F 53' O.5'F RTD19 0.040 19 0-350*F 5' 10.5'F RTD20 0.047 20 0-350*F 5' 10.5'F B. Dewpoint D1 0.042 D1 20-120*F 25' O.5'F D2 0.042 D2 20-120*F 25 !0.5'F D3 0.29 D3 20-120*F 140' O.5'F D4 0.465 D4 20-120*F 53' 20.5*F DS- 0.047 D5 20-120*F 5' O.5*F D6 0.114 D6 20-120*F 45' O.5*F C. Pressure TI #1 N/A N/A 0-100 psia N/A 0.01% of TI #2 N/A N/A 0-100 psia N/A reading D. Superimposed Leakage Verification Test Mass Flow Meter ( } Volumetrics N/A N/A 0-13 scfm N/A 1% F.S. Flow Trans-mitter #2
Attachment 3.2B ILRT Temperature and Dewcell Detector Locations Profile View
.=...
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s b ATTACHMENT 3.3A _ ILRT SENSOR DATA VAPOR CONTAINHENT l ATE HOUR TEMP PRESSURE PRESSURE COUNT.1 COUNT 2
. 4/04 1608 82.2896 .2434 31.0743 31545 0 IRTD RTD RTD RTD RTD ' RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 .T 8 T9 T10 80.023 80.890 81.342 80.023 82.170 83.448 84.874 82.997 80.098 82.921 RTD RID RTD RTD RTD
- RTD RTD RTD RID RTD T11 T12 T13 T14 TIS T16 T17 T18 T19 T20 82.907 82.563 82.386 82.586 82.879 03.139 83.111 83.172 81.615 81.787
^ D1 D2 D3 D4 05 DS
- 58.599 57.685 58.661 58.412 58.448 59.067 VAPOR CONTAINMENT - ;TE HOUR TEMP FRESSURE PRESSURE COUNT 1 COUNT 2
. 4/04 1613 82.2856 .2434 31.0743 31545 0 1TD RTD RID RTD RTD RTD RTD RTD RTD RTD ' t1 T2 T3 T4 T5 T6 T7 T8 T9 T10 30.098 80.927 81.229 80.098 82.170 83.410 84.949 83.034 79.985 82.907 . 1TD RTD RTD RTD RTD RTD RTD RTD RTD RTD Ill T12 T13 T14 TIS T16' T17 T18 T19 T20
- 32.772 82.58G 82.405 82.605 82.856 83.014 83.121 83.227 81.629 81.843 11 D2 D3 D4 D5 D6 i8.822 57.649 58.787 58.473 58.186 58.548 4
. VAPOR : CONTAINMENT DATE ' HUUR TEtiP PRESSURE F . PRESSURE ' COUNT 1 COUNT 2
.2421
04/04 1618 82.3303 31.0757 31545 0 RTD RTD RTD'a RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 'T5 T6 T7 T8 19 T10 80.061 80.927 81.229 80.174 82.207 83.448 84.911 83.147 80.174 82.944 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T12 T13 T14 T15 T16 T17 T18 T19 T20 T11 82.921 82.596 82.433 82.623 82.874 83.306 83.130 83.209 81.685 81.852 D1 D2 D3 D4 D5 .D6 59.016 57.294 57.914 58.696- 58.186 58.580 e.oon............................................ VAPOR 'CONTAINHENT
;DATE HOUR TEMP PRESSURE PRESSURE ' COUNT 1 COUNT 2 04/04 1623 82.3417 .R460 31.0738 .31547 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T2 I3 T4 T5 T6 T7 T8 I9 T10 79.948 80.890 81.304 80.249 82.207 .83.410 84.874 83.185 80.098 83.028 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS T16 T17 T18 TI9 T20 82.930 82.619 82.461 82.688 82.916 83.074 83.204 83.195 81.671 81.917 D1 D2 D3 D4 D5 DG 58.402 57.552 60.045 58.409 58.283 58.289
, VAPOR CONTAINMENT DATE HOUR TENP PRESSURE PRESSURE COUNT 1 COUIIT2 l04/04 ! 1628 82.3496 .2435 31.0763 31547 0 t RTD RTD RTD RTD RTD RTD RTD RID RTD _RTD T1 T2 T3 T4 T5 T6 T7 T8 I9 T10 83.009 1 80.098 80.965 81.304 80.098 82.358 83.448 84.874 83.185 80.098 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T13 T14 T15 T16 T17 T18 T19 T20 T11 T12 02.930 82.647 82.470 82.656 82.860 83.093 83.158 83.209 81.680 81.945 D1 D2 D3 D4 D5 D6 58.370 57.872 58.754 58.570 58.251 58.325 o................................................
VAPOR CONTAINHENT
-DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04'1633 82.3695 .2425 31.0792 31549 0 RTD RTD RID RTD ' RTD RTD RTD RID RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.174 81.003 81.229 80.136 82.282 83.410 84.949 83.185 80.136 83.009 RTD RID RID RTD RTD , RTD RTD RTD RID RTD Til T12 T13 T14 TIS T16 T17 T18 119 T20 82.884 82.661 82.498 82.684 82.907 83.283 83.107 83.316 81.699 82.001 DI D2 D3 D4 D5 DS , 58.790 57.973 58.108. 58.635' 58.412 58.451 VAPOR CONTAINMENT ;DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 -
- 04/04 1638 82.3717 .2415 31.0802 31549 0 RTD RTD RID RTD RTD ' RTD RTD RID RID RTD TI T2 T3 T4 T5 T6 T7 T8 T9 T10 80.287 80.927 81.266 80.174 82.282 83.373 85.024 83.147 80.174 83.018 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 TIS T16 T17 T18 T19 T20
' 02.935 82.675 82.521 82.633 82.916 83.204 83.181 83.246 81.699 81.950 D1 D2 D3 D4 D5 DG 58.987 58.070 57.950 58.441 58.057 58.709 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04 1643 82.3950 .2425 31.0792 31549 0 { 1 RTD RTD RTD RTD RTD RTD RTD RTD l RTD RTD T9 T10 l T1 T2 I3 T4 T5 T6 T7 T8 80.212 80.927 81.455 80.249 82.320 83.410 84.986 83.260 80.098 83.037 RTD RID RTD RTD .RTD RTD RTD RTD RTD RTD i Til T12 T13 T14 T15 ~T16 T17 T18 Tl9 T20 82.972 82.675 82.489 82.665 82.902 83.209 83.311 83.200 81.731 81.959 D2 D3 D4 D5 D6 l D1 58.745 i 58.029 58.554 58.273 58.441 58.157
;aaaaponna,a.ma..... ana.aananon=================== . VAPOR CONTAINMENT lDATE HOUR TEMP PRESSURE - . PRESSURE COUNT 1 COUNT 2 104/04 1648 82.3984 .2414 31.0823 31551 0 RTD RTD RTD RTD RTD' RID RTD RTD RID RTD T1 T2 T3 T4 T5 -
T6 T7 .T 8 T9 T10 80.212 80.965 81.379 80.287 82.320 83.485 85.024 83.297 80.136 82.981
- RTD RTD RTD RTD RTD ' RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.046 82.656 82.479 82.698 82.916 83.125 83.232 83.241 81.736 81.968
~ D1 D2 D3 D4 D5 D6 58.538 57.947 58.209 58.477 58.160 57.969 ..aan.aa.......................................... i VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 ~ COUNT 2 14/04 1653 82.4123 .2423 31.0814 31551 0 1 RTD RTD RTD RTD RTD RTD RTD 'RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.098 80.965 81.417 80.212 82.358 83.448 85.024 83.250 80.174 83.032
- RTD RTD RID RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS T16 T17 T18 Tl9 T20 82.935 82.693 82.507 82.698 83.014 83.325 83.241 83.357 81.750 81.996 D1 D2 D3 D4 D5 D6 58.670 58.270 58.212 58.638 57.998 58.134 j .................................................
VAPOR CONTAINMENT !) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 {l4/04 1658 82.4267 .2440 31.0816 31553 0 i RTD RTD RTD RTD RID RTD RTD RTD RTD RTD !T1 T2 T3 T4 T5 T6 T7 T8 83.260 T9 80.174 T10 83.065 l80.249 81.003 81.342 80.287 82.395 83.448 85.024 . ' RTD RTD RTD RTD RTD RTD RTD RTD RTD RID T11 T12 T13 T14 .T 15 * . . T16 T17' T18 T19 T20 '02.995 82.G98 82.521 82.712 *83.009 83.093 83.311 83.353 81.792 81.996 4
'Di ' D2 D3 D4 D5 DS 58.925 58.076 58.470 58.638' 58.354 59.006 ooooona........................................**
VAPOR - CONTAINHENT 2 DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04 1703 82.4203 .2421 31.0836 ' 31553 0 RTD RTD RID RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 19 T10 80.212 81.040 81.455 80.325 82.358 .83.523 85.061 83.297 80.174 83.042 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD Til- T12 T13 T14 TIS T16 T17 T18 T19 T20 83.046 82.707 82.512 82.707 82.963 82.977 83.134 83.302 81.759 81.996 D1 D2 D3 D4 D5 D6 58.800 58.015 57.986 58.606 58.192 58.590 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
!04/04 1708 82.4418 .2427 31.0830 31553 0
~
RTD RID RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5' T6 T7 T8 T9 T10 80.174 81.078 81.417 80.400 82.395 83.523 85.024 83.335 80.136 83.083 RID RTD RTD RTD RTD RTD RTD RTD RID RTD . T12 T13 T14 T15 T16 T17 T18 T19 T20 Til 83.004 82.730 82.549 82.707 82.916 83.269 83.213 83.288 81.773 81.996 D1 D2 D3 D4 D5 D6 58.699 57.847 58.176 58.541 58.418 58.942 f VAPOR CONTAINHENT
) ATE HOUR TEMP PRESSURE PRESSURE- COUNT 1 COUNT 2 )4/04 1713 82.4740 .2423 31.0834 31553 0 t
J. RID RTD RTD RTD RTD l RTD RTD RID RTD RTD - T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 l80.207 81.003 81.455 1 80.400 82.433 83.560 85.099 83.297 80.136 83.069 : RID RID RTD RTD RTD , RTD RTD RTD RID RID
,, . - . - - .-- ., n
Til T12 T13 T14 TIS . TI6 T17 T18 T19 T20 83.'028 82.772 82.568 82.716.' 83.004 83.409 83.316 83.316 81.834 82.015 DI D2 D3 D4- - DS D6 58.606 58.108 57.986 58.606, 58.483 58.687 _oeooano.......................................... VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE . PRESSURE COUNT 1 COUNT 2 04/04 1718 82.4632 .2425 31.0851 31555 0 RTD RTD RTD RTD RTD .. RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.212 81.040 81.455 80.325 82.395 83.560 85.136 83.335 80.098 83.074 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.004 82.744 82.568 82.763 83.065 83.251 83.186 83.427 81.792 82.024 D1 D2 D3 D4 D5 DG 58.832 57.300 58.018 58.738 58.192 58.622 4 ... .......................................... VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/04 1723 82.4709 .2444 31.0833 31555 0 RID RTD RTD RTD RTD . RTD RTD RTD RID RTD T1 T2 T3 T4 .T5 TS T7 T8 I9 T10 80.174 81.078 81.568 80.212 82.470 83.560 85.061 83.335 80.174 83.093 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 Tl8 T19 T20 83.032 82.706 82.577 82.749 83.004 83.209 83.297 83.330 81.848 82.043 DI D2 D3 D4 D5 D6 59.026 57.788 58.829 58.674 58.454 58.299 VAPOR CONTAINMENT iATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/04 1728 82.5135 .2436 31.0841 -31555 0 RTD RID RID RTD RTD- RID RTD' RTD RID RTD T1 T2 T3 T4 'T 5 T6 T7 T8 T9 T10
80.,2,12 ,8.1.078 81.530 80.362 .82.470 83.560 85.099 83.297 80.212 83.158 RTD RTD RID RTD RTDI RTD RTD RTD RID RTD T11 T12 T13 T14 ' TIS- T16 T17 T18 T19 T20 83.107 82.786 82.637 82.795 83.032 83.464 83.255 83.413 81.838 82.075 D1 D2 D3 D4 D5 D6 59.032 57.533 58.541 58.709 58.263 58.302 .oomaan........................................... VAPOR CONTAINHENT DATE HOUR TEMP PRESSURE PRESSURE , COUNT 1 COUNT 2 '04/04 1733 82.5169 .2445 31.0852 31557 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 .T5' T6 T7 T8 T9 T10 80.287 81.153 81.643 80.438 82.470 83.598 85.174 83.297 80.249 83.125 < RTD RTD RTD RTD RTD RTD RTD RTD RID RTD Til T12 T13 T14 TIS T16 T17 T18 T19 T20 83.055 82.795 82.619 82.805 83.009 83.195 83.344 83.320 81.838 82.117 DI D2 D3 D4 D5 D6 58.842 57.536 58.380 58.906 58.490 58.758 VAPOR CONTAINMENT LATE HOUR TEMP PRESSURE . PRESSURE COUNT 1 COUNT 2 14/04 1751 82.5428 .2445 31.0871 31559 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD 'TI T2 T3 T4 T5 T6 T7 T8 T9 T10 80.325 81.040 81.643 80.325 82.508 83.635 85.136 83.410 80.249 83.162 RTD RID RTD RTD RfD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.032 82.823 82.651 82.800 83.107 83.548 83.348 83.399 81.861 82.122 D1 D2 03 D4 D5 D6 58.800 58.011 58.696 58.706 58.322 58.683-VAPOR CONTAINHENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/04 1806 82.5915 .2441 31.0895 *31561 0
-e - -. -
~ '
RTD RTD RID RTD RTD' RTD RTD RID RID RTD Ti' 12 T3 T4 T5 T6 T7 T8 I9 T10 80.325 81.116 81.417 80.249 ~82.508 83.673 85.174 83.485 80.400 83.227 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD Til T12 T13 T14 T15 T16 T17 T18 T19 T20 83.227 82.884 82.656 82.884 83.148 83.655 83.469 83.436 81.931 82.191 DI D2 D3 D4 . D5 D6 58.861 58.000 58.722 58.699 58.477 58.163 ao............................................... VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04 1821 82.6190 .2430 31.0926 31563 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD TI T2 T3 T4 T5 T6 T7 T8 I9 T10 80.400 81.342 81.530 80.362;82.583 83.748 85.286 83.523 80.287 83.237 RTD RID RTD RTD JRTD RTD RTD RTD RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.032 82.898 82.712 82.907 83.186 83.539 83.455 83.464 81.992 82.215 D1 D2 D3 D4 D5 DS 58.793 57.488 58.596 58.599 58.444 58.002 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 04/04 1836 82.6833 .2454 31.0921 31565 0 i RID RID RTD RTD RTD RTD RTD RID RTD RTD T1 T2 T3 T4 T5 .T6 T7 T8 I9 T10
- 80.626 81.342 81.756 80.362 82.546 83.786 85.174 83.485 80.475 83.283 i RID RTD RTD RTD RTD Li RTD' RTD RTD RID RTD
. Til T12 T13 T14 T15 : T16 T17 T18 T19 T20 83.223 82.967 82.740 82.939 83.209 83.701 83.571 83.469 81.996 82.252 DI D2 D3 . D4 DS D6 58.825 57.782 59.239 58.764 58.541 58.002
- .o.....................................**........
VAPOR . CONTAINMENT
-) ATE HOUR TEllP PRESSURE PRESSURE COUNT 1 COUNT 2 14/04 1851 82.7211 .2454 31.0961 31569 0
3 . t
~
RTD RID RTD RTD . RTD , RTD RTD RTD RTD RTD TI T2 T3 T4 "T5 T6 T7 T8 I9 T10 80.400 81.229 81.756 80.588 82.658 83.823 85.324 83.5G0 80.475 83.348
^
RID RTD RTD RTD l RTD ,' RTD RTD RTD RTD RID T11 T12 T13 T14 ' TIS T16 T17 T18 T19 T20 83.316 82.986 82.823 83.023- 83.209 83.548 83.604 83.585 82.066 82.284 D1 D2 D3 D4. D5 D6 59.116 58.364 58.590 58.922 58.347 58.741 P VAPOR CONTAINHENT DATE HOUR TEMP PRESSURE.. PRESSURE COUNT 1 COUNT 2 04/04 1906 82.7642 .2487 31.0947 ' 31571 0 RTD RID RID RTD RTD RTD RTD RTD RID RTD T1 T2 I3 T4 T5 T6 T7 T8 I9 T10 80.551 81.342 81.756 80.626 ' 82.696 83.861 85.399 83.673 80.475 83.357 RTD RID RTD RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS T16 Tl7 T18 T19 T20 83.436 83.014 82.805 83.028 83.320 83.664 83.520 83.627 82.071 82.312 DI D2 D3 D4 DS D6 59.213 50.037 59.784 58.987 58.506 58.741 VAPDR CONTAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1 14 / 0 4 1921 82.7990 .2469 31.0985 31573 0 RID RlD RID RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.626 81.417 81.718 80.664 82.734 83.936 85.436 83.673 80.513 83.418 RID RTD RID RTD RTD RTD RID RID RID RID T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.255 83.000 82.921 83.097 83.311 83.548 83.720 83.673 82.131 82.354 D1 D2 D3 D4 D5 DG 59.374 58.2G3 58.848 59.113 58.635 58.645 aoaaaa..........................................
9 VAP[1R ' CONTAINMENT
. . _ . . ~
JkTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04' 1936 82.8530 .2456 , 31.1019 i 31575 0 RTD' RTD RTD RTD 'RTD 5 RTD - RTD RTD RID RTD
'T1 T2 I3 T4 T5 T6* T7 T8 T9 T10 80.664 81.342 81.982 80.701 82.771 83.898 85.474 83.711 80.588 83.469 RTD RTD RTD RTD RTD .
