AECM-84-0438, Semiannual Radioactive Effluent Release Rept, Jan-June 1984
| ML20098E592 | |
| Person / Time | |
|---|---|
| Site: | Grand Gulf  |
| Issue date: | 06/30/1984 |
| From: | Dale L MISSISSIPPI POWER & LIGHT CO. |
| To: | James O'Reilly NRC OFFICE OF INSPECTION & ENFORCEMENT (IE REGION II) |
| References | |
| AECM-84-0438, AECM-84-438, NUDOCS 8410010114 | |
| Download: ML20098E592 (83) | |
Text
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Grand Gulf Nuclear Station SEMIANNUAL RADI0 ACTIVE EFFLUENT RELEASE REPORT January 1 - June 30, 1984 8
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TABLE OF CONTENTS SUBJECT PAGE I. INTRODUCTION.................................................. 1 II. DETAILED INFORMATION.......................................... 2 A. . Regulatory Limits........................................ 2
- 1. 10CFR20 Limits
- a. Fission and Activation Gases. . . . . . . . . . . . . . . . . . . 2
- b. Radioiodines and Particulates.................. 2
- c. Liquid Effluents............................... 2
- 2. 10CFR50, Appendix I Limits ,
- a. Fission and Activation Gases................... 3
- b. Radioiodines and Particulates.................. 3
- c. Liquid Effluents............................... 3
- 3. 40CFR190 Limits..................................... 4 B. Maximum Permissible Concentrations....................... 4 -
- 1. Airborne............................................ 4
- 2. Liquid.............................................. 4 C. Average Energy........................................... 4 D. Measurements and Approximations of Total Activity........ 4
- 1. For Fission and Activation Gases.................... 5
- 2. For Particulates and Radiciodines................... 6
- 3. For Continuous Releases............................. 6
- 4. For Batch Releases: Gases........................... 6
- 5. For Batch Releases: Liquid Effluents................ 7 Batch Releases........................................... 7 E.
- 1. Liquid.............................................. 7
- 2. Gaseous............................................. 8 F. Abnormal Releases........................................ 8
- 1. Liquid.............................................. 8
- 2. Gaseous............................................. 8 G. Estimate of Total Error.................................. 8
- 1. Liquid.............................................. 8
- 2. Gaseous............................................. 8
- 3. Counting Error...................................... 9
- 4. Solid Radioactive Waste............................. 9 H. Solid Radioactive Waste Shipments........................ 9 Radiological Impact on Man................................ 9
~ I ~.
Water-Related Exposure Pathways..................... 9 1.
- 2. Gas-Related Exposure Pathways....................... 10 10 J. Meteorol ogi cal Da ta . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
i K. Radioactive Effluent Monitoring Instrumentation Inoperability Reports.................... 11 12 i III. 1984 RADIATION DOSE
SUMMARY
IV. OFFSITE DOSE CALCULATION MANUAL / PROCESS CONTROL-PROGRAM REVISIONS............................................ 13 l
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LIST OF TABLES Table Page a
1A Gaseous Effluents - Summation of All Releases....... lA-1 IB- Gaseous Effluents - Elevated Releases. . . . . . . . . . . . . . 1B-1 1C Gaseous Effluents - Ground Level Releases........... IC-1 2A Liquid Effluents - Summation of All Releases....... 2A-1 2B Liquid Effluents - Continuous and Batch Modes...... 2B-1 -
3 Solid Radioactive Waste and Irradiated F u e l S h i pme n t s . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3-1 4A Joint Frequency Distribution - January 1-March 31, 1984..................................... 4A-1 4B Joint Frequency Distribution - April 1-June 30, 1984...................................... 48-1 4C Classification of Atmospheric Stability..........'.. 4C-1 5 Padioactive Liquid Waste Sampling and Analysis Program.................................... 5-1 6 Radioactive Gaseous Waste Sampling and Analysis Prcgram.................................... 6-1 11 46aly
9 LIST OF ATTACHMENTS 4
. ATTACHMENT 1: Revision 0 to-the Process Control Program
- 2 Revision 1 to the Process Control Program f.
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I. INTRODUCTION
-This Semiannual Radioactive Effluent Release Report for the period of January 1 to June 30, 1984,.is submitted in accordance with Section 6.9.1.8 of Appendix A to Grand Gulf Nuclear Station (GGNS)LicenseNo.NPF-13. That portion of Appendix A that refers to the monitoring of radioactive effluents, Sections 3/4-11 and 3/4-12, will hereafter be referred to as the Radiological Effluent Technical Specifications (RETS).
Airborne discharges at GGNS are ground level releases. All liquid and airborne discharges to the environment were analyzed in accordance with the RETS requirements. Also, all effluent releases ~
were within the concentration and total release limits specified by
~t he RETS.
There was an instance when Station Operations personnel were unable to restore operable status to radioactive effluent monitoring instrumentation. Additional discussion (Section II.K) has been provided to explain why this inoperability was not corrected within the time specified by GGNS Technical Specifications.
The calculations and terms utilized in this report are definrd in the GGNS Offsite Dose Calculation Manual (00CM).
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t' II. DETAILED INFORMATION ,
A. Regul'aqoryLimits s 3
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- 1. 10CFR20 Limits i
- a. Fission and Activation Gases - The relesse, rate limit at any time for noble gases to afeas 'a.t pr, beyond the site boundary shall be such th'at :.'
D avera g3=yearge; (mremtota)'bodydoserateinthe(u'r.MNt'
/yr[ , (
=X K Q$ $ 500 mrem /yr and D = ave n ge skir dose rate in the cu. rent year -
8 (mrem /yr)s s i ; i ;c , _ ,,
= X/Q $
(Lg + 1.1 M g) Q, 5 3000 mrem /yr wherethetermsAredefinediktheGGNSODCM. \'
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- b. 'Radiciodines and Particulates i ~ The release rate limit for the sampling period fer all radiciodines, tritium and radioactive materials in particulate form with half-livesN G eater than 8 days shall'be such that: ls i
D = average organ' dose rate in current year *
(mrem /yr) i j WPj Q 5100 mrem /yr ,
where the terssisia' defined'in the GGNS ODCM.
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- c. Liquid Effluents --The benceritration of radioactive materials released in, liquid ,e'ffluents to unrestricted areas from all reacto'r5Jat the site shall not eaceed at'any tine thd values specified in 10CFR20,i Apperdix B, Table II, Column 2; The concehtration of dissdived or. entrained noble gases, released is 1 Xuid effluents tonrestricted, u areas reactors at the sitc, shall be limited to
" froneal}
2 x'10~ microcuries/ml total' activity. :
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e 2.- 10CFR50, Appendix _I Limits
- a. Fission and Activation Gases - The dose from noble gases in gaseous effluents to areas at or beyond the site boundary shall be such that:
D y= air dose due to gama emissions from noble gases
= 3.17 x 10-8 $jM X/Q' Qg s5 mrad 7/qtr
$10 mrad T/yr p=airdoseduetobetaemissionsfromnoblegas
= 3.17 x 10-8 $$ N X/Q'Q$10 4 mrad [/qtr -
$20 mRadp/yr where the terms are defined in the GGNS ODCM.
- b. Radioiodines and Particulates - The dose from tritium, radioiodines and radioactive material in particulate form with half-lives greater than 8 days in gaseous effluents shall be such that:
Dp = dose to an individual from radioiodines and radionuclides in particulate form with half-lives greater than 8 days (mrem)
= 3.17 x 10-8 R W' Qg' 1 7.5 mrem /qtr Any Organ 1 15 mrem /yr Any Organ where the terms are defined in the GGNS ODCM.
- c. Liquid Effluents - The dose from radioactive materials in liquid effluents shall be such that DTau " i[Ai Tau t-1 att C $g y 1 1.5 mrem /qtr Total Body 5- 5 mrem /qtr Any Organ
- 3. 3 mrem /yr Total Body i 10 mrem /yr Any Organ where the terms are defined in t.he GGNS 00CM.
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- 3. 40CFR190 Limits Doses are calculated for Fission and Activation Gases; Radioiodines and Particulates; and Liquid Effluents according to equations contained in Sections 2.(a), (b), and (c), respectively, with the exception that the limits applied are 5 25 mrem /yr, Total Body and Any Organ except thyroid 5 75 mrem /yr, Thyroid i10 mrad 7/qtr orf 20 mrad 7/yr Fission and Activation Gases 5 20 mRadp/qtr. or$40 mrad [/yr, Fission and Activation -
Gases
< 15 mrem /qtr ors 30 mrem /yr, Any Organ, Iodine and Particulates
$ 3 mrem /qtr ors 6 mrem /yr, Total Body, Liquid Effluents S 5 mrem /qtr ors 20 mrem /yr, Any Organ, Liquid Effluents .
B. Maximum Permissible Concentrations
- 1. Airborne The Maximum Permissible Concentration (MPC) of radioactive materials in gaseous effluents is limited by the dose rate restrictions of 10CFR20. In this case, the maximum permissible concentrations are actually determined by the dose factors in Table 2.1-1 of the GGNS 00CM.
Liquid ^.
2.- ,
The MPC of radioactive materials in liquid effluents is limited by 10CFR20, Appendix B, Table II, Column 2. The MPC chosen is the most conservative value,of-either the soluble or insoluble MPC for each radioisotope.
C. -Average Energy Not Applicable for GGNS RETS.
' D. Measurements and Approximations of Total Activity The following discussion details the methods used to measure and approximate total activity for the following:
- 1. Fission and Activation Gases 3. Particulates 2., 'Radiciodines 4. Liquid Effluents 9
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- Enk5es 5 and 6 give sampling frequencies and minimum
-fo.tstble.-sensitivity requirements for the analysis of liquid
- a m setum effluent streams.
- thes.in the attached tables given as zero do not
- wriemrify infer that the radionuclides were not present. A
. ,:erndit:stes that the radionuclide was not present at levels
' engweltwa the sensitivity requirements shown in Tables 5 I
s . anc. 3 Rir some radionuclides lower detection limits than nyretasse be readily achievable; when a radionuclide is vesensttsedow its stated limits it is reported.
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':1. B d5 nsion and Activation Gases ITi4&T1owing noble gases are considered in evaluating ~
r Jaseousiairborne discharges:
r
' Ar-41 Xe-131m
[
_ Kr~85m Xe-133 k-85 Xe-133m s it-87 Xe-135m i W-88 Xe-135 I W-89 Xe-137 7 Xe-138.
PeFmtic grab samples from Station effluent streams are
- makyged Ly a computerized pulse height analyzer system E AiYrring high resolution germanium detectors. (See 6 GTim6 for sampling and analytical requirements.)
Tlinspic values thus obtained are used for dose release
- rate calculations as given in Section II.A.1. of this
- . etysart. Only those radionuclides that are detected are E used in this computation. During the period between grab i samples, the amount of radioactivity released is based on
" the effluent monitor readings. Monitors are assigned a caIitration factor based upon the last isotopic analysis
- raisery the following relationship
i
- WITETT C$=U$+m s
C. = isotopic calibration factor for isotope 1.
1
[ U = concentration of isotope i in the grab sample, in Ci/ml.
m = net monitor reading associated with the
- effluent stream. (Determined at the time of E grab sampling)
F
=
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These calibration factors, along with the hourly effluent monitor values and flow rates, are entered into the laboratory computer where the release rates for individual radionuclides are calculated and stored. If no activity is detected in the grab sample, the calibration factor for Kr-85 and the dose factor for Kr-89 are entered into the laboratory computer.
- 2. For Particulates and Radioiodines The radiciodines and radioactive materials in particulate form to be considered are Zn-65 I-133 Cr-51 Cs-134 Mn-54 Cs-136 -
Fe-59 Cs-137 Co-58 Ba-140 Co-60 Ce-141 Sr-89 Other Nuclides Sr-90 with half-lives Zr-95 greater than Sb-124 8 dajs.
- 3. For Continuous Releases Continuous sampling is performed on the continuous release points (i.e., Radwaste Vent, Containment Purge, FHA Vent, Turbine Building Vent). Particulate material is collected by filtration. Radioiodines are collected by adsorption onto a charcoal filter. Periodically these filters are removed and analyzed on the pulse height analyzer to identify and quantify radioactive materials collected on the filters. Particulate filters are then analyzed for gross alpha and Strontium-89 and -90, as required. Gross alpha determinations are made using a 2-pi gas flow proportional counter. Strontium-89 and -90 values are obtained by chemical separation and subsequent analysis using 2-pi gas flow proportional counters.
During major operational occurrences, the frequency of
- sampling is increased to satisfy the requirements of footnote "C" of Table 6, " Radioactive Gcseous Wa:te,
-Sampling'and Analysis," (GGNS RETS, Table 4.11.2.1.2-1).
- 4. For Batch Releases: Gases The processing r,f batch type releases (from Containment Purge) is analogous to that for continuous releases.
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- 5. For Batch Releases: Liquid Effluents The radionuclides listed below are considered when evaluating liquid effluents:
H-3 Mo-99 Co-58 Tc-99m Co-60 1-131 Fe-55 I-132 Fe-59 I-133 Zn-65 -I-135 Mn-54 Cs-134 Cr-51 Cs-137 Sr-89 Ba-140
- Sr-90 La-140 Nb-95 Ce-141 Zr-95 Ce-144.
Representative pre-release-grab samples are obtained and analyzed as required by Table 5. Isotopic analyses are performed using the computerized pulse height analyses system previously described. Aliquots of each pre-release sample, proportional to the waste volume released, are composited in accordance with the requirements of Table 5. Strontium determinations are made by performing a chemical separation and counting the separated strontium using a 2-pi gas flow proportional counter. Gross alpha determinations are made using 2-pi gas flow proportional counters. Tritium and Iron-55
~
concentrations are determined by using liquid scintillation techniques. Dissolved gases are determined employing grab sampling techniques and then counting on the pulse height analyzer system.
