ML18010A854

Flow Calibration Rept Carolina Power & Light Harris Plant.

ML18010A854
Person / Time
Site:	Harris
Issue date:	10/09/1992
From:	CONTROLOTRON CORP.
To:
Shared Package
ML18010A852	List: ML18010A851 ML18010A853 ML18010A854 ML18010A855 ML18010A856 ML18010A864 ML18010A865 ML18022A904 ML18022A905 ML18022A906 ML18022A907
References
NUDOCS 9210280219
Download: ML18010A854 (27)

Text

S16-231-3334 P.2 OCT 89 '92 18:81N CONTROLOTRON

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'L'OV 'CM'XRRA'TXOH REPORT

'CA'KOL'X%A 'PODEX '8 LT5KT Vo'8' 2'1'0'4 5 ro. i xrcoo:goals 5 ONTROLOTRON ORPQRATlON cypf 0/B0pjp p@$ 0$

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P C CAROLINA POWER & LIGHT M.o.8 921045 PDC 994P5GLS-3 U2415 TRANSDUCER - 991PMS-2 U4077 PIPE SIZE 3SS40 PREPARED BY:

Date iG QNTROLOTRON ORPORATION 155 Phot Avenue ~ Heuppauge, NY 11788 ~ (518) 231-3800

516" 231-3334 18: 8ZAPl KNTROLOTRON Ch n~ 4 O

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~op RTIFICATE OF FLOg CAZ,IBPATION AMENDMENT d3

~CHASE ORDER NO. XT00000075 CAROLINA POQER 6 LIGHT HARRIS PLANT OUR CWORK ORDER NO. 921045 DATE 10-9-92 XT XS HEREBY CERTIFIED THAT ALL HA~RING 6 TEST EQUXPHEHT USED TO XNSPECT, TEST 8 CALIBRATE OUR PRODUCXS ARE TRACEABLE TO THE NATXONAL INSTITUTE OF STANDARDS AND TECHNOLOGY (NIST) ~ TEST AND/OR INSPECTION REPORTS INDICATING CONFORMANCE ARE ON FILE. FLASH CALIBRATION AT CONTROLOTRON OR AT EXTERNAL FACILITIES ARE PERFORHED BY KVQ2KB CONTROLOTRON PERSONNEL'ND ALL FACXXiETX EQUXPMERiT UTILIZED ARE TRACEABLE TO NXST. THE MATERIAL IDENTIFICATION AND ACCURACY IS XN ACCORDANCE HXTH THE FLOH CALIBRATXON REPORT XNDXCATED BELOg-994P5GLS-3 u2415 991PMS-2 U4077 QUAL T'I SUPERVXS DATE ATTACHMENTS FLOg CALIB. REPORT NO. 9107 2 C3NTRC3LOTRON ORPO RATION CC2O4-B.1 155 Plant Avonvo Havnpavge. NY 117'9e ~ (51el 731-1+<>

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<og FLOR CALIBRATION REFERENCE DATA SHEET CAL. f 9107 2 MODEL P/N: 9 4PSG S/N CUSTOMER: C RO P/0 LOCATION: N/0 DATE OF CERTIFICATION: 10-9-92 TEST E UIPMENT TEMPERATURE Di itec 5820 S/N CCT-301. Due TIMER NEWPORT Model 6130A S/N 36 ue 1 2 INDICATOR BLH Mode1 LCP10 VR2.26 S/N CCT-380 Due 7-6-93 CALIBRATION METHOD CONTROLOTRON TEST PROCEDURE CS-2 REV 3A 6/29/92 THIS CALIBRATION.IS CERTIFIED TO BE ACCURATE WITHIN A MAXIMUM ERROR OF +- 1X APPROVED BY: DATE CC-246-3 o~v'aocov'aoN OaPORATlOM 155 Plant Avenue ~ Hauppauge, NY 11788 ~ t516) 231.3600

