ML11320A129

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2011 Updated Final Safety Analysis Report, Revision 29, Drawings Part 5 of 5
ML11320A129
Person / Time
Site: Hatch  Southern Nuclear icon.png
Issue date: 10/24/2011
From:
Southern Nuclear Operating Co
To:
Office of Nuclear Reactor Regulation
References
NL-11-1812
Download: ML11320A129 (97)


Text

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NORMAL SHUTDOWN AFTER BLOWDOWN TO MAIN CONDENSER CSEE NOTE 8 ),

CONTINUATION OF NORMAL SHUTDOWN FROM PLANT MODE E (0 PSIG) & FUNCTIONAL TEST FOLLOWING SHUTDOWN ACCIDENT W/RECIRC LINE BREAK IN SIDE IT WITH STRAINER SO"70 PLUGGED AND ONE i~~~ (ObEpRtl6~~1 MAXIMUM RUNOUT CONDIT-RH R. SYSTEM TEST DURING PLANT OPERATION MINIMUM FLOW BYPASS MODE F.

H.

J.

E.

NOTES I--EMPTY DATA BLANKS ARE TO BE FILLED IN BY OTHERS (BASED ON HIS ARRGT'S) AND SUB-MITTED TO 8WRSD FOR REVIEW_ IF SIDE I AND SIDE n ARE NOT SYMMETRICALLY ARRANGED.

VALVES FOR 80TH SHALL BE SUBMITTED SEE SHEET 2 THE MINIMUM PUMP NPSH AVAILABLE DURING

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~~PSII SHALL BE DETERMINED BASED ON POOL TEMPERATURE OF 20TF AND CONTAINMENT PRESSURE OF 4.2 PS1G. FOR MODE C2 AND 165'F AND CONTAINMENT PRESSURE OF 2.0 PSIG. FOR MODE G, AND THE SUCTION STRAINER BEING PLUGGED WITH THE MAXIMUM POST-ACCIDENT DEBRIS LOADS.

ELEVATIONS ARE NOT INCLUDED IN t. P VALVES GIVEN ELEVATIONS SHALL BE INCLUDED WHEN DETERMINING FINAL VALVES FOR THE EMPTY DATA BANKS-.

4.

DASHED LINES INDICATES FLOW DOES -NOT PASS THROUGH THESE POINTS SERVICE WATER CROSS-TIE SHALL BE SIZED TO FLOW,200 GPM REF. SH 2 (J-ll).

6.

LINE SHALL BE SIZED BASED ON FLOW TO FUEL POOL SH 2 (B-9)

TABLE

! INDIC.<\\TES YI-LYE POSITIONS DURING VARIOUS MODES OF OPERATION SHUTDOWN OPERATION '( MODE E) MAY BE INITIATED AT A MAXIMUM REACTOR VESSEL PRESSURE OF ns PSIG 9.

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7 1970
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PLAN WEW MU'-nPL~$NErA5S~ THIS ORAW'lIG IS TII£ P_EIITY OF TIE OIICAGO IIItIDGE a,_ c-PANY AIID IS TO

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7 1970
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PLAN WEW MU'-nPL~$NErA5S~ THIS ORAW'lIG IS TII£ P_EIITY OF TIE OIICAGO IIItIDGE a,_ c-PANY AIID IS TO