E. -Batch Releases
- 1. Liquid 1st Quarter 1984
- a. Number of batch releases: 42
- b. Total time period for batch releases: 14508 minutes
- c. MaWLm t' :e pericd for a t'atch release: 600 minutet
.d. Average time period for batch releases: 345 minutes
- e. Minimum time period for-a batch releases: 10 minutes 2nd Quarter 1984
- a. Number of batch releases: 108
- b. Total time period for batch releases: 45864 minutes
- c. Maximum time period for a batch release: 3695 minutes
- d. Average time period for batch releases: 425 minutes
- e. Minimum time period for a batch release: 242 minutes 46aly L
- 2. Gaseous 1st and 2nd Quarter 1984
- a. Number of batch releases: None
- b. Total time period for batch releases: 0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />
- c. Maximum time period for a batch release: 0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />
- d. Average time period for a batch release: 0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br />
- e. Minimum time period for a batch release: 0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> F. Abnormal Releases
- 1. Liquid
- a. Number of releases: None
- b. Total activity released: N/A
- 2. Gaseous
- a. Number of releases: None
- b. Total activity released: N/A G. Estimate of Total Error
- 1. Liquid The maximum errors associated with sampling, laboratory procedure and discharge volume are collectively estimated to be:
Fission and Activation Gases Isotopic H-3 Fe-55 Sr 29% 21% 26% 36% 29%
- 2. Gaseous The maximum errors (not including sample line loss) associated with sample flow, vent flow, sample collection, menitor calioration and laboratory procedure are collectively estimated to be:
Fission and Activation Gases Iodine Particulate Tritium 39% 43% 42% 31%
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. . .-. .- .- -. . . - . . , . - _ = . . . . _ - . - - . - . - . _ -
o
- 3. Counting Error (1) Isotopic counting errors are computed by the equation:
Error = 1.96 C B
+ C3 Background counts Where: CB=
C = Sample counts 3
The isotopic counting errors are estimated to be 60%
due to the low sample activity. -
(2) The gross counting errors associated with H 3, Sr-89, Sr-90, and Fe-55 are computed by the equation:
Error = 1.96 C B
+ C3 Background counts Where: CB=
C = Sample counts 3
The estimated error for gross counting is estimated to be 60% due to the low sample activity.
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- 4. Solid Radioactive Waste. See Table 3 for error terms.
H. Solid Radioactive Waste Shipments See Table 3 for shipment infonnation.
I. Radiological Impact On Man
- 1. Water-Related Exposure Pathways The values calculated in this section utilize information provided in Tables 2A, 2B and the ODCM.
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Total Dose (mrem)
Ist Quarter 1984 2nd Quarter 1984 Whole-Body 2.57E-05 5.32E-05
-Bone ' 1.46E-04 1.11E-03 Liver 1.03E-04 1.86E-04
' Thyroid 7.14E-08 2.85E-07 Kidney 5.67E-07 6.68E-06 Lung 5.62E-05 9.11E-05 GI-LLI 8.13E-05 2.90E-04
- 2. Gas-Related Exposure Pathways .
The values calculated in this section utilize information provided in Tables IA, 1C and the ODCM.
.lst Quarter 1984 2nd Quarter 1984 Total Body 3.30E-2 mrem 4.19E-2 mrem Skin 2.02E-2 mrem 2.57E-2 mrem Particulate. Radioiodine and Tritium 1st Quarter 1984 2nd Quarter 1984 Organ Dose 3.24E-4 mrem 2.14E-3 mrem Lower Limit of Detection (LLD) Methodclogies If gaseous activity detected in the monthly isotopics is less than the LLDs, a Kr-85 calibration factor and a-Kr-89 dose factor are inserted for the effluent monitors.
The monitor net count rate is assumed to be zero whenever the monitor net count rate is less than two times the square,roct of the monitor background ccunt rate.
J. Meteorological Data See Tables 4A and 48.
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= K. Radioactive Effluent Monitoring Instrument Inoperability Reports
! During the reporting period, the-a was one event pertaining to
- the RETS that necessitated entering into a Limiting Condition for Operation (LCO) where the time period as specified in the Action Statement was exceeded. The following explanation is provided as required by Technical Specifications 3.3.7.11.b and 3.3.7.12.b.
- 1. LC0 EVENT 83-805
- a. Recap Date/ Time Affected Closed Out '
Entered Channel Duration Date/ Time 11/14/83, Liquid Ongoing Open 1700 hrs. Radwaste Flow
- Interlock
- b. Description f
' On November 14, 1983, a temporary alteration was performed in order to defeat the flow interlocks on the liquid radwaste discharge monitor. This would allow discharge of liquid radwaste when circulating water blowdown is not available for dilution flow, a condition that exists during circulating pump shutdown. Technical Specifications Position Statement 018 was approved by.the Plant Safety Review Committee (PSRC) on December 13, 1983, to
- l. allow inoperability.of this channel for longer than 30 days when extended shutdown of circulating pumps is necessary.
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- It should be noted that dilution is still provided
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by Plant Service Water return flow. A single service water pump provides 2500 gallons per minute dilution flow to the discharge basin. Discharges via this pathway will be discontinued upon loss of all service water pumps.
Flow rates will be estimated every 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> during periods of release in accordance with Technical Specifications Table 3.3.7.11.-1 (Action 111). It is intended to leave this alteration in place until circulating water blowdown flow is available.
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III.1984 RADIATION DOSE SUNi4ARY A. This sumary will be provided in the end-of-year report.
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IV. OFFSITE DOSE CALCULATION MANUAL / PROCESS CONTROL PROGRAM REVISIONS A. ODCM Revisions: N/A B. Process Control Program (PCP) Description, Revision 1 Revision 0 and 1 of the PCP are included as Attachments 1 and 2 to this report.
Revision 1 of the PCP was initiated for the following reasons:
e compliance with the requirements of 10CFR61 ~
e dewatering of resins e control of contractor performance.
- 2. The original GGNS PCP Description contained detailed operating instructions for the non-operational in-house Radioactive Waste Solidification System.
Revision 1 is a major rewrite of the original PCP Descriptinn therefore a line-by-line justification is inappropriate.
Revision 1 addresses 10CFR61, dewatering and controls to ensure a contractor performs solidification / dewatering services properly.
Revision 1 does not compromise or reduce the overall confomance of the waste product to existing waste criteria.
It merely addresses the current controls GGNS employs when
. using the services of a contractor to solidify or dewater liquid wastes. These controls require that GGNS review and approve any contractor's solidification / dewatering procedures for compliance with applicable criteria (i.e., 10CFR61).
Revision 1 was reviewed and approved by the GGNS Plant Safety Review Comittee (PSRC) on February 29, 1984.
The Highlights of Revision 1 are present2d below:
Introduction The~ introduction' states t'h'at liquid or~ wet solids will be either solidified or dewatered using approved procedures and instructions. This assures compliance with 49CFR, 10CFR20, 10CFR71 and other applicable regulations. Additionally, if a contractor does the waste processing, the PSRC must review cnd approve the contractor's procedures along with any major equipment used. If the contractor's PCP Topical Report has been accepted by the U. S. Nuclear Regulatory Comission, then J
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the approved report ensures compliance with 10CFR20, 10CFR61 and 10CFR71-as required by the GGNS Technical Specifications.
.If the contractor's PCP Topical Report has not been NRC-approved, then the PSRC will ascertain that the contractor procedures and equipment are adequate to ensure compliance
3 Administrative Controls Added to Section IV (Administrative Controls) of the original PCP Description is the statement that contractor procedures will be reviewed and approved by the PSRC to ensure conformance to the PCP Description. Also, changes made to the c
contractor procedures will be screened and forwarded to the PSRC when the changes significantly affect equiptrent or process parameters. This ensures that GGNS has control over-the end waste product. Further, the requirement to maintain documentation on each batch of processed waste has been added.
Waste Streams
' Waste streams remain the same as in the original PCP Description except for the elimination of Stream #9 - Future.
Revision 1. allows for the future designation of additional waste streams if applicable.
Conditioning of Specific Batches of Waste This section states that processing parameters such as pH, percent solids, and chemical contaminants will be analyzed and
, conditioned in accordance with approved plant procedures. If the specific activity of the waste exceeds the parameters for processing, the waste will be adjusted according to directions from the GGNS Chemistry / Radiation Control Superintendent or his designee.. When a contractor provides services, the contractor must specify acceptable ranges for the physical and chemical characteristics of the waste being processed and use procedures approved by the PSRC.
o Sampling for Verification of Solidification i-A verification of the solidification must be performed on at least every tenth batch of waste processed, unless trends Eindicate more frequent sampling is required. If a contractor.
l 1s performing the solidification services, then the contractor j procedures for verification of solidification must be approved l by the PSRC.
Packagina Requirements f
Prior to shipment of each container, GGNS personnel will l ensure compliance with the requirements of 49CFR, 10CFR61, 10CFR71 and other applicable regulations and burial site criteria.
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Sampling for Verification of Curie Content Revision 1 requires that an isotopic analysis be perfomed on at least every-tenth batch of each waste stream (more frequent if required) and also ensures waste is properly classified.in accordance with the requirements of 10CFR61.
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TABLE 1A Gaseous Effluents-Summation of All Releases i Unit i Guarter i Guarter IEst Total; i
IGrcnc Gulf Nuclear-Power Plant UNIT li i 1 1 2 i Error % i A. Fission & activation vases i .1. Iutai reiease i C1 i 1.17E+01i 1.49E+01i 7.20E+01i i 2. Average release rate for period i uC1/seci 1.49E+00 1.89E+001
% ; 6.63E-01 8.44E-011 i 3. % of Technical specification limit ;
'B. locines l ' 1. Total socine-131 i C1 1 0.00E+001 0.00E+001 7.40E+011 1 2. Averase release rat'e for Period i uC1/seci 0.00E+001 0.00E+001
- 3. */. ' o f Te c n n i c a l specification limit t */. t 0.00E+00 2.54E-05; 1
C. Particulates i 1.'Particulates with nalf-11ves>8 days C1 1 5.866-Udi /.5y6-051 7.30E+01
! uC1/seci 7.46E-06; 9.65E-061 1 2. - Averate release r ate for Perloc
- 3. % of Technical specification limit i */. I 2.20E-02i 2.85E-021 1 0. Gross alena racioactivity i C1 i 9.21E-06; 2.30E-07i D. Trstzum i F 1. lotal release i C1 1 0.00E+001 0.00E+001 6.80E+01 i 2. Averase release rate for period i uC1/ sect 0.00E+00 0.00E+00; i 3. % of Technical specification limit i % i 0.00E+001 0.00E+00; E.. Tritium,raciocines and Particulates
% of Technical specification limit i C1 i 2.20E-02; 2.866-02:
i 1.
- Percentages are based on Technical Specifications as specified in 10CFR50, Appendix I.
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TABLE IB Gaseous Effluents - Elevated Releases (Not Applicable - GGNS Releases are considered ground level) 1B-1 46aly
p..- e TABLE IC Gaseous Effluents-Ground-Level Release CONTINUOUS MODE BATCH MODE
- i. ~Nuclides Released i Unit i Quarter i Quarter i Quarter ii Quarter 2 ii i i 1 i 2 i 1
-i
- 1. Fission sases C1 1 0.00E+00 0.00E+001 0.00E+001 0.00E+00; i- Xe-133 1 i xe-131M i C1 0.00E+001 0.00E+001 0.00E+00 0.00E+00; i Kr-88 i C1 i 0.00E+001 3.51E-03i 0.00E+001 0.00E+001 i xe-133M i C1 i 0.00E+001 0.00E+001 0.00E+001 0.00E+00:
I xe-135 i C1 1 0.00E+00: 0.00E+005 0.00E+001 0.00E+00 i Kr-85M i C1 i 0.00E+00i 0.00E+001 0.00E+001.0.00E+001
-I Kr-87 i C1 : 0.00E+00i 0.00E+00: 0.00E+001 0.00E+00:
xe-138 : C1 i O.00E+00i O.OOE+00i O.OOE+00i O.OOk+00i 1 0.00E+00 0.00E+001 0.00E+001 0.00E+00; 1
i Xe-13/ i C1 i Kr-85 : C1 i O.00E+001 0.00E+001 0.00E+001 0.00E+00i i C1 i O.OOE+00; 0.OOE+001 0.UOE+00i U.00t+001 i xe-135M i Kr-09 i C1 1 1.17E+011 1.49E+01 0.00E+00i 0.00E+001
'l Ar-41 i C1 i O.OOE+00i 4.YOE-03i O.OVE+09i U.00E+09
- i C1 1 0.00E+001 0.00E+00; 0.00E+001 0.00E+00; Kr vu i i i i i
i 0.00E+001 i Total for persoo i C1 i 1.17E+01: 1.49E+011 0.00E+00
- 2. locines i '1-131 : C1- t 0.00E+00 0.00E+00i 0.00E+00 0.00E+00 C1 0.00E+001 1.13E-061 0.00E+001 0.00E+00; I I-133
.i 1-132 i C1 1 0.00E+00 0.00E+001 0.00E+00: 0.00E+00; i I-134 : C1 1 0.00E+00 0.00E+005 0.00E+001 0.00E+001 I C1 1 0.00E+001 0.00E+00; 0.00E+005 0.00E+001 i I-135 i i i i i i I
i Total tor Period i C1 3 0.00E+001 1.13E-Ott 0.00E+001 0.00E+00:
- 3. Particulates i Yr-89 i C1 1 0.00E+00i 0.00E+001 0.00E+001 0.00E+00i i Sr-90 i C1 1 0.00E+001 0.00E+001 0.00E+001 0.00E+00i i C1 1 0.00E+005 0.00E+001 0.00E+001 0.00E+00; i CE-141 i CR-51 C1 1 0.00E+001 0.00E+001 0.00E+001 0.00E+00i i EA-140 : C' i 0.00E+00 0.00E+00* 0.00E+001 0.00E+00*
i CS-134 i C1 0.voE+09: 0.OVE+091 0.OOkv00 0.OOt+00; i CS-13/ i C1 0.00E+001 0.00E+001 0.00E+00 0.00E+00; CE-144 i C1 1 0.00E+001 0.00E+001 0.00E+001 0.~00E+001 0.OOE+00 0.OOE+001 0.OOE+001 0.00t+09:
i-ZR-95 i C1
- C1 1 0.00E+001 0.00E+001 0.00E+001 0.00E+00; i NB-Y5 .