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CONTROLOTRON CORPORA::-OS 990 :":OR CALIBRATION DIAGNOST C DATA SEE T CUSTOMER: CAROLINA POUER & LIGHT Y.O.: 921045 FDC P/N: 994PSGLS-3 FDC S/5: U2415 TRANSDUCER P/N: 991PMS'-' TRANSDUCER S/N: U4077AIS SITE NAME: 3SS40CAL PER:" B~:

PIPE SIZE: 3SS40 DATE: 10-8-92 TRACK MOUNTING (D/R): DIR LIQUXD TEMP: DEGRESS P 78 TRACK SPACING INDEX: B-8 KC FACTOR: +3. 5 NOTE: The diagnostic data listed helena is the Uniflov set-up data at the time of calibration. The diagnostic data will vary somewhat due to variations in app ication conditions.

This data is listed for information and reference purposes only.

DIAGNOSTIC DATA Vs: 1495 (Liquid Sonic Uelocizy)

Vale: (Liquid Signal Streng ")

Px (Transmit Frequency)

N: 30 (Transmit Count) n 13 (Receive Count) x 10 (Receive Displacement)

Vfmax: 2119.99 (Maximum Flow Velocity in Ft/Sec)

TN 91.98 (Total xmit. to rcv. "ime in micro-seconds)

TL 55 '3 (Computed time for sonic beam in liquid)

Checksum 02B31E78 100792-0016 (Software integrity check)

Code (Controlotron Corpora-=on control code)

LTN (Transducer Spacing)

Contour .906 (Receive Signal Quali=y)

CC240 ONTROLOTRON ORPORATiQN 455 >lant Avenue ~ HauPPauge. NY 11788 ~ i516 231-36M

Ol vv I ag 7C ACI ~ cl~h<'i E Vl'II tiVLVI EVE Dlo C~l 990 FLN CALIBRATIOH DATA SHEET (IKI6H TANK hETHOD) SHEET ÃI.

CUST(NER: CAROLIHA PS(ER 6 l.l6HT Nl 92l045 POI 1 T0000007$

FDC: PH 994P56LS-3 FDC SIN U24l5 PIPE SIZE 3SS40 TRC ITS (0/R) DlR TRANSDUCER: PN 991PhS.2 TRANSDUCER S/h U4077AIB TRANSDUCER CC} 4030 FLON STANDARD CCT: 380 TlhER CCT: 362 TENP Ql%E CCTl 301 SITE MANE: 3SS40CAL Vs 1495 Kc FACTOR 3.5 SPACE IIGEI B.S Fx: 6 H: 30 n: 13 1: 10 Tn: 91,98 TLs $ 5.93 Yafcc &6 PERFORRED BT DATE 10-8-92 RN TANK HEISHT DELTA @ST HATER NTER ACTUAL IOICATEO START STOP'ELTA Quet had DEETI 0 X ERRN l.BS LBS TENP DHOITTYOL VOL T1% TI% SEC(NDS SPll SP}l SP% .

DE6 F Yact Yin4 START STOP 1 3l8 2844 2526 78 8.30698 304.0816 301.3 0 435.31 43$ ,3} 4f.9}2Q 4}.$2902 Wa3C39  %.9}5f

, 2 386 3N9.$ 2963.$ 78 Oo30698 356.748} 353.$ 2 0 342.99 342.99 62.40674 6}i@203 4.$ 647}  %.90$ f 2.5 4258.$

4781 3816 4232.$

79 79 8.30580 459.4379 8.30580 $ 09.$ 836 455.9 507.$ 4 0

0 346.25346,25 79.6}3N 79.0N72 W.Cf3N 303.22 3N.22 100.&344 }00.4300 <.40439 4.770f 4.4011

CAROLINA P8cL,WO 92't 045,PO XT00000075 FDC U2415,XO 04077,PlPK 3SS40 2.00%

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.91 5'0.905% -0.770K

-1.00K

-1.50K

-2.005 60 80 100 CPM

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P.M 18:GSN CONTROL,OTRON 516-Z31->884 0