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1. ATMOSPHERIC PRESSURE OF 14.7 PSIA WAS USED IN CALCULATIONS.
2. WATER FLOWS ARE SHOWN IN GPM, STEAM FLOWS IN 1000 LB/HR.
3. THE MAXIMUM POOL WATER TEMPERATURE FOR CONTINUOUS SYSTEM

~~~~~TI~~~~III~~~~~~OE~C;{DHI~~i'~' T~~~~~~~UR~~~ ;~I~gT~~~;~SION SHALL BE BASED ON 170"F.

4. THE FOLLOWING ADDITlONAL ACCIDENT OPERATING MODES ARE POSSIBLE:

SUCTION FROM CONDENSATE STORAGE, SUPPRESSION POOL AT LOW PRESSURE, REACTOR AT HIGH OR LOW PRESSURE. SUCTION FROM SUPPRESSION POOL, SUPPRESSION POOL AT HIGH PRESSURE, REACTOR AT HIGH OR LOW PRESSURE. THESE POTENTIAL OPERATING MODES DO NOT CONTROL PIPE OR VALVE SIZING OR SPECIFICATION, AND NO DATA IS SHOWN. 5. DELETED c REAC. TOR ~IlNOZZLE 6. THECONTIlOLLtNlMOOES FOR LINE SIZING A",., ARRANGEMENT

ARE, SUCTI ON FRCJ04 CONJ.

STORAGE - ~ MOOE A SUCTlGNFROMSUPPRtSSIONPOOL__ MCO£C PUMPOISCHARGE------ MCOE*( ST£AMSUPPLY-------*- __ MOOEB TURBINEEXHAUST---------MOOtA"C4.0 TESTLlNE--------- MOOEE COOLINGSYSTEM----- MOD£A 7. THEPRtSSURE Loc.ATlON@ ISESTIMATEDFRCfoIPRElIMINARYPUMPDATA. 8. ~t~= MINIMUM 1~~~~ME"N~MMAYMOf~~v~~b~Rt:l~~~T~~ MOOE. 9. DELETED D CONDENSATE r---------+....., 'STORAGE TANK --__....~_FEEDWATER MODE B ACCIDENT MODE: SUCTION FROM CONDENSATE STORAGE, REACTOR AT LOW PRESSURE. SUPPRESSION POOL AT HIGH PRESS. o 18 MODE A ACCIDENT MODE: SUCTION FROM CONDENSATE STORAGE, REACTOR AT HIGH PRESSURE. SUPPRESSION POOL AT HIGH PRESS. o MODE C ACCIDENT MODE: SUCTION FROM SUPPRESSION POOL. REACTOR AT HIGH PRESSURE. SUPPRESSION POOL AT LOW PRESS. Southern ComPF~Rny Services, Inc. PLANT: HATCH UNIT: 1 TITLE: PROCESS DIAGRAM - HIGH PRESSURE COOLANT INJECTION SYSTEM v~;~~RAL ELECTRIC IP'~~H-002 S-16122 B _MOOE ~E AND ~ 15 PSI MINI",",M NPSH AT PUMP SUCTION ~ ~1 FtrT MAXI",",M PR£SSUR£ fUSE ~ ~BOO FEET 8 HIGH ~ 5~5 FEET 8 HC'W MAXI",",'" PRESSURE DR'OPBErwt:£N Loc.ATlONS MAXI",",'" PRESSURE ~ 65 PSIA SUFHCI£NT PRESSURE TO RETURN TO SUPPRESS I SUFFICIENT PRE~SURE TO RETURj'l'TO CONJ. MAXI",",'" PRESSURE AVAILABLE ~ &5 PStA StlFnCIENTPRESSURETORETURNTO"'IJMP OP£R"'TlON. ACCIDENT MODE: SUCTION FROM SUPPRESSION POOL. REACTOR AT LOW PRESSURE. SUPPRESSION POOL AT LOW PRESS. ll(=TH£ PRESSURrAT THIS LOOTlOND£PENDSUPONPIPING A,NDMAYBEIIllRI£DIoIITH-INTHEFOUC'WINGLIMITS. ~ (i) TO<~ MODE E TEST MODE: SUCTION FROM CONDENSATE STORAGE, REACTOR AT HIGH PRESSURE. SUPPRESSION POOL AT LOW PRESS. 1J TOTAL LEAKOFF FROM TURBINE

t RO t
- 5.