U.00h+00i CO-58 i Ct i O.OOE+00 O.OOE+00i O.OOk+00 i
i MN-54 i C1 1 0.00E+001 0.00E+001 0.00E+001 0.00E+001 FE-59 i C1 i O.OOE+00i O.OOE+00i O.OOE+09i O.00t+0Vi i Ci i 0,00E+00i 0.0QE+001 0.00E+001 0.00E+00i i CU-69 i LA-140 C1 O.OOE+00i O.OOE+00i O.OOE+00i O.Och+09i i C-14 : C1 i 0.00E+00i 0.00E+001 0.00E+00t O.00E+00i i F-32 i C1 i O.OOE+00 0.OOE+001 0.OOk+005 0.09t+00; i C1 ; 0.00E+001 0.00E+001 0.00E+001 0.00E+00; i FE-b5 1 &@ i C1 1 0.OOE+00i O.COE+00i O.00k+00i U.00t+U9:
TABLE 1-C (continued)
I' ZN-65 : C1 i 0.00E+00i 0.00E+001 0.00E+001 0.00E+00;
,3: Y-91. I C1 i O.00E+00i O.OOE+00i U.OUE+00i U.Oct+00i i Ru-103 i C2 i 0.00E+001 0.00E+00i 0.00E+001 0.00E+00i
- ' - RU-106 i C1 i 6.86E-05i 7.59E-05; O.00t+00; O.00t+00i i" AU-ilon i C1 : 0.00E+001 0.00E+00i 0.00E+00i 0.00E+001 i- CS-136 : Ct i 0.00E+00 0.00E+001 0.00E+00i 0.00E+001
, i PR-143 i- C1 i O.OOE+00i O.OOE+00: O.OOE+00i U.Out+00i
- i. 1-131 : C1 1 0.00E+001 0.00E+001 0.00E+00 0.00E+001 i- : : i i
- YotcI tor werioo i C1 : 5.86E-051 7.59E-05: 0.00E+00i 'O.'00E+001 4
d t
s D
e IC-2 46aly
. . - . ~- . . -. . . - . -
l TABLE 2A Liquid Effluents-Sunnation of All Releases l Unit : C!va r t e r : Out ter Est "l o t t i :
1 1 1 1 2 : Error *'.
A, Fission t activatierr Products i 1. Total release (not includine H3, ,
cases, alpha) : C1 i 3.47E-02:- 7.66E-03; ?.90E+01:
i ; ;
I 2. Averase dilutec concentr ation durifie Period i uC1/ml I 4.64E-09; ?.20E-0**
-l '
- % ; 6.73E-04 1.47E-09; i-3. Percent of APP 11cata e limit B. Tritium
- C1 i 5.63E-0?: 0.00E+00; 4.?OE+01-l'1._ Total release i '2. Averase cliuted concentration l UC1/mI : 7.52E-09; 0.OVE+00; i durins Per1oo i 2.51E-Oa; O.09t+00; I 3. Percent of aP*11 cat le 11mit : %
C. DIsJolved anc enira:ned eases C1 ; 0.00E+001 0.00E+00; e.70E+01-i- 1 . Total release
- ; i i l'2. Averaet diluted cercentration ; uC1/mi 0.00E+00
- 0.00E+00; i dul 1 tis Period i 3. Percent of a*F11catle limit ; % i 0.00E+00i 0.00E+001 D. Gross alena racioa:tivst'.
- C1 ; 0.00E+00: 0.00E+00: 6.40E*01I I 1. Total release i t:. . Yotume of waste (Pr^1or to d1Iution)l 11ters : 5.?4E+06' 4.15E+07; 1.00E+01 IF. Volume of citution water usec liters 7.44E-06! 2.?6E+00: 2.00E+01:
- Percentages based on 10CFR20, Appendix 8. Table II, Column 2.
2A-1 46aly
TABLE 2B Liquid Effluents-Continuous and Batch Modes 3.'UN I INUUUS M' ODE BATCH f10DE i~ Nuclides Released i Unit i Quarter i Quarter i Ouarter i Quarter 2 i : 1 i 2 : 1 1 i
- - strontium-89 i C1 i O.00E+00
- 0.00E+00i 0.00E+00: O . 00E +'.") .
- strontium-90 i C1 : 0.00E+001 0.00E+00: 0.00E+00: 0.00E+00-i- cesaum-134 : C1 i O.OOE+00i O.00E+00i O.OOE+00i 0.006+00:
C1 1 0.00E+00; 0.00E+00: 0.00E+00: 0.00E+00
- cesium-1?7 :
- 0.00E+00: 0.00E+00: 0.00E+00; 0.00E+00:
locane-1?1 : C1 cota!t-58 i C1 : 0.00E+00: 0.00E+00; 6.11E-05: ?.00t-04; I coDalt-60' : C1 : 0.00E+00: 0.00E+00: 3.95E-05: 2.Y1E-04 tron-59 i C1 1 0.00E+00; 0.00E+00; 0.00E+00 0.00t+00 i
-i :Inc-65 i C1 : 0.00E+001 0.0vE+001 0.00E+00: 0.00t+00:
-maneanese-54 i C1 : 0.OOE+00; 0.OOE+001 6.45E-06: /. Y:4 t - Ut.:
cnromium-51 : C1 1 0.00E+00: 0.00E+00: ?.14E-05; 2.10E i 1rcon1um-n1ot.:um-95 i C1 1 0.00E+001 0.00E-001 0.00E+00: 0.00E+00:
i molvecenum-9c . Ci : 0.00E+00; 0.00E+00; 0.00E+00: 0.00t+09 E
i technetium-99m i C1 i 0.00E+001 0.00E+001 0.00E+00: 3.S?E-00
- Darium-lanthanum-140 i C1 i 0.00E+00: 0.00E+001 0.00E*00: 0.09E+00'
! cerium-141 C1 : 0.00E+00: 0.OOi+00: 0.OOE+001 U. 096+ 0' -
- C1 : 0.00E+00; 0.00E+00 3.46E-05; 1.22h-04:
Cu-64 1 0.00E+00; 0.00E-00: 0.00E+00: ?.tSt-04 Mn-56 i C1 Na-24 i C1 : 0.00E+00: 0.00E+00; 0.00E+001 1.42E-05' i
Ru-loc ; C1 1 0.00E+00; 0.00E+00: 0.00E+001 1.1?E-04; Zr-97 i C1 i 0.00E+001 0.00E+00; 0.00E+00: 1.94E-06 i 1 0.00E+00; 0.00E+00: 0.00E+00: 4.90E-06:
- Nd-147 : C1 Fe-55 : C1 i O.00E+00: 0.OOE+00; 3.30E-04: 6 . 6 2 6 - 9': :
i i C1 0.00E+001 0.00E+00: 'd. 4 /t-Or i 7. 68E-0~S '
i Total t or Perloc (above) rencn-1:' r ::' : 0. 0'.'E+00 : 0 . 0 0 f. .'O . 0.00E+00: 0 . 0 5.' ' . + 0 .'
- C1 i 0.00E+00; 0.00E+00; 0.00E+00; 0.00E+00:
, i . xenon-135 2B-1 46aly
TABLE 3 Solid Radioactive Waste and Irradiated Fuel Shipments A. Solid Waste Shipped Offsite' for Burial or Disposal
- 1. Type of Waste 6-month Est. Total Unit period Error, %
3
- a. Spent resins, filter sludges, m 2.04E+02 evaporator bottoms, etc. C1 4.74E 00 3.41E+01 3
- b. Dry compressible waste, m N/A N/A contaminated equipment, etc. Ci N/A N/A 3
- c. Irradiated components, m None N/A control rods, etc. Ci None N/A 3
- d. Other m None N/A Ci None N/A
- 2. Estimate of major radionuclide composition (by type of waste as identified above)
- a. Cr-51 % 5.22E+01 Co-58 % 2.07E+01 Mn-65 % 5.40E 00 Fe-59 % 1.13E 00 Co-60 % 1.95E+01 Ni-63 % 3.20E-01
.- C % 3.40E-02 H-3 % 9.40E-03 Nb-95 % 8.98E-02 Zn-65 % 1.82E-01 Zr-95 %- 2.63E-01 Hg-203 % 6.04E-04 Co-57
% 1.84E-02 Ba-La-140 % 5.03E-02 4,
I-131 % 1.32E-02 Nb-95 % 5.09E-02 Cs-136 % 5.64E-04
- b. N/A % N/A
- c. N/A % N/A
~ shipped in LSA containers.
31 46aly
TABLE 3 Solid Radioactive Waste and Irradiated Fuel Shipments (cont'd) 3.. Solid Waste Disposition Number of Shipments Mode of Transportation Destination 9 Truck Barnwell, SC B. Irradiated Fuel Shipments (Disposition)
Number of Shipments Mode of Transportation Destination -
None N/A N/A 4
1 i
3-2 46aly
TABLE 4A Joint frequency Distribution 50 Meter Level 1
EXTREMELY UNSTABLE STABILITY CLASS A PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) l I .
la Av t.
.) . 2 3-5 6-8 3-11 12-14 15-17 Atib UP TOTAL SPEdis a .5 1.1 . 'J 0 9 0 .o 1.6 .1
! .. r: 6. 1.1 0 0 0 0 0 .0 1.1 0 1.1 0 0 .0 .o 1.1 .0
}
uE .u .J r.r.L 1.1 5 0 0 .d 0 0 1.6 .0 D L .5 1.1 .O 0 0 .0 .0 1.6 .0
- I uSc 2.7 4 . ') .0 0 0 .0 .u 7.7 .3
- it LS .d 2.2 1.1 0 .0 .0 .0 3.8 2
- k. E LSG 1.1 5 5 0 .0 .0 0 2.2 .1 I C5 .0 5 .0 0 9 .0 .o 5 0 0 0 0 1.1 0
- 1. i' oSu .o 1.1 ..C .0 l 0 1 :.% 3.a 8.2 0 0 .0 0 . t, 11.5 .4 I il L54 5.5 12.1 2.2 5 .0 0 .0 20.3 9 j u a 8.2 7.7 _1. 5 5 .0 .0 .u 18.1 7
- eso 2.2 3.3 2.7 0 0 .G 0 8.2 .4
... 2.2 d.0 5 0 0 0 .u 11.5 .5 7 7.7 .3
...e 3.8 3.6 .0 0 .0 .0 .u 0
CAbb .0 TOTAL 33.0 57.1 3.8 1.1 0 0 0, LOO.0 2 l
1.6 PERCE.it F3.1 185 Hr,uas
! 3. rlGLits. JP uaD OR . ISSI.iG >ATA JR 33 Fay 33_3
_ m
TABLE 4A (cont'd)
Joint Frequency Distribution 50 Meter Level MODERATELY UNSTABLE STASILITY CLASS B <
PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) lb AVG 0-2 3-b 6-d 9-11 12-1. 15-17 AsiD JP TOTAL SPEED u 2.4 2.4 .J 0 .u 0 0 4.7 .1
! 4, J t: .u 1.2 0 0 0 0 .0 1.2 .0 6 0 0 1.2 .s' I ..E 0 1.2 .U 6 0 0 t.i. d .0 0 .0 0 0 0 0 J i; 0 .J 0 0 0 .o 0 0
.0 0 5.9 3 1 dSd A.e 2.4 2.4 .0 0 .0 R SE .s 3.5 .o 0 .0 .0 .0 3.5 .2 U E abL 2.s 4.7 7.0 0 0 0 .0 14.1 7 1CS .0 4.7 0 .O .0 0 .0 4.7 .2 l 0
- ti Y LS.1 . 2. 4 0 0 0 .0 0 .0 2.4 0 7.0 3 1 D 1 du 2.s 4.7 0 0 .0 .0 a 6.54 !s . 4 t.2 1.2 0 .d 0 .0 11.6 .3
- i. d 1.0 1.2 0 0 .0 .0 .u 8.2 2 i '.. fa r. 3.a 1.2 1.2 0 0 0 .0 5.9 .2 a.a a.2 10.6 1.2 0 .0 0 .u 20.0 7
. : ri .1 2.s 7.0 .0 0 0 0 0 9.4 .3 CAL.i .0 .0 f0TAL 41.2 45.9 12.9 .0 0 0 .0 100.0 3
- 2.3 PEhCLciT FOR 87 tiOURS
- 2. Itisb
.G 0 0 0 6 0 .G .O .0
.4 T hSd 1.J 0 .0 0 0 0 .o 1.0 0 D I sw 4.2 4.2 .O 0 .v .0 0 8.3 3 0 1.9 0 .3 0 0 2.1 .1 u w3e 1.v la W 11.4 4.2 .0 0 .0 0 0 15.o .4 6 0 .O 11.4 5 h ti r u.3 2.1 3.1 .O 4
- a. d 6.3 5.2 .0 .o .0 0 0 13.5 t a i. .. 4.2 5.2 0 .0 .0 0 .0 9.4 .5 0
CALM .0 ........... ... ...
TOTAL 47.9 42.7 9.4 .0 0 0 0 100.0 2 2.0 pct <CCur Ftik 96 HOllf.5
- 2. bab% of de.D Od :.ISSI.lG OATA Git 3
11Fav I
TABLE 4A (cont'd)
Joint Frequency Distribution 50 Meter Level NEUTRAL STABILITY CLASS D PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) id AVG 02 35 58 9 11 12 14 15 17 add UP fUTAL SPEE D I' 9.0 a.5 6 .0 6 0 .u 1H.2 .6 a.i.E 3.o 2.9 .o 0 .0 .0 .O 6.7 .2
.e d 1.d 1.3 0 .3 0 .0 .0 2.7 .1
.. 4 d 1.3 2 .u .0 0 0 .u 1.5 .G D a. 1.0 1.0 .0 0 .0 .0 .o 2.1 0 1 JSt 2.1 5.0 0 .4 .0 0 .o 7.5 3 it tic 1.o 3.5 1.3 .0 .0 0 .0 5.8 3 ri C aSE .4 d.S 3.S 0 .) 0 .0 9.8 5 I C :, .s 1.3 .0 0 .) .o .o 1.7 .1 14 T bSr. 1.3 .o .0 0 .0 0 .o 2.1 .0 D I SW 2.7 1.3 4 0 3 0 .0 4.4 .1 at u s.: .o 4 .2 0 0 .0- .u 1.3 0 il .. 2.9 .o 1.5 1.5 .0 0 .G 6.5 3 i.'it ! 3.o 2.9 2.1 0 0 0 .0 8.8 3 i.h 3.3 2.3 0 .0 .0 0 .0 S.s .2
.. ie s. 1.0 7.5 3.1 .2 .o 0 .0 14.6 .7 CALA .4 .4 TuTAL 39.7 45.5 12.7 2.1 0 .0 0 100.0 .2 29 tidtJRr. UF S AJ net ei1SSI'lG D A*1 A OR b.7 t>dF. CENT 'F0lt 508 H0i'RS
> $ c ..