"- POLIClES AND PROCEDURE5 o

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Type CUSTOMER SERVICE Ad~in-'-y CUST SERV CS-2 Subject ~g CALIBRATION (I4gp/96p/99p) Prep. By Appr.By Flov Curve, Density Chart; NR Dare 5/5/82 Da=e 5/>0/C2 Calc Re uest for Flov Cal Data Sheet CUSTOMER SERVICE .C. ENGINEERING PURPOSE OR OMZCTXVE:

Yo define the details of flow calihratian and operation of the flow station.

w QGtgf with the CL1&toIRex'exvLce MRx4Lger

~ti RESPONSIBXXZTY FOR AUHXHXSTM5KON 6 CX86?XZ2LHCE=

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have I! g t. KI~

Compliance with specifia tasks a?a~ he as designate hp the t

been certified by 4~Ming record to epmate the scar stand and e~pment to be calibrated. Changes +ay en1y'e by or with the approval of Quality As:~u~ce.

~e REVXSIOH RECORD l f 3

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I QA Pile 3 11/D/Sl l l l l f l l l Separated 480/960/990; provided 3 9/16/88 I l l -data sheets; Min Flow = 1'/s; NR { 3 3 I H/A,.for 990 ~

3 3 l l l f l l 2 l Expanded initial conditions; flow 10/18/90 f 10/21/90 f l time & weight requirements; certifig 3 Re-isaac l I cation. l 1 /20/90 l l l l l . l 3 Para 2.8 to allow initial calih at, 8/30/91 I '",!>/ l I l any flow rate; added l. 7, 2. 8 l l l l l l I 3A Para 1.6, 2.8, 2.14 added Pgen use 6/29/~} </&/lZ l in 480. l l ONTROLOTRON ORPQRATiON

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18:84FN CGNTRGLOTRON 516-F31-33~4 GCT 89 "92 a

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CONTROLOTRON CORPORATION a80/960/990 FLOM CALKBRATION PROCEDURE XHXTXAL CoNDXTXoNS '

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The stancXax6 flow calibration vi11 be done at, zero Ma+ g1as 4 l

points up to customers maxixnzm flov, or to lo Ct/sec 5X met, specified.

1-2 f A 1m'alibration vozk order shal3. be Customer Sexvice Rmministzatian as d'art of fin~ ~ eat hp Sa~ cxr BnB:iaX ~xR order and sent, to the Customer Seztrice Emagex Sar 2'. customer purchase orders that contain gL cmr Nuclear Saittey statements aze to be red.eved bp'm~~ ~ban 1o4 to perfoxuung the vezk.

Prior to starting any fRov ca16mddan, been intrinsica11y ca1ihrateC zmk th N 1t t I l~

~y teste@

+ear enik Customer retaxned equipment aha11 Xo33.ov caatxaam P.o. zecpBxa-ments, and/or the following:

mme %we in A. electronics and transducexs are M be checked 59m e~yCganent foz pzoyoz iocctionihg w~ith t aigastizg, chcmgihg, cz repairing any function, or zemava1 of custaaer data in memory ~

B. Xf a malfunction is found, the customer is to be notiXiek that there is a defect and customer instruction of continued vozk (in writing} is to be obt~ed, does not, pmvide such instructions.

if the P o Unless othexwise specified, net equipment eh Q.l ce1y recpdxe "as cleft" data; custcnnez retazned ecpipmezrt slue zecpxixe founcP and <<as left" data: repaired customer equipment sbz61

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require "as left" unless the repair is Known not to affect the acquisition and/or processing of floe data.

1.6 The calibration status of the Plow Stand and test, equipment shall be checked ta assure that they are within the calibration dates. The Timer, Temperature Cuage, and Floe def~

Stand CCT numbers shall be entered on each data sheet >4r 480 systems include the frequency counter.