RTD ' RTD RTD RTD RTD Til T12 T13 T14 T15 : T16 T17 T18 T19 T20 83.344 83.125 82.930 83.125,83.409 83.906 83.701 83.659 82.159 82.382 DI D2 D3 D4 DS 'D6 58.919 58.296 58.716 58.854 58.470 '58.900 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE ~ PRESSURE COUNT 1 COUNT 2 34/04 1951 82.8695 .2450 31.1064 31579 0 !RTD RTD RTD RTD RID RTD RTD RTD RID RTD lT I T2 T3 T4 T5 T6 T7 T8 T9 T10 !80.739 81.379 81.982 80.626 82.809 83.973 85.474 83.748 80.551 83.497 RTD RID RID RTD RTD RTD RTD RTD RID RTD !T11 T12 T13 T14 TIS ' T16 T17 T18 T19 T20 (83.492 83.167 82.972 83.102. 83.390 83.720 83.580 83.683 82.210 82.484 D1 D2 D3 D4 DS 'D6 59.100 58.460 58.787 58.664 58.412 58.842 VAPOR CONTAINMENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/04 2006 82.9523 .2471 31.10G2 31581 0 RTD RTD RTD RTD RTD - RTD RTD RTD RID RTD T1 T2 13 T4 T5 T6 T7 T8 T9 T10 80.890 81.492 82.019 80.890 82.846 84.086 85.624 83.786 80.701 83.511 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS TIS T17 T18 T19 T20 83.539 83.186 83.018 83.181 83.511 83.780 83.827 83.794 82.247 82.479 D1 D2 D3 D4 DS DG 59.600 58.070 59.332 58.858 . 58.635 58.641
~
--e-- ,mn,, - - - - ,,,__.._,n_, _ _
VAPOR CONTAINMENT , DATE HDUR TEMP PRESSURE -PRESSURE COUNT 1 COUNT 2 04/04 2021 82.9828 .2469 31.1084 31583 0 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 .T5 T6 T7 T8 T9 T10 80.852 81.605 82.057 80.852. 82.922 84.086 85.586 83.861 80.701 83.571 RTD RTD RTD RTD RTD ' RTD RTD RTD RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.580 83.213 83.032 83.241' 83.520 83.887 83.720 83.790 82.275 82.572 D1 D2 D3 D4 D5 DS 59.342 58.457 58.460 59.177 58.829 59.226 VAPOR CONTAINHENT DATE HOUR TEMP PRESSURE PRESSURE . COUNT 1 COUNT 2
,04/04 2036 83.0043 .2469 31.1124 31587 0 RTD RTD RID RTD RID RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.814 81.568 81.982 80.890 82.959 84.124 85.699 83.861 80.739 83.590 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 T15 T16 T17 T18 T19 T20 83.622 83.278 83.079 83.278 83.553 83.794 83.743 83.859 82.317 82.600 D1 D2 D3 D4 DS DG 59.310 58.263 58.845 59.084 58.380 58.874 VAPOR CONTAINMENT ) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 34/04 2051 83.0624 .2480 31.1132 31589 0 l
- RTD RTD RID RTD RTD RTD RTD RTD RTD RID T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.040 81.643 82.094 80.927 82.959 84.161 85.699 83.898 80.701 83.641 RTD RTD RID RTD RTD . RTD RTD RTD RTD RfD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 83.604 83.311 83.121 83.339 83.622 84.022 83.873 83.831 82.359 82.633 D1 D2 D3 D4 DS- DS 59.410 58.170 59.493 58.890 58.764 58.967 e
. s VAPOR - CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04 2106 83.0857 .2480 31.1153 31591 0 RID RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 '
. T 5 '- T6 T7 T8 T9 T10 80.777 81.605 82.094 80.852 82.997 84.236 85.736 83.973 80.814 83.706 RTD RTD RTD RTD RTD - RTD RTD RID RID RTD Til T12 T13 T14 T15 ' T16 T17 Tl8 T19 T20 83.752 83.371 83.190 83.423 83.608 83.836 83.841 83.957 82.410 82.656 D1 D2 D3 D4 D5 DG 59.339 58.490 59.329 58.984 58.567 58.900
..no ............................................
J VAPOR CONTAINMENT -) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/04 2121 83.1207 .2487 31.1166 31593 0 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.852 81.680 82.207 80.777 83.072 84.236 85.774 84.048 80.814 83.776 RTD RTD RTD RTD RTD RTD RID RTD RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 4 83.576 83.413 83.241 83.399 83.748 83.980 83.934 83.999 82.461 82.698 D1 D2 D3 04 DS D6 (59.271 50.551 59.326 59.203 58.661 58.703
.....n.......................**.................
l VAPOR CONTAINMENT ! ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/04 2136 83.1548 .2486 31.1206 31597 0
- RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T 5- T6 T7 T8 T9 T10 80.852 81.831 82.207 80.890 83.034 84.236 85.774 84.011 80.814 83.799 RTD RTD RTD RTD RTD C. RTD RTD RTD RTD RTD
.T11 T12 Tl3 T14 TIS a T16 T17 T18 T19 T20 !83.757 83.455 83.260 83.436 .83.692 84.013 83.831 84.087 82.461 82.763 lD1 D2 D3 D4 J' DS D6 .
RTD - .fMD RTD RTD RID RTD RTD JM RTD RTD RTD Til T12 T13 T14 .i TIS ? TI6 T17 84.979 84.696 T18 I19 T20 84.519 84.607 84.946 85.160 85.193 85.318 83.780 84.068 D1- - D2 D3 D4 ' DS DS 60.487 58.993 59.526 60.016 59.835 aconoce..............................****........59.523 VAPOR CONTAINMENT
- DATE HOUR TEMP PRESSURE ' PRESSURE COUNT 1 COUNT 2 04/05 0554 84.4831 .2571 31.1971 31683 0 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 'T 7 T8 T9 T10 82.282 83.185 83.523 82.282 84.349 85.624 87.159 85.361 82.170 85.025 RID RTD RTD RTD RTD RTD RTD RTD RID RTD Til T12 T13 T14 T15 T16 T17 T18 T19 T20 85.039 84.737 84.528 84.691 85.049 85.444 85.355 85.378 83.780 84,105 D1 D2 D3 D4 D5 DS 60.387 59.510 60.042 60.177 59.739 59.874 VAPOR CONTAINMENT
. ATE HOUR TEMP PRESSURE PRESSURE COUNTI COUNT 2 4/05 0609 84.5030 .2539 31.2024 31685 0
!RTD RTD RID RTD RTD RTD RTD RTD RID RID
- T 1 T2 13 T4 T5 T6 T7 T8 IS T10 32.320 83.034 03.711 82.433 84.386 85.586 87.196 85.399 82.245 85.058 ITD RTD RID RTD RTD RTD RID RTD RTD RTD fil T12 T13 T14 TIS T16 T17 T18 TI9 T20 35.086 84.737 84.551 84.742 85.058 85.378 85.323 85.239 83.813 84.143
)I D2 D3 D4 DS D6 10.129 59.606 59.071 60.016 59.897 59.903 .... ao..................*****............ ..**.
VAPOR CONTAINMENT TE IIOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/05 0624 84.5192 .2571 31.2012 31687 0 i
RTD R.TD RTD RTD RTD- RTD RTD RTD RID RTD T l' ' 'T 2 T3 T4 T 5 T6 T7 T8 T9 T10 82.320 83.034 83.598 ,82.245 84.461 85.661 87.309 85.436 82.207 85.132 RID RTD RTD RTD RTD RTD'- RTD RTD RID RTD T11 T12 T13 T14 T15 '. T16: T17 T18 T19 T20 85.049 84.793 84.612 84.709 85.035 85.369 85.369 35.444 83.836 84.189 D1 D2 D3 D4 DS DS 60.261 59.351 60.042 60.084 59.835 60.232 on.o.oa........................ ** .............. VAPOR . CONTAINMENT 9 ATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 04/05 0639 84.5632 .2581 31.2041 31691 0 RTD RID RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 I3 T4 T5 T6' T7 T8 T9 T10 82.320 83.185 83.823 82.395 ,84.499 85.699 87.271 85.474 82.282 85.104 RTD RID RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 Tl4 T15 T16 T17 T18 T19 T20 85.072 84.816 84.589 84.709 85.128 85.467 85.471 85.378 83.855 84.273 D1 D2 D3 D4 D5 D6 60.258 60.090 60.264 60.113 59.674 60.326 VAPOR CONTAINMENT ' ATE HOUR TEMP PRESSURE PRESSURE COUNTI COUNT 2
- 4/05 0654 84.6079 .2615 31.2027 31693 0 l
' RID RTD RTD RTD RTD RTD RTD RTD RTD RTD
- T 1 T2 I3 T4 T5 T6 T7 T8 I9 TIO l82.433 83.147 83.786 82.245 84.574 85.736 87.271 85.549 82.320 85.155 RTD RTD RTD RTD RTD RTD RTD RTD RID RID
!T11 T12 T13 T14 T15 T16 T17 T18 119 T20 85.244 84.844 84,658 84.835 85.151 85.467 85.509 85.504 83.878 84.240 ,D1 D2 D3 D4 D5 D6 l50.387 59.668 61.003 60.429 60.023 60.322 l.o.............................................. l VAPOR CONTAINMENT
- 1TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/05 0709 84.6449 .2582 ,31.2080 31695 0 i
RID RTD RID RTD RTD- RTD RTD RID RID T1 T2 T3 T4 '.RTD T5 7- T6 T7 T8 I9 T10 82.358 83.260 83.786 82.470 84.536 85.774 87.309 85.549 82.358 85.216 RTD RID RTD RID RTD' RTD RTD RTD RTD RTD Til T12 T13 T14 T15 ' T16 T17 T18 Il9 T20 85.244 84.900 84.696 84.844' 85.221 85.504 85.536 85.462 83.943 84.315 DI D2 D3 D4 D5 DG 60.835 58.632 60.290 60.203 60,148 60.126 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0724 84.6877 .2585 31.2097 31697 0 RTD RTD RID RTD RTD RTD RTD RID RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 82.54G 83.335 83.786 82.433 84.611 85.811 87.383 85.624 82.395 85.262 i RID RTD RTD RTD RID '. RTD RTD ' RID RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 85.193 84.960 84.742 84.886 85.253 85.318 85.708 85.634 83.989 84.328 D1 D2 D3 D4 DS D6 60.284 60.148 60.193 60.329 60.019 59.835 l ! VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0739 84.7342 .2601 31.2101 31699 0 RTD RID RID RTD RTD~ RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 ' 16 T7 T8 T9 T10 82.G21 83.335 83.973 82.470 84.649 85.849 87.496 85.661 82.500 85.286 RTD RTD RTD RTD RTD - RTD RTD RTD RID RTD Til TI2 113 T14 T15 - T16 T17 T18 T;9 T20 85.355 84.979 84.7G5 84.919 85.155 85.541 85.667 85.518 84.022 84.398 D1 D2 D3 D4 D5 DG 60.603 59.209 60.738 60.261 59.726 60.571 VAPOR CONTAINMENT
@ ATE.. HOUR TEMP PRESSURE . PRESSURE COUNT 1 COUNT 2 @4/05 0754 84.7577 .2594 0 31.2127 . 31701 0 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD TI T2 T3 T4 T5 T6- T7 T8 T9 T10 82.546 83.297 83.823 82.583 84.649 85.811 87.496 85.699 82.508 85.309 RID RTD RTD RTD
'RTD'N RTD - RTD RID RTD RTD T11 T12 T13 T14 T15 T16 - T17 T18 T19 T20 85.341. 85.011 84.793 85.002. 85,332 85.657 85.606 85.629 84.059 84.431 D1 D2 D3 D4- DS D6 60.377 60.048 60.348 60.293 59.887 60.474 .o...............................................
VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE . PRESSURE COUNT! COUNT 2 14/05 0809 84.7879 .2578 31.2162 31703 0
.I l RID RTD RTD RTD RTD' - RTD RTD RTD RTD RTD
'T1 T2 T3 T4 -T 5 T6 T7 T8 T9 T10 82.658 83.373 83.898 82.696 84.649 85.886 87.533 85.736 82.395 85.351 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 ,85.369 l 85.067 84.844 84.928 85.378 85.657 85.588 85.653 84.096 84.431 'DI D2 03 D4 DS D6 60.732 59.887 59.542 60.487 59.884 60.216 i VAPOR CONTAINMENT JATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/05 0824 84.8435 .2553 31.2227 31707 0 RID RTD RID RTD RTD RTD RTD RTD RID RTD TI T2 T3 T4 T5 T6 T7 T8 T9 T10 82.583 83.448 83.936 82.658 84.761 85.924 87.608 85.811 82.508 85.392
- RTD RTD RTD RTD RTD ' RTD RTD RTD RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 85.397 85.0G3 84.867 85.063 85.420 85.815 85.662 85.736 84.152 84.542 lD1 D2 D3 D4 DS D6 160.861 59.658 59.251 60.129 60.013 59.990 .
l________________________________________________ l L
4 l VAPOR ' CONTAINHENT i DATEL HOUR TEMP PRESSURE PRESSURE - COUNT 1 COUNT 2 104/05 0839 84.8750 .2582 - 31.2218 " 31709 0
. RTD s RTD RTD RTD RTD RTD RTD RTD RID RTD
' T'1 T2 T3- T4 T5 T6 T7 T8 I9 T10 , 82.658 83.373 84.086 82.583 84.836 85.998 87.570 85.886 82.546 85.439 RTD RTD RTD RTD RTD - RTD RTD RTD RTD RTD T11 T12 T13 T14 T 15 . 4 T16 T17 T18 TIS T20 ' 85.481 85.137 84.914 85.007 '85.434' 85.848 85.722 85.764 84.161 84.561 D1 D2 D3 D4 . ' D5' 'D6 60.764 59.661 60.155 60.193 60.045 60. 245 VAPOR . CONTAINMENT
- ) ATE HOUR . TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
-14 / 0 5 0054 84.9055 .2616 31.2204 31711. 0 - I e i RTD RTD RTD RTD RTD - RTD RTD RTD RID RTD cT 1 T2 T3 T4 T5 - T6 T7 T8 T9 T10 '82.696 83.373 84.011 82.771 84.761 86.036 87.720 85.811 82.621 85.457
- RID RTD RTD RTD RTD RTD RTD RTD RTD RTD
'T11 T12 T13 T14 - T15 T16 T17 T18 I19 T20
- 85.555 85.160 84.951 85.044 85.411 85.769 85.848 85.838 84.217 84.570 I D1 D2 D3 D4 D5 D6 l60.761 59.887 60.829 60.l;80' 60. 60.406
- ...................................... 235 .........
l VAPOR CONTAINMENT RTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 i4/05 0909 84.9377 .2600 - 31.2240 31713 0 tTD RTD RTD RTD RTD - RTD RTD RTD RTD RTD I1 T2 13 T4 T5 T6 T7 T8 T9 T10 12.734 83.485 83.861 82.809 84.836 86.073 87.645 85.924 82.546 85.499 tTD RTD RTD RTD RTD i RTD RTD RTD RTD RTD
'11 T12 113 T14 T15 T16 T17 T18 Tl9 T20 15.513 85.193 85.016 85.132 85.481 85.857 85.783 85.890 84.250 84.635 11 D2 D3 D4 D5 D6 10.500 59.658 60.216 60.606 60.010 60.145 ._____=________..___...._________._._____.___.__
..~'
3' p . VAPOR ' CONTAINMENT DATE HOUR TEMP PRESSURE ; PRESSURE COUNT 1 COUNT 2
.04/05 0924 84.9749 .2597 . '31.2263 31715 0
~
RTD RTD RTD RTD ' RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 .T 5 T6 T7 T8 T9 T10 82.696 83.635 84.199 82.658 84,949 86.073 87.757 85.924 82.658 85.532 RTD RID RTD RTD RTD .. RTD . RTD RTD RTD RTD T11 T12 T13 T14 T15' T16 T17 T18 T19 T20 ,85.555 85.234 85.007 85.179 85.532 85.759 85.843 85.815 84.287 84.658 D1 D2 D3 D4 D5 DG 60.893 59.919 60.509 60.226 59.981 60.438 a................................................ VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE . PRESSURE COUNT 1 COUNT 2 04/05 0939 84.9983 .2613 31.2286 31719 0 RID RTD RTD RTD RTD RID RTD RTD RID RID ,T1 T2 I3 T4 T5 T6 T7 T8 T9 T10 l 82.771 83.598 83.936 82.696 84.949 86.111 87.720 85.998 82.734 85.536 RID RTD RID RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS T16 T17 -T18 Tl9 T20 85.564 85.267 85.063 85.225 85.564 85.922 85.820 85.996 84.305 84.677 D1 D2 D3 D4 D5 DG 60.696 59.916 60.858 60.348 60.426 60.532 i VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/05 0954 85.0505 .2613 31.2306 31721 0 l , RTD RID RTD RTD RTD ~ RTD RTD RTD RTD RID T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 82.009 83.523 84.274 82.734 84.986 86.186 87.720 85.961 82.696 85.592 , RTD RID RTD RTD RTD - RTD RTD RTD RTD RTD 'Til T12 113 T14 T15 T16 T17 T18 T19 T20 . 85.639 85.290 85.063 85.193 85.606 86.089 86.159 85.927 84.342 84.714 D1 D2 D3 04 D5 D6 60.G87 59.816 60.854 60.345' 60.232 60.529
. c. -
.o.......................... ...................
t.
.i VAPOR- CONTAINMENT.
