ML17221A606

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Forwards Addl Info Re Util ASME Code Relief Requests for Various safety-related Pumps,Per NRC 871214 Request.List of Data Util Unable to Gather from Pump &/Or Motor Vendors to Date Also Encl
ML17221A606
Person / Time
Site: Saint Lucie NextEra Energy icon.png
Issue date: 01/28/1988
From: Woody C
FLORIDA POWER & LIGHT CO.
To:
NRC OFFICE OF ADMINISTRATION & RESOURCES MANAGEMENT (ARM)
References
L-88-48, NUDOCS 8802030049
Download: ML17221A606 (36)


Text

REGULATO INFORMATION DISTRIBUTION '.

TEM

< R IDS )

ACCESSION NBR: 8802030049 DOC. DATE: 88/01/28 NOTARIZED:

NO FACIL 50335 St.

Lucie Planti Unit 1I Florida Power Zc Light Co.

AUTH. NAME AUTHOR AFFILIATION WOODY'. Q.

Florida Power 9x Light Co.

REC IP. NAME RECIPIENT AFF IL I AT ION Document Control Branch (Document Control Desk)

DOCKET 0 05000335

SUBJECT:

Forwards addi info re util ASME code relief requests for various safety-related pumps'er NRC 871214 request. List of data util unable to gather from pump Zc/or motor vendors to date also encl.

DIBTRIBUTION CODE:

A0470 COP IEB RECEIVED: LTR I

ENCL J SIZE:

TITLE:

OR Submittal:

Inservice Inspection/Testing/Relief.

from ASME Code NOTES:

RECIPIENT ID CODE/NAME PD2-2 LA TQURIGNYi E INTERNAL: AEQD/DOA ARM/DAF/LFMB NRR/DEST/MTB OGC/HDS2 RES/DE/EIB EXTERNAL:

EGhG ROCKHQLD> H NL 007 HEMMING NSIC COPIES LTTR ENCL 1

0 1

1 1

0 1

1 1

0 1

REC IP IENT ID CODE/NAME PD2-2 PD AEOD/DSP/TPAB NRR/DEST/MEB N

S/ILRB FILE 01 LPDR NRC PDR COPIES LTTR ENCL 5

5 1

1 1

1 1

1 1

1 1

TOTAL NUMBER OF CQP lES REQUIRED:

LTTR 21 ENCL 18

I I It

P. O.Bo, JUNO BEACH, FL 33408.0420

,y>> hiI 'Ij

)ANUARl', 2 8 1S88 L-88-48 U. S. Nuclear Regulatory Commission Attn:

Document Control Desk Washington, D.

C.

20555 Gentlemen:

Re:

St. Lucie Unit 1 Docket No. 50-335 Request for Additional Information ASME Code Relief Re uests for Various Safet -Related Pum s The purpose of this letter is to provide the additional information requested in your December 14, 1987

letter, "Request for Additional Information

ASME Code Relief Requests for Various Safety-Related Pumps" (TAC No.

64819).

Attachment 1 provides the addit'ional information.

In conducting our research for the additional information on pump data and motor data, we determined that certain of that data is not, readily available.

Attachment 2 provides the list of data which we have not been able to gather from the pump and/or motor vendors to date.

On January 26,

1988, we discussed the status of our response with the NRC project manager and stated that efforts are continuing toward obtaining the data from the pump and motor vendors.

Should there be questions, please contact us.

ery truly yours, E e O.

Woody cutive Vice President COW/MSD/gp cc:

Document Control Desk, USNRC Senior Resident Inspector, USNRC, St. Lucie Plant MSD/027.ASME 8802030049 880128 PDR ADQCK 05000335 PDR pyg7 an FpL Group company

p k

)I~

qy)$ A) p I-fB ll 1

'I P

ATTACHMENT 1 ST+ LUG IE UNIT ¹ 2

RESPONSE

TO NRC QUESTIONS ASME SECTION XI TEC HNI GAL J USTIF I C ATION FOR RELIEF FROM PUMP FLOW MEASUREMENT REQUIREMENTS J PE-PSL-SEM J-88-009 FLORIDA POWER 8 LIGHT COMPANY POWER PLANT ENGINEERING JUNO BEACH, FLORIDA

J PE-PSL-SEM J-88-009 REV. 0 PAGE 2 of I I

J PE-PSL-SEM J-88-009 REV. 0 PAGE 3 OF /9

RESPONSE

TO NRC RAI: ASME CODE RELIEF REQUESTS FOR VARIOUS SAFETY RELATED PUMPS (TAC NO. 64819)

PART IIA RE: FPL TECHNICAL EVALUATION,JULY 31, 1987, FIGURE 1

When a pump degrades due to wear that affects hydraulic performance, there is a loss of both pump flow and total head.

