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

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

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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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CAROLINA POWER

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

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

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

~4 O~r~op RTIFICATE OF FLOg CAZ,IBPATION CAROLINA POQER 6 LIGHT HARRIS PLANT AMENDMENT d3

~CHASE ORDER NO.

XT00000075 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 CALIBRATIONAT CONTROLOTRON OR AT EXTERNAL FACILITIES ARE PERFORHED BY KVQ2KB CONTROLOTRON PERSONNEL'ND ALL FACXXiETX EQUXPMERiT UTILIZED ARE TRACEABLE TO NXST.

THE MATERIAL IDENTIFICATIONAND ACCURACY IS XN ACCORDANCE HXTH THE FLOH CALIBRATXON REPORT XNDXCATED BELOg-994P5GLS-3 991PMS-2 u2415 U4077 ATTACHMENTS FLOg CALIB.

REPORT NO.

9107 2 QUAL T'I SUPERVXS DATE CC2O4-B.1 C3NTRC3LOTRON ORPO RATION 155 Plant Avonvo Havnpavge. NY 117'9e

~ (51el 731-1+<>

pl AHd gl Ch A

O+p<og FLOR CALIBRATION REFERENCE

~q 'h DATA SHEET CAL. f 9107 2 MODEL P/N:

9 4PSG CUSTOMER:

C RO LOCATION:

DATE OF CERTIFICATION:

10-9-92 S/N P/0 N/0 TEST E UIPMENT TEMPERATURE Di itec 5820 TIMER NEWPORT Model 6130A INDICATOR BLH Mode1 LCP10 VR2.26 S/N CCT-301. Due S/N 36 ue 1 2 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 MAXIMUMERROR OF

+-

1X APPROVED BY:

DATE CC-246-3 o~v'aocov'aoN OaPORATlOM 155 Plant Avenue ~ Hauppauge, NY 11788 ~ t516) 231.3600

UU I U0 '0C lU:U~HM l UN IkULDlkON 516-231-3334 O

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CONTROLOTRON CORPORA::-OS 990

":OR CALIBRATION DIAGNOST C DATA SEE T

P.s CUSTOMER:

CAROLINA POUER

& LIGHT FDC P/N:

994PSGLS-3 TRANSDUCER P/N:

991PMS'-'

Y.O.:

921045 FDC S/5:

U2415 TRANSDUCER S/N:

U4077AIS SITE NAME:

3SS40CAL PIPE SIZE:

3SS40 TRACK MOUNTING (D/R):

DIR TRACK SPACING INDEX:

B-8 PER:"

B~:

DATE:

10-8-92 LIQUXD TEMP:

DEGRESS P

78 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:

Vale:

Px N:

nxVfmax:

TN TL Checksum Code LTN Contour 1495 30 13 10 2119.99 91.98 55 '3 02B31E78 100792-0016

.906 (Liquid Sonic Uelocizy)

(Liquid Signal Streng ")

(Transmit Frequency)

(Transmit Count)

(Receive Count)

(Receive Displacement)

(Maximum Flow Velocity in Ft/Sec)

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

(Computed time for sonic beam in liquid)

(Software integrity check)

(Controlotron Corpora-=on control code)

(Transducer Spacing)

(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 FDC:

PH 994P56LS-3 TRANSDUCER:

PN 991PhS.2 Nl 92l045 FDC SIN U24l5 POI 1 T0000007$

PIPE SIZE 3SS40 TRC ITS (0/R) DlR 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 l.BS LBS TENP DHOITTYOL VOL T1%