TABLE 4A (cont'd)
Joint Frequency Distribution 50 Meter !evel SLIGHTLY STABLE STABILITY CLASS E PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) 18 AVG Ar.u UP TOIAL SPEED 6-3 9-11 12-14 15-17 2 o-2 3-b .o 7.4 3.5 1 0 .a 0 2.7 1
- i. 3.o 0 0 0 .0 0
. . - -l 1.4 1.3 9 0 0 0 1.7 9 0 0 1
.!d .c 0 .0 0 .o 3.0 a.ii d .c ?.2 .o 0' .0 0 0 6.3 3 S.0 0 0 12.3 6 Dd .6 2.7 .v 0 6
1 cSd .3 4.1 0 1
.0 .0 0 11.7 it LE 3 8.3 3.0 0 0 .o 6.8 3 5 0 7.2 3 el . SSc; 9 5.4 .0 0 .J 3 0 1CS 1./ 5.0 0 .0 0 .0 6.1 3 1.3 4.7 .1 .0 3.9 .J
- 1 T dSW 1.9 .o 0 .0 0 3.9 .3 D I St. 1.4
.d .O 0 0 .u O i. S .I 1.o 1.6 0 0 0 ou 3.6 .1 2.1 0 7.1 3
.1 1.6 0 .o 0 .J 4.1 9 5.7 2 41:a 2.1 0 0 .o 0 .o
.N 3.o 2.7 1 0 0 .J 9.0 3 2.8 6 1.4 m e .1 5.4 CAbri 1.4
.------- --- --- --------- - -3 --- --------------~~~~~-~~-
0 .o 0 Un o . O ----- 2 TOTAL 28.4 01. '> 9.d .
1.b PCMCE..I FOR 644 H00155
.ir-,
TABLE 4A (cont'd)
Joint Frequency Distribution 50 Meter Level MODERATELY STABLE STABILITY CLASS F PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) 15 . AVG 0-2 3-a 6-8 9-11 12-1s 1S-17 AllD UP TOTA 1. S P F.El,
.. 3.v 5.6 0 0 .0 0 0 R.6 3
...s d 4.3 2.6 0 0 .o 0 0 6.9 .2 a.C 3.o 7 . J. 0 0 0 .0 4.3 .1 6.s d 1.o 1.6 0 0 .v 0 .0 3.3 .1 06 1.3 7.6 1.3 0 6 0 .0 10.3 .s 1 CSd 2.5 10.9 .3 0 .9 0 0 13.9 6 R SJ 1.6 6.3 0 . 0 .. .J 0 .0 7.3 .3 d d SSE. 1.G 4.3 3 0 .0 .0 .0 5.6 .2 ICS los 3 .0 0 0 0 .0 2.0 0 ti T JS.J 2.3 2.3 0 0 .0 0 0 4.6 .1 D 1 S.! 2.0 4.0 3 0 0 0 .G 6.9 .3 0 .54 5.0 1.0 3 0 .0 0 .o 6.3 .2 il .J i.3 3 0 0 .J 0 .0 2.6 0 i
i le .. 2.3 1.6 3 0 .0 0 .6 4.3 .1 alti 2 . c, 0 ,0 .0 .o 0 .o 2.6 0
- i. i = 4.o 4.0 1.J 0 .0 0 .0 9.6 4 CAbh .7 7 IteTAL S2.7 53.3 4.0 .0 .0 0 .0 100.0 2
]
l I 1. :19LRS OF dA) Ok . tid 31iG DATA Od . 3 PEi(CCs.T /.1R 303 HOURS i
i j
4A-6 11Fav
TABLE 4A (cont'd)
Joint Frequency Distribution 50 Meter Level EXTREMELY STABLE STABILITY CLASS G ~S PERIOD OF RECORD: .1/1/84 000 Hours 4/1/84 000 Hours 9 'D
~
WIND SPEED (m/sec) 4
' 1H AVG -
.- w ,.
16-17 Al.as UP TOTAL M'I'*dn -
~~e a-r 6-d V-11 12-1k '
i .
.a 5.7 .1
.. 5.3 0 e 4 , 0 ~
0 0
'.0 0
.o 6 . '
7.1 .2 / 'j/ .
i.i n d b.o 4 0~
0 .o ' /; 3,1 1 ,
2;uf 1- - 0 0 . is im ,
0 ' ;3.5 .1
. 0 _ ', ', .0,_
2,2 1;1 0 .0 '
i:o d . . .e /2.6 .1 ,
i'. 4 0, .0 ~
9 ' .)
ou 1.3
',0 0, .0 .a ' ih ls 5 2.2 - 9.7 't;3 I ude.
.4 .Q .o -
.0 -
.of 14.6 5 -
it SC 2.o 11.9 ' 0" .G 5.7 .1 w d SSE '
- 9. C 1.3 ,.J ,;,U' ,. u f' .
9.3 j'^ - -
b.7 3.5 ~.0 '
.d -
2,0 0/ o .0 - .,. 2 ,
1CJ N T dS.s o.c s 2.2
'f '. J ^ - / 0 ' o:. 0 .0 0
d.d 7.5
- J. 't '
.2 2.2 / .~ 0 0',_ 0- .0 u I S.' $.3 ,
2.6 0 -1 o us;4 2.u 0 .r-
- 0 J- ..0- 0 .0 0 2.2 0
- l e 2.e .) 0 0
0 0
.0
.d 0
0 . .J 1.8 .0 w . 4 .4 1.5 .O 0 0 3.1 .3 2.o 1 0 0 .0
- i. .J 0 0 .J b.6 2 3.1 9 0 isi .i 2.o 2.2 Cl.w i 2.1 ---------- --- ----- -
.--- --- --- --------- ----- - ..----- 0 100.0 2 37.o 3.1 .0 0 .0 T uT ht, 59.3
. (. PEKCEi4T Pdk 226 10U8tS 3
0.- ' tiid RS ar' lisD 04 .LISSIlld DATA OR
,,r,.. 43_7
TABLE 4A (cont'd)
Joint Frequency Distribution 10 Meter Level EXTREMELY UNSTABLE STABILITY CLASS A PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) la AVG 0-2 3s 6-8 9-11 12-16 15-11 AuD !JP TOTAL SPEEn 5 0 0 .o 0 .0 2.2 3 i! .o i ...s- ~> 2 0 0 0 0 0 .J 2.2 0 oC 1.1 0 0 0 .0 0 .0 1.1 .0 0 0 .0 0 .U 2.2 0 C id i.2 .0 5 0 0 .O 0 .0 1.6 0 i
- 1) d 1.o 1 ess 2.2 1.. .a .o .o 0 .a 3.8 .1 l 3 0 0 .0 3.3 .1
! It SE 2.7 5 .d el C 6S c. 2.2 1.1 .d .0 .o .0 0 3.3 .1
- 1CS .5 5 0 0 6 0 .0 1.1 .c 5 0 0 0 .0 1.6 0 i, T
..S . 1.1 .0 4
11.9 6.C .o 0 .u 0 0 17.9 5 l D I Lei il sis 12. :) 7.2 0 0 .0 .0 0 14.7 . .e l
.1 11.y 1.o .J 0 0 0 .o 13.6 .3 0 0 0 10.3 3
'.. u d 7.1 3.3 0 .d
.l e 7.1 5.= 0 4 .0 0 .0 12.5 .3
....-. 3 . '> 1.9 .J .0 .J 0 .0 6.1 .2 CAmi .a 5 TOTAL 71.7 25.3 0 .0 0 .0 0 100.0 .?
- 1. .Ga;% OF sh) Od .ll 5S I h, D A C A .M .5 Pt.kCC.4T h1R 185 liritJH3 j
4 ur,,,
TABLE 4A (cont'd)
Joint Frequency Distribution 10 Meter Level s
1 0
'M'0ERATELY UNSTABLE STABILITY CLASS B - '
4/1/84 000 Hours PERIOD OF RECORD: 1/1/84 000 Hours -
WIND SPEED (m/sec) 14 's V G Ai4:s UP TOTAL S.- U.D
'O-2 J-d 6-8 9-11 12-11 l 's - 17 0 ., u 4.6 .1 \
1.o 3 ,)
0 .5 o 0 .0 1.2 .0 l
i.18 .a 1.2 3 -.0 .0 3
0 .o 0 .J 0
- .G .o 0 .J 0 0 0 .J 0 .0 1.2 .O
- t. . n. 1.4 2.3 1
- 2. 3 0 3' 0 .o 0 .o 0
13 i; 3 0 6 0
.; 6 .J .0 I dSc 0 .o 0 .J 2.3 .1 H Sis 1.2 1.2 .J
.o 16.3 6 12.6 0 0 .v .0 al C SSS 3.d 0 .o 7.0 3 IC5 l'.2 5.5 .0 0 .0 1.2 0 i 0 0 0 . .J il T SSii .0 1.2 0
,0 .0 9.3 .2
~
3.5 0 0 .o j . D I SW 5.n 0 .0 0 .J 9.3 .1 0 45J ,9 . s 0 .J 1 0 . .) ,0 9 8.1 11 W J.1 0 .J 2 0 .o 0 .) 8.1 L. 1 +i 7.o 1.2 .J 0 0 1f.4 .1 0 0 .0
.. d 15.1 2.3 0 .0 -11.6 .3 5.o d.8 3 0 .0 a.e4 4 0 CAwA .s 34.9 0 .0 0 0 0 100.0 2 TOTAL v5.1 i
hudG uf .)AD On .ll.;S1!40 DATA UK 1.1 PdRCEtiT FOR 87 iindRS 1
i J
l 4A-9 33Eav
TABLE 4A (cont'd)
Joint Frequency. Distribution 10 Meter level t
4 SLIGHTLY UNSTABLE STABILITY CLASS C
< PERIOD OF RECORD: 1/1/84. 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec)
' is AV3 2 3-5 6-8 v-11 12-1i 15-17 As.J LIP TOTAL, S P i?..'s
.a '2 . 1 1.0 .0 0 .0 0 .0 3.1 .1
.0 1.0 0
.. 1 -; . ') 1.0 .0 0 .0 .0 su 3.t .J .o .0 .0 0 .o 3.1 .1 0 .0 0 .0 0 .G 0 0 t.. i d . ')
s) r. S.2 0 .O 0 .o .o .0 5.2 .1 I JSc 3.1 0 .0 0 0 .0 0 3.1 .1 R Sd 6.3 1.0 0 0 0 0 .e 7.3 2 ti C SSF. 3.2 b.3 0 4 0 0 .c 11.4 4 ICS '4.2 .J 0 0 .u 0 .o 4.2 .1 il T SSu 3.1 0 0 0 0 0 .0 3.1 0 o 1 S'.1 6.3 .0 0 0 .0 0 .0 6.3 .1 tJ '.4 5.. ..e 2.1 0 0 0 0 .o 6.3 .1 il .i 10.'4 .0 0 0 0 .0 .s 10.4 2
.o 0 0 14.6 3
.t il .. 11.. 3.1 0 .0
- di 14.o 0 0 0 0 0 .0 14.6 3 0 6.3 2
.. il .1 .2 2.1 3 0 .0 .0 0
CAu.l .3 100.0
' . ') .o 0 0 0 2 To t Al. 63.I lo.7
{
,,r..
,m TABl.E 4A (cont'd)
Joint Frequency Distribution 10 Meter Level NEUTRAL STABILITY CLASS D PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec)
Ad AV3 9-11 12-14 15-17 AIJo UP TOTAL, SPid3 2-2 2-S c-d 0 18.6 4 0 0 0 0
- i. 16.3 2.1 0 0 6.0 .1
.w c; d.d 2 3 .-1 .0 0 0 1.9 1
.d. 1.6 2 .J .0 .0 1
0 0 0 .0 3.5 3.3 2 .J d .J c.
2.3 2 0 0 .0 0 .o 2.5 3 0 C 0 2.5 1 I LSc 2.5 0 .J 0 .o .0 "
0 3 0 0 0 0 .0 2.1 R Si? 2.1 0 0 13.2 4 W E SS; 4.I d4 3 0 0 1.4 1." 0 0 3 0 .o 2.9 .1 ICs .0 2.1 3 Il f SS.i 1.o ." 0 0 0
.J
.0 ,0
.0
.o 4.9 .1 D L 6W 3.5 1.4 .J 0 2.1 .1 0 ' 5.. 1.o 1 0 .0 .0 .0
.1 0 0 0 .0 4.1 h .1 2.3 1.9 .s 0 .0 8.2 .2 2.1 0 0 0
.. d a 6.2 0 4.9 .1 dd 4.7 2 0 .9 0 .0 0 .3 0 0 18.J 5 i.r. e 12.e . b.8 2 1.9 C Ai .t 1.9 ------- -----~~-----~~~~-------
.. -- --- ....--------- ----- 1*>0.0 1 2 9 .J'
.0 TurAb 74.9 24.9 .J 4.5 ebact;i.T r'JR Sots ria.lRS
- 23. riO9:<J M d AJ Ost AI S$1rk. D A T A dit 4A-11 11Fav
TABLE 4A (cont'd)
Joint Frequency Distribution 10 Meter Level l
SLIGHTLY STABLE STABILITY CLASS E
- PERIOD OF RECORD
- 1/1/84 000 Hours 4/1/84 000 Hours WINDSPEED(m/sec) la A/J 15-17 AUD IJP TOTAL SPdZa8 o-2 3-S 6-8 9-11 12-1. .1 l 6 .0 0 0 6.4
- s. 5.3 1.1 0 0 .u 4.7 0 0 .o 0 .O 9 i, W r; 9.7
.o 3 0 3.1
.a d 3.1 0 .0 .O 6.4 .1 0 .0 0 .0 .0 0 dE 6.4 0 0 0 .0 S.2 .1 0 *d a.s 1 .0 3.1 0 0 0 .9 .0 .0 .u 1 r.Sc 3.1 .
0 0 0 .0 7.9 1 0 0 2 R Sr; 7.9 0 0 .0 .o 10.7 d E SSc 6.i 2.5 .0
.0 0 8.0 2 1CS 6.9 1.1 .J .0 .0
.1 0 9 .o 0 .0 4.9
- 14 T SSW 3 . .a 1.4 0 0 .0 0 .0 4.7 .1 1.1 D I Su 3.o .u 3.0 .1 2.7 3 .0 0 .a .0 0
U .a d e!
0 .0 0 3.1 l
3.1 0 .0 6 i s <. 0 6.0 1 i
0 .0 0
.tiv o 5.k 6 .0 6.1 1
) 0 3 ,, 0 0 b.7 5 .0 2
- i. 3 0 9.9 l d.3 1.6 .0 0 .0 0
..i a :4 6.6 CALa 6.o 10.5 0 .O 0 0 0 100.0 .1 j TOTAL 69.5 y .
