ML19224B130

Surveillance Procedure 2301-3D1,Revision 3:reactor Coolant Sys Inventory

ML19224B130
Person / Time
Site:	Crane
Issue date:	02/05/1979
From:	Metropolitan Edison Co
To:	Mullinix W NRC/IE
References
2301-3D1, TM-0043, TM-43, NUDOCS 7906140083
Download: ML19224B130 (33)

Text

{{#Wiki_filter:- 5 . ~ TMI DOCUMENTS DOCUMSNT NO: /N-3 COPY MADE ON [) f 0F DOCUMENT PROVIDED BY / / METROPOLITAN EDISON COMPANY. 4 b-Wilda R. Mullinix, NRC h 7906140083 188 165 -3

CONTROLLED C^?y I; CESTRAL FILE E 12 2 SU 02/05/79 THREE MILE ISLAND NUCLEAR STATION U' LIT #2 SURVEILLANCE PROCECURE 2301-301 APR p 3 W9 - ^ RCS INVENTCRY Table of Effective Pages Pg Date R evision Pace Date R evision Pwe Drte R evision 1.0 08/19/77 0 26.0 02/05/79 3 51.0 2.0 02/05/79 3 27.0 02/05/79 3 52.0 3.0 02/05/79 3 28.0 02/05/79 3 53.0 4.0 02/05/79 3 29.0 02/05/79 3 54.0 5.0 02/05/79 3 30.0 02/05/79 3 55.0 6.0 02/05/79 3 31.0 02/05/79 3 56.0 7.0 02/05/79 3 32.0 02/05/79 3 57.0 8.0 02/05/79 3 33.0 58.0 9.0 02/05/79 3 34.0 59.0 10.0 02/05/79 3 35.0 60.0 11.0 02/05/79 3 36.0 61.0 12.0 02/05/79 3 37.0 62.0 13.0 02/05/79 3 38.0 63.0 14.0 02/05/79 3 39.0 64.0 ' 5.0 02/05/79 3 40.0 65.0 16.0 02/05/79 3 41.0 66.0 17.0 02/05/79 3 42.0 67.0 18.0 02/05/79 3 43.0 68.0 19.0 02/05/79 3 44.0 69.0 20.0 02/35/79 3 45.0 70.0 21.0 02/05/79 3 46.0 71.0 22.0 02/05/79 3 47.0 72.0 23.0 02/05/79 3 40.0 73.0 24.0 02/05//9 3 49,0 74.0 25.0 02/05/79 3 50.0 75.0 1 Unit 1 Staff Recommends Approval Unit 2 Staff Recommends Approval Approval A, Date Approval M D ate Ccgniunt Dept. Head Ccgnizant Dept. Head Unit 1 PORC Recemmends Approval Unit 2 PORC Recommends Approval 2 !i 79 4. Date MN Date ~ Chairrnan cf PORC V Chairman of FORC / I Unit 1 Superintendent Approval Unit 2-Superintendent Approval / P J l k &r ft'G Date ~~ Y 9 /?/ Date y' / Manager Ger.eration Quality Assurance Approval M Date 188 164 - -.m O 9e

!) u' - s 2301-301 ~ Revision 0 'Y 08/19/77 IE 2 3 G79 THREE MILE ISLAND NUCLEAR STATION UNIT #2 SURVEILLANCE PROCEDURE 2301-3D1 RC SYSTEM INVENTORY 1.0 PURPOSE To insure ccmpliance with TMI Unit 2 Technical Specification 3 4.6.2 whicn states: a. No pressura boundary leakage. b. 1 GPM Unidentified leakage. c. 1 GPM total primary to secondary leakage through steam generators. d. 10 GPM Identified leakage from the Reactor Coolant System. e. 8 GPM Controlled leakage at a Reactor Ccolant System pressure of 2155 1 20 psig. By performance of Technical Specification 4.4.6.2.d which states: Reactor Coolant System leakages shall be demonstrated to be within the above limits by performance of neactor Coolant System Water inventory balance at least once per 72 hours during steady state operation. 2.0 APPLICABLE SURVEILLANCE FREOUENCY AND MODES Surveillance Frequency - At least once per 72 hours during steady state operation. Modes - 1, 2, 3, and 4. 3.0 LIMITS AND PRECAUTIONS t 3.1 Avoid addition and removal of water from the reactor coolant and a ^ Make-up systems during this test. The following operations should not be conducted during this test: 188 167 6

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__) E 2301 -3 D1 Revision 3 j[ t 02/05/79 ,/'. ~ ' s y_, a. Make-up or chemical addition to the make-up system. 4pg 2 g qg _ b. Sampling of the RCS or make-up system. c. Venting or draining of the RCS or make-up filters. d. Changing purification demineralizers or make-up filters in service. e. Boration or deboration. 3.2 The RCS and make-up system should be maintaired in a steady state condition during this test. Changes in valve line-ups, coolers-in-service, pumps-in-service, etc. should be e. voided. 3.3 For the most accurate determination of the RCS leak rate, the initial and final conditions of reactor power, RCS temcerature, pressure and pressurizer level should be identical. 3.4 The same scorces should be used when recording initial and final RCS temperature, pressurizer level, make-up tank level and RCDT level. Differences in sources could be misinterpreted as RCS leakage when comparing successive readings. 3.5 Minimize power level variations during this test. 4.0 LOCATION OF SYSTEM / ASSEMBLY NOTE: See enclosure two for source of dat'. 4.1 The computer is the favored source of informati. 4.2 If two or more inputs are not obtainable en the romputer, the patch panel is to be used to obtain the required data. 4.3 NOTE: Below 520 f, the computer cannot be used fer the calculation. f A hand calculation must be performed using alternate ccmputer points for data input. 5.0 ECUIPMENT REGUIRED 188 168 2.0 S