DE6 F Yact Yin4 START STOP STOP'ELTA Quet had DEETI 0 X ERRN TI%

SEC(NDS SPll SP}l SP%

1 3l8 2

386 2.5 2844 2526 78 8.30698 304.0816 301.3 3N9.$

2963.$

78 Oo30698 356.748}

353.$ 2 4258.$

3816 79 8.30580 459.4379 455.9 4781 4232.$

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

435.31 43$,3} 4f.9}2Q 4}.$2902 Wa3C39

%.9}5f 0

342.99 342.99 62.40674 6}i@203 4.$647}

%.90$ f 0

346.25346,25 79.6}3N 79.0N72 W.Cf3N 4.770f 0

303.22 3N.22 100.&344 }00.4300 <.40439 4.4011

2.00%

CAROLINA P8cL,WO 92't 045,PO XT00000075 FDC U2415,XO 04077,PlPK 3SS40 1.50%

0 0

20F 1.00%

0.50K O.QOX

-0.50K

-1.00K

.91 5'0.905%

-0.770K

-0.401%

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(!3 I

E!3l!i t!3

-1.50K

-2.005 60 CPM 80 100

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

"- POLIClES AND PROCEDURE5 o

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P.M Type CUSTOMER SERVICE Subject ~g CALIBRATION (I4gp/96p/99p)

Flov Curve, Density Chart; NR Calc Re uest for Flov Cal Ad~in-'-y CUST SERV Prep. By Dare 5/5/82 CS-2 Appr.By Da=e 5/>0/C2 Data Sheet CUSTOMER SERVICE

.C.

ENGINEERING PURPOSE OR OMZCTXVE:

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

RESPONSIBXXZTY FOR AUHXHXSTM5KON 6 CX86?XZ2LHCE=

w QGtgf ~ti Kth1 l I -~h with the CL1&toIRex'exvLce MRx4Lger Compliance with specifia tasks a?a~ he as designate hp the t

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t who have been certified by 4~Ming record to epmate the scar stand and e~pment to be calibrated.

Changes +ay en1y'e ~e by or with the approval of Quality As:~u~ce.

REVXSIOH RECORD l

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Sa~e of Change f

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3 f

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QA Pile 3

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l Separated 480/960/990; provided 3

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-data sheets; Min Flow = 1'/s; NR

{

H/A,.for 990

~

3 l

l l

Expanded initial conditions; flow time

& weight requirements; certifig cation.

l l

Para 2.8 to allow initial calih at, l

any flow rate; added l.7, 2. 8 l

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Para 1.6, 2.8, 2.14 added Pgen use in 480.

l

"'3 l

11/D/Sl l

f l

9/16/88 I

3 3

3 f

l 10/18/90 f

10/21/90 f

3 Re-isaac l

l 1 /20/90 l

l l

8/30/91 I

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l 6/29/~}

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l ONTROLOTRON ORPQRATiON

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

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CONTROLOTRON CORPORATION a80/960/990 FLOM CALKBRATION PROCEDURE

~ ~ ~ ~

XHXTXALCoNDXTXoNS '

1-2 1o4 1.6 The stancXax6 flow calibration vi11 be done at, zero Ma+ g1as 4

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

A f1m'alibration vozk order shal3. be fin~ eat hp Sa~ cxr Customer Sexvice Rmministzatian as d'art of~ 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 to perfoxuung the vezk.

Prior to starting any fRov ca16mddan,

+ear mme %we been intrinsica11y ca1ihrateC zmk ~y teste@ enik in th N 1t t

I l~

Customer retaxned equipment aha11 Xo33.ov caatxaam P.o. zecpBxa-

ments, and/or the following:

A.

59m e~yCganent electronics and transducexs are M be checked 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, ifthe P o does not, pmvide such instructions.

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

The calibration status of the Plow Stand and test, equipment shall be checked ta assure that they are within the def~

calibration dates.

The Timer, Temperature

Cuage, and Floe Stand CCT numbers shall be entered on each data sheet

>4r 480 systems include the frequency counter.

ONTROL.OTRON RPORATlON

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

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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

~ "

rates repeateR.

2 ~

ON PRO BURR 2-2 Review f3.ov calibration work order and Purchase Order te assare th th ~

Ml &eh~

it I-ls8 of pohzts; max Qov, proper pipe, axe recpd;reX acaaacy ) ---- ---

Hount the pipe'of the designated, size in the f3ear +ted~ aaR t-~~t g ~

Sp fh 8I ~$

th Control~~ Tnstal1atiau Hannah.

PIcv water Xcc. a 3aast 5 minutes to stabiLixe aeeitbxi.