DATE. . HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1009 85.0799 .2622 31.2317 31723 0 i RTD RID RTD RTD RTD$ RTD' RTD RTD RTD RTD T1 T2 T3 T4 T5' T6 .T7 T8 T9 T10 82.846 83.711 84.349 82.771 85.024 86.223 87.795 86.073 82.771 85.606 RTD RTD RTD RTD . RTD'. RTD RTD RTD RTD RTD Til - T12 T13 T14 .T15 i T16 T17 T18 Tl9 T20
-85.694 85.323 85.132 85.290: 85.615 85.764 85.955 85.922 84.398 84.784 DI D2 D3 - ' D4 D5 DG 60.819 59.652 61.177 60.374 60.290 60.529 VAPOR CONTAINMENT IATE HOUR TEMP PRESSURE -PRESSURE COUNT 1 COUNT 2
/4/05 '1024 85.1239 .2604 31.2374 31727 0 RID RID RTD RTD RTDk RTD RTD RTD RTD RID T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 82.884 83.711 84.424 82.771 '85.099 86.186 87~795 86.073 82.884 85.704 RTD RTD RTD RTD RTD ' RTD -RTD RTD RTD RTD T11 T12 T13 T14 T15 ' T16 T17 T18 T19 T20 85.667 85.392 85.183 85.327 85.671 85.903 85.950 86.010 84.421 84.853 D1 D2 D3 D4 . D5 D6 60.461 59.587 60.464 60.438 60.226 60.587
. O VAPOR CONTAINMENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/05 1039 85.1636 .2620 31.2378 31729 0 e
ITD RTD RTD RTD RTD. RTD RTD RTD RTD RTD I1 T2 T3 T4 T5 T6 T7 T8 T9 T10 33.072 83.711 84.161 82.959 85.136 86.261 87.870 86.073 82.884 85.718 iTD RTD RTD RTD RTD '- RTD RTD. RTD RTD RTD Ill TI2 T13 T14 TIS T16 T17 TI8 Tl9 T20 35.750 85.406 85.183 85.341 85.727 06.048 86.034 86.089 84.473 84.853
i D1 .D2 D3 D4 . . D5 D6 61*.138 ' 59.487 60.687 60.596- 60.190 l60.684 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 ' 04/05 1054 85.2008 .2619 . <31.2419 31733 0 RID RTD RID RTD -RTD RTD RTD RTD RTD RID Ii T2 T3 T4 T.5 T6 T7 T8 I9 T10 83.110 83.673 84.424 82.922 .85.174 86.373 87.982 86.148 82.922 85.741 RTD RID RTD RTD 'R TD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 - TIS T17 T18 T19 T20 85.746 85.467 85.225 85.276 85.713 86.182 86.182 86.010 84.528 84.886 D1 D2 D3 D4' D5 DG 61.070 59.968 60.393 60.919 60.093 59.874 VAPOR 'CONTAINHENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1109 85.2325 .2642 31.2415 31735 D RID RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 83.072 83.786 84.311 82.997 85.099 86.261 87.944 86.223 82.997 85.843 RTD RID RID RTD RTD-. RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 85.764 85.495 85.281 85.439 85.811 86.094 86.085 86.099 84.551 84.946 D1 D2 D3 D4 D5 DG 61.067 59.645 61.551 60.529 60.380 60.709 A VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1124 85.2735 .2641 31.2436- 31737 0 e RID RTD RTD RTD RTD - RTD ' RTD RTD RTD RID l' T8 T9 T10 T1 T2 T3 T4 T5 T6 T7 82.997 83.748 84.349 83.072 85.136 86.373 88.019 86.223 82.959 85.843 RID RTD RTD RTD RTD RTD RTD RTD RTD RID Til T12 113 T14 TIS . T16 T17 T18 T19 T20
85.,852 85.518 85.332 85.471' 85.876 86.247 86'.178 86.136 84.598 84.979
'- D6 D1 D2 D3 D4 60.777 60.322 61.389
- ooooooo..........................................
60.622.60.280 'D5 . 60.516 VAPOR '.-CONTAINMENT ' DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 85.2893 31.2431 1139 .264G 31737 0 RTD RTD RTD RTD RTD ' RTD RTD RTD RTD RTD T1 T2 T3 T4 . T 5 ,. T6 T7 T8 I9 T10 82.997 83.786 84.274 82.959 ,85.249 86.448 88.131 86.298 83.034 85.880 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T11 T12 T13 T14 115- T16 T17 T18 T19 T20 85.792 85.574 85.383 85.495 85.834 86.247 86.108 86.196 84.658 84,998 D1 D2 D3 D4 D5 DG 61.099 59.445 61.290 60.877 60.474 60.322 VAPOR CONTAINMENT 1 ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 !)4/05 1154 85.3512 .2659 31.2458 31741 0 RID RTD RID RTD RTD RTD RTD RTD RTD RTD T1 T2 I3 T4 T5 T6 T7 T8 T9 T10 ' 83.222 83.786 84.574 82.959 85.286 86.448 88.094 86.336 83.034 85.922 RTD RTD RTD RID RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 118 T19 T20 l85.927 85.611 85.402 85.555 85.890 86.261 86.312 86.164 84.654 85.035 D1 D2 D3 D4 D5 D6 61.028 60.187 61.737 60.777 60.535 60.509 l VAPOR CONTAINMENT 1 ATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 14/05 1209 85.3978 .2655 31.2482 31743 0 4 RTD RID RTD RTD RTD . RTD RTD RTD RID RTD T1 T2 I3 T4 T5 - T6 T7 T8 T9 T10 83.185 84.011 84.574 83.110 85.361 86.523 88.131 86.373 83.110 85.941
- l
RTD - .R:TD RTD RTD RI D .r. RTD' RTD RTD RTD RTD Til T12 T13 T14 T15 ' T16 T17 T18 T19 T20 85.987 85.555 85.378 85.588. 85.982 86.396 86.317 86.224 84.696 85.081 D1 D2 D3 D4 -D5 DG 61.093 59.929 61.509 60.777 60.403 60.832
.a.aaaa..........................................
VAPOR CONTAINMENT
- DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
- 04/05 1224 85.4157 .2621 31.2556 31747 0 P
RID RTD RID RTD RTD ' RTD RTD RTD RTD RTD T1 T2 T3 T4 .T 5 T6 T7 T8 T9 T10 , 83.297 84.011 84.311 83.072 85.361 86.485 88.206 86.410 83.185 85.992 RTD RTD RID RTD RTD RTD - RTD RTD RTD RTD T11 T12 T13 T14 ' TIS T16 T17 T18 T19 T20 85.969 85.685 85.476 85.601' 85.992 86.377 86.275 86.294 84.747 85.114 D1 D2 D3 D4 DS DG 61.064 60.026 60.516 60.713 60.567 60.348 own... .......................................... VAPOR CONTAINHENT JATE HOUR TEMP PRESSURE PRESSURE . COUNT 1 COUNT 2 04/05 1239 85.4577 .2629 31.2567 31749 0 RTD RTD RID RTD RTD RTD RTD RID RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 83.297 84.048 84.724 83.034 85.361 86.598 88.169 86.448 83.147 86.015 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD. T11 T12 T13 T14 TIS Tl6 ' T17 T18 119 T20 86.010 85.699 85.462 85.676 85.973 86.284 86.470 86.284 84.756 85.160 DI D2 D3 D4 DS DG 61.161 60.577 60.742 60.584' 60.600 60.867 t VAPOR .CONTAINHENT ' nATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
'4/05 1254 85.4996 .2630 . 31.2585 31751 0 RID RTD RID RTD RTD RTD RTD RTD RID RTD
T1 T2 I3 T4 T5 T6 T7 T8 I9 T10 83.'185 .84.124 84.574 83.297, 85.436 86.598 88.281 86.485 83.222 86.080 RTD RID RID RTD RTD RTD ' RTD RTD RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 86.085 85.732 85.527 85.671 , 86.057 86.456 86.363 86.322 84.807 85.216 D1 D2 D3 D4 ' DS DG 67.C37 60.190 60.580 60,780 60.667 60.448 ono.a............................................
. u VAPOR CONTAINMENT -
DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1309 85.5440 .2672 31.2564 31753 0 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 I9 T10 83.335 84.086 84.686 83.373 85.511 86.560 88.243 86.485 83.260 86.099 RTD RTD RTD RTD RTD., RTD RTD .RTD RTD RTD T11 T12 T13 T14 T15 TI6 T17' T18 TI9 T20 86.140 85.764 85.564 85.746 86.057 86.503 86.433 86.387 84.863 85.239 DI D2 D3 D4 D5 D6 61.290 59.739 61.802 60.970 60.696 60.767 l VAPOR CONTAINMENT IDATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 '04/05 1324 85.5710 .2657 31.2598 31755 0 RTD RID RTD RTD 'RTD RTD RTD RTD RTD RTD , T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 i 83.448 84.086 84.724 83.260 85.474 86.710 88.243 86.560 83.260 86.071 i l RID RTD RID RTD ' 'RTD RTD RTD RTD RID RTD l T11 T12 113 T14 115 T16 T17 T18 T19 T20 l 86.140 85.815 85.601 85.755 86.052 86.577 86.531 86.470 84.867 85.304 D1 D2 D3 D4 . DS D6 59.797 61.509 l ................................................. 61.319 60.838- 60.596 60.700 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1339 85.6174 .2G67 31.2608 '31757- 0
RID RTD RTD RTD RTD . RTD RTD RTD RID RTD
-T 1 T? T3 T4 T5- T6 T7 ~T8 T9 T10 83.485 84.236 84.836 83.373 85.511 BG.710 88.430 86.635 83.335 86.168 e
RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T!! T12 T13 T14 ' T15 - T16 T17 T18 TI9 T20 86.159 85.876 85.653 85.736 86.192 86.345 86.619 86.480 84.919 85.276 D1 D2 D3 D4 D5 DS 60.932 59.990 61.541 60.999 60.822 ~ 60.829 a....n........................................... VAPOR . CONTAINMENT DATE HOUR TEMP PRESSURE . PRESSURE- COUNTI COUNT 2 04/05 1354 85.6247 .2661 , 31.2G34 31759 0 RID RTD RTD RTD RTD . RTD , RTD RTD RTD RTD T1 T2 T3 T4 .T5' T6 T7 T8 T9 T10 83.410 84.274 84.686 83.373 85.586 86.710 88.355 86.598 83.335 86.159 RTD RTD RTD RTD RTD . RID RTD RTD RID RTD T11 T12 T13 T14 T15 - T16 T17 T18 T19 T20 86.196 85.857 85.643 85.806 86.122 86.540 86.573 86.484 84,937 85.383 D1 D2 b3 04 . D5 DS 59.893 61.283 60.932 60.851 61.151 !.61.222 1 _________________________________________________ VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1409 85.6782 .2657 31.2658 31761 0 1 RTD RID RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 83.485 84.274 84.761 83.560 85.586 06.785 88.505 86.635 83.335 86.187 l RTD RTD RTD RTD RTD 1 RTD RTD RTD RTD RTD
- Til T12 T13 T14 TIS T16 T17 T18 T19 T20 86.257 85.931 85.671 85.862 86.247 86.419 86.721 86.498 84.998 85.388
, D1 D2 D3 D4 DS D6 60.703 60.280 61.409 60,900 60.819 60.635 VAPOR CONTAINMENT l) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
04/05- 1424 85.7126 .2666 ' 31.2669 31763 0 j ; s. RTD RID RTD RTD RTD ;.- RTD RTD RTD RID RID TI T2 T3 T4 T5" T6 T7 T8 I9 T10 83.485 84.386 04.799 83.523 85.661 86.822 88.542 86.710 83.448 86.219 RTD RTD RTD RID RTD '. RTD RTD RTD RID RTD T11 T12 T13 T14 !T15 T16 T17 T18 T19 T20 86.261 85.913 85.722 85.820 .86.247 86.693 86.670 86.614 85.035 85.425 D1 D2 D3 Do - D5 D6 61.447 60.023 61.734 60.838 60.722 60.732 o................................................ VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNTI COUNT 2 04/05 1439 85.7726 .2664 31.2691 31765 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 I9 T10 83.711 84.311 84.949 83.448 85.699 86.897 88.542 86.785 83.448 86.308 RID RID RTD RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS T16 T17 T18 Il9 T20 86.303 85.969 85.801 85.917 86.312 86.689 86.814 86.624 85.072 85.476 DI D2 D3 D4 D5 DG 61.157 60.571 60.861 61.190 60.758 61.215 no............................................... l VAPOR CONTAINMENT
. DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 ' 04/05 1454 85.7739 .2644 31.2750 31769 0 i
RTD RTD RID RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 83.485 84.424 84.761 83.523 85.661 86.897 88.580 86.747 83.485 86.345 RTD RTD RID RTD RTD RTD RTD RTD RTD RTD l T11 T12 T13 T14 T15 T16 T17 T18 T19 T20
- 86.317 86.029 85.834 85.955 86.312 86.740 86.665 86.656 85.076 85.513 D1 D2 D3 D4 .D5 DG 61.480 60.574 60.700 60.935 60.819 60.671 9
e k
VAPOR ' ' CONTAINMENT ! DATE HOUR TEMP PRESSUREJ' PRESSURE.- COUNT 1 COUNT 2 04/05 1509 85.8031 .2672 31.2742 ' 31771 0 RTD RTD RID RTD RTD ) , RTD: 'RTD 'RTD RID RTD T1 T2 T3 T4 T5 TS T7 'T8 T9 110 83.485 84.424 85.061 83.523 85.736 86.860 88.617 86.822 83.523 86.340 RTD RTD RTD RTD RTD ' RTD ' RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 TI9 T20 86.391 86.034 85.801 85.941 86.350 86.689 86.717 86.679 85.132 85.569 D1 D2 D3
- D4 '. . D5 . D6 61.222 60.345 61.312 61.128 60.851 61.086 VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1524 85.8297 .2669 31.2744 31771 0 4
RTD RTD RTD RTD RTD - RTD RTD RTD RTD RTD TI T2 T3 T4 T5 T6 T7 T8 T9 T10 83.673 64.461 84.874 83.523 85.736 86.897 88.580 86.822 83.560 86.391 RTD RID RID RTD RTD RTD RTD RTD RID RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 26.415 86.052 85.843 85.987 86.359 86.707 86.721 86.777 85.165 85.611 D1 D2 D3 D4 DS DS 61.383 60.474 61.731 60.838 60.851 60.893 VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 )4/05 1539 85.8821 .2675 31.2759 31773 0 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 I9 T10 83.635 84.536 85.024 83.598 '85.811 86.935 88.617 86.822 83.635 86.419 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 Il9 T20 86.521 8G.066 85.852 86.075 '86.452 86.805 86.749 86.772 85.207 85.639 DI D2 D3 D4 D5 ' DG l 61.319 59.897 61.895 60.964 60.883 60.667 .a.a..a..........................................
S
VAPOR. CONTAINMENT ' ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/05 1554 85.9236 .2677 31.2796 31777 0 4 RTD i' RTD RTD RTD RTD RTD RTD ' RTD RTD RTD "I I T2 I3 T4 T51 T6 T7 T8 T9 T10 86.447
- 83.598 84.461 85.249 83.635 85.849 87.009 88.654 86.860 83.635 RTD .
RTD RTD RTD RTD !. RTD 'RTD RTD RTD RTD T11 .T12 T13 T14 T15 '. T16 : T17 T18 T19 T20 86.494 86.164 85.950 86.122 86.428 86.884 86.888 86.782 85.202 85.662
- D1 D2 D3 D4 D5 DS 61.512 60.251 61.476 61.157- 61.012 60.893 VAPOR CONTAINMENT ATE HOUR IEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/05 1609 05.9391 .2671 31.2822 31779 0 RTD RTD RTD RTD RTD ' RTD RTD RTD RID RTD T1 T2 I3 T4 T5 T6 T7 T8 I9 T10 83.748 84.386 85.249 83.598 85.811 87.084 88.766 86.972 83.673 86.480
'RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T11 T12 T13 T14 T15 ' T16 T17 T18 T19 T20
- 86.549 86.145 85.927 86.089 86.424 86.833 86.916 86.842 85.234 85.694
)DI D2 D3 D4 DS DG 61.447 60.316 61.412 61.096 60.790 60.861 VAPOR CONTAINHENT ATE HOUR TEMP PRESSURE. PRESSURE ' COUNT 1 COUNT 2 4/05 1624 86.0019 .2654 31.2858 31781 0
?
RTD RTD RTD RTD RTD .' RTD - RTD RTD RTD RID TI T2 T3 T4 T 5 T6 T7 T8 T9 T10 83.898 84.649 85.361 83.711 85.924 87.122 88.729 87.047 83.748 86.517 RTD RTD RTD RTD RTD 'i RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 86.531 86.229 85.982 86.126 86.484 86.819 86.953 86.856 85.286 85.741 D1 D2 D3 D4 DS DG
61.708 60.706 60.703- ' 61.193 6;0.916 60.445 coo.s _ _ _ _'_ _'.c o no p o o
- a p e w o ooo o w onocoma nooum on osomnaocu ma ,
s , e . VAPOR ' CONTAINMENTt DATE HOUR TEMP PRESSURE. . PRESSURE COUNT 1 COUNT 2
~04/05 1639 86.0099 .2677 ' 31.2855 31783 0 RTD -
RTD RTD RTD - RTD f RTD RTD RTD RTD RTD T1 T2 T3 T4 T5- T6* T7 T8 T9 110 83.898 84.611 85.099 83.635 86.036 87.084 88.804 '86.897 83.786 86.577 RTD RTD RTD RTD . RTD'- RTD RTD RID RTD RID Til T12 T13 T14 - T15 T16 T17 T18 TI9 T20 86.582 86.243 86.066 86.150 86.526 86.953 86.912 86.870 85.313 85.727 D1 D2 D3 D4 DS DS G1.870 60.835 61.541 60.999 60.951 61.054 aa.a.a........................................... VAPOR- CONTAINMENT-DATE HOUR TENP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 1654 86.0304 .2680 31.2872 31785 0 RID RID RTD RTD RTD '. RTD RTD RTD RTD RTD T1 T2 I3 T4 T5 T6 T7 T8 T9 T10 83.861 84.574 85.211 83.635 85.998 87.159 88.841 86.972 83.560 86.545 RTD RTD RTD RTD . RTD RTD RTD RTD RTD l RID T16 T17 T18 T19 T20 i T11 T12 T13 T14 T15 85.829 86.591 86.247 86.043 86.201 86.554 87.023 87.079 86.847 85.351 D1 D2 D3 D4 D5 DG 61.644 60.255 61.505 61.322 60.883 60.477 o.................................** .**......... VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE , PRESSURE COUNT 1 COUNT 2 t 04/05 1709 86.0801 .2706 31.2866 31787 0 RTD RTD RTD RTD RTD RTD RTD RID RTD RTD T1 T2 T3 T4 T5 l' T6 T7 T8 T9 T10 83.786 84.686 85.324 83.711 86.073 87.159 88.878 87.084 83.786 86.614 RTD RTD RTD RTD RTD 2. RTD . RTD RTD RID RTD Til T12 Tl3 T14 T15 " .T16 T17 ' T18 T19 T20
- 86.G61' 86.275 86.034 86.192 86.619' 87.042 87.255 86.902 05.397 85.825 l -
D1 ' D'2 D3 - D4 "- . D5 - D6 61.805 60.419 61.734 61.483 60.983 ' 61.380 ,
.oooooo..........................................
VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE.' PRESSURE ' COUNT 1 COUNT 2 .)4/05 1724 86.1128 .2678 31.2914 -
31789 0 e, - RTD RTD RTD RTDb RTD RTD RTD RTD RTD RTD TI T2 T3 T4 ' T5 T6 T7 T8 T9 T10 83.861 84.761 85.324 83.973 86.111 87.234 88.841 87.047 83.898 86.610 RTD RTD RTD RTD . RTD RTD RTD RTD RID RTD T12 T13 T14' T15 - T16 T17 T18 T19 T20 T11 86.684 86.336 86.103 86.215' 86.647 86.888 87.149 86.958 85.444 85.866 D1 D2 D3 . D4- '. D5 D6 60.519 60.677 61.383 61.196 61.115 61.219
.ooooon......................*******..... ***....