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b: 2301-301 Revision 3 7 02/05/79 // 5.1 Leads for patch panel to voltmeter. Apg g 3 6.0 PROCEDURE 6.1 If the computer is available, initiate the " Reactor Coolant Leakage Test" as detailed in Encisure II. Data sheets for hand calculations are provided for use as follows: Data Sheet For Use When 1 Comcuter is operational but not available for RCS program. 2 Computer not operational. 6.1.1 Cbtain samples of secondary coolant from OTSG's and perform a gross activity analysis of the sample per 2304-303. If activity levels are significantly above background (>T where T = 3 x background + background) this indicates a possible leak. When a primar/ to secondary leak is indicated, the magnitude can be determined from the growth of specific nuclides in the secondary system. If the gross activity analysis indicates no leakage, enter 0, on line 27 on Data Sheet I or line 29 on Data Sheet 2, 6.2 If a hand calculation is being performed, obtain the aoplicable data sheet (see step 6.1) and take the initial set of data. After a minimum on one hour, take the final set of data and determine the net RCS leak rate as per instructions on the data sheet. 6.3 If chan;es to the RCS inventory must be made during the performance of this test, they must be accounted for using Data Sheet 4. } Operations such as adding water to the Make-up Tank or sampling the RCS may be accounted for in this manner, however, these should be avoided if at all possible. 188 169 3.0 l ~

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~ 2301-3D1 p/ * ~ Revision 3 02/05/79 6.4 If the net RCS leakage is excessive as defined by the acceotance AFR 2 3 G79 criteria in sectio. 7, proceed as follows: 6.4.1 Perfora ar;ther determination of the RCS leak rate. 6.4.2 Insure s .t no un-accounted for operator action has occurred that would change the RCS inventory. (See section 3.1 for a listing of possibilities). If such an action has occurred, it invalidates the measurement. Enter this in the " Remarks" section of the data sheet, clearly describing the action that invalidated the measurement. 6.4.3 Initiate action to determine the source of leakage. Check items such as: 1. Proper valve line-up. 2. Valve stem leakage. 3. Make-up packing glands. 4. Relief valves not seated properly. 6.4.4 If sources of leakage are found, initiate Data Sheet 3, Identified Leakage. 1. Document completely the source of leakage. (Example: MU-V-159A, 3/4" Make-up line drain to A loop, stem leakage through packing gland). 2. Determine the leak rate. The most perferred method is to collect the leakage in a calibrated container. (Obtain from Chemistry Dept) over a known period of time. Use Data Sheet 3, Identified Leakage, to document the method used to determine the leak rate. Include: equipment used, length of measurement and quantity of leakage collected (Example: Used 50 cc graduated cylinder to collect 40 cc of water in 10 seconds). 88 170 4.0 l O '~

/7E / '. - 2301-301 Revision 3 / 02/05/79 s. AFA 2 3 9 79 3. Determine the leak rate and enter en Data Sheet 3, Identified Leakage. 4. The Shift Supervisor shall make the initial determination of the safety implications of the leak. If he decides that there are possible safety implications, he shall notify the proper personnel in accordance with Station AP 1014, Call of Standby Personnel to Plant. 7.0 ACCEPTANCE CRITERIA 7.1 If the identified reactor coolant leakage rate (Line 30 of RCS Leakage Data Sheet 1 or line 32 on Data Sheet 2 exceeds 10 gpm, proceed with ACTION statement 3.4.6.2.b. 7.2 If unidentified reactor coolant leakage (Line 31 of Data Sheet 1 or line 33 on Data Sheet 2 exceeds 1 gpm, proceed with ACTION statement 3.4.6.2.b. 7.3 With any PRESSURE BOUNDARY LEAKAGE, proceed with ACTION statement 3.4.6.2.a. 7.4 With primary to secondary CTSG tube leak greater than 1 gpm, proceed with ACTION statement 3.4.6.2.b. 7 1-188 171 5.0 l [

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]i 2301-301 Revision 3 Il.; - 02/05//9 /j i DATA SHEET 1 Apg ; 3 gg l_ RCS LEAK RATE [ t For Use When Computer is Available j i Initial Conditions - To be taken at one minute intervals ~ Computer t) t t 2 3 Point Line 1 Time 2= +3= FT Line 2a T Lo p A 393* + + = c CA Line 2b T L pA 390* + + = +3= FT H g4 Line 2c T Loop B 396* + + = +3= FT c CS O Line 2d T L op B 391* + + = +3= FT H HB Line 2e Unit Tave (Sum of Lines 2a, 2b, 2c, and 2d + 4) +4= F Tave Line 3 Przr Level 1682 + + = +3= in L PZR Line 4 MU T Level 347 + + = +3= in L k MUT Line 5 RCDT Level (Patch Panel + + = +3= VL RCD.i DVM #64) Line SA R.C. Pressure 398 + + = +3= psig. Line SB R.C. Pressure absolute. (Line SA) + 14.7 = psia.