1.2 pt:RCdr3T r'OR n 4 <. iiodd5 8 liddHS Jf W8 On r:1SSIt.G DATA OR 4A-12 33Eav
- 1 s 1 l
1 I
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4 8 O
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- O m 44 m O c t~ 4 @ 9 8 H e e o e e e e e -e-* o e me-*o e o.-eeCDe 4e30 o
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= be N & _, rq 4&W v M ,
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% S C .M 0e y > E 1 I I U Q .J v 4
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- >< w O G W Q. I
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- 'C 7 T 3 ': .C ' t */? . :4 : ::: s to 0 i : :_' 'J 4 '?. '.': *3 W ') .2 .: J "a U R 2 3
O w % ~;.*'J 9 4
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~. .- _ . . - - - , . - ., _ . , . - .--
TABLE 4A (cont'd)
Joint Frequency Distribution 50 Meter Level 4
STABILITY CLASS A - G PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours WIND SPEED (m/sec) 18 AV3 15-17 AuD UP I O l' A L SP6.:,D 6-2 3 6-8 9-11 12-16 i
'.2 0 .o 0 .a 9.1 .3 1 i 9.o 4.2 .2 0 0 .0 4.5 .1
.. M; 2.9 1.6 .0 0
.1 2.4
.) 0
.0 0 0 0 I . . f. l.i 2.4 .1 0 0 .0 0
! I; L 1.2 1.2 .0 0 4.6 .2
.2 0 .0 9d .a 3.5 .0 0 0 10.6 5 7.d 1.2 1 0 I i.Sd 1.5 8.8 .4 1.1 0 .J 0 .v it SC 1.s ca . 4 0 0 .0 7.1 3
.d d SS6 1.3 4.3 1.5 .G 0 .u 4.3 .1 ICS 1.6 2.6 .1 0 .J
.1 0 .u 0 .0 4.4 il T SSa 1. 's 2.4 .J 0 .u 5.9 .2 4
o I du 'e . 'l 2.9 .3 0 0
.2 i 0 0 0 5.2 O '.iS J 2.n 1.9 6 .o
.o 6.1 .2 3.6 1.8 .S 4 0 .C il u 6.7 3
- 6. 15 2.7 2.7 1.3 0 .o 0 0 1
3.4 2.9 .1 0 .0 0 .u 6.5 2
.. e 10.1 3 4.5 1.2 .1 .o 0 .0 .4
- i. i i i .' 9 i
Ch u.L 4.3 S1.8
... ..8.9
.7 0 .0 0 100.0 ....... .2 l TisTAL 38.6 .
i 181'. apjJdd of 3AD OH f.ISSING DATA ud 8.3 l'6kCE:nT FOR 2185 liodRS i
4A-15 33Fav . - - ~ - - - - - - _ _ _ _ _ _ _ _ _ _ _ __
TABLE 4A (cont'd)
Joint Frequency Distribution 10 Meter Lovel STABILITY CLASS A - G I PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours i
J WIND SPEED (m/sec) 18 AVJ A!.:s UP TU1AL 3?h:d;n 3-d 6-6 9-11 12-1i 13-17
.i.2 0 0 .J 0 .0 8.0 2 i .. o . a. 1.1 0 0 4.6 .1
..iiC .1 .0 0 .0 3.0 0
...)
1 0 6 .o 0 .o
. . r: 2.) S.3 0 0 .0 .0 .J .J 1 ser S.e 0 .0 0 .o 6.6 1
.b.7 1 0 i o u 0 .O 0 0 3 3.7 0
- 1 63a 3.S 2 0 9 4.8 .1 0 0 .d i R Srl 4.7 1 0 0 0 9 R.9 3 W :: SSr; 5.1 3. ij .0 0 .O 0 .o 4.1 .1 ICS 3.4 1.3 .J 0 0 2.7 .a 6 0 0 0 il T SSW 1.(
0 0 0 0 5.5 1 b i .o# 9.1 1.5 .J 0 0 3.7 1 ,
.0 0 .i S .. 3.2 5 .O .o l
6 .0 0 .v 0 .a 4.1 .1
) . e 3.3 0 .C 5.9 1 0 0
..il; 4.7 1.3 0 0 .0 6.0 .1 S.2 8 0 0 .0
' n .1 0 .4 0 0 11.0 3 i . .b; 7./ 3.3 0 11.6
! CAL:4 7.7 .. ....... .. ...............
....... ... .............. ....... .. 0 0 100.0 .1 0 .0 0 4
fuTAL 84.7 13.2 7.7 L'6KCEtiT FOR 2185 HOURS 169. alubi<J ur iii D OR hlSSidG ilA A' A JR 1
4A-16 t
11Fav
d 4
TABLE 4A (cont'd)'
PERCENT BAD DATA REPORT.
4
- PERIOD OF RECORD: 1/1/84 000 Hours 4/1/84 000 Hours i
1
-sadURS . L'c:R Co.4T Sosi L81ste Cfld'8 33. 1.31-f 00, 3.66 sod W 1.sJ bl%.sb l un D1.tr.CTIu.4 33 1.31 Lis.i . u .:.e J Pi.r.D 6 8. - 3.11 Ts 6PKRhidhE o3. J.oO DC.J PJIsi f #334, 43.06 134. u.13 l
DdLTA T PdEC i r> J T A T I Jii 870. 39.62 i
i i
4 1
4 1
33Eay 4A-17
TABLE 48 Joint Frequency Distribution 50 Meter Level EXTREMELY UNSTABLE STABILITY CLASS A PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) 18 AVG 0-2 3-5 6-8 9-11 12-14 15-17 Adu UP TOTAL SPEC.D 0 6.6 3
!. ti 1.2 5.4 0 0 .J .0 arid 6 6 .0 0 .0 0 0 1.2 0 3 uC 4.6 2.4 0 0 .o 0 .o 7.2 .2 C4d 3.J 1.2 0 0 .0 .0 0 4.2 .1 DE d.4 1.8 0 0 .0 .0 0 7.7 .2
- I I
- S6 2.6 1.2 0 0 0 0 .0 3.6 .1 R LK 2 . <t 2.4 3 0 ou 0 .0 4.8 .1 l
W C SSE 1.o 3.6 0 0 .0 0 .0 S.4 .2
{
ICS 1.2 1.2 0 0 .0 0 .0 2.4 .1 l
i N T SSW 1.2 .0 0 0 .o 0 .0 1.2 0 D 1 SW 1.6 1.2 0 0 0 0 .u 3.0 .1 4.2 .0 0 0 0 .0 8.4 3 O USd 4.2 i N w 4.2 12.0 1.B 0 .0 0 0 18.1 .7 j W4W 2.4 12.6 6 0 .0 0 .0 15.7 .7 4W 3.0 6.0 .0 0 .0 0 0 9.0 .3 min .u 6 1.2 0 .0 0 .0 1.8 .1 CALM .0 0 4
TOTAL 39.7 bb.6 3.6 .0 0 0 0 100.0 2 4
- 0. HtiUHa of BAD Uk h!SSillG DATA flu 0 PERCE.aT FOR 166 HiluRS I
4B-1 33Eay i _ _ _
TABLE 4R (cont'd)
Joint Frequency Distribution 50 Meter Level 1
MODERATELY UNSTABLE STABILITY CLASS B i
PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours
- WIND SPEED (m/sec) 18 AVG U-2 3-s 6-8 9-11 12-14 15-17 Ailu UP TOTAL SPEED il .o 0 9 0 .o 0 .0 .9 .0
- i. T SSn z.6 9 0 0 .9 0 .o 3.7 .1 i D I Sn 3.7 1.9 .0 0 .0 0 .0 b.6 .1 i u v.S d 8.9 4.7 .0 0 .0 0 0 13.1 3 i 11 W 2.8 9 9 0 .0 0 .0 4.7 .1 0 0 9.3 3
.;it ti 4.1 3.7 9 0 .0 l la w 3.1 2.8 .0 0 .0 0 .o 6.5 2 r..hl .9 3.7 .9 .u 0 0 .0 5.6 3 4 CAbri .J .0 TOTAL 42.0 48.6 9.3 .0 0 .0 0 100.0 2
]
1
- 0. !!!!U HL uf DAD OR rilSS1HG 1)ATA Ott .0 PERCEilT FOR 107 ilnURS 4
1 4B-2 33Eay
TABLE 48 (cont'd)
Joint Frequency Distributior.
50 Meter Level SLIGHTLY UNSTABLE STABILITY CLASS C PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) 18 AVG 15-17 AGO UP TOTAL, SPEED 3-d 6-8 9-11 12-14
'0 - 2 0 .O 0 .o 4,6 .2 d 1.5 2.3 .-
.0 8 0 8 .a 0 .0 .0 udE .0 0 0 0 0 2.3 .1 -
e.K 1.d .9 0 0 .0 3.8 .1 9 0 0 9 E:aE 3.o 0 .0 3.8 .1
.8 0 0 .0 DE 3.0 0 0 0 0 .o 2.3 .1
I USd 1.6 3
.o 7.6 2 R SE 3.H 3.o 0 0 .o 0 5
8.4 3 0 0 0 .u 9.9 W E SSE .d 8 .o 0 .0 9.2 4 ICS 1.5 6.9 0 0 0 5.3 2 3.8 0 0 0 il T SSd 1.5 0 0 0 .0 0 6.9 .2
- 0 I SW b.3 1.5 0 .0 11.4 3 a.4 3.0 0 0 .0 4
- u uSn 0 .o 10.7 .2 ,
10.7 0 0 0 .0 11 '.J 0 0 .0 .o 9.2 .3
- k. ii n o.1 2.3 8 0 ou 6.1 .2 r;u 4.0 1.5 0 0 .0 0 0 6.1 2 3.o 2.3 0 0 .0 N riv! 0 C A L.-l .9 i
.......................a............. 0 .0 100.0 2 TuTAL $7.2 39.7 2.3 .u 0 l
.0 PCRCt.i4T VHR 131 HOURS O. !!dbHi, of OAD Uk MISSluG 11ATA nH .
4B-3 99r, ,
TABLE 4B (cont'd)
' Joint Frequency Distribution 50 Meter Level NEUTRAL STABILITY CLASS D 1
PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours 4
WIND SPEED (m/sec) 18 AVG u-2 35 68 9 11 12 14 15 17 Ailu Uu TOTAL SPEED
.4 2.1 0 0 .0 0 0 2.5 .1 14 4 0 0 .2 0 .0 2.5 .1
.lilE 1.9 0 0 1.9 0 laE 1.3 6 0 0 9 l
0 0 0 0 2 2.6 1 Et4 E .9 1.S DE .4 .a 0 0 .0 0 0 $.1 0 2.8 0 0 0 0 4.7 .2 1 ESE 1.7 2 0 0 11.5 .5 R SK 2.o 7.9 9 0 0 3.0 6.6 4.3 0 .0 0 0 14.0 .7 W E SSE 13.1 ICS 2.3 6.6 4.2 0 0 0 .o .6 0 0 .o 6.4 2 N T SSd 3.o 2.3 .o .0 0 0 8.9 .2 6.1 2.6 2 0 0 D I Sri 0 8.5 .2 0 0 0 .J 0 LSW 7.4 1.1 0 6.4 .t 9 0 0 0 0 it >! b.5 S.9 ,2 Wil d 3.4 1.7 8 0 0 0 .o _
0 0 0 0 4.9 2 r.tl 2.o 1.7 0 0 4.5 .3 3 , ,a 9 2 0 0 .0 i.N W 4 CALA 4 TUTAL 47.0 40.7 11.9 .0 .2 0 2 100.0 2 l
.0 PERCErJT ruft 52b itDURS 0, llOul<d JF BAD Olt HISSlalG UATA OR i
11Fav 4B-4
l-TABLE 4B (cont'd)
Joint Frequency Distribution 50 Meter Level SLIGHTLY STABLE STABILITY CLASS E ,
i PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours i UIND SPEED (m/sec) id AVG 02 3-:2 6-8 9-11 12-14 15-17 Ai1D UP TOTAL SPEED fl 1.3. 1.1 1.7 1 0 0 .o 4.3 2 f ied 1.1 6 0 .1 .0 0 0 1.9 .1 i 1. E 1.9 2.4 0 0 .0 .0 .1 4.S .2 Erld .o 3.7 1 0 .o 0 .o 4.5 .2 i U6 1.s 2.9 1 1 .U 0 0 4.o .2 I LSE 2.2. 7.3 .1 0 9 0 .O 9.7 .4 It SC 4.3- 15.6 1.1 0 .J .0 .0 21.1 .6 W C SSS 2.o 9.9 3 0 .o 0 0 12.H .5 ICS 2.1 4.0 1.1 0 0 0 0 7.2 .3 11 T SSd 4.1 1.9 0 0 .7 0 .o 6.1 .2 D I SW 3.B 1.1 0 0 0 0 .o 4.9 .1 u WSW 1.o 6 .0 0 .0 0 0 2.2 0 11 u 3.3 2.4 0 0 .o 0 .o S.7 .2 5.1 4
l UNn 1.3 3.d 0 0 0 0 0 .2 i tid .9 1.4 .1 0 .0 0 0 2.6 1 i tirJ 4 9 1.o .1 .o 0 0 .0 2.7 .1 CALA .0 .0 4
, ..............................................a.......................
TOTAL 33.7 60.b S.1 .5 0 .0 .1 100.0 .2 1
4 1
O. Ild'JitJ OF DAD OR i41SSIt4G DATA Uit .0 PERCdilT FOR 62o HntlRS i
d 1 4B-5 19r.u
TABLE 48 (cont'd) ~
Joint frequency Distribution 50 Meter Level MODERATELY STABLE STABILITY CLASS F-PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours i
i WIND SPEED (m/sec) 18 AVG 68 9 11 12 19 13 17 Ar4D UP TurAL SPEED 02 a.5 0 2.o .1 0 0 .0 0 l l. .9 1.7 ,o 0 .0 2.3 .1
. o' 1.7 0 0 iir4C 0 0 0 3.8 .1
' 2.9 0 0 LE .9 0 .3 3.8 .2
- 1. I- 2.0 0 0 .0 i Ed6 0 0 .0 4.9 .2
' 1.4 3.0 0 0 oE 0 0 0 25.1 .b 12.s 6 0 I ESE 1.7 0 0 18.9 6 R bE 9.0 9.9 .0 0 .0 0 15.4 .S 0 0 0 0
' Wii rl 1.2 1.4 0 .u 0 9 0 0 0 0 0 0 .o bd .9 0 0 .0 2.0 .1
- ^
1.4 0 0 it!! el .o 1.4 j
i ............................................
CALA 42.4 1.' 4 So.7 .6 .0 0 0 3 100.0 .2 TOTAL i
0 P6hCLwT FOR, 344 HOURS l 0. liulhtS UF BAo uk tilSS1tlG DATA UR 4
1 i
4B-6 l 11Fav
TABLE 48 (cont'd)
Joint Frequency Distribution 50 Meter Level EXTREMELY STABLE- STABILITY CLASS G PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours 4
WIND SPEED (m/sec) 18 AVG 15-17 A F. D UP TOTAL SPEED 02 .3 - 5 6-8 9-11 12-14 .1 0 .o 0 .0 2.9 4 0 0
- i. 2.5 0 0 0 0 .o 1.7
!.r4 .6 8 0 0 3.8 .1 0
f.E 2.v 8 0 .J 9 0 0 4.6 .)