..3 Check the ~kicable genexaL of oZ~ration.

after at 3.east M mba.

a.

2arplitade b.

Have Shape c.

Slew Rate Abilityto Set 2'ero e.

Zero Ringe Zero Stab&.9.ty g.

H Position (F/A far 990 Sys) 2 4 2.5 Chec3c data scatter at zero KLov by records~

2D mmmm~.

The average should be mmdmua of.01 ~sec.

Set-up and fillout 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 ~ within the maciIma acRuevable flow rates for the particular pipe specified.

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 minixrm'ifferential veight specified belov in order to assu e r ~m 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 FowTme I

Di ferential Hei 60 SEC (Kin. Time) 120 SEC 180 SEC 240 SEC 300 SEC (or greater) 2000 LBS 1000 XBS 800 XiBS 750 XLBS 700 XaS 2-10 2 11 2 13 2; 14' 15 2 16 2-17

2. 18 Suhtract staxting ~Qc weight frcaa Xa11 tax'eight to get ~ V.

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 Qact (Actual P1ow) = Vact/Time.

Qind {P1owmeter Reading)

~ Tota1izerfTima.

Por 450 System:

find ~ Pgea Couut/KC.

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

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

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

FLOW CAL BROOM'CORVES 3.2 ~

Review calibration work oxder to see if any curves vere specified.

If thexe are no special requirements,'he standard plot. vi11 be percent deviation Us actual flow.

ONTROi'aTRON ORPORATION

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C7C OH 3-3 The plot'. sha3.1 include the error '-'ts, as given in t" 3c 3.4 A1 'dM MplL~1h th

k. M ~

l~

h pt,1 I

St 6

TXON 4.1 A11 f1'allbzatians s

Si.

CtX s gn hy a xepxeseatative of the m>X9.~

ans sha13. &clara a Cezt~lcate oX caXi ONTROLOTRON ClRPQ RAT)GN

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i d9 d 18: 86I=N CON TPOLOTRON 516-231-3334 NOg a

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

P. 14 NSXTY (lhs/gal) 4**+%**4*%4***%*

TEMP.

P DE

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

32 '

33.0 34.0 35.0 36.0 37 0

38.0 39 '

40 '

41-0 42.0 43 0

44.0 45 '

46.0 47.0 48 0

49.0 50.0 51 0

52.0 53.0 54.0 55.0 56.0 57.0 58 '

59.0 60 0

61.0 62 0

63. 0

64. 0

65. 0

66. 0

67. 0 68-0 69.0 70.0 71.0 72 0

8.33061 8 33088 8.33115 8 33141 8.33151 8.33160 8 33169 8-33179 8 33188 8'3177 8.33164 8 33153 8.33140 8 33129 8 33101, 8 33070 8.33042 8.33012 8.32984 8 32935 8 32889 8.32842 8.32795 8-32747 8 32684 8-32620 8 32557 8 32497 8 32430 8 32351 8 32275 8 32196 8.32120 8 32041 8.31949 8.3l857 8.31764 8.31672 8.31580 8-31474 8.31369 QNTROLOTRON ORPORATlGN ice ni

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1U:8aHPl UVNiROLOtRON 516-231-3334

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

TEMP.

4*****4k 73 '

74.0 75 0

76. 0 77 0

78.0 79.0 80.0 81 0

82.0 83.0 84 0

85.0 86.0 87.0 88 ~ 0 89 0 90 0

91.0 92.0 93.0 94.0 95.0 96.0 97.0 98.0 99 '

100.0 F

DENSITY (1hrs/gal)

• • • • • • • +*+****+**+*%4k*%****4 8.31263 8.31158 8.31052 8 30933 8 30815 8 30698 8.30580 8.30461 8 30330

& 30202 8 30071 8.29942 8.29811 8.29670 8 29527

&~ 29386

&.29243 8.29102 8.28949 8.28797 8.28644 8.28492 8.28340 8.28176 8.28013 8.27853 8.27690 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 DIFfERENTIAL PRESSURE TEST RESULTS