ONTROL.OTRON RPORATlON

516-<31-333 OCT 89 '92 18:GSN CONTROLOTRON

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oc aqs 1.7 Znitia3. flov points to establish the calibration slope azxX adjust the instrument may be made, during the "calibration phase" of the flowmeter. The data sheet is to izxU.cate that an adjustment was made, and a11. prior data are not to be used,.

l.7.1 Xf any flov rate is found, to be outside the xecpxized, fLov rate

~

.. tolexa~, the'slope may'be aigasted and a13. no~em Mav

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rates repeateR.

2~ ON PRO BURR Review f3.ov th th of pohzts;

~ calibration work order Ml max Qov, proper

&eh~ and Purchase Order it te I-ls8 assare pipe, axe recpd;reX acaaacy ) ---- ---

2-2 t-~~t Control~~ Tnstal1atiau Hannah.

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Hount the pipe'of the designated, size Sp fh in the PIcv water 8I ~$a+ted~

f3ear Xcc.

th 3aast 5 aaR minutes to stabiLixe aeeitbxi.

..3 Check the ~kicable genexaL after at 3.east M mba.

of oZ~ration.

a. 2arplitade e. Zero Ringe

b. Have Shape Zero Stab&.9.ty

c. Slew Rate g. H Position (F/A far 990 Sys)

Abilityto Set 2'ero 2 4 Chec3c data scatter at zero KLov by records~ 2D mmmm~. The average should be mmdmua of .01 ~sec.

2.5 Set-up and fill out a stan~ data sheet (CC174) for st-a&an%

4 points plus zero data zan. Additional data points can be ran if contracted with the custcaner and specified an the vaxk order. P1an flov points approximately ecpxally spa~%,

. including xwdmum and a~mrna points as specified by the customer. These points must flow rates for the particular pipe specified.

~ within the maciIma acRuevable

2. 6 Measure taxeveight of tan3c and record value.

2.7 Measure water temperature and record value.

2.8 Start flow run at a selected flow rate. Close weigh tan3c outlet valve and start totalizer and timer simultaneously.

For 480 systems connect the frequency counter to Plea and start the counter instead of the totaliaex.

ONTROLOTRON ORPORATIC)N

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2.9 Continue floving for the specified time and the veight specified belov in order to assu e r ~m minixrm'ifferential 0.254 flov stand accuracy. Shut off timer and totalize simul-taneously and read the tank veight at. that moment. Record tank weight, t:otalizer count, and time M seconds.

HEH3XUK TXME AND SEICEP I

FowTme Di ferential Hei 60 SEC (Kin. Time) 2000 LBS 120 SEC 1000 XBS 180 SEC 800 XiBS 240 SEC 750 XLBS 300 SEC (or greater) 700 XaS 2- 10 Suhtract staxting ~Qc weight frcaa Xa11 tax'eight to get ~ V.

2 11 Using water temperature measured Kook ap anC 'xeccxecX tea md~

density (9) as shown'n Tab3.e 1 Ca1cu1ate actuaa1 volume (Vact) . Vast ~ ~V/P 2 13 Qact (Actual P1ow) = Vact/Time.

2; 14' Qind {P1owmeter Reading)~ ~ Tota1izerfTima.

Por 450 System: find Pgea Couut/KC.

15 ~Q - P1omreter reading - 2ketua1 F1' ging pact.

2 16 4 error = ~Q/@an't x 100 2- 17 Repeat, the abave procedure at: a11 designated flow rates, recording starting tank weight.

2. 18 Xf any flow measuxement does not meet xecpuzed acamcy make slope ad)ustment and xepeat all floe runs.

FLOW CAL BROOM'CORVES Review calibration work oxder to specified.

see if any curves vere 3.2 ~ If thexe are no special requirements,'he standard plot. vi11 be percent deviation Us actual flow.

ONTROi'a TRON ORPORATION

>16-231-3334 Vt i 6N NC ~d <am"l cvNIrcULVI i.ON g AXO 0

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3-3 The plot'. sha3.1 include the error '-'ts, as given in t" - 3c 3.4 A1 'dM MplL~1h M ~

th pt,1 k.