CONDENSER j I LoEi f::.p '3.0 P:>I K M I1T""T.N.l IREViBY1 THIS DWG. PART OF VENDOR MANUAL N/A REVISED PER REA HT-96660. Ov~~ZS ~ '"Pil(SS-R(ACTClltIlESSElPQ(SSURE', SOM -Si'tITorrICAo,r....""'S) MODE H F'LOW-GPM 7,700 7,700 15,400 1'!>,40Cl PRC)~.-PSIA 14.7 'X X X 'Yl x x x "X""'x: I nMP.Of' MAX, ~. OROP-FEE1' I 34.7 10,10010,100110,100-I J Xl I MODE A (SEE NOTE 13) TEMP. Of" 1 1% F'LOO-GPM 1-10,100 10,100 10,100 TE,VP. ~ 1~"";;~5,.....-+-+--+-+--+-+--+--t--+-+--+-t-+f%- Rrr[R!:IjC[OOClMNTSJ ~ 1. RESI:lUAL HEAT Rr"'O~41 SVSTEM ~AI t> - "eU-1010 ? RrtlRcUlATIONWSTrM PIlOtESS FLC100i DnA - - *** -.!!I*I040 3. "k.ICUAR eollEI; ~ROC(SS DAT.- - .. - '.' -111-1020 X 14.7 .SOH575/620. ~.-PSIA TEMP. Of' MAX. PRE~. CROP-FEET ["'XX 'x:' 34.7 MODE B(SEE NOTE 13) ~-PSU~ 14.7 MOOEC-I MODE S MODES: A. p~J:ID!~~(6~~~~rwo~NlN~RJ-f'~~NERSI~6::!;'I p~rr~GED. f~8ID!~~W6~~~~rwo~NA~DBRS1AR~I~~RSIg6%1I p~rr~GED. POST ACCIDENT CONTAINMENT SPRAY W/HEAT RE- ~~~~r~~Ti~~~.nr~o~~~{sOJpEpRtm70~N~06[RAlNER C-2 m;;~o~C~~WSN(C~N~e-rMNpMEcl'~E~ATI~~~~~~tR~~ER ~~;Tlf~~GGED. PEAK SUPPRESSION POOL TEMP-D-1 DELETED D-2 DELETED E. NORMAL SHUTDOWN AFTER BLOWDOWN TO MAIN CON-DENSER. (SEE NOTE B) ~~~~~~~6g~~~) N2R~~~c~~~1?LOf~s[RF~~Lb~NT ~~~~A~§~,§Ei~~) W~UEGJ3ERDEAfN6N 0~~Ep5MP H, R.H.R. SYSTEM TEST DURING PLANT OPERATION. J. MINIMUM FLOW BYPASS MODE. S. SYSTEM ON STANDBY DUTY. POSITION 0 ~ DISABLED (------------'/\\'---------~ DE.5IGN PRE5SlJ~E. t TE.MPERF>:rURE.. GIVEt-I BE.LO'V( IS FOR INrORM",110N ONL'( ~ IS TI-4E. Bp..SI~ FOR DESIGN OF' BWRSP SUPPLIED EQUIPME.N1. 24 B 25 B 24 B 25 B B,OOOB,OOO B,OOOB,OOO xx 14.7X!X14.7 -- ---f--~ 19 B 19.5 19.1 B 20 B l.1 22 B 23 B 7,7007,300_7,300'-400400 x x x I


1.-

11,55010,950!-10,950 600600 t...4OOE. cot (SEE NOTE 2) 1B B BB 9 B 10 B 12 B 19 B 19.5119.1 B 20 B 1.1 22 B 23 B DUTY PER HX847x 106 RTlJ/HR (1

HXOPERATlNG)

DUTY PER HX56.1 x

1Q6 BTU/HR (1

HXOPERATlNG)

~'TIONO,

2 B&D. 3 B&D 4 B&D 5 B&DI6 B&D 7 B 17 B FLOW GPM 5,775 5,775 11,550 D

PCS'T\\ONO I

2 B 3 B 4 B 5 B 1 6 B 7 B 17 B 1B B BB 9 B 10 B 12 B fl.OW-GPM -

7,700 PR£S'5,-fl'51A 14.7 x:

X T£MP~-f=

1lM** ~,

(JIllDP-f:"EET F

TABLE 2 -

LIMITING LINE LOSSES MODE A MODE B MODE C1 THIS DWG.

PART OF VENDOR MANUAL N/A Southern ComPF~Rny Services, Inc.

PLANT:

HATCH UNIT:

2 illLE:

RESIDUAL HEAT REMOVAL SYSTEM PROCESS DIAGRAM VENDOR:

IP'~~H2-2 GE S25140 N

10. THE PRESSURE SHOWN AT POINT 1 ON MODE C-2 ISA MIN. VALUE FOR NPSH CALCULATIONS.
11. THE WEIGHT OF WATER IN THE SHUTDOWN COOLING

~lg~~i:i~~!~¥~~~it~\\jJ~~~~l~:~ORBER BELOW MINIMUM REQUIREMENTS.

12.