2.1 2.5 0 .0 B.0 2 Lud 0 0 .o 0 .o DE 4.2 3.9 0 0 0 10.5 4 h.3 4 0 I ESd 3.d 0 0 0 10.5 .3 4.2 4 0 l R SE b . ').
0 0 0' 0 .o 10.5 .3 i
W C SSd ti . 0 2.S 0 0 .o 10.9 .3 4.2 0 0 ICS 6.7 0 0 .0 0 .o 16.8 .4 Il T bSe 14.7 2.1 0 0 .0 6.7 .1 8 0 0 D I S4 S.9 0 0 .o 5.0 1 0 0
' - 0 45w 4.2 8 0 0 .c 0 3.4 .1 4 0 0 fl .1 2.9 0 0 0 0 0 1.7 Wr4 4 1.3 4 0 0 0 .o 0 .0 0 0
) JW 0 0 0 .o 0 0 1.7 0 i.il W .d 6 1.3 CAL:4 1.3
... . ... ............. .. .............100.0 8 .0 0 0 0
.......... 2 TuTAL 68.1 31.1
- 2 31, sti)U R S 0 PERCENT FOR' O. ItuOi
0 0 1.9 0 tilU 1.9 9 .0 .0 .0 0 0 2.8 .1 D 1; 4.7 0 0 0 .0 0 0 4.7 .1 1 ESr; .9 0 0 0 .o 0 9 9 .>'
H SE 5.b 3 .J 0 0 0 .o 5.6 .1 W L SSE 11.2 7.5 0 0 0 0 .0 18.7 6 ICS 7.5 3.7 0 0 .u 0 .0 11.2 3 il T SS.i 3.7 9 .u 0 0 0 .0 4.7 .1 D I SH 6.4 0 0 0 0 0 .o 8.4 .1 O WSil 11.2 0 0 0 .0 0 .o 11.2 2 si W 5.o 1.9 0 0 .0 0 0 7.5 .1 WI w 9.3 0 0 0 .0 0 .a 9.3 .2 li'i 1.9 0 0 0 0 0 .o 1.9 0
.h171 4.7 2.8 0 0 0 0 .0 7.5 .2 0
CAbd .0 TuTAL 61.3 13.7 0 .0 0 0 0 100.0 1 O . IlO Ul< S U F G A D u rt r11SSilJd DATA UK 0 PEHCE.4T FOR, 107 HOURS
, , r.. . .
i TABLE'4B (cont'd)
Joint Frequency Distribution 10 Meter Level SLIGHTLY UNSTABLE STABILITY CLASS C PERIOD 0F RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) 16 AVG 0-2 3-b 6-d 9-11 12 14 15 17 AtaD UP TOTAL SPEED d 3.0 2.3 0 0 0 0 .0 5.3 .1 tellE 3.0 8 0 0 0 0 0 3.8 .1 0 0 0 0 0 .6 . 8 0 DE .o ENE 3.0 0 .V 0 9 0 .0 3.0 .1 DL 2.J. 0 0 0 0 0 0 2.3 0 1 ES6 3.0 0 .o 0 0 0 .0 3.0 .1 R SE 3.0 0 0 0 .0 0 0 3.0 0 W E SSd 3.0 2.3 8 0 0 0 .0 6.1 2 0 13.0 4
NW 8.4 8 0 0 0 0 .0 9.2 .2
- iPi r.' 4.0 1.5 0 0 0 .0 .o 6.1 .1
. 0
- CALH .0 TOT Al. b6.2 IJ.u 8 .0 0 0 .0 100.0 .1 9
l 0 HOURL of t$AO UR M1bSIllG DATA Oit .0 PERCEi4T fur , 131 HOURS 4B-10 i W~ _ _ _ _ - - - - _ _ - _ - _ _ _ _ _ _ - _ _ _ - _ _ _ _ _ _
TA8LE 48 (cont'd)
Joint Frequency Distribution 10 Meter Level NEUTRAL STABILITY CLASS D PERIOD 0F RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) 18 A Ve, 02 3.d 6-8 9-11 12 1% 15-17 Atau UP TOTAL SPEEli a 2.3 1.1 0 .o .0 0 0 3.4 .1 t.rl d 1.J 0 .0 0 .0 .0 0 1.3 .0
'J E '3.1 2 .u 0 0 0 .0 3.6 .1 EHC 3.4 0 0 0 .0 0 .0 3.4 .1 DC 2.5 2 0 0 .0 0 .0 2.6 0 I ESE 2 .' 1 2 0 0 0 0 0 2.3 .0 R SE 4.2 2 0 0 .0 0 .0 4.3- .1 W E SSE 7.9 6.6 0 0 0 .0 .0 14.6 .4 ICS a.7 7.9 .0 0 0 0 0 lb.7 .S ti T SSn 7.0 9 0 0 .0 .0 .0 7.9 .1 D I dW 10.o 2 0 0 0 0 .0 11.0 .2 0 WSd 6.4 0 0 0 .0 0 .0 6.4 .1 la w S.S 0 0 0 .0 .0 .o S.5 .1 WNd 6.1 6 0 0 .0 0 .0 6.6 .1 NW 4.7 4 0 .0 0 0 0 5.1 .1
- 1. ti d 2.6 0 0 0 0 0 .0 2.8 0 CALH 2.3 2.3 TlaTAL 81.4 18.6 0 .0 0 0 0 100.0 .1
- 0. litlURJ ur BAD Un< .ilSSilhi D ATA OR .0 PERCE'4T FOR 521., liquRS B-11 33Eay
TABLE 4B (cont'd)
Joint Frequency Distribution 10 Meter Level SLIGHTLY STABLE STABILITY CLASS E PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) 16~ AVG 1 0-2 3-5 6-d 9-11 12-1e 15-17 Allu UP TOTAL SPEdD i; 3.3 6 0 0 .o 0 .0 4.0 1
.;:J E 3.6 0 0 .0 9 .o 0 3.8 0
.1 0 0 0 .0 .o S.6 .1 j ud 5.4
.1 1 0 0 0 0 .0 5 . t>
LtJ d 5.4
)
5.7 .1 0 0 9 0 .o 5.9 .1 i DE 1 .56 1.b .1 0 0 0 .0 .0 4.9 .1 R SE 5.3 ~ .S 0 0 0 0 .0 5.7 .1 W E SSd 12.3 1.1 .O 0 0 0 .o 13.4 .2 4
ICS 13.1- 3.0 0 0 .0 0 .0 16.1 3 I 0
.1 0 0 0 0 0 4.0 N T SSd 3.0 j p i SW 3.B .1 0 0 0 0 .o 4.0 0 0 0 0 0 4.1 0 0 .lS d 4.1 0 0 iJ W 3.5 0 0 0 0 0 .0 3.5 0 0 0 0 0 0 0 2.9 .0 w' i d 2.9
- i d 2.2 0 0 0 6 0 0 2.2 0 l
4.3 0 0 0 0- 0 0 4.3 .1
.r J W CAbh 9.7 9.7 l ..................... ......................... ...............---....
I TuTAL 's3.8 6.2 .0 .0 0 0 .0 100.0 .I i, .
.0 PEHCd G FOR , 626 HOUrls
) O.-Il0dRS OF dAv On PISSil4G UATA OR "Fa" An-1?
TABLE 48 (cont'd)
Joint Frequency Distribution 10 Meter Level i
MODERATELY STABLE STABILITY CLASS F
':RIOD J OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) l 18 AVG 0-2 3-a 6-8 9-11 12-14 15-17' A.o UP TOTAL SPdED 0 0 0 0 2.9 0
- i. 2.9 .u 3 a:lt: 3.2 0 0 0 .0 0 .0 3.2 0 E 6.1 0 .0 0 .u 0 .0 e.1 .1 EllE 10.7 0 .) 0 .0 .0 0 10.7 1 DC 10.7 0 0 0 0 0 .0 10.7 .1 0 0 0 5.5 3 I r:SE 5.5 .o 0 0 1
i R de o.7 0 0 0 .0 0 .0 6.7 .1 I w E SSE 7.3 0 0 0 .0 0 .0 7.3 .1 0 0 0 0 0 0 3.5 0 1
1CS 3.5 i N T SSW 2.3 0 .0 0 .0 0 .0 2.3 .0 D 1 Svl 1.7 0 .0 0 .0 0 .0 1.7 0 0 0 0 .o 0 ,o .9 0
! O tiSn .9 il w 3 0 0 0 0 .0 0 3 .0 11:1 4 1.2 0 .0 0 .0 0 .u 1.2 0 N .1 1.2 9 0 0 .0 .0 .o 1.2 .0 0 0 0 .0 0 .0 1.4 0 l . s h. 1.4 CALH 34.3 34.3 100.0 TOTAL tu0.0 .o 0 .0 0 0 0 1 l
O. HUURu UF bad OR d1SSING DATA OR .0 PERChriT FOR '
344 tiOURS 4B-13 33Eay - - . - - _ _ _ _ _ _ _ _ . _ _ _ _
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TABLE 48 (cont'd)
Joint Frequency Distribution 4
50 Meter Level
, STABILITY CLASS A - G PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours WIND SPEED (m/sec) 1 18 AVG 0-2 12-14 15-17 3-6 6-8 9-11 A JD HP TOTAL SPEED IJ 1.1 1.7 6 0 0 0 .0 3.4 2 OtJE 1.0 7 0 0 .0 .0 .0 1.9 .1 DE 1.9 1.7 .0 0 .0 0 . 0. 3.6 .1 E JE 1.4 2.2 0 0 .0 0 .1 3.8 .1
, DE 1.9 2.4 0 0 .0 0 0 4.3 .1 I
I UStd 2.1- 5.9 3 0 0 .0 0 8.4 .3 I R SC 4.7 9.3 6 0 .0 0 .0 14.6 .5 I W E SSE 3.u 7.5 1.3 0 0 0 .0 12.6 .5 1.5 ICS 2.9 4.5 0 0 0 .0 9.0 4
.2 N T SSW 4.7 1.9 1 0 .0 0 .0 6.8 i D I Ski 4.4 1.0 0 0 .0 0 0 6.2 .1 l . O WSW 4.3 1.1 0 0 .0 0 0 S.7 .1 i i4 t! 4.2 2.3 2 0 .0 0 .0 6.7 2 WNW 2.3 3.1 3 0 0 0 .0 5.8 .2
- li d 1.8 1.5 2 0 0 0 .0 3.5 .1
] IJil d 1.6 1.4 2 0 0 0 .0 3.2 .1 d CALM 1.6 .5 TOTAL 44.b 49.o 5.5 .2 .0 .0 .1 100.0 .2 j 44. HuuRL ul' DAD uR MISSING DATA OR 2.0 PERCEllT FOR, 2184 HOURS s
l i
4B-15 j Wav
TABLE 48 (cont'd)
Joint Frequency Distribution 10 Meter Level STABILITY CLASS A - G PERIOD OF RECORD: 4/1/84 000 Hours 7/1/84 000 Hours
- WINDSPEED(m/sec) 18 AVG i 0-2 3-5 6-8 9-11 12-14 15-17 Arid UP rural SPEED li 2.4 1.0 0 0 .u 0 .u 3.4 .1 taild 2.7 1 .0 0 0 0 0 2.7 0
- LC 4.3 1 .0 0 .0 0 .0 4.4 .1
- Eii t. 0.6 1 0 0 .0 0 0 6.7 .1 D 1: 5.o .1 0 0 .o 0 0 5.9 1 I CSd 3.o 1 0 0 0 0 .0 3.7 0 i R SC 1.5 .2 0 0 0 0 .0 4.7 .1 W E SSE 7.o 2.6 0 0 0 .0 .0 10.3 .2
, ICs 7.9 3.4 0 0 .0 0 .0 11.4 .3 il T SSW 4.1 4 0 0 .) 0 .0 4.6 1
- D I SW 5.o 1 0 0 0 .0 .0 5.6 .1 0 WSW 5.0 0 .0 0 0 0 .0 5.0 .1 l .1 il u 4.7 1 .0 0 0 0 0 4.8
.J tJ W 4.4 2 0 0 .0 0 .0 4.6 .1 taw 3.2 2 .0 0 .J 0 .0 3.4 .1 f.fi:1 3.0 3 0 0 0 0 .0 3.3 .1 CALn 3.) 15.4 TOTAL 90.9 9.1 .0 .0 0 .0 .0 100.0 1 44, iluUib UF dAu UR dISSIl1G DATA OR 2.0 PCRCDJT FOR ' 2184 HOURS t
33 Fay 4B-16
TABLE 48 (cont'd)
PERCENT BAD DATA REPORT
~
PERIOD 0F RECORD: 4/1/84 000 Hours 7/1/84 000 Hours l
houRd- PdH Ct.;iT 4 SOM 01HCerla.v 1. .05 SGM dia.s dPCC.; 1 .05
} lur4 UlHCCTIuri 1. .05
) 10% '.firsD SPEED 1. .0S TEMPERATuicE 1. .05 DEW POI;1r 85. 3.ti9
- DELTA T g4. 2.J1
,' PRECIPi r AT1 oil 2164. 10u 00 1
I 4
i 1 ,
I i
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~
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~
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~
Table 4C ,
w
-w CLASSIFICATION OF ATMOSPHERIC STABILITY Stability Pasquill c6* I Temperature Change Classification Categories (degree.s) '
,with Height (C/100m)
Extremely Unstable A 25.0 <-1 . 9 Moderately Unstable. B 20.0 -1.9 to -1.7 ,
Slightly Unstable C 15.0 -1.7 to -1.5 Neutral D 10.0 -1.5 to -0.5 Slightly Stable E 5.0 -0.5 to -1.5 Moderately Stable F ' 2.5 1.5 to 4.0 Extremely Stable G 1.7 >4.0
- Standard deviation of horizontal The windvalues direction fluctuation over a shown are average.for period of 15 minutes to 1 ho'ur.
each stability classification.-
s 3
l\ ,
t 1
't A
\
I Table 5 ,
RADIOACTIVE LIQUID WASTE SAMPLING AND ANALYSIS PROGRAM Lower Li=it !
Liquid Release Sampling Minimum Type of of Detection !
Frequency Analysis Activity (LLD)
Type (pCi/ml)
{.