VAPOR CONTAINMENT HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
) ATE
.2703 .31.2908 31791 0
')4/05. 1739 86.1351 RTD RTD RTD RTD RTD RTD RTD RID RTD RTD T1 T2 T3 T4 T5- T6 T7 T8 T9 T10 85.286 83.861 '86.073 87.309 88.953 87.159 83.823 86.684 83.973 84.724
~
RTD" RTD RTD RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 T15 T16 T17 T18 Tl9 T20 86.182 86.275 86.656 86.907 87.107 86.958 85.420 85.871 86.712 86.363 D1 D2 D3 D4 D5 D6 61.712 60.999 61.834 61.357 61.212 61.157 VAPOR CONTAINMENT
- ) ATE TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 HOUR
)4/05 1754 8G.1521 .2685 31.2946 31793 0 RTD !". RTD RTD RTD RTD RTD RID RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 85.324 83.823 86.148 87.271 88.916 87.159 83.973 86.670 83.936 84.724
RID
' RID ,. RTD RTD RTD RID RTD RID RTD RTD T19 T20 T14 '. T 15 S i T16 { T17 , T18 T11'
- T12 T13 .
85.471 85.950 8G.340 86.140 86.266 '86.651.,87.619 87.163 '87.032 86.786 4
. .1 .
D3 D4 DS D6 D1 D2 . 61.512 ' 61.225.
~' 60,954 61.415 60.874 -60.548 a.oo.a ..........................................
y...
- a
- .g ,,
VAPOR , CONTAINMENT COUNT 1 . COUNT 2
-DATE HOUR TEMP PRESSURE.i. PRESSURE D 86.2241 .2685- -31.2966 31795
- 04/05 1809 RTD RTD RID RTD
^ RID RTD RTD :RTD E l.' RTD -
T10 RTD T4 T5~- T6 T7 T8 T9 T1 T2 T3 83.936 86.763 84.048 84.799 85.436 83.898 86.111 87.309 89.065 87.234 RTD RTD RTD RTD RTD RTD RTD R T D .. RTD' RTD T16 -
- T17 T18 T19 T20 T12 T13 T14 TIS i 85.987 Til 87.209 87.209 87.125 85.499 86.754. 86.410 86.229 86.382 86.740 DI D2 D3 D4 :- 'D5 .D6 .
60.322 61.447 61.196- 61.051 61.509 61.489 VAPOR . CONTAINMENT PRESSURE COUNT 1 . COUNT 2 DATE HOUR TEMP PRESSURE 31.2974 31797 0 04/05 1824 86.2452 .2697 1 RTD RTD RTD RTD RID RTD RTD RTD RTD T10 RTD T4 T55 T6 T7 T8 T9 T1 T2 T3 89.065 87.309 83.936 86.772 83.936 84.949 85.286 83.898 86.223 87.383 t RTD RTD RTD RTD RTD RTD RTD RTD ! RTD RTD T17 T18 T19 T20 T12 T13 T14 T15 - TIS 86.001 i T11 86.707 87.167 87.274 87.102 85.523 86.847 86.466 86.247 86.424 i D3 D4 D5 - DG l D1 D2 60.967 61.641 61.325 '60.893 61.348 61.776' l VAPOR CONTAINMENT l PRESSURE , PRESSURE COUNT 1 COUNT 2 HOUR TEMP 0 lDATE 86.2557 .2689 *31.3022 31801 04/05 1839 . RTD RTD RTD RTD RTD RTD RTD RTD RTD HTD T8 T9 T10 T1 T2 T3 T4 T5"' T6 , T7
89.028 .87.309 83.936 86.791 85.474 83.936 86.223 87.421 3.973 - 84.036 .. RTD RTD RID RTD RTD . RTD * , RTD RTD T20
- TD RTD
' TIS T16 T17 T18 TIS
. T12 T13 T14 ..
85.550 86.061
~11 86.419 86.754 87.009 87.237 87.130
- 6.884 86.466 86.252 D4 DS D6 D2 D3 11 61.319 61.354 61.309 61.351
;1.779 60.290 .oooooon........................................
9 VAPOR CONTAINMENT PRESSURE COUNT 1 COUNT 2 ITE HOUR TEMP PRESSURE 0 8G.2894 .2736 31.2994 i 31803 1/05 1854 RTD RTD RTD RID RTD RTD RTD RTD T10 ITD RTD
. T5 T6 T7 T8 T9 r1 T2 T3 T4 89.102 87.271 84.048 86.823 84.911 85.399 84.011 86.298 87.421 33.973 RTD RTD RTD RTD RTD RTD RTD RTD
.1TD RTD < T17 T18 T19 T20 T13 T14 T15 . T16 T11 T12 87.102 87.181 87.204 85.588 86.061 , 86.517 86.317 86.489 86.809 i36.851 D4 D5 D6 -01 D2 D3 62.768 61.422 61.344 . 61.512 51.779 60.713 VAPOR CONTAINMENT PRESSURE COUNT 1 COUNT 2 ATE HOUR TEMP PRESSURE 0 86.3461 .2709 31.3041
- 31805
-4/05 1909 RTD RTD RTD RTD RTD RID RTD
- RTD RID RTD T7 T8 T9 T10 T2 T3 T4 T5 T6 84.086 86.819
- T 1 86.261 87.421 89.102 87.346 i84.086 85.061 85.511 84.086 RTD RID RTD RTD RTD RTD RTD RTD RTD RTD Tf7 T18 T19 T20 T13 T14 TIS T16 86.103 Til T12 87.381 87.492 87.190 85.639 86.540 8G.289 86.452 86.921 86.902 D4 DS 'D6 02 D3 D1 61.802 61.454 61.212 61.512 ,
61.557 60.841 i,.....o............................** ........... VAPOR CONTAINMENT COUNT 1 COUNT 2 TEMP PRESSURE PRESSURE .) ATE HOUR 31807 0 14/05 1924 8G.3646 .2685 31.3085 e a r - , . - . . - , _ _ _ _ _ . - _ _ . . _ _ . _ . _ _ , , . .
RTD RTD RTD RID RTD RTD" RTD RTD ' T1 RTb T2 T3 T4 'T5'k.*RTD- ' T6 87.496 89.140 T7 T8 87.309 T9 84.086 T10 86.856 84.161 84.949 85.511 84.274 .86.298 RTD RTD RTD
'RTD RTD RTD RTD ', :RTD Y RID RTD T18 T19 T20 T13 T14 ., T I S T16 T17 T11 T12 87.228 87.223 85.653 86.140 86.888' 86.614 86.373 86.494 '86.893 87.362 D4 D5 DS D1 'D2 D3 .
61.064 , 61.522 60.713 61.322 61.325 61.280 V VAPOR CONTAINMENT-PRESSURE COUNT 1 COUNT 2 IATE HOUR TEMP PRESSURE 0 86.3884 .2706 31.3083 31809 14/05 1939 RID RID RID RTD RTD RTD RTD RTD ' RTD RTD T4 T5 T6 T7 T8 T9 T10 T1 T2 T3 89.177 87.383 84.161 86.902 84.274 84.836 85.436 84.08G 86.336 87.496 RTD .RTD RTD RID RTD RTD RTD RTD RTD RTD TIS T19 T20 T13 T14 T15 T16 T17 Til T12 87.423 87.399 87.307 85.704 86.108 86.953 86.600 86.424 86.517 86.958 D3 D4 D5 D6 D1 D2 60.619 61.483 61.586 61.280 61.483 !.61.750............................................... VAPOR CONTAINHENT PRESSURE COUNT 1 COUNT 2 I DATE HOUR TEMP PRESSURE 0 86.4169 .2698 31.3111 31811 04/05 1954 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T7 T8 T9 T10 T1 T2 T3 T4 T5 T6 86.963 86.410 87.645 89.214 87.421 84.048 84.161 85.024 85.586 84.124 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T17 T18 T19 T20 T12 T13 T14 'T15 T16 85.694 86.187 Til 86.540 86.916 87.399 87.288 87.242 8G.991 86.633 8G.447 l D4 D5 D6 l D1 02 D3 61.441 61.447 , 61.267 60.684 61.515 61.422 t o................................................ l_________________________________________________ VAPPR CONTAINMENT PRESSURE COUNT 1 COUNT 2 DATE HOUR TEMP PRESSURE 31813 0 04/05 2009 86.4741 .2702 31.3127 L
RTD - RTD RTD RTD (TD
- RTD RTD RTD 9'l RTD RTD '
T9 T10 r1 I2 T3 T4* 'T5 - T6 T7 T8 84.161 86.410 87.608 89.289 87.458 84.199 86.991 14.236 85.061 85.699 .
. RTD .,. . RTD RTD RTD RTD RTD ITD RID RTD RTD
*T15 T16 T17 T18 T19 T20 fil TI2 T13 T14. '
86.192 86.484 86.591 87.079 87.455 87.581 87.381 85.746
'36.912' 86.707 .
D2 D3 D4- - DS' D6 .
')1 ,
51.779 60.680 61.254 61.515' 61.277 ' 61.928
.aoaaaa.........................................
VAPOR CONTAINMENT PRESSURE PRESSURE COUNT 1 COUNT 2 iTE HOUR TEMP 1/05 2024 86.4999 .2718 31.3151 31817- 0 RTD RTD RTD 4 RTD RTD RTD RID RTD
- tTD RTD T8 T9 TIO T2 I3 T4 T5 T6 T7
- I I 84.236 86.485 87.608 89.252 87.533 84.311 87.019
'34.274 84.986 85.511 RTD RTD RTD RTD R!D RID
- tTD RTD RTD RTD T16 T17 T18 T19 T20 lIll T12 T13 T14 .T15 86.201 86.507 86.642 87.046 87.581 87.497 87.367 85.820 l37.079 86.744 D3 D4 D5 D6 11 D2
- 51.940 61.067 62.189 61.451 61.244 61.093 l........................................
i VAPOR CONTAINMENT PRESSURE COUNT 1 COUNT 2 STE HOUR TEMP PRESSURE
.2690 31.3198 31819 0 4/05 2039 86.5448 RTD RTD RTD RTD RID RID l lTD RID RTD RTD T2 T3 T4 T5 T6 T7 T8 I9 T10 I1 89.401 87.458 84.236 87.111 34.349 85.099 85.586 84.161 86.523 87.683 RTD. RID RTD RTD RTD RTD RTD RTD RTD RTD IIS T17 T18 Il9 T20 Til T12 T13 T14 T15 86.744 87.005 87.701 87.423 87.358 85.811 86.298 87.139 86.749 86.573 D2 D3 D4 D5 DS D1
'61.715 61.003 60.738 61.744 61.341 61.093 c
ATTACHMENT 3.35 ILRT AVERACE SENSOR DATA VAPOR CONTAINNENT' JnTE HOUR TEMP PRESSURE PRESSURE ; 34/03 0700 72.2779 .1905 30.6306 J4/03 0715 72.1721 .1902 30.6250 34/03 0730 72.1146 .1893 30.6200 - 34/03 0745 72.0955 .1888 30.6165 34/03 0800 72.0519 .1900 30.6134 J4/03 0815 72.0546 .1870 30.6144 14/03 0830 72.0446 .1901 30.6092 34/03 0845 72.0450 .1874 30.6100 ., 14 / 0 3 0900 72.0394 .1868 30.6106 14/03 0915 72.0593 .1892 30.6062 - 14 / 0 3 0930 72.0731 .1883 30.6071 14/03 0945 72.094? .1895 30.6059 14 / 0 3 1000 72.1209~ .1879 30.6075 , 14/03 1015 72.1593 .1893 30.6061 - 14/03 1030 72.1962 .1880 14 / 0 3 1045 30.6075 .a 72.2176 .1888 30.6066 .:? 14/03 1100 72.2434 .1885 30.6070 t'.
- J.:
14/03 1115 72.2697 .1899 30.6055 i!f. ;- 14/03 1130 72.3068 .1900 30.6054 ' 14/03 1145 72.3415 .1896 30.6058 .r. 14/03 1200 72.3437 .1909' * . . 14/03 30.6065 . 1215 72.3735 .1887 30.6087
'4/03 1230 72.4273 .1910 30.6064 '
4/03 1245 72.4343 .1898 - 30.6076 .- 4/03. 1300 72.4588 .1906 30.6068 - 4/03 1315 72.4966 .1909 30.6065 - 4/03 1330 72.5161 .1898 30.6076 4/03 1345 72.5577 . 1904 30.6089 - 4/03 1400 72.5713 t,.1912 30.6082 :4 - 4/03 1415 72.6056 * .1915 30.6079 . - .-" - 4/03 1430 72.6242 .1910 30.6084 :;?' 4/03 1445 72.6526
. l 4'
.1916 30.6078 ...:. -
4/03 1500 72.6778 .1921 30.6093 4- J : t..'."' 4/03 1515 72.7243 ~.1927 ' 4/03 1530 72.7443 30.6086 :$1 : ", -
.1925 30.6088 i- C' ' - 1 4/03 1545 72.7544 .1928 30.6085 GJ T 4/03 1600 72.8023 .1930 4/03 1615 72.8125 30.6103 ur/.'. . .
.1928 30.6085 T' 'J- -
4/03 1630 72.8216 .1934 30.6079 ,h.:. ' 4/03 1645
.t . , -
72.8623
.1928 30.6086 d...
4/03 1700 72.8847 .1924 30.6089 .p- ?- - 4/03 1715 72.9177 i.1943 30 . 6 09 0 :.4 . ' .. ". ' ' 4/03 1730 72.9199 '.1953 . 3 0 . 6 0 83 0 .. './." ,'
- 4/03 1745 72.9448 . S'; . '. -
1/03 1800
.1918 30.6115 72.9845 .1922 30.6111 "A,1 s. ,t"? ? . ;.~ ,'
4/03 1815 73.0032 .1935 1/03 1830 73.0178 .7,~' . . ,'.i ' K
.1936 30.6097;@}e3 0 . 6 0 9 8 4. Y i 4/03 1845 73.0437 .1948 30.6085 c.. 36 .'.
1/03 1900 73.0749 .1949 30.6 084 .' ' J'-?':.i -f".. .. 4/03 1915 J 73.0790 ' .1940 30.6093 4,:
- ./
4/03 1930 73.1145 v.1937 30.6096 ' 4/03 30.6061- ; 7.6 ; 36,,9. b..: . -'-O 1945 t. . 73.1355 . 1/03 2000 73.1535 0.: 1949 1953 30. 6064 ;;.].r. ,' j , !. 1/03 2003 73.1496 .1940 30.6054 , L' ;" rt;d, ' -
.9 :.. : ',l. 'i e
10A/03 .2010' 73.1585 .1942 30.6051 04/03 2011 73.1493 .1964 30.6030 04/03 '2012 73.1525 .1943 30.6031 .1* 94/03 2013 73.1510 .1942 30.6032 - J4/03 2030 73.1862 .1946 30.6008
- 04/03' 2031 73.1773 .1949 30.6005 ..
. 04/03 2045 73,1997 .1939 30.5996 04/03 2100 73.2239 .1949 30.5985 .y.-
04/03 2115 73.2513 .1954 30.5961 L , 04/03 2130 73.2615 .1967 30.5928 04/03 2145 73.6260 .1955 30.6137 04/03 2200 74.5989 . .1988 30.6520 04/03 2215 75.1709 .2014 30.6771 . 04/03 2231 75.5843
.2045 30.7017 04/03 2746 75.9443 .2040 30.7200 4 04/03 2300 76.2419 .2060 30.7338 _
04/03 2315 76.4840 .2067 30.7470 [". ,
~ 04/03 2330 76.6936 .2089 30.7587 +
04/03 2345 76.8935 .2129 30.7666 - 04/04 0000 77.0967 .2124 30.7809 -
. 34/04 0015 77.2695 .2133' 30.7899 - - ' , 04/04 0030 77.4463 .2128 30.8002 .;
4 34/04 0045 77.6062 .2145 30.8085 *
- 34/04 0100 77.7582 .2140 30.8169 ;
34/04 f. 1 0115 77.8833 .2157 30.8231 . . 34/04 0130 70.0166 .2150 30.8337
'J .
34/04 0145 78.1427 .2150 i,:. ' '
' 30.8416 34/04 34/04- 0215 0200 78.2826 .2171 30.8454 .. '..': .
i
'4/04 0230 78.3009 .2201 30.8503 .'P 78.4996 . 2207 30.8557 s 14/04 0245 78.6255 . 2195 30.8667 .
14/04 0300 78.7227 . 2193 30.8729 .;' - 14/04 0315 78.8325 . 2201 30.8800 f. 14/04 0330 78.9648 . 2221 30.8859 ... -
- 14/04 0345 79.0608 . 2209 30.8911 J.
14/04 0400 79.1571 . 2230 30.8970 '? . , 4/04 0415 79.2388 . . 2271 30.8987 .9.) .y. .. . .. 14/04 0430 79.3422 . 2232 30.9086 '.,i. '. -
!4/04 0445 79.4705 . 2259 30.9098 ..k;1 . .. . ; .
'4/04 0500 79.5193 . 2233 30.9204 .1'- -
+ 4/04 0515 79.6274 -
. 2276 30.9200 c,:
- 5.
4/04 0530 79.7055 .. . 2261 4/04 0545 79.8106 . 2263 30.9274,t..~ 1.f!. .Ji: 30.9312
.f . ,
4/04 0600 79.8981 . 2268 30.9367 .!.. .. ; 4/04 0615 79.9760 _ . . 2291 30.9402 . W . < -' ' 4/04 0630 80.1074. .':.2300- 30.9453 4/04 0645 80.1492: * %,
.-[, ..';..: ' .e <. ,-(c.
2266
- 30. 9527 . i 4/04 0700 80.2324~. ,.2303. 30.9549 .-
4/04 0715 80.3364 .,1;;.2290 3 1 4/04 0730 80.3953 . :'.2303 30.9621 30.9648IP.C. M; >l9...;;@,% J.-
- j. .:
4/04 0745 80.4922'. :.'.2327 30.9683 g...!.y.'h..,& s 4/04 0800 80.5642 '.' 2316 30.9754im...j e '. . ~ i 1' ' , 4/04 0815 80.6344..i - 2317 . . 30.9792 : '. c. 'r s' . 'U E : s 4/04 0830 80.7464 : . 2322 3 0 . 982 7 ' :, 9. ". 'J.: < ' . ,'. 4/04 80.7892':/;i.2338 0845 i 30.9890' 4 'I M .% ! 4/04 '0900 80.8899 : i. 2340 30.9927 .'y ' 3-y'.j:ld(. l'%: 'c%, 80.9215 :; ;:.2352 l '.' . 4/04;'0915 - 30.9955 4 .' ~ J. :- j 4/04 0930 81.0028'.U.2334 31.0013' t..' ii.%m,[, l 1/04 0945 81.0885 : j'{.2353 31. 0033 .5.! .f'?:'/. .'79 s W ;.. ,g$ .-'.