~~~AI~~~E5~%BpL8~tiD~ AND G ASSUME 1

13. i~~;~}i~E~~N~~~:~i~r!i~e~~:l~:;~t;~M

~g~St%~: C~~~ gW e!NL~~J~pl1N~~gTI~~M

~T~U~IN~R~~T~c RE&R~I~~TI~~

f~~PHIGH END OF A +4007-0 GPM SIZING TOLERANCE.

14. ~~~~t'ffgW~~Lm~9g~E~r81~B~:~%~SJi'
15. HEAD SPRAY DISCONNECTED AT RPV.

3.

!~~~~~~~tw~~~J~!L&~~~:~~t~~t~:~WJDATA 4.

DASHED LINES INDICATES FLOW DOES NOT PASS THROUGH THESE POINTS.

5.

~~§~C~p~~TJ~E CsRH~~sr~1 ~~ALL BE SIZED TO FLOW 6.

LINE SHALL BE BASED ON FLOW SHOWN ON FUEL POOL PROCESS DIAGRAM.

7.

~~~r6u~

I.\\W6~~TEd'FV~~¥~A~g~~ONS DURING B.

SHUTDOWN OPERATION MAY BE INITIATED AT A MAXIMUM REACTOR VESSEL PRESSURE OF 135 PSIG.

9.

DELETED DELETED DELETED DELETED MODE J MODE G MODE D2 MODE H MODE E MODE C2 MODE F MODE D1 MODE D2 (CONT) 10 o

0 0

~

0 0 T 8

01 0

OTOO I

TOo o

0000 P =

STRAINER PLUGGED BLANK SPACE INDICATES VALVE IS CLOSED T-C =

VALVE THROTILED OR CLOSED O-T =

VALVE OPENED OR THROTILED o

=

VALVE OPEN T =

VALVE THROTILED 7

I'lOOE E IGE. Cl I

B5192,7 B,ODOIB,DOO RX PRESS. B5 PSIG (SEE NOTE B)

MODE E (SEE NOTE 2)

DUTYPERHX30.Bx1Q6 BTU /HR(2HX'SOPERATING)

MODE F 3

MODE. G (SEE NOTE 2 &

13) ffMP. -F

......-+--+---+--+--~-...125 1117

........-+--l---+-~I---+-~I---+----..I DUTYPERHX1B7.1 x

1Q6 BTU/HR (2 HX'SOPERATING)

PRES~. PSIA l100 /"'-..x..

>c:

>c:

>e:

.x.

ex:

X

'100 xrx f}..OW-GPM 10,900 10,900 TEMP.

"'F 1-32B N/A FU*-GAIII I-15,400 15,400 7,700 7,700 <7,700

<7,700 7,700 7,700 7,700 7,700 7,700 7,700 7,700 N/A......--t---<I--~N/A B,OOO B,OOO

~,P'5IA 14.7 J)<""~""x"'" x.... x x

x x ""X 14.7

~FlDlI~!:1I~sr-~~II-t=t1=5,~400:L1~5,4~00:t-7~,7~00~=-t==t:=t~:t=::j;;:::::t:::::t=1=::t=i=:::t=t::::I~7,700 PAE'$:-PSIA IX!XC><l><'"

'X x

x x

'XIX" 'X' 14.7 J

L REV.

PER REA HT-96660.

SEEMICROFlLMFORPREVIOUSREV.SIGNATURES.

(VENDOR REV. 11 BY SCS)

2 to A

FGF':'2.!BXI3IBAGZ" E!iHOZO

~'rRENCEOOC~

~

1.

RCICSYSrE'-IP.!olu---------_E51-1010 2.

NUC.LEAR BOILEP PP~'CE%

'tAGF,AI~ -

821-1020 1.

ATI-10SPHERICPRlSSUREOF14.7PSIAWASUSEDINCALClJLATir;NS.

2.

\\oIATERfLOWSARES~INGPM.STEAMF'L~IN1000LBlHFl.

TH£ M4Xiroi.;;'; POOL MT~R TEMPf;FtArURE r~ GONiiNliOU5 5Y5iEM

~~T~~MII~~RA~r~X~~E~1~;F'T~~ts~l~?N~i~~TI AL PANSIO'lSHALLB£BASEDO'l170"F'.

4.

~~E~~V~~~~~O~m:~S~sr~ ~. OF' ". ~ PSI IS A

~.

~~~~\\gUTf~E@E~~R~~ OF 3.0 PSI IS A mED LOSS 6.

H£ CON TROlLI NG MODES FOR LINE SI ZING AND ARRANGEMENT ARE:

SUCTj<l'<

FROM CONO STORA.-oE:****** MOO£ A SUCTlctl FROM SUPPRESSION POOl****

MOO( C

?\\1MPOISCHARGE *********** /I4OOEC STEAM SUPPLY ************

MOO£ A 05 e

~~~I~~~~~U:T:

=~.c & 0 COOLING SYSTEM *********** I400E II.

7.

THERE ARE OH£R f>OTENTlAL oPERATING I'o4OOES WHICH 00 HOT CeJO'FlOL

~GOI,!,.t~V~~I~~

g~E~~r~~ e~r~~ ~r.~

~~I(~~'