• NOTE:

Computer points 390, 391, 393, 396 are not accurate below U 520 F. Point 394 must be used instead of 393, and point 397 used instead of 396. T L p A & B cannot be read and will be assumed H to be at the same temperature as Tc. Final Conditions - To be taken at one minute intervals. Computer t) t t A 2 3 Point d 188 172 6.0 4

2301-3D1 Revision 3 /z/ f 02/05/79 DATA SHEET 1 (CONT'D) 0D L Line 6 Time 2= U Line 7a T L cp A 393* + + = +3= FT c CA Line 7b T loop A 390* + + = +3= FT g HA +3= DT Line 7c T cop 6* + + = c CS +3= DT Line 7d T Loop B 391* + + = H HB Line 7e Unit Tave (Sum of Lines 7a, U 7b, 7c, and 7d + 4) +4=_ F Tave Line 8 Przr Level 1682 + + = +3= in L PZR Line 9 MU T Level 347 + + = +3= in L<UT k i Line 10 RCDT Level (Patch Panel + + = +3= VL RCDT DVM #64) Line 10A R.C. Pressure 398 + + = +3= psig Line 10B R.C. Pressure absolute (Line 10A) + 14.7= psia.

• NOTE:

Computer points 390, 391, 393, and 396 are not accurate below U 520 F. Point 394 must be used instead of 393, and point 397 used instead of 396. T loop A & B cannot be read, and must be H assumed to be at the same temperature at Tc. NOTE: Carry Algebraic signs through all steps. 1. Mass change due to RCS Temperature change. (Use line 2e, Sb, and Figure 1, or Table 1 to determine density. Interpolate from Table 1 as necessary). 3 Line 11 a. Initial Density lbm/ft (Use line 7e, 10b and Figure 1 or Table i to determine density. Interpolate from Table 1 as necessary). .i Line 12 b. Final Density lbm/ft ^ c. RCS Volume change (line 11 minus line 12 x 10,678* ft ) 7.0 188 173

(l: 2301-3D1 Revision 3 02/05/79 DATA SHEET 1 (CONT'D) APR 2 3 793 3

• NOTE:

10,678 ft is the RCS Volume for 582 F I minus the pressurizer. For other temperatures, use the following table and interpolate as necessary. TEMP ( F) VOLUME (ft ) 582 10,678 532 10,673 140 10,620 70 10,613 Line 11 lbm/ft 3 -Line 12 lbm/?t Line 13

• ft x lbm/ft" =

lbm 2. Mass ch.cge in Parz. Level a. Calculate density in pressurizer. Assume saturation temperature at RC pressure. Use Line 58 and 10B to get an average RC pressure. (Line SB plus line 108 divided by two) Line 5B psia Line 10B+ psia Line 13A To tal +2= psia b. Use line 13A and Table 2 to get a saturated liquid specific volume (V ). Interpolate as necessary. f Line 13B V= ft3/lbm f c. Mass of pressurizer per inch h (3.208 ft3 + line 138 ( ft3/lbm}) I inch lbm Line 13C 3.208 + inch. = line 138 d. Calculate level change ~ /ff /7}' ':.~

/ 0.: 2301-301 Revision 3 4 02/05/79 '/ DATA SHEET 1 (CONT'D) I93 Line 3 in -Line 8 in Line 13D inch e. Mass Change (line 13C x Line 130) line 13C lbm/ inch x line 13D inch Line la lbm 3. Mass change in MU Tank Level (Line 4 minus Line 9 x 255 lbm/ inch) Line 4 in -Line 9 in lbm Line 15 255 in x in = lbm 4. '.al RCS fdass Change ( Algebraic sum of lines 13,14, and 15) Line 13 RCS Tave change of mass Line 14 Pressurizer mass change Line 15 MUT mass change Line 16 RCS alba 5. Total RCS change in gallons Mean Tave (line 2e plus line 7e + 2) a. Line 2e F +Line 7e F Line 17 RCS +2= OFT MEAN 188~175 9.0 O

lli 2301-3D1 Revision 3 L 02/05/79 i DATA SHEET 1 (CONT'D) l-b. Use Figure 2 and Line 17 to find Line 18 Conversion factor from lbm to gallons: gal /lba Interpolate as necessary. 97. b. Lse line 13A, 17 and table 1, (interpolate as necessary) to find Line 18 Conversion factor from lbm to gallons: gal /lbm NOTE: Density (gal /lbm)=7.4805 Gal + (v) lb/ft3 ft3 c. RCS Inventory change (Line 16 times line 18) Line 16 lbm Line 19 xLine 18 gal /lbm = gal = RCS Volume Change d. Operator caused changes to system Line 20 (From Data Sheet 4): gal e. Total RCS Leakage (Algebraic sum of linec 10 end 20) Liiie 19 gal. +Line 20 gal. Line 21 RCS = gal. Total Leakage 6. Total Leak Rate a. Duration of Test (Line 6 minus Line 1) Line 6 n m -Line 1 h m Line 22 h m= min = b. Leak Rate (Line 21 divided by Line 22) Line 21 188 176 10.0