I St 6 l~ h TXON 4.1 A11 f1'allbzatians ans s sha13. &clara a Cezt~lcate oX caXi s gn CtX Si. hy a xepxeseatative of the m>X9.~

ONTROLOTRON ClRPQ RAT)GN

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Cgc f, CS2 DENSITY OF RATER IN AIR TABLE l (Sht l of 2)

TEMP. P DE NSXTY (lhs/gal)

%%*****4*%*****+4*%+* 4**+%**4*%4***%*

32 '

33.0 8.33061 8 33088 34.0 8.33115 35.0 8 33141 36.0 8.33151 37 0 38.0 8.33160 8 33169 39 '

40 ' 8-33179 8 33188 41-0 8 '3177 42.0 8.33164 43 0 8 33153 44.0 8.33140 45 ' 8 33129 46.0 8 33101, 47.0 8 33070 48 0 49.0 8.33042 50.0 8.33012 51 0 8.32984 8 32935 52.0 8 32889 53.0 8.32842 54.0 8.32795 55.0 8-32747 56.0 8 32684 57.0 8-32620 58 ' 8 32557 59.0 8 32497 60 0 8 32430 61.0 8 32351 62 0 8 32275

63. 0 8 32196

64. 0 8.32120

65. 0 8 32041

66. 0 8.31949

67. 0 8.3l857 68-0 8.31764 69.0 8.31672 70.0 8.31580 71.0 8-31474 72 0 8.31369 QNTROLOTRON ORPORATlGN ice ni ~ ~

1U:8aHPl UVNiROLOtRON 516-231-3334 ui i VS 'Sc.

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C7 CS2 DENSITY OF WATER IH AIR TABLE 1 (Sht 2 o 2)

TEMP. F DENSITY (1hrs/gal) 4*****4k*******+*+****+**+*%4k*%****4 73 ' 8.31263 74.0 8.31158 75 0 8.31052

76. 0 8 30933 77 0 8 30815 78.0 8 30698 79.0 8.30580 80.0 8.30461 81 0 8 30330 82.0 & 30202 83.0 8 30071 84 0 8.29942 85.0 8.29811 86.0 8.29670 87.0 8 29527 88 ~ 0 & ~ 29386 89 0 &.29243 90 0 8.29102 91.0 8.28949 92.0 8.28797 93.0 8.28644 94.0 8.28492 95.0 8.28340 96.0 8.28176 97.0 8.28013 98.0 8.27853 99 ' 8.27690 100.0 8.27527 QNTROI OTRON ORPORATION

ENCLOSURE 4 CPELL POSITION ON TECHNICAL SPECIFICATION REQUIREMENT

CP&L POSITION ON TECHNICAL SPECIFICATION REQUIREMENT FOR ALTERNATE MINIFLOW ISOLATION VALVES The operability of the motor-operated valves associated with the alternate miniflow system is required for Charging and Safety Injection Pump (CSIP) operability. If an alternate miniflow valve becomes inoperable, a 72 hour8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br /> Limiting Condition for Operation would exist for the associated CSIP under the existing Technical Specifications, The safety injection portion of the alternate miniflow isolation valve logic signal is already tested in accordance with Technical Specifications. The pressure signal to the motor-operated valve logic is a portion of the safety injection required actions; therefore, similar to the Auxiliary Feedwater System, verification of actual actuation will be performed every eighteen months. Calibration of the pressure transmitters is already included in Technical Specifications (as part of the Reactor Vessel Level Instrumentation System) and is performed on a refueling interval. Based on the above, CP&L has determined that no changes to Technical Specifications are required.

ENCLOSURE 5 MOTOR-OPERATED VALVE DESIGN BASIS REVIEW SET"UP CRITERIA f

DIF ERENTIAL PRESSURE TEST RESULTS