~~~ i~E=Df1~~"'r>~rs~~Nit~~

~~~GE~~S~~f\\~R~~ES-

_il(),jPOCL.

B.

f'UMF 1~INII4.)M FU)II REQUIRO£Nr MAY OCCUR DURING ANY OPERATIN:;

'4CDE.

rLO~' RE:'QUiREto£NT is 50 GPM j.iiNii'ti,jr-i..

OURiNG t;:;DE A..

MINIMUM NPSH AT PUMP SUCTION = 20 FEET.

MAXIMUM PRESSURE RISE ACROSS PUMP = 2880 FEET FOR MODES A & C

=

525 FEET FOR MODES B & D MAXIMUM PRESSURE DROP BETWEEN LOCATIONS AND 9

= 15 PSI MAXIMUM PRESSURE ALLOWED = 25 PSIA 0

MAXIMUM PRESSURE ALLOWED = 75 PSIA SUFFICIENT VACUUM TO PREVENT TURBINE SHAFT-OUT-LEAKAGE, TO BE SPECIFIED ON TURBINE VENDOR DRAWING.

MAXIMUM PRESSURE AVAILABLE = 25 PSIA MAXIMUM PRESSURE AVAILABLE = 65 PSIA SUFFlCIENTPRESSURETO RETURN TO SUPPRESSION POOL.

SUFFlCIENT PRESSURE TO RETURN TO CONDo STORAGE.

r~~~~~e:RA.TUQ£~

GIvEN. ~ AlaE.. R:lR.. ttJl=Q'iCNlA.TIQfo..I

<:::NL~J,Ilo,NO ~T\\oE.~~FOQ.~OF~ ~e.o e..c::NIPMENT.

ltx:".*nONO \\-,

3'SA~'41 7-,

~-~P-I\\ ~12.1'Z-I~ \\~-14

\\~

\\'?'

1'0-2. 9*r:>>~-(o

~*20 lO-'

~~G~ \\'t5 1300 (\\)

\\1.5 liSa \\~ 1300 11.5 \\tS 7S

'75

\\2.5 1300 \\z.5 1300 12.5

~\\~~~ 100 110 (2.)

';0 S75.7 I"TO 170 \\10 teO lQO

\\QO \\70 170

\\70 100

~~ 40 4C (2.)

40

'10 10 40 40 40 40 40 40 40 40 4 0

(\\,)~ QQJi.-oeUQ&. ~ ae. ~u.

I'~OO PQ\\G~ DE:~T ON l=e.e.o-W"T&~ ~M *

......,,..-o~~ ~ I~~\\"=' Ci:::lNOI'TIO..... 1!.X.c,ee.oe.,~oo

~\\G.

Cl.)F'OR Q&"iM:;aN ~~\\U~"b aES=&.R. iO N~ eo\\\\..ESC. ~&"'"E.M

~C.iE"" O\\~~

  • N\\~- ~i.\\ -IOZO.
  • = THE PRESSURE AT THIS LOCATION DEPENDS UPON PIPING ARRANGMENTS, AND MAY BE VARIED WITHIN THE FOLLOWING UMITS.

LOCATION ill ill

@)

@)

RE~tTOR FEEOWl'TER D

c H

I'"

S25171 Southern ComPr~Rny Services, Inc.

PLANT:

HATCH UNIT:

2 filE:

R.C.I.C.

SYSTEM PROCESS DIAGRAM v~;~~RAL ELECTRIC IP'~~H2-2 S-25171 C

16

\\'J o

0 0

0 0

0 000 110501050

~

II.lTtRlA\\TTt.aT FLOWTl4PJJ DIlAIN'T1'}\\l' S't!I

£,

7 I e 9

10 II o

0 0 1- -

0 0

EGoUIPMEIoJT NOT OPERA.TING irATI i,Al\\(,

\\If}()

HEAD o

0

~TAND'8Y F'L.OW-SEE NOfE 'l.

0 LOC.ATlON 0 PR£tf.:lURE* PSIA MOOES L-.....------w POOl,.

It

'0 HATCH I I MPL UESI-I()~

THIS DWG.

PART OF YEN DOR MAN UAL N/A N/A REVISED PER REA HT-96660.

SEEMICROF1LMFORPREVIOUSREV.SIGNATURES.

(VENDOR REV. 3 BY SCS)

9L~C;l-S 10 CUEUl@mCTIIC lCoiE '2..106 HIGHcpRESSURrCOoLANT INJECTION 5YS FIRST MAOE FOR STANDARD PLAtJT

'2.:,,,,

,50BG4 A

MI'3CE:LlANEcOU'O INFORMATION:

I. DE-51 GtJ PRESSURE';:) AND TEMPERATURE5 GlvE"l BELOW ARE FOR INFORMATION ONl't', A~D ARE. Tf-\\E BASiS FOR DESIGN OF Af-i'cc:.

SUPPLIE.D EQUIPMEl\\lT, FCF; '2.3BXI30BG2.

E41-1010 N/A S-25176 D 2

HATCH PROCESS DIAG.

HPCI SYSTEM Southern ComPr~Rny Services, Inc.

G.E.

THIS DWG.

PART OF YEN DOR MAN UAL N/A i

rTTMMHl IREYtBY1

NOTES, 1.

ATI'()SPHERIC PRESSURE OF 14.7PSIA....AS USED INCALCULUIONS.

2.....ATERFLO\\ISARESHOWNINGPM,STEAMFLOIo'SIN1000LIl!MR.

3.

THE MA~IMUM POOL WI\\TER TEMPERATURE FOR CONTINUOUS SYSTEM OPERATION.,1 LL NOT E~CEED 140'r. HOIo/EVER, DUE TO POTENTIAL SHORT TERM OPERATION AT HI GHER TEMPERATURES, PIPING E~PAi'lSION SHALLSE SASED ON 170"F.

4.

THE FOLLOIo/INGADDITIONALACCIDENTOPERATINGMODESAREPOSSIBLE:

SUCTIONFROMCONJENSIITESTORAGE,SUPPRESSION POOLATLOWPRESSURE,REACTORATHIGHORLOIoi PRESSlJR£,

SUCTIONFROMSUPPRESSIONPOOL,SUPPRESSIONPOOL AT HIGH PRESSURE, REACTORU HIGH OR LOW PRESSURE.

THESE POTENTIAL OPERIITINGMOOESDONOT CONTROL PIPE OR VALVE SIZING ORSPECIFICATION,A/ol)NODATAISSHOwN.

REFERENC.E DOCUMEN"TS:

MPl. 11E.M NOS.

I.

HPCI SYSTEM peID---..... --~--------E4H010 2.

NUCLEAR BOILE.R PROCESS DII\\GRAM-------B21-I02.0 6.

THrCONTROLlII<<;MOOESFORLINESIZINGAM)ARRANGEMENTARE, SUCTIONFIlO>4CONJ. STORAGE---MODEA SUCTIONFROo4SUPPRESSIONPOOL--MlDEC PUIf'DISCHARGE---------MOOEC STEAM SUPPLY -

MOOE AlB TURBINE EXHAUST** -

MOOE A,e a. 0 TESTLINE------------MOOEE COOLING SYSTEM -

MOOE '"

7, THE PRESSURE AT LOCATION (j) IS ESTIMATED F'ROM PRELIMINARY PUMP DATA.

B.

F'lM'MIi'lIIlUM F'LCfW REQUIREMENT MAY OCCUR DURING ANY OPERATING MOOE.

F'LCfW REQUIREMENT IS ~MINIMVM,DVRIN('MODE A.

= 15 PSI

~ 11 I

'----..----J IN1E.RMliTEN"r FLOWTHRUDRAIN TRAP S'ISTeM

!1MB IAMB 56);'0 56;';0 AMB

!1MB

!1MB AMI:>

AMB IIM8 1Il'18 AMB AMB 11MB At'IB AMB 10 TEST MODE; sue TION FROM CONDENSI'\\TE 5TOR.

f, REACTOR "'T HIGH PRESS., SUPPRESSION POOl. AT l.OW PRESS.

II'>

19 20 21 ACCIDENT MODE, 5UCTION FROM 5UPPICE551ON

POOL, REA-CTOII AT l.OW PIIE55URE, SUPPRESSION POOL AT LOW PRESS LOCAilON 0

I 2

3 4

5 G 17 6

9 10 II 12 13 14 FlOW-SEE. NOiE. 2 0

0 0

0 f-0--+I_O-+---t-_--+-O-+-O-+_t--+----t------t------t-----jt--+----t------t----j PRE.SSURE

  • PSIp.,

W~]C W~]C 1--1 MINIMUM NPSH AT PUMP SUCTION = 21 FEET MAXIMUM PRESSURE RISE = 2880 FEET @ HIGH PRESS MODE

=

525 FEET @ LOW PRESS MODE MAXIMUM PRESSURE DROP BETWEEN LOCATIONS AND MAXIMUM PRESSURE = 65 PSIA SUFFICIENT PRESSURE TO RETURN TO SUPPRESSION POOL SUFFICIENT PRESSURE TO RETURN TO CONDo STORAGE MAXIMUM PRESSURE AVAILABLE = 65 PSIA SUFFICIENT PRESSURE TO RETURN TO PUMP SUCTION DURING OPERATION MODE:. S SySTEM STAND*BY, EQUIPMENT NOT OPERATING

= THE PRESSURE AT THIS LOCATION DEPENDS UPON PIPING ARRANGMENTS, AND MAY BE VARIED WITHIN THE FOLLOWING UMITS.

LOCATION (j)

(j)TO(D

@)

@&@)

RE At TOR CC~::;~N5ATE'

TSRAGE TANK (1) DESIGN PRESSURE SHALL BE EITHER 1300 PSIG OR DEPENDENT ON FEEDWATER SYSTEM SHUT-OFF HEAD IF THIS CONDITION EXCEEDS 1300 PSIG.

(2) FOR DESIGN TEMPERATURES REFER TO NUCLEAR BOILER SYSTEM PROCESS

DIAGRAM, MPL #B21-1020.

o c

B

v1 r

4A F

i0 (2)

H

0

~

~

e 11

--r;~

K j0 ll.P =3.0 PSI

~

I.

MIN FLO"" LINE

@x

~

II L

~

SY~TEM TEST LINE I'p °4.5 PSI M

~--

4

,if 8

REVISED PER REA HT-96660.

SEEMICROF1LMFORPREVIOUSREV,SIGNATURES.

(VENDOR REV. 4 BY SCS) 9L~C;l-S 10 CUEUl@mCTIIC lCoiE '2..106 HIGHcpRESSURrCOoLANT INJECTION 5YS FIRST MAOE FOR STANDARD PLAtJT

'2.:,,,,

,50BG4 A

MI'3CE:LlANEcOU'O INFORMATION:

I. DE-51 GtJ PRESSURE';:) AND TEMPERATURE5 GlvE"l BELOW ARE FOR INFORMATION ONl't', A~D ARE. Tf-\\E BASiS FOR DESIGN OF Af-i'cc:.

SUPPLIE.D EQUIPMEl\\lT, FCF; '2.3BXI30BG2.

E41-1010 N/A S-25176 D 2

HATCH PROCESS DIAG.

HPCI SYSTEM Southern ComPr~Rny Services, Inc.

G.E.

THIS DWG.

PART OF YEN DOR MAN UAL N/A i

rTTMMHl IREYtBY1