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/ cr) - l' 2301-3D1 Revision 3 /\\, ~x " 02/05/79 s APR 2 3 :379-DATA SHEET 1 (C0:lT'D) o' Line 23 +Line 22 = gpm Total Leak Rate (Identified and Unidentified) 7. Identified Leak R.;e a. Volume change in RCDT (Use Figure 3 for level to volume conversion) Line 5 V= gal -Line 10 V= gal Line 24 RCDT Volume Change = gal b. Operator caused change to the RCDT Line 25 (From Data Sheet 4: gal CAU TI0ti: Removing water from the RCDT should be entered as a negative change to the water inventory. Line 26 c. Identified leakage: gpm (sign should be minus) (From Data Sheet 3) Line 27 d. Primary to Secondary OTSG Tube Leak: gpm (Sign should be minus) e. Identified Leakage to RC Drain Tank. (Algebraic sum of Line 24, and 25). DA'lA SHEET 1 (cont'd) Line 24 RCDT Volume change Line 25 RCDT change by operator Line 28 gal Identified RCS Leakage to RCDT F. Identified Leak Rate to RCDT a Line 28 gal. Line 29 + Line 22 m= gpm Identified Leak Rate to RCDT (should be negative or zero) 188 177 i 11.0 l

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E 2301-301 Revision 3 ] Q, 02/05/79 DATA SHEET 1 (CONT'D) APR 2 3 1979 g. Total identified leak rate (Sum of line 26,27 and line 29) Line 26 gpm identified leakage (From Data Sheet 3) Line 27 gpm primary to secondary leakage + Line 29 gpm identified leak rate to RCDT Line 30 gpm total. Line 31 Abs value of line 30 gpm total identified leakage. LIMIT: Line 31 shall not exceed 10 gpm. (See Acceptance Criteria 7.1) Line 27 shall not exceed 1 gpm (See Acceptance Criteria 7.5) 8. Unidentified RCD leak rate (Subtract Line 31 from Line 23) Line 23 _ _ gpm total leak rate -Line 31 gpm identified leak rate Line 32 gpa unidentified leak rate (1 gpm maximum) LIMIT: Line 32 shall not exceed 1 gpm (See Acceptance Criteria 7.2) REMARKS: PERFORMED BY DATE APPROVED BY DATE i 12.0 188 178 S

/4 2301-3D1 Revision 3 02/05/79 f/ DATA SHEET 2 APR 2 3 375 r.- RCS LEAK RATE For Use 'When Computer is Not Available Initial Conditions - To be taken at one minute intervals Patch t) t t 2 3 Panel Line 1 Time 2= Line 2 Tave

• 36

+ + = +3= V Tave (meter) Line 3 Przr level 22 +3= VL + + = p73 Line a MU Tank 96 + + = +3= VL MUT Line 5 RCDT 64 DVM + + = +3= VL RCDT U

• If Tave is less than 520 F, Patch Panel point 36 cannot be used.

Instead, take the following data: I (panel meter Line 21 Tc loop A 31 + + = +3= V (panel) meter Line 28 Tc loop B 34 + + = 43= V Line 2C Tave Line 2A 'Line 2B +2= V = NOTE: Assume T nd T r equal for each loop. H c (panel) meter Line SA Rc pressure 25 + + = +3= V CAUTICN: '! hen using patch panel voltages, be sure to record the voltage colarity (+ or -) and treat this as an algebraic sign. Final Conditions - To be taken at one minute intervals j Patch 3 Panel t) t t 2 3 Point 188 179 , 3. 0 O e M

jr /Di 2301-3D1 Revision 3 02/05/79 [ / DATA SHEET 2 (CONT'D) APR23"d79 3 Line 6 Time 2= t Line 7 T.- 36 +3= V Tave + + = (** Line 8 Przr Level +3= VL F ^ = PZR Line 9 MU Tank (meter) 96 + + =_ +3= VL MUT Line 10 RCDT 64 DVM +3= VL ^ + = RCDT

• If Tave is less than 520 F, use the following points:

(meter) Line 7A Tc loop A 31 +3= V + + = (meter) Line 7B TC icap B 34 + + = +3= V Line 7C Tave Line 7A + Line 7B +2= V = NOTE: This assumes T and Tc are ecual. H (meter) Line 10A RC pressure 25 + + = +3= V NOTE: Carry Algebraic Signs Through all Steps 1. Volume change due to RCS temperature. a. Temperature conversions 1) Initial temperature (570 minus, line 2 times 5): Line 11 570 F - (Line 2 V x 5 F/V = F E Initial temperature (350 plus line 2C times 30) 0 0 Line 11 350 F + (line 2C vx30 F/V)= F. 2) Final temperature (570 minus line 7 times 5): U Line 12 570 F - (Line 7 V x 5 F/V = F E Final temperature (350 plus line 7C times 30): U O Line 12 350 F + (line 7c Vx30 F/V= F. b. Pressure conversions 188 180 1. Initial pressure (abs) (Line SA times 250 +14.7) ~ 14.0

/b 2301-301 Revision 3 1 h/.. 02/05/79

• f DATA SHEET 2 (CONT'D)

APR 2 s yg!' a Line 13 Line SA v x 250 psi /v = ps ig + 14. 7= psia 2. Final pressure absolute (Line 10A times 250 + 14.7) Line 14 Line 10A v x 250 psi /v = osi g + 14. 7= osia. c. Initial Censity (Use line 11 and Figure 1 or line 11, line 13, and Table 1 to determine density. Interpolate from Table 1 as Line 15 necessary.) lbm/ft d. Final density (Use line 12 and figure 1, or line 12, j line 14, and Table 1 to determine density. Interpolate Line 16 from Table 1 as necessary.) lbm/ c. i l e. RCS Volume change (line 15 minus line 16 x 10,678* ft ) NOTE: 10,678 ft is the RCS volume for 582 F minus the pressurizer. For other temperatures, use the following table and interpolate as necessary. 3 Temo(UF) Volume (ft ) 582 10,678 532 10,673 140 10,620 70 10,613 3 Line 11 lbm/ft -Line 12 lbm/ft j 3 Line 17