Figure 1 illustrates these effects graphically and shows the relative changes in indicated system parameters that result at both minimum flow and rated flow.

Pump total head curve "A" represents a typical head-flow curve for a centrifugal pump defined to be operating at rated performance.

In contrast, pump total head curve "B" illustrates the relative change in head and flow for the same pump with degraded hydraulic performance.

Total system curves "A" and "B" illustrate typical system curves for a minimum flow path (recirculation flow path) and full flow or rated flow path, respectively.

These curves are representative of the respective system curves for the referenced St. Lucie pumps.

The points at which the system curves intersect the pump curves determine the corresponding head and flow values for each of the four operating conditions, i.e.,

nonMegraded pump at minimum flow; degraded pump at minimum flow; non-degraded pump at rated flow,'egraded pump at rated flow.

The crosshatched area extending to each axis of the graph serves to illustrate the relative change in total head and flow for the respective systems when pump hydraulic performance degrades.

It should be noted from this illustration that the flow loss is considerably less for a given amount of degradation if the system total head curve is steep (recirculation flow conditions) compared to a flat system total head curve (full flow conditions).

However, for the same pump degradation the loss in total head remains relatively constant regardless of the slope of the system curve.

It is also notable that, with a steep system curve, a change in the shape of the pump "curve produces a greater corresponding change in pump total head.

The purpose for including Figure 1 was to illustrate that, for fixed resistance systems operating at pump recirculation flow rates, total pump head is relatively independent of minor changes in system conditions.

Therefore, measurement of total pump head should provide a more reliable indicator of relative pump degradation while eliminating the need to introduce additional measurement'error to establish specific flow conditions.

PART II B An analysis was made of industry failures reported by LER/NPRDS (Appendix A) for the subject pumps.

The reports indicate that hydraulic degradation can be attributed to 7~a of those reported and that these failures were caused by wear P

J PE-PSL-SEM J-88-009 REV. 0 PAGE 4 OF l9 related mechanisms.

The remaining 93Ho were attributed to mechanical degradation and were caused by mechanical seal/packing area (47~o), bearing lubrication problems (17'), alignment (14%), and other items such as imbalance, loose studs, etc. (1596).

An analysis of St.

Lucie maintenance records (Appendix B) indicates that the maintenance performed follows the industry reporting of failures; i.e.,

the degradation measured is typical, of the industry.

The maintenance records indicate that hydraulic degradation accounted for 4~o of -the maintenance performed, and that mechanical degradation accounted for the remaining 96~~o.

Based on the data available, mechanical degradation is more of a concern than hydraulic degradation, i.e., degradation of mechanical seal sealing surfaces, packing, improper lubrication, bearings, alignment, imbalance, etc.

Analysis of operating times (Appendix C) for the subject pumps at St. Lucie indicates that pump operation can be considered as intermittent based on the low service usage.

It is reasonable to expect industry data on operating times for pumps in the same application to be typical of St. Lucie and that these pumps be considered to operate intermittently.

Because of this low service

usage, normal wear to components related to hydraulic performance (i.e., impeller, wearing rings, etc.)

is also expected to be low, and in fact, this is confirmed by the data previously submitted as Apppendix A; PART II C There are presently no other AFW system bypass lines on PSL-2 that could be used for surveillance testing at greater than miniflow rates.

.. Page Vo=.:

1

'f/13/87"

'- tfPSI PSL< SAFETY IEIATED PINP DfOJNTIOtf REPORT FORH 'PINPS'NRIC ACID NE lP J PE-PSL- >EMZ-N-~'f

'i @v!o:;-

pAGE:*i-oz.

" SECTIN 8 PIP DATA 01 tR 02 SIZE 03 N. STAGES 04 CNFIQNATIN 05 I%M/OPPOSED QETINt 07 DIS.NNER 08 DISCH SIlE 09 SPEED 10 FLOtf ll SIET.PJKSS 12 'ISCH PRES 13 JIPSHR 14 SPEIFIC SPEED iS Sm.

SPEC.SPD 16 PN INTEH.FACT 17A tEAD.VS FLN

'1?B EFFIC. VS FLNf I?C fNP VS FLOff 170 HPSN VS FLNf 1&

HIHIFLNf SECTISI C HOTOR DATA 01 tf6 02 RQS@ERll 03 SPEED 04 TORXE 05 VOLTS 06 A%BES 07 HORSEPNER 08 SERVICE FACTN 09 TTK IOA SPEED VS TOIOE lm I3RREtfl VS lONE 10C EFFICIHCY VS TOJOE 10D PN FACTOR VS TONE 81%HAH 3X4X9 7

CEHT.IIORll IJU%

SME VOLIJIE 3'M 315 GPH 25IN HAX N0 FT.