' i'. '
! 1/04 1000 81.1503 . 2362 . ti J
*; Q 1/04 1015 81.2304 ' ".2351' 31.0064Y.7 VD7'*:
31.0115 W4 .D '
- - - - - - . , - . - a-,,----r-m...e..,--,---n,- n- , , , , , . ,-,,,-n,,,,,-,_,,___.,_.c-- -- -
'04/04 1030 81.2997 .2393 31.0131 04/04 1045 01.3721 .2333 31.0212-04/04 -1100 81.4537- .2381 31.0223
.04/04 1115 81.5274 .2371 31.0272 3 ~)4/04 1130 81.6001 .2394 31.0289 -
04/04 1145 81.6506 .2366 31.0357 o 04/04 1200 81.7201 .2390 31.0372 04/04 -1215 81.8058 .2399 31.0443
.04/04 1230 81.8640 .2406 31.0455 04/04- 1245 81.9460 .2397 31.0523 04/04- 1300 82.0259 .2407 31.0533 04/04 1315 82.0430 .2391 31.0609 04/04 1330 82.1001 .2413 31.0626 04/04 1345 82.1812 .2417 31.0642 i
04/04 1400 82.2429 .2421 31.0678 34/04 1415 82.3190 .2418 31.0720
.34/04 1430 82.3541 .24'40 31.0738 34/04 1448 82.4G62 .2396 31.0821 i 34/04 1453 82.4720 .2411 31.0826 -
34/04 1458 82.4554 .2451 31.0786 34/04 1503 82.4380 .2422 31.0815 ' , 34/04 1508 82.4078 .2425 31.0792
)4/04 1513 82.3906 .2438 31.0780 14 /0 4 1518 82.3668 .2424 31.0793
, J4/04 1523 82.3393 .2436 31.0761 14 / 0 4 1528 82.3085 .2438 31.0740 14 / 0 4 1533 82.3152 .2427 31.0751 14/04 1538 82.2953 .2426 31.0752 i 14/04 1543 82.2966 .2455 31.0703
'4/04 1548 82.2754 .2436 31.0722 1 4/04 1553 82.2824 .2398 31.6760
'4/04 1558 82.2941 .2442 31.0716
- 4/04. 1603 82.2738 .2419 31.0759 4/04 1608 82.2896 .2434 31.0743 -
4/04 1613 82.2856 .2434 31.0743 . 4/04 1618 82.3303 .2421 31.0757 ' 4/04 1623 82.3417 .2460 31.0738
- 4/04 1628 82.3496 .2435 31.0763 .
l 4/04 1633 82.3695 .2425 31.0792 - 4/04 1638 82.3717 .2415 31.0002 ' 4/04 1643 82.3950 .2425 31.0792 - 4/04 1648 82.3984 .2414 31.0823 4/04 1653 82.4123 .2423 31.0814 , 4/04 1658 82.4267 .2440 31.0816 ! 4/04 1703 82.4203 .2421 31.0836 ' 4/04 1708 82.4418 .2427 31.0830 4/04 1713 82.4740 .2423 31.0834 . l 1/04 1718 82.4632 .2425 31.0851 1/04 1723 82.4709 .2444 31.0833 1/04 1728 82.5135 .2436 31.0841 '. I I/04 1733 82.5169 .2445 31.0852 '" ! :/04 1751 82.5428 .2445 31.0871 .- ' I/04 1806 82.5915 .2441 31.0895.~
./04 1821 82.6190 .2430 31.0926 ..
- /04 1836 82.6833 e .2454 31.0921 ;;. '
/04 1851 82.7211
.2454 31.0961 *: ."
./04 1906 82.7642 .2487 31.0947 - '
./ :
./04 1921 82.7990 .2469 31.0985 .
./04 1936 82.8530 .2456 .
/04 1951 31.1019 :i- -
82.8695 . 2450 31.1064 'l -
/04 2006 82.9523 .2471 31.1062
04/04 2021- U2.9828 .2469 31.1084 0'4/04 '2036 83.0043 .2469 31.1124~' 04/04 2051 83.0624 .2480 31.1132 14/04 2106 83.0857 .2480 31.1153
;4/04 2121 83.1207 .2487- 31.1166 04/04 2136 03.1548 .2486 31.1206
-04/04 2151 83.2021 .2521 31.1191 04/04 2206 83.2543 .2491 31.1241 04/04 2221 03.2549 .2466 31.1285 04/04 2236 03.3253 .2472 31.1319 04/04 2251 83.3619 .2481 31.1350 04/04 2306 83.3976 .2489 31.1361 04/04 2321 83.4349 .2485 31.1385 04/04 2336 83.4876 .2488 31.1402 04/04 2351 83.5056 .2523 31.1407 04/05 0006 83.5835 .2501 31.1448 04/05 0021 83.6020 .2512 31.1458 04/05 0036 83.6375 .2483 31.1525 34/05 0051 83.6992 .2508 31.1521 04/05 .0106 83.7348 .2520 31.1529 -
34/05 0121 83.7607 .2526 31.1561 - 94/05 0136 83.8129 .2532 31.1575 s 34/05 0151 83.8442 .2533 31.1594 - 34/05 0206 83.8871 .2553 31.1614 14/05 0221 83.9110 .2536 31.1651 - 34/05 0236 83.9665 .2539 31.1687 34/05 0251 83.9996 .2492 31.1754
]4/05 0306 84.0437 .2535 31.1731 34/05 0321 84.0635 .2537 31.1749 '
4/05 0339 84.1171 .2560 31.1766 i A/05 0354 84.1669 .2544 31.1801 14/05- 0409- 84.1939 .2586 31.1779
- 14 /0 5 0424 84.2584 .2580 31.1805 14/05 0439 84.2755 .2571 31.1833 14 / 0 5 0454 84.2892 .2564 31.1880 14/05 0509 84.3256 .2529 31.1935 24/05 0524 84.3994 .2570 31.1913 24/05 0539 84.4207 .2546 31.1957
- 4/05 0554 84.4831 .2571 31.1971 4/05 0609 84.5030 .2539 31.2024 h' 4/05 0624 84.5192 .2571 31.2012 -
+ 4/05 0639 84.5632 .2581 31.2041 ,
-4/05 0654 84.6079 .2615 31.2027 4/05 0709 84.6449 .2582 31.2080 4/05 0724 84.6877 .2585 31.2097 4/05
+ 0739 84.7342 .2601 31.2101 - - 4/05 0754 84.7577 .2594 31.2127 . 4/05 0809 84.7879 .2578 31.2162 4/05 l 0824 84.8435 .2553 31.2227 4/05 0839 84.8750 .2582 31.2218 . 1/05 0854 84.9055 .2616 31.2204 ,i - 4/05 0909 84.9377 .2600 31.2240 - t 1/05 0924 84.9749 .2527 31.2263 - i 4/05 0939 84.9983 .2613 31.2286 F t i/05 0954 85.0505 .2613 31.2306 -
./05 .1009 85.0799 .. 2622 31.2317 !,:
4/05 1024 85.1239 .2604 31.2374 "l
-l 1/05 1039 85.1636 .2620 31.2378 iT:;/e- r
.t 1/05 1054 85.2008 .:2619 31.2419 : i -
i 1/05 1109 85.2325 .2642 31.2415 ' - '
~ Q4/05 1124 .85.2735 .2641 31.2436 04/05' 1139 85.2893 .2646 31.2431
'04/05 1154 85.3512 .2659 31.2458 94/05 1209 85.3978 .2655 31.2482
~J4/05 1224 85.4157 .2621 31.2556 04/05 1239 85.4577 .2629 31.2567 04/05 1254 85.4996 .2630 31.2585 1
04/05 1309 85.5440 .2672 31.2564 04/05 1324 85.5710 .2657 31.2598 04/05 1339 85.6174 .2667 31.2608 04/05 1354 85.6247 .2661 31.2634 04/05 1409 85.6782 .2657 31.2658 04/05 1424 85.7126 .2666 31.2669 04/05- 1439 85.7724 .2664 31.2691 04/05 1454 85.7739 .2644 31.2750 04/05 1509 85.8031 .2672 31.2742
- 04/05 1524 85.8297 .2669 31.2744 04/05 1539 85.8821 .2675 31.2759 04/05 1554 85.9236 .2677 31.2796 04/05 1609 85.9391 .2671 31.2822 04/05 1624 86.0019 .2654 31.2858 04/05 1639 0G.0099 .2677 31.2855 4
34/05 1654 86.0304 . 2680 31.2872 34/05 1709 86.0801 . 2706 31.2866 34/05 1724 86.1128 . 2678 31.2914
, 34/05 1739 86.1351 . 2703 31.2908-34/05 1754 86.1521 . 2685 31.2946 34/05 1809 86.2241 . 2685 31.2966 34/05 1824 86.2452 . 2697 31.2974
'4/05 1839 86.2557 . 2689 31.3022
,4/05 1854 86.2894
. 2736 31.2994 14/05 1909 86.3461 . 2709 31.3041 14/05 1924 86.3646 . 2685 31.3085
.14/05 1939 86.3884 . 2706 31.3083 14/05 1954 86.4169. . 2698 31.3111 e ...
4/05 2009 86.4741 2702 31.3127 ..-; 4/05 20.24 86.4999
' * ' (
4/05 2039
. 2718 31.3151 9 :.d ., ; .4 86.5448 . 2690- 31.3198 .: ii., ' .
4/05 2054 86.5455
. . 2711 31.3217, . (;T .
4/05. 2109 86.6032 . . 2687 31.3261 "3 4/05 2124 8G.6526' . 2699 31.3289 'i?- -"'/ - 4/06 '1626 89.0820 .
. 2915 31.4457 .,. -
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-r-ewymp - . - - - -,,,,,w...,-: -a_,,, -,m,_, ..,--,,__.,,.-_,nn,,.. -,--m_,, _,_,-,.g,,n,, ,,_,,,gw_,,_, nw,--,
AMAGMENT 3.3C HJtT ABS 0WTE METHOD - MASS POINT ANALYSIS TEST RESULTS - CONT CONT LSF UPPER 4 VAPOR DEW ' COUNT' COUNT. AIR AIR LEAK CONF
.NE TEMP PRESS PT . s1 -
s2 PRESS NASS RATE LEVEL
- 036 542.704 0.2469 58.932 31587 00000 31.112 345448 0.00E+00 0.00E+00
. 051 542.762 0.2480 59.059 31589 00000 31.113 345420 0.00E+00 0.00E+00 , l 106 542.786 0.2480 59.049 31591 00000 31.115 345428 2.69E-01 0.00E+00 l
- 121 542.821 0.2487 59.132 31593 00000 31.117 345420 2.10E-01 6.02E-01 j 136 542.855 0.2486 59.119 31597' 00000 31.121 345443 2.53E-02 3.35E-01 151 542.902 -0.2521 59.513 31599. 00000 31.119 345396 1.58E-01 4.03E-01 1 206 542.954 0.2491 59.179 31601 .00000 31.124 345418 1.22E-01 2.91E-01 l 221 542.955 0.2466 58.900 31603 00000 31.129 345467 -1.69E-02 1.81E-01 ;
236 543.025 0.2472 58.967 31607' 00000 31.132 345459 -6.G8E-02 9.22E-02 l ! 251 543.062 0.2481 59.064 31611' 00000 31.135 345470 -1.05E-01 2.60E-02 306 543.098 0.2489 59.158. 31613. 00000 31.136 345460 -1.09E-01-3.00E-03 _ 321 543.135 0.2485 59.113 31615 200000 31.138 345463 -1.09E-01-2.25E-02 l 336 543.188 0.2488 59.139 31617' 00000 31.140 345449 -9.32E-02-1.86E-02 ) 351 543.206 0.2523 59.529 31621 00000 31.141 345443 -7.53E-02-9.22E-03 ! 6 543.284 0.2501 59.291 31623; 00000 31.145 345439 -5.91E-02 1.28E-04 21 543.302 0.2512 59.406 31625 00000 31.146 345437 -4.62E-02 6.98E-03 36 543.337 0.2483 59.092 31629 00000 31.153 345490 -6.50E-02-1.46E-02 51 543.399 0.2508 59.361 31631 00000 31.152' 345446 -5.56E-02-1.00E-02 106 543.435 0.2520 59.497 31633 00000 31.153 345432 -4.18E-02 1.15E-03 121 543.461 0.2526 59.570 31637 00000 31.156 345452 -3.91E-02-4.63E-04 136 543.513 0.2532 59.635 31639 00000 '31.158 345434 -3.01E-02 5.82E-03 151 543.544 0.2533 59.645 31641 00000 31.159 345435 -2.34E-02 9.86E-03
- ' 206 543.587 0.2553 59.858 31645 00000 31.161 345430 -1.66E-02 1.45E-02 i 221 543.611 0.2536 59.678 31647 00000 31.165 345455 -1.81E-02 1.04E-02 l '36 543.666 0.2539 59.707 31651 00000 31.169 345461 -2.05E-02 5.74E-03 i 251 543.700 0.2492 59.191 31653 00000.31.175 345513 -3.47E-02-6.76E-03 306 '543.744 0.2535 59.663 31655 00000 31.173 345460 -3.40E-02-8.13E-03 i 321' 543.764 0.2537 59.687 31657 00000 31.175 345467 -3.46E-02-1.06E-02 339 543.817 0.2560 59.935 31661 00000 31.177 345452 -3.18E-02-9.35E-03 354 543.867 0.2544 59.764 31663. 00000 31.180 345459 -3.07E-02-9.78E-03 109 543.894 0.2586 60.216 31665 f00000 31.178 345418 -2.26E-02-1.64E-03
+
124 543.958 0.2580 60.154 31667 00000 31.180 345405 -1.39E-02 7.48E-03 439 543.975 0.2571 60.059 31669 00000 31.183 345426 -9.74E-03 1.07E-02
- 454 543.989 0.2564 59.987 31673 00000 31.188 345468 -1.21E-02 7.25E-03 509 544.026 0.2529 59.601 31675 00000 31.193 345506 -1.91E-02 3.74E-04 i24 544.099 0.2570 60.049 31677 00000 31.191 345436 -1.61E-02 2.52E-03 i39 544.121 0.2546 59.786 31679 00000 31.196 345471 -1.76E-02 2.69E-05
.54 544.183 0.2571 60.064 31683 00000 31.197 345447 -1.62E-02 5.93E-04 109 544.203 0.2539 59.711 31685 00000 31.202 345492 -1.97E-02-3.41E-03 i L24 544.219 0.2571 60.054 31687 00000' 31.201 345469 -2.02E-02-4.80E-03
! L39 544.263 0.2581 60.166 31691 00000 31.204 345474 -2.11E-02-6.40E-03
- -54 544.308 0.2615
, 60.530 31693 00000 31.203 345430 -1.77E-02-3.37E-03 i
'09 544.345 0.2582 60.177 31695 00000 31.208 345464 -1.78E-02-4.11E-03
! 24 544.388 0.2585 60.209 31697 00000 31.210 345456 -1.71E-02-4.01E-03 1M) 544.434 0.2G01 60.380 31699 00000 31.210 345431 -1.44E-02-1.66E-03 60.304 31701' 00000 31.213 345445 -1.32E-02-9.09E-04 54 544.458 0.2594 i 09 544.488 0.2578 60.139 31703 00000 31.216 345465 -1.35E-02-1.74E-03 ! 24 544.544- 0.2553 59.864 31707' 00000 31.223 345502 -1.63E-02-4.72E-03 ' 39 544.575 0.2582 60.183 31709 00000 31.222 345471 -1.67E-02-5.56E-03 54 544.606 0.261G 60.548 31711' 00000 31.220 345436 -1.47E-02-3.86E-03 i 09 544.G38 0.2600 60.368 31713 00000 31.224 345456 -1.41E-02-3.73E-03 l 24 544.675 0.2597 60.336 31715 00000 31.226 345458 -1.37E-02-3.72E-03 , 2 SM) 544.658 0.2613 60.517 31719 00000 31.229 345468 -1.39E-02-4.29E-03 i '54 544.750 0.2613 60.509 .31721 00000'31.231 345458 -1.35E-02-4.22E-03 i TH) 544.700 0.2622 60.609 31723 00000 31.232 345450 -1.27E-02-3.73E-03
! ~024 544.824 0.2604 60'.418 31727 00000 31.237 345486 60.590 31729. 00000 " 31.238 345465 -1.38E-02-5.10E-03 039 54A.864 0.2G20 O'5'4 544.901 0.2619 60.575 31733. 00000 '31.242 345487 -1.47E-02-6.53E-03 -1.37E-02-5.33E-03~
109 544.932 0.2642 60.824 31735 00000 31.242 345463 1 124 544.973 0.2641 60.810 31737' 00000 '31.244 345460 -1.44E-02-6.51E-03 139 544.989 60.864 31737 00000 .31.243 345444 -1.40E-02-6.36E-03 i 0.2646 154 545.051 0.2659 60,999 .31741 00000 31.246 345435 -1.29E-02-5.47E-03 209 545.098 0.2655 60.956 31743 ~00000 J 31.248 345432 -1.15E-02-4.19E-03-1.01E-02-2.88E-03 224 545.116 0.2621 60.593 31747 00000 31.256 345502 -1.16E-02-4.45E-03
; 239 545.158 0.2629 60.686 '31749 00000. 31.257 345487 -1.24E-02-5.41E-03 i 254 545.200 0.2630 60.699 31751: 00000 31.259 345481 -1.29E-02-6.09E-03 1 309 545.244 0.2612 61.137 317531100000.31.256 345429 -1.14E-02-4.66E-03 t
324 545.271 0.2657 60.982 31755 00000 31.260 345450 -1.08E-02-4.21E-03 339 545.317 0.2667 61.083 31757 00000 31.261 345432 -9.57E-03-3.10E-03 354 545.325 0.2661 61.023 31759. 00000 '31.263 345456 -9.24E-03-2.94E-03 i 409 545.378 0.2657 60.979 31761[ 00000 31.266 345448 -8.68E-03-2.54E-03
- 424 545.413 0.2666 61.072 ~ 31763j 00000 31.267 345439 -7.86E-03-1.84E-03
! 439 545.472 0.2664 61.050 31765 '00000 .31.269 345425 -6.67E-03-7.06E-04 454 545.474 0.2644 60.839 31769; 00000 31.275 345490 -7.5tE-03-1.65E-03 4
309 545.503 0.2672 61.135 31771 00000 31.274 345462 -7.47E-03-1.76E-03 ! 524 545.530 0.2669 61.112 31771 00000 31.274 345448 -7.0lE-03-1.44E-03 i 539 545.582 0.2675 61.167 31773 00000 31.276 345431 -6.12E-03-6.22E-04
! 554 545.624 0.2677 61.190 31777. 00000 31.280 34544G -5.68E-03-3.14E-04
! 109 545.639 0.2671 61.128 31779 00000 31.282 345464 -5.76E-03-5.28E-04
'24 545.702 0.2654 60.954 H31781" 00000 31.286 345465 -5.84E-03-7.37E-04 139 545.710 0.2677 61.190 31783 00000 31.286 345457 -5.71E-03-7.29E-04
;54 545.730 0.2680 61.227 31785: 00000 31.287 345462 -5.70E-03-8.45E-04
'09 545.780 0.2706 61.489 31787 00000 31.287 345424 -4.80E-03 1.66E-05
] 12 4 545.813 0.2678 61.199 31789' 00000 31.291 345456 -4.70E-03
'39 545.835 0.2703 61.466 31791. 00000 31.291 4.36E-06 I 54 545.852 0.2685 61.274 31793 00000 31.295 .345436
-4.13E-03 4.88E-04 345467 -4.30E-03 2.15E-04 09' 545.924 0.2685 61.273 31795 00000 31.297 345443 -3.94E-03 24 545.945 0.2697 61.403 31797 00000 31.297 345438 -3.50E-03 8.52E-04 4.83E-04 39 545.956 0.2689 61.314 31801. 00000 31.302 345485 -4.03E-03 2.46E-04 54 545.989 0.2736 61.804 31803 00000 31.299 345433 -3.49E-03 09 546.046 0.2709 61.529 31805 00000 31.304 345448 -3.29E-03 7.26E-04 8.44E-04 24 546.065 0.2685 61.275 31807 00000 31.308 345485 -3.81E-03 2.63E-04 39 546.088 0.2706 61.496 31809 00000 31.308 345469 -3.98E-03 8.98E-06 54 546.117 0.2698 61.415 31811 00000 31.311 345481 -4.37E-03-4.46E-04 i 09 546.174 0.2702 61.451 31813 00000 31.313 345463 -4.39E-03-5.59E-04 i 24 54G.200 0.2718 61.619 31817 00000 31.315 345473 -4.59E-03-8.30E-04 j 39 546.245 0.2690 61.327 31819 00000 31.320 345497 -5.20E-03-1.47E-03
! < ALLOWABLE LEAK RATE : . 1102 l / OF NAX ALLOWA8LE LEAK RATE .08265
'RI EDUATION sG IS SATISFIED.