• ft x lbm/ft =

lbm 2. Mass change in pressurizer level. a. Calculate density in pressurizer. Assume saturation temperature at RC pressure. Uselite13and14'1o81 188 get an average RC pressure. 15.0 G g

17; 2301-3D; Revision 3 7 )# 02/05/79 DATA SHEET 2 (CONT'D)

1. I973'-

Line 13 osia +Line 14 psia Line ld Total +2= csia. b. Use line 18 and Table 2 to get a saturated licuid specific volume (V ). Interpolate as necessary. f Line 19 V= ft /lba f c. Mass of pressurizer per inch j 3 (3.208 ft / inch + line 19 (f t /lbm}) lbm Line 20 3.203 + inch. i = Line 19 i d. Pressurizer level change 1. Initial level (200 inches plus line 3 times 20 inches /v) i Line 21 200 + (line 3 x20 in/v) = inch i. 2. Final level (200 inches plus line 8 times 20 inches /v) { Line 22 200 + (line 8 x20 in/v) = inch. 3. Level change (line 21 minus line 22) l Line 21 Line 22 Line 23 Level change inches. e. Mass change in pressurizer (line 20 times line 23) i lbm I Line 24 line 20 in x line 23 in= lba 3. Mass le in MU tank level. I: IT a. me conversions. l-1. Initial level (50 plus line 4 times 5 inches /v) Line 2. 50 + (line 4 x 5 in/v) = inches. i 2. Final level (50 plus line 9 times 5 in/v) fh8 lg} 16.0 .~.

i 2301-3D1 Revision J 02/05/79 DATA SHEET 2 (CONT'D) APR 2 3 13,9 Line 26 50 + (line 9 x 5 in/v)= inches. 3. Level change (line 25 minus line 26) line 25 -line 26 Line 27 Level change inches. b. Mass change (line 27 times 255 lbm/in) Line 23 line 27 in x 255 lbm/ inch = lbm. 4. Total RCS mass change ( Algebraic sum of lines 15,16, and 17) Line 17 RCS Mass change Line 24 Pressurizer mass change Line 28 MUT mass change Line 29 RCS albm 5. Total RCS change in gallons a. Mean Tave (line 11 plus line 12 + 2) Line 11 F +Line 12 F Line 30 RCS +2= FT MEAN b. Use figure 2 and line 30 to find conversion-factor from ibm to gallons. Line 31 gal /lbm OL Use line 30, line 18, and Table i to find conversion factor frcm iba to gallons. Interpolate (7.4805h+(v)lb/ft3). as necessary. Line 31 7.4805 9 I ft3 lb/ft =_ ga / g + E 17.0

I*. l 2301-3D1 Revision 3 f 02/05/79 DATASHEET2(CONT'DJ AFR 2 3 ISIS _ c. RCS Inventory change (line 29 times linc 31 ) Line 29 albm xLine 31 gal /lbm = gal d. Operator caused changes to system Line 33 (From Data Sheet 4: gal e. Total RCS laakace I (Algebraic sum of Lines 32 and 33) Line 32 gal +Line 33 gal Line 34 RCS gal total leakage 6. Total leak rate a. Duration of test (line 6 minus line 1) Line 6 h m -Line 1 h Line 35 h m= min b. Leak rate (line 34 divided by line 35) Line 34 Line 36 +8.ine 35 gpm Total leak rate = identified and unidentified) 7. identified leak rate a. Volume change in RCDT (Use figure 3 for level to volume conversicil) Line 5,_ V= gal h -Line10 V= gal [ Line 37 RCDT Volume Change = gal l b. Operator caused changes to the RCDT 188 184 18.0

h 0:* 2301-301 Revision 3 02/05/79 I ( I.. ' DATA SHEET 2 (CONT'D) i ,AFR 2 3 ;379 l-n Le e 38 (frca data sheet 4: cal CAUTION Removing water from the RCDT should be entered as a negative change to the water inventory. Line 39 c. Indentified leakage: ,gpm (sign should be minus) (From data sheet 3) Line 40 d. Primary to secondary OTSG tube leak: gpm (sign should be minus) e. Identified leakage RCDT l (Algebraic sum of line 37 and 38). Line 37 RCDT volume change Line 38 RCDT change by operator I Line al gal identified RCS leakage to RCDT (should be negative or zero) f. Identified leak rate to RCDT l Line 41 gal Line 42 + Line 35 m= gpm Icentified Leak rate to RCDT (should be negative) g. Total identified leak rate (Sum of line 39, 40, and 42) Line 39 gpm identified leakage from Data Sheet 3 + Line 40 gpm primary to secondary leakage + Line 42 gpm identified leak rate to RCDT Line 43 9Fa total. h i Line 44 Absolute value of line 43 gpm total identified leak rate. LIMIT-Line 44 shall not exceed 10 gpm. (See Acceptance Criteria 7.1) 00 lQ} 19.0

n ~' 2301-301 Revision 3 02/05/79 /( DATA SHEET 2 (CONT'D) / /, 8. Unidentified RCS leak rate AFA 2 3 ;379 - (Subtract line 44 from line 36) Line 36 gpm total leak rate -Line 44 gpm identified leak rate i Line 45 gpm unidentified leak rate (1 gpm maximum) I LIMIT: Line 45 shall not exceed 1 gpm (See Acceptance Criteria 7.2) Remarks: PERFORMED BY DATE APPROVED BY DATE 7 .t fbb 20.0 O e