10.0 FT.

FIQNE 1 FIQNE 1 FIQNE 1 FIGNE I 306Ptf/6.?l GE 3/60 3575 587 4000 54 400 1.15 INUCTIOH FIQJJK ll FlmfK 114 1%EfmL

&X20 1

CEIIT.VERT N

SIJIGLE DIFFUSER 8'?fn 31M GPH XN NX 350 FT.

17.0 FT.

FIQNE 2 FIQNE 2 FI6%E 2 FI6URE 2 100GPH/2.N IESTItaaSE 3/60 1779 llM 4OM 50 4N 1.15 16JCTIN FIQJIK 7

'IQJfK S~

FINRE P4 IHGERSOL

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KIT.VERT.

N SINE DIFR5ER 8'?f6 28% 6PH 2IN HAX 470 FT.

15.0 FT.

FINE 3 FIQNE 3 FIQNE $

FIQNE 3 1506PH/4.n Slm 3/60 1780 l475'0M 643 5M 1.15 item:TINI FIQNE 9 FIQJJK 15 IIIGERSOL 4X3 10 CENT.HORIZ IN.IJE SINE DIFFUSER 3570 3M 6PH IIXN

~

11M PSIG'1.0 FT.

FINK 4 FI6NE 4 FI6URE 4 FI6URE 4 50GN/12.5X 6E 3/N 3570 515 4N 4?

3M 1.15 IINCTIOH FI6UfK 12 MGNL 6X4 7

COIT.HORIl IRNK SIKLE DIFFUSER 4"

3750 570 6N IIXN 1150 P$16 16.0 FT.

F16URE 4A F168'A FI6NE 4A FIQNE 4A 706PH/8.5 N

N N

N N

N N

N

$l TINIIK N

N N

NU6 3XI 1/2 1

NA'.HORI/

N SDKLE VOLUTE 1

1/2'5M 143 GPH Ilk 231 FT.

9.0 FT.

FIQNE 5, FIQNE 5 FIQNE 5 FI6NE 5 IDGE/5 ?X fKLIAJCE 3/N 3515 54M 460 31 25 1.15 IMJICTIN FlmfK 13 FIQNE 134 GNUS 1X2X10 1

CEHT.HORIZ N

SItfGLE VOLUTE

'0 1750 25 GPH Q

35 PS16 1.0 FT.

FI6URE 6 FIQNE 6 FIQNE 6 FIQNE 6 N

IKSTittGINSE 3/60 1710 460 43..

1.M INUCTINI Current vs torque values ln these cases are not graphed in relation to each other.

Current and torque, however, are graphed together vs speed.

Efficiency and power factor are graphed vs horsepower and not torque..

      • Zero speed torque value obtained from speed vs torque curve.

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CUSTOMER CE/FLORIDA P&L PROPOSAL NO, 001-36382 ITEM SPECIAL NOTES DESIGN CONDITIONS GPM 310IID GFI'.

H. IFT.) 35p BHP 342 Sfst. 0 RPM 1780 DRIVER HP NNB@ma aatlm ReaIIae9 DRAWN BY R. Ponden 7/10/7 CURVE N-695 Rev. 1 8X20WOF Curves ore approximate.

Pump is guaranteed for ona set of conditrons. Capacity, heod and eflicicncy guar-antees are hosed on shop test ond when handling clear. cold, fresh wotor et o temperature of not over SS degrees ond aot over IV suclFon lift.

500 500 0

0 400 fpp O2 80 300 200-VO 300 Epp R

A 0

GO 5

80 j18(/BE 4t'-

Cht -2 LP~

PdWP Lpp I

p w

2Q rr3 0

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C' 10, 0 20 Q

M 30 0

40 0

5 00 GALLONS PER MINUTE

CUSTOMER t. 4A 4(o/~~~F fplgAy7 PROPOSAL NO.O Jrr-3W g(. ITEM SPECIAL NOTES Pc eA 4'rtl /o 7C/Pg DESIGN CONDITIONS GPM 284 >

EFF yr BA T, If.fFT,I +~+

DHP

SG.-

RPM /78'RIVER HP g op@'P/f> TC/Q MiTH I.ISJF DRAWN IIY y,p.~,

DATEg -)g.) 8 HIIICNCBQ'KWIIIe>>tRCIRQCII n

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CURVE PUMP 8 Qg 3 ~g~

Curvet ere epproaImot ~. I'ump I< <Ivor>>>>teed lor one iet ol condrboni. Copocity, heed ond

~ I."iciency Quoi.

~nteet ere bored on

<'hop le<I ond

<<he>>

hondlsng cleor, cold, freih voter ot ~ temper>>lure ol not over 8S dot<reer ond nol over IS'ucbon lilt..

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PsL-2. Co~i<~~

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GALIDNS PER MINIITE

$000

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