- 3RI EDUATION s7 IS SATISFIED r
i i l l i
-ww ,---e -mww---&-y--. ,yw,-,w-w----ww - --*,e - ~'
ATTACHMENT 3.3D
.. . VERIFICATION MASS POINT METROD PATA VAP0ii CONTAINMENT ,
~. HOUR TEMP PRESSURE. PRESSURE COUNT 1 COUNT 2 o, d6 0608 87.7869 .2795 31.3905 31901 0 1
!TD RTD RTD RTD RTD. RTD RTD. RTD RTD RTD , 1 T2 T3 T4 T5 TS T7 T8 I9 T10 '5.586 86.336 86.860 85.511- 87.757 88.878 90.595 88.878 85.624 88.343 !TD RTD RTD RTD RTD' RTD RTD- RTD RID RTD 11 1 T12 T13 T14 T15 T16 T17 T18 T19 T20 8.366 88.045 87.818 87.915 88.343 88.477 88.803 88.621 87.093 87.590 41 D2 D3 D4 D5 D6 i3.142 61.924 62.446 62.385 62.279 62.317 4.............................................. VAPOR CONTAINHENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 0609 87.7973 .2805 , 31.3894 31901 0 is RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T-2 T3 T4 T5 T6 T7 T8 T9 T10 'i.549 86.336 86.860 85.549 87.795 88.953 90.632 88.878 85.624 88.329
!ID RTD RTD RTD RTD RTD RTD RTD RTD RTD
- 11 T12 T13 T14 T15 T16 T17 T18 TIS T20
').333 88.027 87.808 87.906 88.273 88.691 88.830 88.677 87.102 87.604 it D2 D3 D4 D5 D6
!.759 61.341 62.797 62.388 62.243 62.739
! VAPOR CONTAINMENT
'E HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 '06 0624 87.8516 .2809 31.3911 31903 0 'D RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 i 699 86.373 86.972 85.474 87.795 88.990 90.632 88.916 85.661 88.380 RTD RTD RTD RTD RTD RTD RTD RTD RTD ii T12 T13 T14 TIS T16 T17 T18 T19 T20
' .431 88.087 87.846 87.980 88.394 88.826 88.830 88.700 87.121 87.646 D2 D3 D4 D5 D6
'.691 62.111 62.698 62.514 62.211 62.543
6.soon..mo.oo.non.......noueomoono. noon.........
.---sa-- .:-------------------------------------
J VAPOR CONTAINHENT 4TE . HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 A/06 0636 87.8619 .2827 31.3893 31903 0 l, RTD RTD RTD RTD RTD RTD RTD RTD 1TD RTD !T - 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 35.699 86.448 86.822 85.511 87.832 88.990 90.669 88.916. 85.549 88.375 RTD RTD RTD RTD RTD RTD RTD RTD ATD RTD T12 T13 T14 TIS T16 T17 T18 T19 T20 !T11 38.468 88.092 87.859 88.027 88.361 88.584 89.146 E8.747 87.116 87.650 01 D2 D3 D4 D5 D6
- 52.694 61.986 63.058 62.775 62.279 62.156.
- VAPOR CONTAINHENT HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
- RTE 87.8876 .2826- 31.3913 31905 0 (4/06 0642 fRTD RTD RTD RTD RTD RTD RTD RTD RID RTD iT l' T2 T3 T4 T5 T6 T7 T8 T9 T10 i85.661 86.448 87.084 85.661 87.870 88.990 90.706 88.953 85.549 88.375 RTD RTD RTD RTD RTD RTD RTD
- RTD RTD RTD T13 T14 T15 T16 T17 T18 T19 T20 iT11 T12 88.110 87.887 88.003 88.394 88.784- 88.988 88.728 87.135 87.683 iB8.449 D2 D3 D4 D5 D6 101
- 62.981 61.889 63.152 62.640 62.279 62.317 ja...............................................
i 4 . l VAPOR CONTAINHENT TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
! ATE HOUR
.2809 31.3930 31905 0
- 4/06 0643 87.9019 1
RTD RTD RTD RTD RTD RTD RTD RTD RTD lRTDT1 T2 T3 T4 T5 T6 T7 T8 T9 T10 87.309 85.661 87.832 88.953 90.744 88.990 85.624 88.398 699 86.410 RTD RTD RTD RTD RTD RTD 1RTD RTD RTD RTD T15 T16 T17 T18 T19 T20 !T11 Tl2 T13 T14 88.742 87.158 87.678 188.408 88.124 87.901 88.036. 88.338 88.817 88.961 , 4
- sv r.re-,,,-w ,m,,,----,..,-..m,,,,,.,,y..,..~....n,_.,e-- ,, -,,,----.,,---..e-- ,--.,w-.m,-me- - - ~ ~ _ , _,w-w.- -%-w .
- )! DR D3 D4 D5 D6 32.627. 61.986 62.411 62.643 62.408 62.768
.o00.o..........................................
VAPOR CONTAINNENT ITE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 0644 87.8742 .2805 31.3934 31905 0
- TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 I9 T10
- 5.624 86.410 87.009 85.624 87.832 88.990 90.744 88.953 85.624 88.394
- TD RTD RTD RTD RTD RTD RTD RTD RTD RTD
'11 T12 T13 T14 T15 T16 T17 T18 T19 T20 8.431 88.129 87.906 87.999 88.301 88.547 89.044. 88.779 87.163 87.706 al D2 D3 D4 D5 DS .2.888 61.499 62.669 62.514 62.437 62.382 oooeo..........................................
VAPOR CONTAINMENT
't HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 6 0645 87.8876 .2810 31.3929 31905 0
- TD RTD RTD RTD RTD RTD RTD RTD RTD RTD
, 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 5.736 86.336 87.047 85.624 87.870 89.028 90.669 88.990 85.661 88.398 'TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 TIS T16 T17 T18 T19 T20 8.445 88.129 87.887 87.999 88.343 88.677 89.026 88.812 87.167 87.669
- I D2 D3 D4 D5 DG l3.110 62.047 62.604 62.643 62.469 62.156
- 1. .............................................
VAPOR CONTAINHENT
- TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 0653 87.8991 .2797 31.3962 31907 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD T2 T3 T4 T5 T6 T7 T8 T9 T10 i 661 86.448 86.972 85.549 87.870 88.990 90.706 88.990 85.661 88.412 'D RTD RTD RTD RTD RTD RTD RTD RTD RTD
-T12 'T11 .T13 T14 T15 T16 T17 T18 T19 T20-
- 88.510 88.134 87.934 88.087 88.412 88.659 88.868 88.849 87.176 87.725 D1 .
D2 D3 ~ D4 ' D5 DS
.110 62.018 62.314 62.449 62.179 62.672 E
VAPOR - CONTAINMENT JATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 i4/06 0709 .87.8971 .2832 31.3967 31911 0
- RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD iT 1 T2 T3 T4 T5 T6 T7 T8 T9 T10
- 85.549 86.485 86.897 85.549 87.870 88.990 90.744 89.028 85.661 88.459 ,
- RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD ill! T12 T13 T14 TIS T16 T17 T18 T19 T20
!88.426 88.115 87.906 88.059 88.449 88.849 88.863 88.858 .87.176 87.734
- D1 D2 .
D3 D4 D5 D6
- 63.690 61.470 63.248 62.575 62.469 62.672 o.onoon.........................................
i VAPOR CONTAINMENT
- ATE HOUR TEMP PRESSURE . PRESSURE COUNT 1 COUNT 2
!4/06 0724 87.9658 .2816 31.4002 31913 0 i1TD RTD RTD RTD RTD RTD RTD RTD RTD RTD lT 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 l35.699 86.410 87.009 85.736 87.944 89.102 90.781 89.102 85.736 88.538 !!TD RTD RTD RTD RTD RTD RTD RTD RTD RTD lIII T12 T13 T14 T15 T16 T17 T18 T19 T20 18.468 88.166 88.017 88.171 88.515 88.686 88.979 88.896 87.255 87.771
- 11 D2 D3 D4 D5 D6 32.852 62.111 62.797 62.640 62.630 62.221 VAPOR CONTAINMENT MTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
{l/06 0739 88.0024 .2832 31.3986 31913 0 ' 'TD RTD RTD RTD RTD RTD RTD RTD RID RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10
'5.774' 86.5GO 87.234 85.774 87.944 89.102 90.818 89.102 85.736 88.528
$TD*' RT6 RTD RTD RTD RTD RTD RTD RTD RTD 311 T12 T13 T14 .
TIS T16 T17 T18 TI9 T20 M.524 88.194 88.008 88.161 88.552 88.691 89.007 88.951 87.293 87.804 p1 D2 D3 D4 D5 D6 62.888 61.534 62.991 62.836 62.372 62.614 3ao.oco......................................... 0_______________________________________________ VAPOR CONTAINMENT BTE HDUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 0/06 0754 88.0607 .2827 31.4011 31915 0 ITD RTD RTD RTD RTD RTD RTD RTD RTD RTD
*1 . T2 T3 T4 T5 T6 T7 T8 T9 T10 15.774 86.635 87.196 85.774 88.019 89.140 90.855 89.140 85.811 88.575 !TD RTD RTD RTD RTD RTD RTD RTD RTD RTD '11 T12 T13 T14 TIS T16 T17 T18 T19 T20
- 8.663 88.254 88.082 88.213 88.519 89.058 89.184 88.872 87.288 87.841 il D2 D3 D4 D5 DS 3.339 61.696 62.833 62.736 62.404 62.768 oooeoeo........................................
VAPOR CONTAINMENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 0809 88.0945 .2820 31.4018 31915 0
.TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 5.924 86.673 87.346 85.586 88.057 89.177 90.893 89.252 85.811 88.612
- TD RTD RTD RTD RTD RTD RTD RTD RTD RTD
- 11 T12 T13 T14 T15 T16 T17 Tl8 Tl9 T20 3.607 88.315 88.078 88.240 88.561 89.174 89.170 88.970 87.353 87.846 I D2 D3 D4 DS DG 2.917 61.563 63.020 62.575 62.272 62.540
..oaooo ............ ...........................
VAPOR CONTAINMENT HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
.J 0824 88.1077 .2849 31.4009 31917 0
- - - , - - . , . - , _ . , - - . , . - . ,,-..-n-- - - . - . . - , - . - -
ITD RTD RTD RTD RTD RTD RTD RTD RTD RTD ,f 1 T*2 T3 T4 T5 T6 T7 T8 T9 T10 35.924 86.673 87.234 85.774 88.094 89.140 90.967 89.140 85.924 88.612
> RTD RTD RTD RTD RTD RTD RTD RID RlD .111 T12 T13 T14 T15 T16 T17 T18 T19 T20
- 38.612 88.315 88.082 88.213 88.617 88.988 89.253 89.128 87.404 87.920 11 D2 D3 D4 DS D6 33.178 62.082 63.538 62.833 62.501 62.350
....oco.........................................
- VAPOR C NTAINMENT
- 1TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 0839 88.1433 .2800 31.4078 31919 0
,tTD RTD RTD RTD RTD RTD RTD RTD RTD RTD f1 T2 T3 T4 T5 T6 T7 T8 T9 T10 15.849 86.635 87.271 85.961 88.131 89.252 90.967 89.252 85.886 88.631
- tTD RTD RTD RTD RTD RTD RTD RTD RTD RTD
- fi t T12 T13 T14 T15 Tl6 T17 T18 T19 T20
- 18.710 88.352 88.148 88.324 88.724 89.123 89.105 88.942 87.423 87.901 i D2 D3 D4 DS D6
. 981 62.143 62.305 62.575 62.562 62.218 1.oo.............................................
VAPOR CONTAINMENT
)TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 0854 88.1682 .2828 31.4089 31923 0 tTD RTD RTD RTD RTD RTD RTD RTD RTD RTD '1 T2 T3 T4 T5 T6 T7 T8 I9 T10 16.036 86.710 87.271 85.774 88.169 89.289 91.005 89.326 85.886 88.700
- TD RTD RTD RTD RTD RTD RTD RTD RTD RTD
'11 T12 T13 T14 T15 T16 T17 T18 T19 T20 18.696 88.357 88.152 88.315 88.640 89.123 89.244 89.035 87.460 87.948 11 D2 D3 D4 D5 D6 i3.171 61.528 63.239 62.569 62.688 62.504 .oa.aaa.........................................
VAPOR CONTAINMENT iTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 0909 88.1979 .2860 31.4058 31923 0
TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5- T6 T7 T8 T9 T10 998 86.860 87.346 85.886 88.206 89.326 91.079 89.214 85.961 88.663 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD
.11 T12 T13 T14 T15 T16 T17 T18 T19 T20 8.765 88.445 88.171 88.278 88.812 89.091 89.207 89.030 87.483 87.971 1 D2 D3 D4 D5 DS 3.010 62.334 63.529 62.891 62.685 62.952 a.. noon........................................
VAPOR . CONTAINMENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 0924 88.2537 .2836 31.4121 31927 0 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 I3 T4 T5 T6 T7 T8 T9 T10 5.998 86.897 87.458 85.811 88.243 89.326 91.079 89.326 85.961 88.751 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 T15 T16 T17 T18 T19 T20 9.826 88.445 88.231 88.357 88.756 89.286 89.411 89.170 87.520 88.003 , D2 D3 D4 DS D6 3.071 61.750 62.881 62.823 62.785 62.952 oaoo ..........................................
VAPOR CONTAINMENT HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 iTE '/06 0939 88.2597 .2873 31.,4103 31929 0 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 86.822 87.458 85.886 88.281 89.364 91.154 89.326 85.998 88.728 l6.111 'TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 T15 T16 T17 T18 Tl9 T20 l8.803 88.463 . 88.240 88.319 88.812 89.063 89.486 89.170 87.576 88.045 1 D2 D3 D4 DS D6 . l3.232 61.686 63.944 63.016 62.524 62.791
- oo.............................................
l VAPOR CONTAINMENT 'TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
UO6 0954 88.2961 .2825 31.4171 31931 0 1 RTD RTD RTD RTD RTD RTD RTD RTD RTD
.i T2 T3 T4 T5 T6 T7 T8 T9 T10 36.036 86.935 87.309 85.924 88.243 89.438 91.154 89.364 86.111 88.798 1TD RTD RTD RTD RTD RTD RTD RTD RTD RTD III T12 T13 T14 T15 T16 T17 T18 T19 T20 18.840' 88.533 88.301 88.449 88.789 89.351 89.318 89.151 87.599 88.064 )1 D2 D3 D4 D5 DS i3.168 62.169 62.498 62.920 62.685 62.466 .co3.oc..................................** ....
VAPOR CONTAINMENT
- iTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 1009 88.3249 .2875 31.4121 31931 0
>TD RTD RTD RTD RTD RID RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10
-6.036 86.897 87.383 85.998 88.281 89.401 91.116 89.438 86.148 88.858 ' RTD RTD RTD RTD RTD RTD RTD RTD RTD T12 T13 T14 T15 TIS T17 T18 T19 T20
.8.909 88.556 88.310 88.459 88.835 89.216 89.448 89.235 87.599 88.120
.1 D2 D3 D4 D5 D6 3.361 61.589 64.041 62.884 62.714 63.174 .a.............................................. VAPOR CONTAINMENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 1024 88.3937 .2885 31.4131 31933 0 i TD RTD RTD RTD RTD RTD RTD RTD RTD RTD i1 T2 13 T4 T5 T6 T7 T8 T9 T10 5.148 87.009 87.421 86.111 88.318 89.476 91.228 89.513 86.148 88.937 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD
<11 T12 T13 T14 T15 T16 T17 T18 T19 T20 l3.928 88.598 88.389 88.580 88.896 89.351 89.430 89.276 87.678 88.134 1 D2 D3 D4 D5 DG
'64 61.911 63.583 63.271 . 62.681 63.529
...oo........................................
1
.. - VAPOR CONTAINMENT ITE HOUA TEMP PRESSURE PRESSURE COUNT! COUNT 2 1/06 1039 88.4176 .2839 31.4197 31935 0 ITD RTD RTD RTD RTD RTD RTD RTD RTD RTD I1 T2 T3 T4 15 T6 T7 T8 T9 T10 16.298 87.009 87.533 86.186 88.318 89.588 91.228 89.476 86.073 88.965 ITD RTD RTD RTD RTD RTD RTD RTD RTD RTD fil T12 T13 T14 TIS T16 T17 T18 T19 T20 19.007 88.621 88.417 88.515 88.974 89.202 89.421 89.337 87.683 88.157 11 D2 D3 D4 DS D6 13.229 62.424 62.810 63.045 62.553 62.305 saanoaa.......................n.................