/

• 2301-3D1 C" "'
• Revision 3 02/05/79 DATA SHEET 3

/ RCS LEAK RATE APR 2 3 nrg ~ IDENTIFIED LEAKAGE 1. Source of Leakage (Describe in detail, attach drawing if necessary) 2. Method used to determine leak rata (Describe briefly) I 3. Identified Leak Rate: gpm (For use in Line 26, of Data Sheet 1 or Line 39 of Data Sheet 2.) Performed by Date 4. Possible Safety Implications (Shift Supervisor Check One) Yes (Initiate necessary action) No Explain 7 Shift Supervisor Date 188 187 o

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i; a c, O. 2301-3D1 Revision 3 02/05/79 DATA SHEET 4 RCS LEAK RATE M 2 5 133 _ OPERATOR CAUSED CHANGES TO RCS INVENTORY 1. Identify operation that caused change: 2. Time Operation Started: Time Coeration Completed: 3. Calculations: 4. Total change to RCS inventory: gal. NOTE 1: If change is to RCDT enter in section 7 of Data Sheet 1 Line 25 or Data Sheet 2 Line 38. NOTE 2: If change is to any other part of the system, enter in section 5 of Data Sheet 1 Line 20 or Data Sheet 2 Line 33. NOTE 3: SIGNS: Removals from the system have a negative (-) sign. AdJitions to the system have a positive (+) sign. PERFCF.MED BY DATE APPROVED BY DATE i 188 188

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e E.iCLOSURE I SOURCES OF DATA RC SYSTEM LEAK RATE C0flTROL ROOM PATCll PANEL PARAMETER COMPUTER P0lflT If1STRUMENTATION P0lffT RSTGE (VDtT tioTPuT MutTTPLIER T 390 TlLoopA 36 520 - 620 F +10 to -10 T = 570 - (5 x Volts) AVE TfLoopB 391 C0flTROL COUNSEL (Unit TAVE) CEllTER PANEL 392 393 T Loop A c 394 395 396 T l P O c 397 W PRESSURIZER 386 C0flTROL COUNSEL 23 0 - 320 in +10 to -10 0.0625 in/ volt o LEVEL 387 CEllTER PANEL 1947.2 ltun/ volt 388 1682 MAKE-UP TANK 347 C0flTROL COUflSEL 96 0 - 100 in -10 to +10 0.2 in/ volt LEVEL CEf1TER PAtlEL 1275 lbm/ volt REACTOR C00LAf1T flA LEVEL RECORDER 64 70 - 95 in 0 to +10 See Figure 3 DRAlti TANK LEVEL USE PATCll PANEL LWDS PAflEL f40TE: Patch Panel Cata..;f be obtained from the voltmeters installed for a cooldown from outside the cc Control Room. T $U N< O b M.0 a - so a na tn 3 Cc ~P Q

sy. 2301-301 Revision 3 02/05/79 i44 ~ ENCLOSURE II^^^ MR 2 S Gk. Computer Determination of RC Leak Rate 1.0 PURPOSE This program is designed to perform all the calculations acccmplished on Data Sheet 1. The plant ccmputer will automatically gather all inputs and average three minute intervals of the initial and final readings. Thi.s program is run fecm the programmer's console of the Bailey 855 computer. It may be run at any time the programmer's console is not being used by another program. 2.0 PROCEDURE 2.1 Turn on the programmer's selectric typewriter next to the Bailey 855 computer. 2.2.1 If the computer printout on the selectric shows a question mark (?), type "r", then depress the " Return" Key. The computer will respond with an exclamation mark ('). Proceed to 2.2.2. 2.2.2 If the printout on the selectric shows an exclamation mark (' 1, type "RCSL" and then press the " Return" key. (See sample printout: Attachmentll. 2.3 The computer will tnen request the time interval over which the test is to be run. Any interval from 1 to 8 hours in one hour intervals may be choosen. Enter a single digit, then press the " Return" Key. j J 188 193 27.0 e

-; c t cm /; 2301-301 Revision 3 g( 'L) 02/05/79 .j 2.4 The computer will now request known leakage. Enter "Identifie AFR 2 3 137$ Leakage" (as determined by Data Sheet 3) in gallons per minute. Enter operator caused changes to the RCDT or the RCS (as detailed on Cata Sheet 3) in gallons. CAUTION: For the above entries, be sure to enter a decimai point. If no decimal point is entered, the computer will insert one according to the format ' t expects to see. Also remember to use a (-) negative sign for any entry made that would decrease RCS volume. 2.5 The ccmputer will new print out all required duta. Be sure to attach data sheets detailing any entries made in step 2.4. 7 M 4 188 194 t 23.0 _i O