Frequency Analysis Batch Waste P P Principal Gamma ,-
A. d 5x10
Release Each Batch Each Batch Emitters Tanksc '
~
P M Dissolved and 1x10 One Batch /M Entrained Gases (Gamma emitters) 1x10
-5 P M H-3 b
Each Batch Composite
~
. Gross Alpha 1x10
-8 P Q I#~09' Sr-90 5x10 b
Each Batch Composite
-6 Fe-55 1x10
~
B. SSW Basin PrincipagGamma 5x10 (prior to Each Each Batch Emitters blowdown) Blowdown
-6 1-131 1x10 e
5-1
_m__ __ _ __.
l
/
TABLE'6 RADI0 ACTIVE GASEOUS WASTE SAMPLING AND ANALYSIS PROGRAM l 1
I
-=
Gaseous Release Sampling Min h = Type of Lower Limit Type Frequency Analysis Activity Of Detection Frequency Analysis (LLD)
(uci/al)a A. Containment Mb +
gb Principal Gamma lx10-4 Ventilatica Grab Ssaple Emitterse Exhaust H-3 lx10-6 B. Turbine Building Mb gb Principal Gamma 1x10-4 ~
Ventilation Grab Sample Emitters
, Treatment M M Principal Gamma lx10-4 Exhaust, when-ever there is flow Grab Sample Emitters
- D. (1) Radwasta Building Continuousd ye I-131 lx10-12 Ventilation Charcoal Exhaust Sample I-133 lx10-10
~
(2) Fuel Hand-ling
- Continuousd ye Principal Gamma lx10-Il Area Ventila- '
tion Exhaust Particulate E v tres*
1 Saaple (b7M Cthers) e
- g. -.
(3) Containment Contir.uous d M Grues . Alpha 1x10-II Ventilation l Ccaposite Exhaust Particulate ,
Sauple
. i (4) Turbine .
Building 'Co.ntinuousd Q Sr-89,St-90 1x10-11 Ventilation Composite Exhaust Particulate Sample Continuous f Noble Gas Nob]e Geses lv10~'
Monitor Gross ieta
, or Gane.a i 1 Note: Footnotes indicated are listed in GGNS Technical Specifications, Table 4.11.2.1.2-1
.m - - . - - , ~ . - -
ATTACHMENT I PROCESS JONTROL PROGRAM INCIASURE I GRANu .u t.t NUCLEAR STATION TYPICAL IhSTRUCTIONS/REOUIRDENTS TO BE PLOVIDED FOR SOLIDIFICATION OF RADWASTE SLURRIES AND EVAFORATOR BOTTGtS CONCElffRATES A. General
- 1. The Radvaste Solidification System is designed to six waste slurries and evaporator bottoms concentrates with specific proportions of Portland Cement and Sodium Silicate in order to obtain a solid with definite shape and no free water.
~
- 2. Each of the two mixing " trains" (i.e.. Trains A and 5) is provided '
with the ability to select one of nine generie weste stresas identified by numbert Stream #1 - Weste Surge Tsaka (condensate filter backwash)
Stream #2 - ENCU Phase Separator Tanka (EWCU and FPCC filter domineraliser backusah)
Stress #3 - Liquid Radweste Floor Drain Filtet (Idades)
Stream #4 - Ladweste Equipasst Filter (Ecodex)
Stream f5 - Basina 5-05 from condenaste and Liquid Radweste Stream f6 - Evaporator Bottoms from Basin Sageneration Stream f 7 - Evaporator Bottoms from misce 11===s chemicals Stream #8 - Evaporator Bottoms from Floor Drain Wastes Stre.4 #9 - Future
- 3. Parameters have bees established for various pump speeds required to asintain correct flow rates within the system. These have been preset within the system Modicoa Prograsmable controller. Ubon a particular stream type is selected, the controller will operate the various pumps as required for the solidification process. at speeds appropriate for the vase.4 stress type being process.
- 4. The operator will determine which specific generic batch the weste input represents (using methodology specified in Section 3 of this Enclosure) and select the corresponding generic batch position before starting the solidification process,
- s. The operator is not authorized to " adjust" the individual process pump speed settings without apecific authorization from the Radweste Supervisor.
b.. If.the waste input cannot.be categorized into a specific generic batch using Section B of this Enclosure. a ~ sample of the waste input will be obtained and analyzed. Pror. ass selection is then made using Section D of this Enclosure.
- 5. The Solid Radwaste System will be operated in accordance with CCNS operating pro:edures in a manner which will permit segregation of waste inputs into generic batches. With proper segregation. the only parameters that are variable are pH (applicable for evaporator
_i_
B46phl e
bettus.s only) and percent solids. Categorised wastes will be conditioned to adjus6 Ene pu and solid / liquid content within boundarj cor.ditions and then soliditied as a batch with no f urther additions of solids or liquide into the respective waste holding tank (s) until the batch is completely processed.
- 6. beste holding tanka A and 5 should be normally used only to collect radv.vte equipment drain filter and floor dr-*n filter discharges ,
(Ecodez) respectively. Liquid additions any to from the Condensate and Rafueling Water Storage and Transfer System (CRWST) or regenerant evaporator bottoms.
- 7. Waste holding tank C should normally be used for spent resin discharges and filter and filter /demin (Ecodes) sludge with liquid additions from regenerant evaporator bottoes or CRWST.
- 8. Reactor Water Cleanup Systen (RUCU) filter /devin sludge (Ecodes) is, typically, approximately one hundred tisse higher in specific activity than other sludges processed and should be segregated from other wastes and handled with estra care. RUCU filter /demineralizer sledge is normally processed through vaste holding task C.
- 9. Evaporator bottone shonid norus11y be processed through vaste holding tank C.
- 3. Cetegorisina Weste Boldian Taak Costents fato Specific Generic Sotches
- 1. A knowledge of the sources of sludge and segregation of specific types of waste inputs is esseatial.
- 2. The operator will determine from the Water Treatment /Radweste Logbook the type and volse of waste to be transferred to the waste holding tank. Typical impute will be:
- a. Spent resin tank contents; bead resin from the condensate cleanup domineraliser or radveste (i.e. floor drain or equipment drain) dessineralisers.
- b. Filter sludge from the condensate cleanup filter; (Ecodex).
- c. Filter sludge from the RUCU and FpCC filter /deafneralisers; (Ecodex).
- d. Tilter sludge from radweste (i.e., floor drain or equipment drain) filters; Ecodex.
- e. Evaporator bottosa from rebenerant cf resin will notes 11y be 251 sodium sulphate with trace amounts of other dissolved solids and suspended solids,
- f. Evaporator bottoer fros' floor drains will normally be 25% to
! 501 suspended solids with dissolved solids signifteantly below saturation.
3 Evaporator bottoes from miscellaneous chemical waste will normally contain dissolved solids from water treatment chemicals (sodium nitrate. TSP). pH neutra11:ers (H2504 or NaOH). miscellaneous laboratory wastes and trace amounts of suspended solids.
(
~
BEST COPY AVAILABt!
u p n.-
1.
I
~
l obtain adequate information from the inline
- 3. If the operater cac nat instruments (pH. corac-tivity. aco radioactivity) to tetegorize the f waste as a speci:ic generic type des'.gnated f or soliuit ;s.t i.n. s grab sample will be taken, analysed and categorized.
- a. If the batch does not fall within the boundary conditions for any of the specified generic types processing will be in accordance with Section D of this Enclosure.
the various
- 4. A sampling pregram will be established to ascertain that individual batches a.e within established boundary conditions for specific generic batches. Sample analysis will be as follows:
NOTE: The sample shall be analyzed f or pH. conductivity, total -
suspended solids (TSS). silica or presence of oil or grease to determine if its constituents are similar to the original specific generic type or may be solidified in the laboratory using the proportions of solidifying agents specified for the original specific generic type.
a.
It any sample indicates an off-standard batch (i.e., outside the boundary conditions for the specific generic type) the .
sampling frequency will be increased to a higher rate.
- b. Samples will be smalysed from each batch of miscellaneous chemical evaporator bottoms to assure the batch is within the boundary conditions for the generic type.
- 5. If the sampling program indicates a trend in specific generic type constituents beyond the boundary conditions originally established, the Process Control Progree will be modified to assure continuing proJuction of acceptable solidified wastes as follows:
- a. New specific generic types will be established with appropriate changes to the proportion of solidification agent (s).
- 1. These new specific generic types will be tested in a menner similar to the original test program.
b.
Tests will be conducted to determine the acceptable changes in the boundary ccnditions for existing generic types based on the analysis trends.
C. Conditiening of Specific Batches of 'Jasta Conditioning waste holding tank contente for solidification of as thea slurry soectric te geactic type will corsist of adjusting the water content within the solids / liquid boundary conditions and pH to withte the pH beundary condition = specified for the particular vaste.
3 BEST CorY AVAILABtf y;,
u
- 1. nadwasr. .fiter 9.udre as transferred tr the waste holding .ank may )
have an exce4s of solids and therefore need liquid added te preparc it tor sclidification as generic stress #3 or f4 (20% or 27 solids). !
- a. *= *i t ii the ag'tator OFF. add regenerant evaporator bottow. <
(preferred source) or condensate and refueling water until '
there is an observable change in tank level.
NOTE: This will assure that the filter sludge is sufficiently wet to prevent agitator overload,
- b. Turn on agitator and add liquid an indicated cr. sampn.
Attachment 1 (later). to obtain a 201 by weight mixture or Attachment 11 (later) for a 271 by weight aisture.
- c. Start the agitator at least 30 minutes prior to solidifying to assure a homogeneous mixture.
- a. Transf er sludge from the phase separator until the level in the vaste holding tank is (later 1).
- b. Allow contents to settle for at least four hours, then decant ascess liquid to the RWCU phase separator until the decent pump trips.
NOTE: This will leave approximately 1" of free standing water above the sludge.
- c. Start the agitator and add liquid from the regenerant evaporator httoes (preferred source) or condensate and refueling water as indicated on graph. Attachment II (later).
to obtain a 271 by weight mixture.
- d. Start the agitator at least 30 minutes prior to solidifying to assure as homogeneous mixture.
- 3. Spent resin beads as transferred to the waste holding tack have an excess amount of water which must be reduced to prepare it for solidification as generic stream #5
- a. Transfer resin from the spent resin tank until level (later) is reached in the waste holding tank.
- b. Allow contents to settle for at least 30 minutes, then decant excess liquid to the RWCU phase separator until the decant pump trips,
- c. The mixture is now ready to process with approximately 251 by weight of solids.
- d. Start the agitator at ? east .0 minutes prior to soliditying to assure a homogenous mixture.
4 Fegenerant eva;vratpr. bottoms as transferred from the evaporator bottoes tank sc.. be added (after' pH adjustment) to filter, domineralizer. or filter /demineralizer sludges to adjust liquid content as required for specific generic batches or may be solidified directly (i.e., without combining with any additional water as a generic batch.)
- 5. Evaporator bottoms as transferred to the waste holding tank will be
=cliHfied dir.ctiv .1= generic stream f6 or #7, or #8.
-t.
BEST C0FY AVAILABLt bl.a;d -
,,4.. -
1 F9acsSS couTest Faoeman I TABLE I t
i suEAM __. _3T RERAE 5 OR eras AL 00b M
^
! a SGWBCES SATCH WASTE TTFE 79aCESS PASABETERS com1710ps (Ceeest/Weste hatie) i I Condeneste Filter .
Backwash Weste Surae Tanke Ecodes Solid Contente (Later) ,
j 2 FWCU 4 FPCC Filter thase Separator Backweeh Tanks Ecodem Solid Comteste (Later) - =
- 1 1.iquid Radweste Weste Molding s
Floor Drain Filters Tanke A or S Ecoden Solid Centeste (Later) l 0 Liquid Radweste' Weste Holding Equipment Drain Tank A or S Ecedem Solid Coatsets (Later) l 5 Reste Beede Spent Reeles Spent Boein Tank N-Oll 35. Solid Centente (Later)
! 5 Evaporator Dettene Evaporator 50 l (Reseneration) Bottes Tanka Me$1dk So pII. Solid Osetente (Later) 1 7 Fvaporater Bottene Evaporater (Misc. Cheetcals) Betten Tanke Solide 35. Solid contente (Later) l A Evaporator Bottoes Evaporation Botton l (Floor Draine) Tanks Solida DE. Solid Centente (Later) .
! U nn 9 Future (Later) (Later) (Later) (Later) 4 d
l
' 4 i
8 p.
- . . a. .. y . . .
! - y 1"F.t$l, 44 w
. ., m
?, @
- E29tst i
I
D. _
Adb 4*yent/Cep.m.inni g f, Men-Specifte Batche* af Waste AdjustmentlanJ1 tinning of non-specific batches of was's (i.e.. w st 3 not catesurized as ;. ... batch unter) through (late r) .
- 1. If a batch of waste car.not be identified as a specific generic batch designated in C.1 through 5 (above), a grab sample of the M we we will be obtained and the following steps will be performed:
- a. The chemist will analyze the test sample for activity. pH.
conductivity. TS.: silics, and presence of oil or grease.
- b. With the above data, the operator will adjust the vaste to within the boundary conditions of a generic batch,
- c. A sample of the batch wi31 be mixed with cement and sodium silicate according to ratios specified for that generic batch and verified to solidify after a 30 minuta cvring time with rie -
free water.
- d. If the batch is not solidifiable using any of the specific generic batch feed rates available, the operator will receive guidance from the Radvaate Supervisor.
E. Samplina for verification of Solidification Systes
- 1. For batches of specific generic wastes processed according to Section C of this Esclosure, (other than every tenth or twentieth batch) no effluent sampling for verification of solidification is required since these have been proven to be solidifiable in the preoperational test program and this process control proeram. '.
- 2. For batches of non-specific wastes processed according, to Section D of this Enclosure, a grab semple will be obtained and ana13 :ed to determine if its constituents are within the specified parameters of a generic type.
- 3. If the test sample of non-specific waste fails to f all within the boundary conditions for a generic type of weste, the following shall be done:
- a. Ef fluent will be collected in three 500ml plastic beskers,
- b. Three proportions of polidifying agents, specified by the Radweste Supervisor will be added to the three test samples.
- c. The threa test samples will be allowed to cure.
- d. The cured product will be split to verify the mass is a solid with definite shape and no free water.
- e. The test sample proportions used to produce the best product, as deter-ined by the Radwerte Supervisor, will be used for solidifiestion of the non-specific waste.
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Enclosure 2 CRAND CULF NUCLEAR STATION IAOCESS CONTROL PROGRAM .
December 9. 1981 .
P BEST C0Fi AVAILABLE
..3.