VAPOR CONTAINMENT 'lTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 1054 88.4749 .2841 31.4215 31937 0 ITD RID RID RTD RTD RTD RTD RID RTD RTD
'I T2 T3 T4 T5 T6 T7 T8 T9 T10 298 87.084 87.645 86.186 88.430 89.588 91.303 89.513 86.148 88.988 (
S ITD RTD RTD RTD RTD RTD RTD RTD RTD RTD
'11 T12 T13 T14 T15 T16 T17 T18 T19 T20 19.049 88.659 88.431 88.603 88.970 89.569 89.551 89.276 87.715 88.194 11 D2 D3 D4 D5 DS i3.487 62.427 62.714 62.917 62.875 63.010 VAPOR CONTAINMENT iTE HOUR TEMP PRESSURE PRESSURE COUNTI COUNT 2
- i/06 1109 88.4501 .2849 31.4206 31937 0 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 6.298 87.047 87.496 86.111 88.318 89.588 91.303 89.550 86.186 88.951
- TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 T15 T16 T17 T18 T19 T20
" 030 88.696 88.473 88.542 89.026 89.337 89.509 89.318 07.762 88.236 1 D2 D3 D4 D5 DG 3.487 62.488 62.942 62.913 63.004 63.110 anoooo.........................................
VAPOR CONTAkNMENT
- HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/06 1124 88.4927 .2855 31.4201 31937 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 . T6 T7 T8 T9 T10 86.336 87.084 87.608 86.036 88.430 89.700 91.340 89.513 86.298 88.988 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T10 T19 T20 89.053 88.724 88.510 88.607 88.970 89.355 89.602 89.476 87.785 88.231 D1 D2 D3 D4 D5 D6 53.293 61.976 63.297 62.881 63.036 63.078 ooo..oo.........................................
VAPOR CONTAINMENT 1TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 1139 88.5219 .2835 31.4241 31939 0
,s RID RTD RTD RTD RTD RTD RTD RTD RTD I1 T2 T3 T4 T5 T6 T7 T8 T9 T10 16.298 87.122 87.608 86.073 88.468 89.662 91.414 89.625 86.298 89.030 1TD RTD RTD RTD RTD RTD RTD RTD RTD RTD r11 T12 T13 T14 T15 T16 T17 T18 T19 T20 19.105 88.719 88.482 88.686 89.072 89.518 89.653 89.309 87.790 88.287 11 D2 D3 D4 DS DS i3.484 61.847 62.617 62.978 62.807 62.694 .o....o.........................................
VAPOR CONTAINMENT 'iTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 1154 88.5783 .2854 31.4241 31941 0 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 2 T3 T4 T5 T6 T7 T8 T9 T10 .6.336 87.122 87.832 86.223 88.505 89.700 91.377 89.625 86.373 89.049 RTD RID RTD RTD RTD RTD RTD RTD RTD .. T12 T13 T14 T15 T16 T17 T18 T19 T20 9.100 88.789 88.524 88.677 89.077 89.588 89.894 89.458 87.859 88.329 1 D2 s 03 D4 D5 DS i
. . - ~_. - . . . - . .-- . . - - .
~63.168 62.105 63.039 63.045 62.681 63.142
- o.a.oooo..b....onoon............................
VAPOR CONTAINMENT
' ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
- 4/06 1209 88.5834 .2849 31.4266 31943 0
.RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD iT 1 T2 T3 14 T5 T6- T7 T8 T9- T10 . .86.261 87.084 87.645 86.373 88.505 89.700 91.414 89.662 86.373 89.086
- RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD
- T11 T12 T13 T14 T15 T16 T17 T18 T19 T20
.89.146 88.784 88.598 88.803 89.132 89.486 89.551 89.490 87.878 88,380 D1 D2 D3 D4 DS DG '63.616 62.073 63.071 62.913 63.036 62.820
- ....o..........................................
VAPOR CONTAINMENT l ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 !'*16 1224 88.6091 .2868 31.4267 31945 0 'RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 86.336 87.159 87.608 86.148 88.617 89.812 91.526 89.662 86.336 89.123 1TD RTD RID RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 39.221 88.840 88.621 88.738 89.114 89.527 89.792 89.499 87.901 88.357 31 D2 D3 D4 DS D6 l53.390 61.911 63.744 63.010 62.968 62.527 l................................................ l________________________________________________ VAPOR CONTAINMENT iTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 1239 88.6592 .2892 31.4263 31947 0 (TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 !.. 448 87.309 87.683 86.373 88.617 89.812 91.414 89.737 86.336 89.151 tTD RTD RTD RTD RTD RTD RTD RTD RTD RTD
'l l' T12 T13 T14 T15 T16 T17 T18 T19 T20 19.174 88.844 88.603 88.779 89.170 89.774 89.867 89.565 87.897 88.403 gw- - -- ,ee,- ,,,n~, --,,--,,-,--r ,- - - - - - - -- +,,,--r--e,,,- --n---w-- , ,- , - - - , --
31 D2 D3 D4 D5 DG 53.583 62.74G 63.777 63.297 63.004 62.978 cc.coce......................................... VAPOR CONTAINHENT ITE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 1254 88.6759 .2868 31.4307 31949 0 iTD RTD RTD RTD RTD RTD RTD RTD RTD RTD
~1 T2 T3 T4 T5 T6 T7 T8 I9 T10
,16.448 87.309 87.944 86.148 88.617 89.812 91.600 89.774 86.448 89.179
- TD RTD RTD RTD RID RTD RTD RTD RTD RTD 11 T12 T13 T14 TIS T16 T17 T18 T19 T20 s9.272 88.863 88.612 88.724 89.202 89.588 89.983 89.555 87.957 88.417 h1 D2 D3 D4 D5 D6
- 3.516 62.134 63.419 63.039 62.965 63.107 ooooo..........................................
VAPOR CONTAINMENT HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 1309 88.6900 .2847 31.4347 31951' 0
'TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10
- 3.44R 87.309 87.982 86.251 88.654 89.886 91.526 89.774 86.485 89.188 ID RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 TIS T16 T17 T18 T19 T20 r3.202 88.914 88.663 88.738 89.211 89.578 89.801 89.616 87.980 88.501
- I D2 D3 D4 D5 DG 1.416 62.710 62.227 63.229 63.223 63.261
.o... o........................................
VAPOR CONTAINMENT
'E HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 '06 1324 88.7040 .2860 31.4334 31951 0 RTD RID RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 .485 87.309 87.458 86.298 88.654 89.849 91.638 89.774 86.485 89.249
,D RTD RTD RTD RTD RTD RTD RTD RTD RTD
'11 T12 T13 T14 T35 T16 T17 T18 T19 T20
- 9.267' 09.561 88.765 88.S00 89.193 89.513 89.815 89.597 88.003 88.542 d D2 D3 D4 D5 DG
-394 62.482 63.384 62.939 62.962 63.004 ..aaoa..........................................
VAPOR C0it7AINMENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 1339 88.7570 .2869 31.4345 31953 0 -TD RID RTD RTD RTD RTD RID RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 6.523 87.383 87.645 36.448 88.692 89.923 91.563 89.849 86.523 89.300 'TD RTD RTD RTD RTD RTD RTD. RTD RTD RTD 11 T12 T13 T14 T15 T16 T17 T18 T19 T20
- 9.304 88.961 88.751 88.886- 89.276 89.616 89.927 89.695 88.050 88.580 31 D2 D3 D4 D5 D6
.3.767 62.414 63.638 63.000 62.929 62.646 .o.oee.........................................
VAPOR CONTAINMENT iTE HOUR TEtiP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 1354 88.8136 .2880 31.4334 31953 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD 'TD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10
- 6.598 87.383 87.982 86.410 88.804 89.886 91.712 89.961 86.598 89.314 RTD RTD RTD RTD RTD RTD RTD RTD RTD
'TD T12 T13 T14 T15 T16 T17 T18 T19 T20
.11 88.124 88.589
- 9.365 89.030 88.775 88.965 89.337 89.597 89.867 89.806
'1 D2 D3 D4 DS DG
- 3.348 63.252 63.638 63.065 63.055 63.097
.o.ono.........................................
VAPOR CONTAINMENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
-/06 1409 88.8441 .2913 31.4321 31955 0 l
RTD RTD RTD RTD RTD RTD RTD TD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 6.635 87.383 87.944 86.485 88.804 89.961 91.675 89.998 86.598 89.342
RTD .. R.TD RTD RTD RTD RTD RTD RTD RTD RTD Til T12 T13 T14 TIS T16 T17 T18 T19 T20 Co.439 89.035 88.840 88.979 89.355 89.667 89.959 89.783 08.129 88.659 bi D2 D3 D4 D5 D6 '53.574 62.643 64.798 63.126 63.116 62.900 oconooa......................................... VAPOR CONTAINMENT 1TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
- 1/06 1424 88.8497 .2889 31.4364 31957 0
.tTD RTD RTD RTD RTD RTD RTD RTD RTD RTD i1 T2 T3 T4 T5 T6 T7 T8 T9 T10 16.673 87.346 87.907 86.448 88.766 89.961 91.638 89.923 86.710 89.360
- tTD RTD RID RTD RTD RTD RTD RTD RTD RTD
'11 T12 T13 T14 T15 T16 T17 T18 T19 T20 fl9.355 89.067 88.854 89.002 89.346 89.987 89.839 89.792 88.166 88.663 11 D2 D3 D4 D5 D6
- 3.026 62.675 63.506 63.451 62.958 63.065
.aaa.aa.........................................
VAPOR CONTAINMENT TE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 l/06 1439 88.9083 .2871 31.4402 31959 0 TD RID RTD RTD RTD RTD RTD RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 6.673 87.458 87.982 86.560 88.878 90.035 91.824 89.923 86.635 89.421 lTD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 TIS T16 T17 T18 T19 T20 9.458 89.128 88.886 89.030 89.421 89.908 90.057 89.750 88.199 88.714 il D2 D3 D4 DS D6 l3.636 G2.514 62.991 63.258 63.310 63.290
....oa.........................................
VAPOR CONTAINMEl1T l HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 ' o6 1454 88.9174 .2857 31.4417 31959 0 l
RTD' RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 86.710 87.458 88.094 86.448 88.878 90.035 91.787 89.998 86.673 89.421
"'O RTD RTD RTD RTD RTD RTD RTD RTD RTD I T12 T13 T14 T15 T16 89.393 89.146 T17 T18 . T19 T20 88.923 88.993 89.495 89.964 90.066 89.792 88.236 88.733 D1 D2 D3 D4 D5 DG 64.028 62.063 62.543 63.258 62.962 63.326 ...oo.a..........................................
VAPOR CONTAINMENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/06 1509 83.9507 .2915 31.4378 31961 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 36.785 87.570 87.944 86.598 88.953 90.073 91.861 90.110 86.747 89.448 iTD RTD RTD RTD RTD RTD RTD T11 RTD RID RTD T12 T13 T14 T15 T16 T17 T18 T19 39.453 89.151 T20 88.928 89.077 89.472 89.834 90.062 89.839 88.259 88.765 11 D2 D3 D4 DS DS 928 62.968 63.831 63.448 63.155 63.934
- _f*********************I""*********************
VAPOR CONTAINMENT iTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
/06 1524 88.9753 .2906 31.4407 31963 0 l
TD RTD RTD RTD RTD RTD RTD ' RTD RTD RTD 1 T2 T3 T4 T5 T6 T7 T8 T9 T10 6.822 87.496 88.094 86.560 88.916 90.110 91.824 90.147 86.673 89.495 TD RTD RTD RTD RTD RTD RTD RTD RTD RTD 11 T12 T13 T14 T15 T16 T17 T18 T19 9.537 T20 89.197 88.965 89.067 89.518 89.978 90.006 89.825 88.273 88.807 1 D2 D3 D4 DS DS 3.767 62.775 63.860 63.545 63.120 62.871 VAPOR CONTAINMENT ,'E HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 l'06 i 1539 89.0159 .2885 31.4428 31963 0
OTD RTD RTD RTD RTD RTD RTD RTD RTD RTD R T2 T3 T4 T5 T6 T7 T8 T9 T10 822 87.570 88.281 86.635 89.028 90.147 91.824 90.222 86.785 89.499 GTD RTD RTD RTD RTD RTD RTD RTD RTD RTD U11 T12 T13 T14 TIS T16 T17 T18 T19 T20 09.583 89.193 88.974 89.086 89.583 89.890 90.164 89.894 88.268 88.793 D1 D2 D3 D4 D5 D6 - 33.706 62.063 63.'87 63.545 63.248 63.000 3a. ............................................ v----------------------------------------------- VAPOR CONTAINMENT BTE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 1/06 1554 89.0462 .2924 31.4409 31965 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD I1 T2 T3 T4 T5 T6 T7 T8 T9 T10 36.822 87.496 88.281 86.747 89.028 90.147 91.898 90.110 86.860 89.569 tTD RTD RTD RTD RTD RTD RTD RTD RTD RTD Ill T12 T13 T14 T15 T16 T17 T18 T19 T20 551 89.272 89.012 89.165 89.495 90.117 90.122 89.899 88.324 83.835
)1 D2 D3 D4 D5 D6 13.831 62.707 64.891 63.161 63.345 63.226 ............a...................................
I l l 9 l l
b ATTACHMENT 3.3E VERIFICATION MASS POINT TEST RESULTS
~
~HW$S POINT VERIFiCATI0f1 GROSS GROSS NET NET
" " C. MASS LSF 95% UCL SCFM LSF 95% UCL 009 345389 0.00E+00 0.00E+00 03.62 0.00E400 0.00E+00 024 345357 0.00E+00 0.00E+00 03.62 0.00E+00 0.00E+00 339 345414 -3.45E-01 0.00E+00 03.62 -4.58E-01 -1.13E-01 054 345398 -2.29E-01 7.35E-01 03.62 -3.42E-01 6.22E-01 109 345404 -1.95E-01 2.53E-01 03.62 -3.08E-01 1.40E-01 124 345371 -2.61E-02 3.11E-01 03.62 -1.39E-01 1.98E-01 139 345397 -4.00E-02 1.86E-01 03.62 -1.53E-01 7.25E-02 154 345361 3.96E-02 2.25E-01 03.62 -7.36E-02 1.12E-01.
209 345386 2.86E-02 1.69E-01 03.60 -8.43E-02 5.60E-02 224 345371 4.45E-02 1.56E-01 03.62 -6.85E-02 4.27E-02 239 345334 9.71E-02 2.03E-01 03.62 -1.59E-02 8.95E-02 254 345372 8.33E-02 1.71E-01 03.62 -2.98E-02 5.82E-02 309 345408 3.94E-02 1.26E 03.62 -7.37E-02 1.29E-02 324 345384 2.95E-02 1.04E-01 03.62 -8.36E-02 -9.29E-03 339 345363 3.71E-02 1.01E-01 03.62 -7.61E-02 -1.17E-02 354 345316 7.03E-02 1.36E-01 03.62 -4.28E-02 2.26E-02 109 345281 1.10E-01 1.81E-01 03.62 -2.77E-03 6.75E-02
a-
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_-_.1994 \ Ltm LSF
.2094 , , ,
2000 2400 40O 80O 1200 1600 TIME Attachment 3'.3F Graph 1 - Leakage Rate & UCL vs. Time, Mass' Point Analysis I
F
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- - - - 0 2
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'59.187 58.402 59.177 59.184 '.58.738 59.100
- acoaccenaanoon...aaaaaaaenomaanana.aaomaa.amannan ,
i .'
.: . . , ' i.. .i . . .,
VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE. PRESSURE COUNT 1 COUNT 2 04/04 2151 83.2021 .2521 31599 0
. 31.1191i. . :
RTD RTD RTD RTD RTD RTD RTD RTD R1D RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 80.852 81.869 82.057 80.890 83.,147 84.311 85.886 84.086 80.852 83.831 RTD . ' RID RTD RTD RID. RTD RTD RID RTD RTD T11 T12 T13 T14; " TIS - T16 T17 T18 T19 T20 83.803 83.469 83.274 83.506, 83.785 84.203 83.975 84.064 82.535 82.837 D1 D2 D3 3 'D4 ' I'i D5
. DG 59.313 58.593 60.655 59.1135t58.764 58.967
.ao ..a..........................................
. v.
- . ...m.-. .
VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/04 2206 83.2543 .2491 31.1241 31601 0 l it
- RTD RID RID RTD RTD RTD RTD RTD RID RTD T1 'T 2 I3 T4 T5 T6 T7 T8 T9 T10 81.040 81.906 82.207 81.040 83.185 84.349 85.699 .84.161 81.078 83.915
'RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD .T11 T12 T13 T14' T 15 4 T16- T17 T18 TI9 T20 83.864 83.460 83.306 83.576 83.794 84.059 84.073 84.143 82.568 82.823 'D1 D2 D3 D4
'.D5 D6
- 59.474 58.270 59.429 59'.145' 358.961 59.000
.aa.non............................**.......**... VAPOR CONTAINMENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/04 2221 83.2549 .2466 31.1285 31603 0 RTD RID RID RTD RTD RTD RTD RTD RTD RTD
- T 1 T2 T3 T4 T5 T6 T7 T8 T9 T10
- 31.040 81.869 82.282 81.116 83.222 84.349 85.924 84.086 81.003 83.864 ltTD '
RTD RTD RTD RTD - RTD RTD RTD RTD RTD
- T11 T12 T13 T14' T15"!U. T16 T17 T18 T19 T20 .
~33.743 83.543 83.348 83.515 83.701 84.180 84.087 84.036 82.605 82.888
m-RTD RTD RTD RTD - RTD RTD . RTD- RTD RID RID Til . T!2 T13 Tl4 TIS f T16 - T17 T18 T19 T20 83.971 83.641 83.474 83.711 83.966 84.403 84.180 84.296 82.777 82.986 DI D2 D3 . D4 DS D6 59.571 58.209 59.009 59.277' 59.058 59.290
.oe .o ..........................................