Q / (,h)_ .. 2301-3D1 Revision 3 O CyM', 02/05/79 Q rcsl APR 2 3 1379 - ATTAC:#ENT 1 O DATE: 12/14/7; REACTCR CCOL1:!T LU,".'.CE TEST TIME: 8:11:31 SP :'301-301 O i;0TE: IF CPERATCR ACTIC:' CECRE1SES RCS VCLLME THE PATT. E::TRY FOR TPAT ACTIC:; >:USTBE PECATIVE, ...'/CU lijST ENTER DEC. PT. WI TH LEA:7,CE '/AI.UES... O O DES lRED !!!TERVAL (1-8 HC'JRS) 1 O Et:TE.'i CPERATCR CAUSED CHAi!?ES TO THE RCCT FRCM DS L (2301-301) O. E: ITER CP:.UTCH CAUSED C:-:Af;GES FRCM CS 4 (2301-301)' -~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~~ C 1.3 .E.: ITER I DE::TI FI ED_ LEAi' GE i'_?C_M DS 3 (2301-30l} _ CP:D d ( Q E :TER FR!t'.ARY TC SECC:!CARY CTSG TUDE LEAK (GR D i o. O T li.;E TCA THA TCS THB TAVE FRZR LVI. t '.U i R LVL RCDT LVL . ( t- ) _ __ _ ( r_ ) _ _ _(F) ______(c_).___ _(r. _ _.(lil) ...l.,) _ _(,..,,,,--) t i. ...c n :-) O S:11:55: 537.914 535.773 5dS.0dG S06.234 552.250 2G8.047 G2.220 70.223 U,.c u 7 u'. 9. a-l s 5.09-1

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3 t .4 2301-301 Revision 3 02/05/19 O b APR 2 3 B19 - Table 1 Liquid ~ 1 p (t Sat.) 30j sna (467.i 3) 1000 (5.i4.75) lb y h s e u h s e u h t i S a t. .019745 447.70 41153.64904 .021591 533.39 512.33.74320 - 32 .0/6011 01 01 0o001 .015994 00 1.49 00000.0t5967 .03 2.99.cto s 53 .016014 is os /3 oc 01507 .CI5993 15 02 19 50.03599 .015'/72 17 W 29 94.03i12 100 .0161/0 68 03 43.03./1!61 .016106 6 7 F. 7 6U6.I2732 .016N 2 Wi.i G 73 /.3.12901 150 01614J / / 7.93 Ill.95 11304 016313 11 : ^/. I l 9.17 2!457 .01629% 117 Z 170 40 21110 2C'J .016633 15J 03 165 03 19401 .016603 167 6) 16119.27311 .016 % 3 16 E 26 170 32.23231 250 .01700J 11331 113 31.3577? .016972 217 97 2t? 56.36702 .0 l G 41 217 47 220 61 36r03 300 017453 15961 16 v 61 417J2 .017416 26392 2iO 53 41C41 .0 t 7 3,79 '.G.2 4 271.46.43552 350 .0t4000 JJi 39 311.39 jc139 .017954 3 20.7 l 37y37 53y pf .g l 7 7 ;9 y g.y s y y;),,5 $gg g 40 .0/3(64 J74 33 3 74.A 3.jd 74 0 .O I S(,03 371 M 375.49 5 M ri t 015!50 3 7 2.:'. 5 375 )3.5647) 450 .0/9301 479.96 419.96.61970 O ! 91.M 4 ? s.:0 430 19 627 4 .019340 426 '9 230.47.6'633 500 .0?ono 488.1 433.1 6919 02048 4.13 9 447.t 6:94 .023% 4337. 457 5 .6574 510 .0:047 300 3 300) 7044 0:073 M7. 9 499 3 70:1 02260 4?;G '494 .6937 520 .02116 312.7 112 7 .717] .0 100 310.1 31: 0 .7146 .02 CSS 537 G 511.5 .7121 530 .0]!4n 3:33 ils.: .7101 02110 3:16 3:43 .7:7] .02 tit 513.9 523.0 .7245 540 .C21 's $ 33.6 135.6 .7414 02162 3 J 3.3 337.3 740: _0 ? M 4 SiL A'6 3 7372 553 .021:I $ 3 2.1 332.I .7359 .0?!ps $43 4 330.3 .7311 .0:177 33.1 349 2 .7499 $60 .02263 36".1 366.1 2707 .02137 162.0 364 0 isG6 .02211 3.t r 3 36 4 .7610 3io .02313 3!T2 350.8 .?531 .02:31 1 73.0 375.1 .7:04 .0123) $ ?)..s 376 0 .776) STO .02332 3903 3919 .1946 .02:95 332.9 390.1 .7399 590 .02392 606.4 60s.6 .2096 .01349 60.T4 coa.9 .3044 610 .02409 61: 2 620 6 .3189 .0 N C2 637.9 637.5 .8548 l p (t Sat.) '3503 (596.39) 2003 (636.00) 2.500 (663.31) t v u b s e u h s e v. h s Sat. .023 41 (04.97 611.48,50324.025549 662.40 671.59.S6227.02:005 717.C5 730.59.91305 32.015939 .05 4.47.00007.015912 .05 5 95.00003.0158SS .c 5 7.43.00009 50.015946 17.95 22.33 035S4.015920 17.91 23 !! 03575.015505 17.15 25 23.03 M6 100.016053 67.53 71.99.12S70.016034 67.37 73JO.12339 .016010 6720 74 61.I25Ct 150.0162:3 117.10 121.62.21364 .016244 1i6.33 122.S4.21315 .015220 !!6 56 124 07.21272 200.016554 166.57 171.46.29221 .016527 166.49 172.60.29162.01650: 166.11 173.75.29104 250.016910 216.96 221.65 J6554.016380 216.46 222.70.364!2 .016351 !!$.9 6 223 75.35410 300.017343 257.55 272.39 A.4 6 3 .017303 2::6 93 273.33.43376.0l?274 265.29 274 23.41290 350 .017H 5 315.95 323 94 9 034.017322 3 M 15 324.74 A902) 0177S0 317.? 3 325.56.49325 400.015493 371.45 376 59 563 t3.015439 370.33 377.21 562!6 .0'.4336 36934 3 '/ 7 S 4.56092 450.019264 425.44 430.79.62470.019191 424.04 431.14.623I3.019120 422.63 431.52.62160 500 .02024 431.8 437.4 M53 .02014 4793 457 3.6332 02004 473 3 457.3 .6513 510 .0204S 493A 499.1 M74 .02036 491.4 493 9 .6953 .02025 45 u 443.5 .6932 520 .02072 505.3 511.0 .7096 .02060 503.1 510.7 .7073 .02043 50i.0 510 4 7051 530 .020 H 5173 523.1 7219 .02055 514 9 522 6 .7195 .02072 .s t :4 522.2 7171 540 .02127 529.6 535.5.7343 .02112 527.0 5343 .7317 02093 524 5 534.2 .7292 550 .0215S $ 4 2.1 544.' .749 .02141 539 2 547.2 .74.o .02125 535 6 546.4 .7413 560 .02191 554 9 361.0 .7576 .0?t72 551 8 559 3.7565 .02154 54S.9 55s 2 .7536 570 .02224 SAS O 574 2.7725 .02206 564 6 572.s 7691 .02tS6 561.4 Sil 5 .7 6 W SSO .02269 S S I.f, 587.9 .7857 .02213 $ 7 7.S 5 S 6.1 .7420 .02221 574 3 554.5 .7735 590 .02314 594 7 f.0 2 1 .7 N 3 .c 234 591.3 599.8 .7951 .0225S 557.4 597.9 .7913 600 .01346 610 4 616.9 .3114 .02 U 0 605 4 6110. FOS 6 02.100 001 A 611 6 .S N 3 610 .ofsts 6?33 6J2 6 5:37 .0 2 n 2 620 0 623 % 3225 .0 2.U 6 61.3 0 625 9 .6177 620 .ol d e.t 6 e13 640 4 .34J7 .01483 635 8 b l4 5 .517I .023H 624.- 6447 .3315 6.13 .ay)90 660.8 6 6.f 0 .J609 .02514 651.9 e 61 2 U?S .02149 644f1 656 3 .S459 640 .ptouJ oo r.3 o/w 4 ..s o v .025]O 661.2 672.9 .8610 650 .0:1:4 69W1 700 4 .8531 .02G16 675.1 600 ' SN3 y ) 7 .0 2 7.w m.4 7ii Tbn Density l. ~f _3 .v:s v3 m. m.) .n.. _y ft ft /Fcm ~ ~ 30.0 e e e