NOTES, 1.

ATI'()SPHERIC PRESSURE OF 14.7PSIA....AS USED INCALCULUIONS.

2.....ATERFLO\\ISARESHOWNINGPM,STEAMFLOIo'SIN1000LIl!MR.

3.

THE MA~IMUM POOL WI\\TER TEMPERATURE FOR CONTINUOUS SYSTEM OPERATION.,1 LL NOT E~CEED 140'r. HOIo/EVER, DUE TO POTENTIAL SHORT TERM OPERATION AT HI GHER TEMPERATURES, PIPING E~PAi'lSION SHALLSE SASED ON 170"F.

4.

THE FOLLOIo/INGADDITIONALACCIDENTOPERATINGMODESAREPOSSIBLE:

SUCTIONFROMCONJENSIITESTORAGE,SUPPRESSION POOLATLOWPRESSURE,REACTORATHIGHORLOIoi PRESSlJR£,

SUCTIONFROMSUPPRESSIONPOOL,SUPPRESSIONPOOL AT HIGH PRESSURE, REACTORU HIGH OR LOW PRESSURE.

THESE POTENTIAL OPERIITINGMOOESDONOT CONTROL PIPE OR VALVE SIZING ORSPECIFICATION,A/ol)NODATAISSHOwN.

REFERENC.E DOCUMEN"TS:

MPl. 11E.M NOS.

I.

HPCI SYSTEM peID---..... --~--------E4H010 2.

NUCLEAR BOILE.R PROCESS DII\\GRAM-------B21-I02.0 6.

THrCONTROLlII<<;MOOESFORLINESIZINGAM)ARRANGEMENTARE, SUCTIONFIlO>4CONJ. STORAGE---MODEA SUCTIONFROo4SUPPRESSIONPOOL--MlDEC PUIf'DISCHARGE---------MOOEC STEAM SUPPLY -

MOOE AlB TURBINE EXHAUST** -

MOOE A,e a. 0 TESTLINE------------MOOEE COOLING SYSTEM -

MOOE '"

7, THE PRESSURE AT LOCATION (j) IS ESTIMATED F'ROM PRELIMINARY PUMP DATA.

B.

F'lM'MIi'lIIlUM F'LCfW REQUIREMENT MAY OCCUR DURING ANY OPERATING MOOE.

F'LCfW REQUIREMENT IS ~MINIMVM,DVRIN('MODE A.

= 15 PSI

~ 11 I

'----..----J IN1E.RMliTEN"r FLOWTHRUDRAIN TRAP S'ISTeM

!1MB IAMB 56);'0 56;';0 AMB

!1MB

!1MB AMI:>

AMB IIM8 1Il'18 AMB AMB 11MB At'IB AMB 10 TEST MODE; sue TION FROM CONDENSI'\\TE 5TOR.

f, REACTOR "'T HIGH PRESS., SUPPRESSION POOl. AT l.OW PRESS.

II'>

19 20 21 ACCIDENT MODE, 5UCTION FROM 5UPPICE551ON

POOL, REA-CTOII AT l.OW PIIE55URE, SUPPRESSION POOL AT LOW PRESS LOCAilON 0

I 2

3 4

5 G 17 6

9 10 II 12 13 14 FlOW-SEE. NOiE. 2 0

0 0

0 f-0--+I_O-+---t-_--+-O-+-O-+_t--+----t------t------t-----jt--+----t------t----j PRE.SSURE

  • PSIp.,

W~]C W~]C 1--1 MINIMUM NPSH AT PUMP SUCTION = 21 FEET MAXIMUM PRESSURE RISE = 2880 FEET @ HIGH PRESS MODE

=

525 FEET @ LOW PRESS MODE MAXIMUM PRESSURE DROP BETWEEN LOCATIONS AND MAXIMUM PRESSURE = 65 PSIA SUFFICIENT PRESSURE TO RETURN TO SUPPRESSION POOL SUFFICIENT PRESSURE TO RETURN TO CONDo STORAGE MAXIMUM PRESSURE AVAILABLE = 65 PSIA SUFFICIENT PRESSURE TO RETURN TO PUMP SUCTION DURING OPERATION MODE:. S SySTEM STAND*BY, EQUIPMENT NOT OPERATING

= THE PRESSURE AT THIS LOCATION DEPENDS UPON PIPING ARRANGMENTS, AND MAY BE VARIED WITHIN THE FOLLOWING UMITS.

LOCATION (j)

(j)TO(D

@)

@&@)

RE At TOR CC~::;~N5ATE'

TSRAGE TANK (1) DESIGN PRESSURE SHALL BE EITHER 1300 PSIG OR DEPENDENT ON FEEDWATER SYSTEM SHUT-OFF HEAD IF THIS CONDITION EXCEEDS 1300 PSIG.

(2) FOR DESIGN TEMPERATURES REFER TO NUCLEAR BOILER SYSTEM PROCESS

DIAGRAM, MPL #B21-1020.

o c

B

v1 r

4A F

i0 (2)

H

0

~

~

e 11

--r;~

K j0 ll.P =3.0 PSI

~

I.

MIN FLO"" LINE

@x

~

II L

~

SY~TEM TEST LINE I'p °4.5 PSI M

~--

4

,if 8

REVISED PER REA HT-96660.

SEEMICROF1LMFORPREVIOUSREV,SIGNATURES.

(VENDOR REV. 4 BY SCS)

9L ~gZ-S I

10 161 F338 CONDITION I

NORMAL SYSTEM TEST CONDITION II TEST USING CONDENSATE STORAGE TANK I REV. NO. Yo ~ X 4