CRMD CUI.T NUCLEAR STATION t>ROCESS CONTROL PRMRAM
- 1. Interfaces:
A. The Radwaste Solidification Systes receives wet waste input = free the followinR:
Equipment Drain Filter (D001).
Floor Drain Filter (D003).
Evaporator Bottoms Tanks (A014 A and B)
Spent Kesin Tank (A007) e RWLL Phase Separator Tanks (A010 A and B)
Waste Surge Tanks (A002 A and B) .
B. Support Systems include:
Radwaste Building Ventilation Condensate and Refueling Waste Storage Liquid Radwaste Eqefreent and Fluor Drains Instrument Air Service Air 125V DC
'30V DC 120/208V DC II. Operable Solidification Systes Equipment required:
l A. Either A. B or C Waste Boldfog Tank (A001 A. B or C) and assosi.ted Waste Metering Pumps (C001 A. B. or C).
l E. Either A or B train solidification equipment including:
1 Cement feeder valves (D005 A or B).
Air slide conveyor (D017 A or B)
Mixer feed pump (D002 A or B)
Chemical addition pump (C002 A or B)
F111 port (D006 A or B)
C. Transfer cart 2nd capping mechanisa D. Overhead crane III. Interlocks / Instrumentation required:
A. On the opersble Waste Holding Tank:
- 1. Level monitor and associated level alarms (Mi and Low)
.-.v
- b. .On the oper ble mix. .. u .
- 1. Pump discharre low .. e==itre switches and associated lights for waste metering pump. chemical additive setering pump, and mixer feeder
- 2. Drun in blace switch and associated light
- 3. F111 pore down wwitch and associated light BEST Copy Anu am re ;
.. Ne ect fPsw w ach and associated light
- 5. Easte cc.atainer full switch and associated annunciator C. Medit .. ;.rograsraatse controls or manual override controls..
IV. Administrative Controls:
A. Administrative procedures will require that:
- 1. Directions for extensive or couples jobs where reliance on 1 memory canno: he trusted shall require the written procedure to be present and referred to directly.
{
- 2. Directives shall include appropriate quantitative and/or qualitative criteria for verifying that the esecified activitics have been satisfactorily accosylished.
- 3. Operation of the Radwaste Solidification System will be performed by operators using a dire:tive, meeting the Administrative Procedura requirements in IV.A (above) and in accordasca with GG1tS Operations Procedure.
C. Access to process flow control Olodicos Program) will be limited to the Radweste Supervisor or his designated alternate.
T. The interlocka/ instr'umentation provided in III (above) will assure that:
A. The operator knows the level in the Maste Eelding Tank.
- 3. Process flow ir established in all required flow paths.
- 1. This will prevent the introductico of waste to the shipping container without the proper solidification agents.
C. The shipping container is in place under the fillport and the f111part lid is sealed against the container before any process flow can start.
D. The shipping container will not be over filled.
VI. Sampling and Process Parsesters:
A. This section and Raclosure 1 of the Process Control Program will establish the program of sampling, analysis, and verification of solidification. which is necessary to insure couplete solidification of each type of radioactive waste.
- 3. The minimum sampling requirement for verification of solidification is every tenth batch of each ty,w of waste ascept for floor and equipment filter sludges which will be required to have see representative sample at least every twentieth batch.
C. The representative test specimen will be obtained for verification of solidification f rom the first five (5) batches of each generic stream af ter the plant startup to obtain operational characteristics of process parameters.
D. Batch. Process Parameters, and boundary conditions are defined in Table 1.
E. Verification of solidification is as follows:
2 w BEST COPY AVAlLABLE
- 3. T1.ree te-: . :gles docal; sill be taken la plastic beakers.
- 2. The de. age. proportions of solidifying agents. (Table 1), will be aJdco to all test samples.
% Ic:. sampler '11 he allowed to cure. The cured product will be split to verify the ass. 12 a solid with definite shape one no free water.
4 ~ All test samples must past solidification tests. If test fails, retest as per Section E.3 of Esclosure 1.
VII. Packaging Procedures The total contained activity, external dose rate. surface contaminaties, and physt:a1 form of solidified waste will be verified to be withis limits prior to shipment.
A. Containers will be remotely smeared and decontaminated prior to storage.
- 1. Containers that are met within limits will be usamally decontaminated and re-smeared.
B. The caria content of each container will be estimated from the
.! following parameters: ,
- 1. hypeofunstecontained(corrosionproducts,fissionproducts or mined).
- 2. Mid plane, centerline container dose rate.
- 3. Density of asterial is container.
- 4. Geometric configuration.
- 5. Correction factor (C).
C. An isotegic analysis will be performed on every tenth batch of waste input to the solidification system.
l l 1. Total activity in a container will be calculated from the isotopic analysis.
- 2. The calculated activity will be compared to the estiasted activity.
- 3. The correction factor (C) will be adjusted, as necessary, to assure that the estiented activity is greater than or equal to the calculated activity.
l D. Plant operating instruction 04-5 45-4. "Freparation of Solid i
Radwaste for of f Site Shipment" shd1 be followed to assure that the requirements of 49CFR Parts 100 to 199. " Transportation", 10CFt20, and 10CFR70 are met.
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. ATTACHMENT II PROCESS CNTROL PROGRAM DESCRIPTIN GRAND GULF NUCEAR STATICN February, 1984 GRAtO GULF, UNIT 1 Rev. 1 - 2/84
Revision No. 1 Date 2/84 GRAND Gulf NUCLEAR STATICN PROCESS CCNIWL PROGRAM DESCRIPTICN SAFETY RELATED EVAIDATION APPLICABILITY SArrri EVALUATICN DNIRCNOfrAL EVALUATICN APPLICABLE h APPLICABLE h NCTI APPLICABLE X NOT APPLICABLE Reviewed / Approved dm [Md//We s 8/ /S N 6 Supervisor of Radiological SMvices/Date i
Reviewed / Approved: %, o m b _d Q/ /f/8 9' SupEntsor'of Diviromental Services /Date Reviewed / Approved: , /
Manager of Radiologip & Environmental Services /Date Reviewed / Approved: 'I # ' N Manager of Nuclear Services /Date Reviewed / Approved: j- - A/8/efC/
Chaittaan, Plent safety Paview Ccanittee/Date i
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GRAND GUIF, UNIT 1 Fev. 1 - 2/84
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PCP TABLE & CONIDfrS Page i
DESCRIPTION APPR NAL SHEET. .........................
ii TABLE & CONTDirS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
iii LIST & trut nVE PAGES . . . . . . . . . . . . . . . . . . . . . . . . . . . .
1 A. Introduction ..................................
1 B. Administrative Controls . . . . . . . . . . . . . . . . . . . . . . . .
2 C. Waste Stress .................................
Conditioning of Specific Batches of Waste ..... 2 D.
3 E. Sanpling for Verification of Solidification ... 3 3
F. Packaging Requirments . . . . . . . . . . . . . . . . . . . . . . . .
4 G. Sanpling for Verification of Curie Content ....
11 GRAND GUIE, UNIT 1 Rev. 1 - 2/84
PCP LIST OF EECIVE PAGES PAGE REV.
NO. NO.
i - iii 1 1
1-4 ,
1 3
iii GRAND GUIF, UNIT 1 Rev. 1 - 2/84
All containers will be sampled for surface contamination and decontaminated, as necessary, prior to shipment.
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The isotopic and curie content of each container shall be determined.
G. Sampling for Verification of Curie Content 1 An isotopic analysis shall be perfrgwed on at least every tenth batch of each waste stream so that the waste. can be classified in accordance with 10CFR61. However, more frequent analysis may be deemed nec[:ssary by the Chemistry / Radiation Control Superintendent.
The total activity in the container maybe determined by either isotopic analysis or by dose rate conversion. ,
man Rev.1 - 2/84
E. Sampling for Verification of Solidification A verification of the solidification of liquid radwastes must be performed on at least every tenth batch of waste. However, if trends indicate the possibility of changing parameters which may have an effect on the methods and materials used to produce a monolithic solid with no free-standing liquid, then more frequent sampling may be required. When increased sampling is required, the frequency will be established by the Chemistry /
Radiation Control Superintendent.
Verification of solidification shall be performed as follows:
a) Three test samples will be taken from the batch. The normal sample volume as specified in approved procedures will be used unless radiological conditions necessitate a smaller volume, The solidifying agents will be added to the test samples in-b) different proportions, c) The test samples will be allowed to set or cure.
9 d) After curing, the proportions of the solidification agents which produced the rhost stable billet shall be used.
e) If none of the samples are found to be satisfactory, the test shall be repeated until a solidified billet with no free-standing liquid is obtained.
' For batches of miscellaneous wastes, a grab sample will be obtained and a verification of solidification aralysis will be performed as specified in steps a) through e) above.
If a Contractor is performing solidification services, then the 1 Contractor's procedures for verification of solidification may be used if approved by the PSRC.
. The proportions of the solidification agents used for the verification of solidification shall be used for subsequent batches of the same waste
. stream.
F. Packaging Requirements I
Prior to shipment, verification of the following shall be made to ensure compliance with 49CFR, 10CFR20, 10CFR61, 10CFR71 and other applicable
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regulations and burial site criteria:
o total contained activity o external dose rate o external contamination levels o physical form o chemical form o waste classification GRAND GULF, UNIT 1 Rev. 1 - 2/84 i
Documentation will be maintained on each batch of processed waste indicating source of waste, date processed, processing parameters, physical and chemical characteristics, dose rates, contamination levels and other pertinent data required.to classify the waste.
C. Wastejtreams GGNS les eight radwaste streams as follows:
Stream #1 - Condensate Clean Tank or Condensate Phase Separator Tanks (condensate filter backwash)
Stream #2 - RWCU Phase Separator Tanks (RWCU and FPCC filter demineralizer backwash) , ,
Stream #3 - Liquia Radwaste Floor Drain Filter (Ecodex)
Stream #4 - Liquid Radwaste Equipment Filter (Ecodex)
Stream #5 - Resins from Condensate and Liquid Radwaste Systems Stream e6 - E/aporator Bottoms from resin regeneration Stream e7 - Evaporator Bottoms from miscellaneous chemicals Stream #8 - Evaporator Bottoms from Floor Drain wastes Other waste streams will be designated as conditions warrant.
D. Conditioning of Specific Batches of Waste The Radwaste Solidification System will be operated in accordance with approved procedures in a manner which will permit segregation of waste 1 inputs into waste streams. With proper segregation, the only parameters that are normally variable are pH, percent solids, and chemical contaminants (e.g., glycol, oil).
These parameters must be analyzed and conditioned in accordance with approved procedures. Conditioning may include adjustment of wrter content or pH.
In the event that the specific activity of the waste exceeds the limits for maximum activity which can be safely processed, the waste will be adjusted according to directions from the Chemistry / Radiation Control Superintendent, or an appointed designee.
When a Contractor provides solidification services, the Contractor will specify the chemical analysis requirements and the acceptable ranges for the physical and chemical characteristics of the waste being processed.
N ~% RQv. 1 - 2/84
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GRAND GULF NUCLEAR STATION PROCESS CONTROL PROGRAM (PCP) DESCRIPTION REQUIREMENTS FOR_ PROCESSING OF RADIOACTIVE LIQUIDS AND WET SOLIDS A. Introduction A large portion of the waste produced in a nuclear power station is in a form which is either liquid or in a. wet solid form (e.g.. resins, filter sludge, evaporator bottoms) and requires processing to obtain an acceptable, solid, monolithic form for burial. The Grand Gulf Nuclear Station (GGNS) Radwaste Solidificatier. System provides for the ,
. solidification of these radioactive wastes. The radioactive wastes are ,
mixed with cement or other binding media (e.g., asphalt. Dow media) ano conditioning additives to produce a monolithic solid with no free-standing liquids. In addition, radioactive wet solids may also be processed by dewatering to assure there is no free-standing water. Compliance with 49CFR, 10CFR20, 10CFR61, 10CFR71 and other applicable regulations is assured by adherence to approved procedures and instructions.
! If the solidification of waste is being performed by a contractor utilizing a mobile or temporary solidification system, the Plant Safety Review Comittee (PSRC) must review and approve procedures and the major equipment to be-used. If the Contractor.'s PCP Topical Report has been approved by the U.S. Nuclear Regulatory Comission (NRC), the accepted report is justification to ensure compliance with 10CFR20, 10CFR61, and 10CFR71 as i required by GGNS Technical Specifications. If the NRC has not approved the Contractor's PCP Topical ~ Report, then it is the PSRC's responsibility to make certain that the Contractor's equipment and procedures are adequate to g
'B. Administrative Controls Directions for extensive or complex jobs where reliance on memory cannot be trusted shall require the appropriate written procedure to be present and
- referred to directly.
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Directives shall include appropriate quantitative and/or qualitative
- , criteria for verifying that the specified activities have been
- satisfactorily accomplished.
- Contractor procedures will be reviewed and approved by the PSRC, to ensure compliance with the applicable portions of the Process Control Program.
Changes to Contractor's procedures will be screened by the Radwaste Operations Section and Chemistry / Radiation Control and forwarded to PSRC l
for review when changes significantly affect equipment or process parameters.
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- RP '
3FFICIAL COP
f MISSISSIPPI POWER & LIGHT COMPANY Helping Build Mississippi P. O. B O X 16 4 0, J A C K S O N. MIS SI PPI39205 August 31, 1984 04 pjg *,
NUCLE AR LICEN51NG & SAFETY DEPARTMENT U. S. Nuclear Regulatory Commission Region II 101 Marietta Street, N. W., Suite 2900 Atlanta, Georgia 30323 Attention: Mr. J. P. O'Reilly Regional Administrator
Dear Mr. O'Reilly:
~
SUBJECT:
Grand Gulf Nuclear Station' Unit 1 License No. NPF-13 /
DocketNo.50-416/'d File: 0292/15319 Semiannual Radioactive Effluent Release Report AECM-84/0438 Attached is Mississippi Power & Light (MP&L) Company's Semiannual Radioactive Effluent Release Report for Grand Gulf Nuclear Station (GGNS) for the period January 1, 1984 to June 30, 1984.
Questions concerning this report should be referred to Dr. L. R.
McKay at (601) 969-2432.
Yours truly, L. F. Dale Director TGL/G0S/LRM:aly R&ES-416 Attachment cc: Mr. J. B. Richard.(w/a)
Mr. R. B. McGehee (w/o)
Mr.N.S.Reynolds(w/o)
Mr. G. B. Taylor (w/o)
Mr.RichardC.DeYoung, Director (w/a)
Office of Inspection & Enforcement U. S. Nuclear Regulatory Comission Washington, D. C. 20555 q t \
Member Middle South Utilities System M'
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