23Cl-301 Revisicn 3 1' 02/05/79 n Table 2. Saturation: Pressures a 2 3 wr. Spaific Volume Inter nal Energy E nt b atpy Ent ropy W e... Lbr T. = e. ? st Set 94. 5.L S at. Sen $ st. S ea. 3+14 T.hr. LLeod % ear Liv..d Esem 4 avec LW. J F.no. N oe L q. d E.ap. 4ane p t ir, v, u, u,, u, h, h,, h, s, s., s, 200 331 3( 018387 2 :39 354 3 759 6 1114 6 355 6 543.7 1199) .5440 10025 1.5464 235 333 94 013415 2 235 M7t 757.7 1114 5 357 3 541.3 1199 6 .5463 .9>78 1.5444 210 335 97 .013443 2.184 TM1 755 8 1115.1 M00 E. 3 9.9 1:00 0 .5492 .9932 1.5423 215 337 97 013470 2.135 NA 753.9 l'!53 382 : SH I 1:00 3 .5517 .967 1.5403 2:0 339.94 015497 2.033 363 5 752 0 1115.5 M4.3 Sh3 1 006 .5541 .9342 1.5334 225 391 37 .013523 2033 M56 750 2 1115 8 3%3 33+5 1200 3 .5$66 .9 M 1.5365 23J 39336 .014550 2 0U0 M76 743 4 !!16 0 M34 8323 1:01.1 .5159 .9757 1.5346 135 395 63 015$76 1.959 369 6 746 6 1116 2 3 04 831 0 1:01.4 5613 .9715 1.5327 240 397 46 018602 1.919 371.5 7443 1116.4 372.4 529 3 1:01 6 MtM 9674 1.5309 283 399.26 01862: 1.531 373 5 743.1 1116 6 3743 527.5 I:01.9 5653 .9634 1.5292 t nc 40I.04 .013653 1.5443 375 4 741.4 1116.7 376 2 525 3 1:02 1 5610 .9594 1.5274 253 40239 .G13d78 13097 3773 7393 1116.9 373.1 824 2 ? 2M.3 .570 .9555 1.5257 210 4C4.51 .013703 13758 379.1 733 0 1117.1 350 0 U,5 I?25 .5723 .9517 1.5240 205 40610 .0137:8 1.7432 h09 7M3 I117.2 331 3 C39 ::2 ? .5744 .9479 15224 270 407 87 .013752 13I17 3323 734] 11 t 7.4 3333 ?i92 i W .5765 .9442 1.5;C3 275 409 52 013777 1.6313 334.5

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