VAPOR CONTAINHENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/04 2321 83.4349 .2485., 31.1385 31615 0 e RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 .T 8 T9 T10 81.229 82.132 82.470 81.116 83.373 84.574 86.036 84.274 81.116 84.031 RTD RTD RTD RTD RTD - RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 N.. T16 T17 T18 T19 T20 83.966 83.729 83.543 83.683 83.938 84.315 84.347 84.291 82.763 83.018 D1 D2 D3 D4 D5 DG 59.571 58.499 59.042 59.148 59.151 59.190 oooooon.....................***.. ****** ....**** VAPOR CONTAINHENT 'DATE HOUR TEMP PRESSURE PRESSURE COUNTI COUNT 2 '04/04 2336 83.4876 .2488 ., 31.1402 31617 0 R ID RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 I3 T4 T5 T6 T7 I8 T9 TIO . 81.342 l 82.019 82.621 81.191 83.410 84.611 86.186 84.424 81.229 84.082 RTD RTD RTD RTD RTD RTD RTD RTD l RTD RTD Til TI2 T13 T14 ' TIS T16 T17 T18 TI9 T20 84.036 83.762 83.576 83.701 83.999 84.328 84.380 84.338 82.800 83.116 i DI D2 03 D4 DS D6 59.442 58.144 58.913 59.335 58.764 59.322 VAPOR CONTAINHENT 'DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 l04/04 2351 83.5056 .2523 31.1407 31621 0 RTD RTD RID RTD RTD - RTD RTD RTD RID RTD i T1 T2 I3 T4 T5 - .T6 T7 , T8 I9 TIO 1 l
s s 81.304 82.470 81.266 83.448 84.686 8G.148 84.349 81.229 84.115
- 82. 094 RTD RTD RTD RID ~
RTD . RTD . RTD RTD RTD RTD T11 T12 T13 T14 l T15 ' T16. T17 T18 T19 T20 84.157 83.725 83.571 83.762 84.045 84.431 84.315 84.301 82.837 83.121 D1 D2 D3 D4- D5 D6 59.542 58.464 60.361 59.306 59.055 58.900
..o no..........................................
VAPOR CONTAINHENT" DATE HOUR TENP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0006 83.5835 .2501 , 31.1448 , 31623 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.492 82.094 82.546 81.492 83.523 84.649 86.261 84.461 81.342 84.143 RTD RTD RTD RTD RTD 'I . RID RTD RTD RTD RTD Til . -T12 Tl3 T14 TIS
- T16 T17 T18 T19 T20 84.184 83.831 83.622 83.827 '84.171 84.519 84.352 84.440 82.893 83.200 DI D2 D3 D4 D5 D6 59.861 58.887 59.232 59.339 58.961 59.322
.a....a..........................................
VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 ' COUNT 2 14/05 0021 83.6020 .2512 31.1458 31625 0 l RTD RID RTD RTD 'RTD RTD RTD RTD RTD RTD
'T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.455 82.057 82.508 81.417 S3.523 84.761 86.336 84.461 81.342 84.175 RID RTD RID RTD RTD - RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 T16 T17 T18 T19 T20 84.184 83.864 83.687 83.808 84.208 84.551 84.421 84.556 82.911 83.232 D1- D2 D3 D4 DS D6 l59.861 58.173 59.558 59.403 59.087 59.448
.-=_--____.......---------_-------_------_____--- ,
VAPOR CONTAINHENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 44/05 0036 83.6375 .2483 31.1525 31629 0 l l l
)
RTD . R'TD RTD RTD ~ ; R T D *'. RTD RTD RTD RTD RTD T1 T2 T3 T4 ': T - 5' ' T6 T7 T8 T9 T10 81.304 82.207 82.583 ~81.605 ,83.560 84.686 86.223 84.574 81.342 84.217 RTD RTD RID RTD RTD .' RTD RTD RTD RID RTD Til T12 T13 T14 T15 : T16 T17 T18 Tl9 T20 84.152 83.924 83.752 83.934 .84.138 84.505 84.477 84.584 82.972 83.269 D1 D2 D3 D4' D5 DG 59.668 58.464 58.942 59.142 ' 59.184 59.255 VAPOR CONTAINHENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0051 83.6992 .2508 31.1521 31631 0 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.605 82.320 82.959 81.417 83.523 84.761 86.336 84.574 81.492 84.301 RID RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 112 T13 T14 T15 T16 T17 T18 T19 T20 84.268 83.980 83.752 84.003 84.231 84.338 84.426 84.617 82.995 83.311 D1 D2 D3 D4 D5 D6 59.700 58.464 59.297 59.561 59.087 59.029 VAPOR CONTAINHENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0106 83.7348 .2520 31.1529 31633 0 RTD RTD RTD RTD RTD RID RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.568 82.358 82.884 81.605 83.635 84.836 86.3&3 84.611 81.417 84.282 RID RTD RTD RTD RTD RTD RTD RID RTD RTD Til T12 T13 T14 T15 T16 T17 T18 Tl9 T20 84.310 83.999 83.790 83.961 84.305 84.617 84.510 84.579 83.018 83.385 D1 D2 D3 D4 D5 DG 59.923 58.919 59.845 59.335 59.664 59.255 i VAPDR CONIAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/05 0121 83.7607 .2526 31.1561 31637 0
i .. RTD RTD RTD RTD '- RTDMi- . RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.530 82.395 82.959 81.379 83.673 84.911 86.373 84.649 81.417 84.361 RTD RID RTD RTD RTD "- RTD ' RTD RTD RID RTD T11 T12 T13 T14 TIS ' T16 T17 T18 T19 T20 84.296 84.050 83.864 83.938 84.277 84.872 84.514 84.630 83.088 83.371 DI D2 D3 D4 D5 DG 59.926 59.274 59.877 59.464 58.958 59.448 VAPOR CONTAINMENT JATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/05 0136 83.8129 .2532 31.1575 31639 0 RTD RTD RTD RTD .RTD RTD RTD RTD RTD RID T1 T2 I3 T4 T5 T6 T7 T8 T9 T10 81.568 82.395 82.922 81.530 83.673 84.911 86.448 84.686 81.455 84.449 RTD RTD RTD RTD RTD RTD RTD RID RTD RTD Til T12 T13 T14 TIS T16 T17 T18 Tl9 T20 84.454 84.073 83.873 84.119 84.301 84.798 84.603 84.612 83.097 83.395 D1 D2 D3 D4 D5 DG 60.087 58.690 59.745 59.755 59.374 59.158 t................................................. l VAPOR CONTAINMENT 1 ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 4/05 0151 83.8442 .2533 31.1594 31641 0 RTD RTD RID RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.718 82.395 83.034 81.605 83.786 84,986 86.560 84.724 31.568 84.417 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T11 T12 T13 .T14 T15 T16 T17 T18 T19 T20 84.435 84,119 83.948 84.031 84.370 84.709 84.607 84.696 83.153 83.409 D1 D2 D3 D4 D5 DG 59.990 58.657 59.777 59.655 59.632 59.510
o a VAPOR l CONTAINMENT DATE
- HOUR TEMP PRESSURE' PRESSURE COUNT 1 COUNT 2 04/05 0206 83.8871 .2553 31.1614 31645 0 RTD RTD RID RTD RTD , RTD - RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 I9 T10 81.756 82.470 83.034 81.680 83.786 84.949 86.448 84.836 81.605 84.486 RTD RID RTD RTD RTD RID RTD RTD RTD RTD Til T12 T13 T14 . TIS T 16 - T17 T18 T19 T20 84.417 84.175 83.980 84.161 84.491 84,570 84.733, 84.691 83.176 83.534 DI D2 D3 D4 DS DG 60.148 58.751 60.290 59.784 59.500 59.510
- ....o.n..........................................
VAPOR CONTAINHENT .DATE Il0UR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0221 83.9110 .2536 '31.1651 31647 0 RTD RTD RTD RTD RTD RTD RTD RID RTD RID T1 T2 T3 T4 T5 T6 T7 I8 I9 T10 81.756 82.358 82.846 81.605 83.823 85.024 86.523 84.836 81.718 84.542 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD Til T12 T13 T14 T15 T16 T17 T18 T19 T20 84.445 84.175 83.999 84.143 84.496 84.937 84.812 84.802 83.241 83.520 D1 D2 D3 D4 D5 DG 59.923 58.880 60.161 59.523 59.306 59.442 l VAPOR CONTAINMENT l) ATE HOUR TEMP PRESSURE PRESSURE COUNTI COUNT 2
- 34/05 0236 83.9665 .2539 31.1687 31651 0
' RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T1 T2 T3 T4 . T5 T6 T7 T8 T9 T10 , 81.756 82.546 82.997 81.793 83.936 85.099 86.598 84.874 81.718 84.575 1 RTD RTD RTD RTD RTD . RTD RTD RTD RTD RTD ' Til T12 T13 T14 T15 T16 T17 Tl8 T19 T20 84.593 84.212 84.036 84.180 8l4.491 84.751 84.756 84.858 83.283 83.608 D1 D2 D3 D4 D5 D6
- 59.958 59.130 59.903 59.716 59.568 59.348 l...........................................**....
t
-VAPOR 'CONTAINHENT DATE HOUR TEMP PRESSURE ~. PRESSURE , COUNT 1 COUNT 2 04/05 0251 83.9996 .2492 , 31.1754 . 31653 0 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD TI T2 T3 T4 ;T5 T6 T7 T8 T9 T10 81.944 82.658 - 83.072 81.680 ~83.973 85.099 86.710 84.911 81.756 84.607 RTD -
RTD RTD RTD .RTD RTD RTD RTD RID RTD T11 T12 T13 T14 .:T15 T16 T17 T18 T19 T20 84.500 84.296 84.068 84.226' 84.505 84,696 84.881 84.798 83.339 83.655
~
D1 D2 D3 D4 D5 D6 59.635 58.528 58.515 59.555' 59.503 59.381 _________________________________________________ i VAPOR CONTAINHENT DATE HOUR TEMP PRESSUREl PRESSURE COUNT 1 COUNT 2 04/05 0306 84.0437 .2535 31.1731 31655 0 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T1 T2 T3 T4~ T5 T6 T7 T8 T9 T10 81.944 82.621 83.222 81.793 84.048 85.174 86.785 84.911 81.869 84.598 RTD RTD RTD RTD RTD RTD RTD RTD RID RTD T11 T12 Tl3 Tl4 T15 T16 117 T!8 TI9 T20 84.612 84.338 84.101 84.287 84.528 84.700 84.793 84.914 83.404 83.650 DI D2 D3 D4 D5 D6 59.829 59.142 60.161 59.461- 59.277 59.510 VAPOR CONTAINHENT
) ATE HOUR TEMP PRESSURE . PRESSURE COUNT 1 COUNT 2 14 /0 5 0321 04.0635 .2537 31.1749 31657 0 RTD RTD RTD .RTD RTD RTD
- RTD RTD RTD RTD T1 T2 T3 T4 'T 5 '
m T6 T7 T8 T9 T10 81.906 82.583 83.110 81.906 84.011 85.174 86.673 84.911 81.75$ 84.668 2' RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 113 T14 T15 f T16 T17 T18 T19 T20 04.649 84.342 04.133 84.305 84.561' 84,993 84.802 84.937 83.376 83.711 D1 D2 D3 D4 .D5 D6 60.055 59.077 59.774 59.716" .59.503 59.510 ,
-.mr mm .
.esmo.o6ano .............onoomona =neaann ........
VAPOR CONTAINMENT 'DATE , HOUR TEMP PRESSURE- PRESSURE COUNT 1 COUNT 2
- 04/05 0339 84.1171 .2560 31.1766 31661 0
' RID .RTD RTD RTD RTD 1 RTD RTD RTD RTD RID T1 T2 I3 T4 T5 T6 T 7- T8 T9 T10 81.793 82.696 83.034 81.906 84.048 85.211 86.822 85.024 81.831 84.728 RTD RID RTD RTD RTD RTD RTD RTD RID RTD ' Til T12 T13 T14 T15 T16 T17 T18 T19 T20 84.686 84.407 84.203 84.417 84.700 84.937 84,905 85.086 83.450 83.715 D1 D2 D3 D4 D5 D6 60.023 59.271 60,100 59.910- 59.632 59.958 VAPOR CONTAINMENT -
) ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14 / 0 5 0354 84.1669 .2544 31.1801 31663 0
.RTD RID RTD RTD RTD RTD RTD RTD RTD RTD !T I T2 T3 T4 T5 T6 T7 T8 T9 T10 81.982 82.809 83.260 81.869 84.048 85.249 86.860 85.099 81.793 84.742 'RTD RTD RTD RTD RTD " RTD RTD RTD RTD RTD iT11 T12 T13 T14 TIS T16 T17 T18 T19 T20 L84.668 84.431 84.259 84.440' 84.677 85.095 84.998 85.044 83.460 83.859 l lD1 D2 D3 D4 D5 D6 iS9.993 59.693 59.839 59.687 59.442 59.964 l VAPOR CONTAINMENT ATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2 4/05 0409 84.1939 .2586 31.1779 31665 0 iTD RTD RTD RTD RID RTD RTD RTD RTD RTD T1 T2 T3 T4 .T 5 T6 . T7 T8 T9 T10 31.906 82.734 83.448 82.019 84.048 85.324 86.822 85.099 81.831 84.812 ITD RTD RTD RTD . RID t RTD RTD RTD RID RTD fit T12 T13 T14 T15 - T 16 ' . T17' T18 T19 T20 34.728 84.500 84.291 84.445 84.658 84.965 85.030 85.086 83.502 83.836 O 9
..,,.---cm,.- ,.,m.,,- , , . _ . , , , . ,.,,-ne ...,-,,,-,,,--,-,r n,,,g ----,---n- m-.,.
e- w+- - , - - - m-n-- m,,, ,,..-s,..m- ,. -,-v
'D I D2 D3 D4 . DS D6 60.248 59.693 60.551' 60.235 *59.793 4 59.642 .ocouano..'....................................... .
4 VAPOR CONTAINMENT
.DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0424 84.2584 .2580 31.1805 31667 0 RTD RTD RID RTD ,' R TD ' '. RTD RTD RID RTD RTD T1 T2 T3 T4 T5/ T6 T7 T8 T9 T10 81.982 82.771 83.373 82.019 84.161 85.361 86.972 85.174 81.869 84.886 RTD RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 -
TIS T16 T17 . T18 T19 T20 84.928 84.482 84.315 84.542 84,779 85.132 85.053 85.169 83.515 83.864 DI D2 D3 D4 D5 DS 60.187 58.984 61.064 59.816 59.664 59.835 l VAPOR CONTAINMENT 1 ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 14/05 0439 84.2755 .2571 31.1833 31669 0 RTD RTD RTD RTD RTD RID RTD RTD RTD RTD
- T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 l82.019 82.922 83.222 82.057 84.124 85.361 86.935 85.249 82.019 84.914 RTD RTD RTD RTD RTD RTD RTD RTD RfD RTD T11 T12 T13 T14 T15 T16 T17 T18 Tl9 T20 84.826 84.524 84.370 84.575 84,793 85.216 85.039 85.114 83.594 83.906 DI D2 D3 D4 DS D6 60.316 58.919 60.258 60.074 59.539 60.029 VAPOR CONTAINMENT ATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2
!4/05 0454 84.2892 .2564 31.1880 31673 0 ITD RTD RID RTD RTD RTD RTD RTD RTD RTD ,i 1 T2 T3 T4 T5 T6 I7 T8 T9 T10 il2.019 82.809 83.297 82.019 84.274 85.474 87.009 85.249 82.057 84.881 IID RTD RTD RTD RTD RTD RID RTD RID RTD l
T11 T12 T13 T14 TIS i T16'. T17 T18 T19 T20 84.949 64.589 84.370 84.5G1 84.793 85.081 85.086 85.128 83.622 83.985 D1 D2 D3 D4 D5 D6 60.219 59.048 60.358 59.848 59.693 59.993 ooo.. ...........................................
.s .
VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0509 84.3256 .2529 31.1935 31675 0 4 RTD RTD RTD RTD RTD - RTD RTD RTD RTD RTD T1 T2 T3 T4 T5 T6 T7 T8 T9 T10 81.982 82.959 83.485 82.094' 84.311 , 85.474 87.084 85.324 82.019 84.895 RID RTD RTD RTD RTD RTD RTD RTD RTD RTD Til T12 113 T14 TIS T16 Tl7 T18 119 T20 84.914 84.621 84.394 84.542 84.835 84.942 85.234 85.174 83.669 83.975 D1 D2 D3 D4 D5 D6 59.929 59.100 59.261 59.784 59.793 59.674 o ...........................**.................. VAPOR CONTAINMENT DATE HOUR TEMP PRESSURE PRESSURE COUNT 1 COUNT 2 04/05 0524 84.3994 .2570 31.1913 31677 0
- RTD RTD RTD RTD RTD RTD RTD RTD RTD RID
, TI T2 T3 T4 T5 - T6 T7 T8 T9 T10 ! 82.245 82.997 83.448 82.170 84.311 85.511 87.122 85.324 82.057 84.979 l RID RTD RTD RTD RTD RTD RTD RTD RTD RTD T11 T12 T13 T14 T15 - T16 T17 T18 T19 T20 l 84.993 84.Gl2 84.426 84.621 84.928 85.392 85.221 85.295 83.706 84.022 l D1 D2 D3 D4 D5 D6 60.058 58.887 60.035 60.171- 59.858 60.093 VAPOR CONTAINMENT
) ATE HOUR TEMP PRESSURE PRESSURE COUNT! COUNT 2
!)4/05 0539 84.4207 .2546 31.1957 31679 0 s
- RTD RTD RTD RTD RTD ' RTD RTD RTD RID RTD T1 T2 T3 T4 T5 T6 T7 T8 I9 T10 ,
82.282 83.072 83.560 82.094 84.349 85.511 87.122 85.436 82.132 85.016
1 s = a . CONNECTICUT YANKEE ATOMIC POWER COMPANY HADDAM: NECK PLANT RR # 1 BOX 127E. EAST H AMPTO;4. CONN. 06424 September 18, 1986 Dr. T. E. Murley U.S. Nuclear Regulatory Commission Region 1 631 Park Avenue King of Prussia, PA 19406 Gentlemen: Haddam Neck Plant Containment Operation and Testing Report The attached report is submitted in accordance with the requirements of Connecticut Yankee Technical Specifications, Section 4.4 and 10CFR50, Appendix J. This report covers the containment operation and testing from November 1984 through May 1986. Included are the results of the reactor containment building integrated leak rate test, the reactor containment building local leak rate tests, the recirculation system test and the air filtration system test. Included with the reactor containment local leak rate tests are a corrective action plan and local leak rate test results from July 1986. The corrective action plan provides the failure cause, action taken and future actions for containment penetrations which were significant contributors to the as-found local leak rate. Additional local leak rate tests were conducted as part of an unscheduled outage during July 1986. Sincerely, Richard H. Graves Station Superintendent lac 1 i g 01 l}}