TITlE PROCESS DIAGRAM I

CORE SPRAY SYSTEM CON'Y ON SHY.

F SHY. NO.1 NUCLEAR BOILER SYSTEM 236X350BA A

LOCATION 0 1

10 11 12 LOCATION 0 1

10 11 12 FCF:

238X129BA (E21-1020)

CONDITION IV CORE SPRAY INJECTING AT REACTOR PRESS CONDITION III PUMP OPERATING ON BYPASS PRESS-PSIA 19.3 6.

100 GPM IS INCLUDED IN THE FLOW RATE GIVEN FOR MODE IV TO ALLOW FOR LEAKAGE IN THE REACTOR INTERNALS.

7.

THE LP BETWEEN LOCATON <1l> AND @ WILL BE DETERMINED IN PRE-OPERATroN TEST.

THE LP WILL BE ADJUSTED TO MEET THE FLOW REQUIREMENTS OF CONDITION IV.

8.

THE AVAILABLE NPSH IN CONDITION V SHALL BE EQUAL TO OR GREATER THAN 25 FT.

NOTES:

1.

FINAL VALUES SHALL BE REPORTED "BY OTHERS" FOR ALL POINTS LISTED.

2.

THE BYPASS FLOW IS APPROXIMATE AND WILL BE SPECIFIED BY THE PUMP VENDOR.

3.

ONLY ONE CORE SPRAY LOOP IS

SHOWN, THE SECOND LOOP IS IDENTICAL.

4.

IN CONDITION II THE NET POSITIVE SUCTION HEAD (NPSH)

AVAILABLE AT THE PUMP INLET (LOCATION 2)

MUST BE 32 FEET.

5.

~~Af~~~~I~~ +~dNP~~~ ~~~E;(ig~JTI6~Ci\\0~U~~A~E(NPSH)

J EQUAL OR GREATEfi UiAN 15 FTJADEQUATE NPSH MUST BE DEMONSTRATED FOR PUMP OPERATION WITH POOL TEMPERATURE AT 206T

~

o 0

11 12 11 12 175 175 4725 4725 10 10 175 475 175 132.3

._633 14-------e.- 18_

._900______

N/A 475 475 0

N/A 4725 r------+---+----+-------<-J 4725 0

175 175 175

6. P-FT.
6. P-FT.

SEE NOTE SEE NOTE PRESS-PSIA LOCATION 0 1

FLOW GPM LOCATION 0 1

FLOW GPM TEMP-OF 175 TEMP-'F 6200 6200 6200 14.7

~

ONDENSATE STORAGE TANK

~

IO,01 F005 A FOO4 A lJ-........

A

.... -"\\

to A~~.4. A<r;-001A '\\

r\\...

~ F006A Z,

ICEJ REACTOR PRESSURE VESSEL f-F_L_0_W_GP_M_-+-_N_/_A+--4_72_5:_'-_-_-_++--_-_----_--1-+-4_7_25-+-_0--+_0--+_4_7_2_5t--_O--+_---t__+--_0-----i FLOW GP M N/A 6200 r------+---+----+-------<-J 6200 0

PRESS-PSIA 14.7 N/A N/A N/A N/A PRESS-PSIA 14.7 f-T_E_M_P_-_'F__t--A_M_B:~~~:~~~~;-~~~-+-A_M_B-+-N_/_A--+_N/_A--+_A_M_B-+-_N_/_A+--N_/_A-+-_--+-_N_/-----iA f-T_E_M_P_-_'F__t--N_/_A+--9_5---t__+--_-+--_-+-_--+_95---t_N/_A-+-_N_/_A-+-_9_5-+-_9_5--+-_9_5-----i SEE NOTE SEE NOTE 4

6. P-FT.

._633 8 -------e

6. P-FT.

._590 14-------e.- 341 ______

c CONDITION V

CORE SPRAY INJECTING AT ZERO (0)

REACTOR

PRESS, DIFF, LOCATION 0 1

10 11 12 PUMP C001A TEMP-'F 200 200 200 200 I_S6._E_~-_NFT_O_~E_

___J CONDITION VI

ACCIDENT, SYSTEM INJECTION AT RUNOUT VALVE POSITIONS HATCH 2

UNIT:

Southern ComPF~Rny Services, Inc.

@)-----,--------,

[AutoCAD I S25178 I

12 11 175 175 o

4725 4725 o

5900 5900 10 175 14.7 14.7 VALVE NO I

~~j.

I 175 I-.--+-----+---+----+-~

N/A 59001---+--+---+-------<-1 5900 0

N/A 4725 I--.---+----+---+-------<-i 4725 0

FLOW GPM FLOW GPM PRESS-PSIA 14.7 PRESS-PSIA 14.7 LOCATION 0 1

TEMP-'F MAX PRFSS I DROP-FT I

SUPPRES7 SION CHAMBER

~o

~O 00 A,

F015 A

-~

1 rr81

~.'--+---,

\\

....,...----;1~::..=:~----tI

\\

.at :u

)~m\\

~ j1I

~(j§)A 9 F~~l A

~'eYA


41~

...If FOO~A

~

~

L

~A 1._ T

'------(>Ic:........l----------*I-F*O....~*l.-A-..1.----f CORE SPRAY LOOP A

(SFI: NOT'E

~)

TO LOOP "B"......---

CONDITIONS F001 I

0 II C

III 0

F002 F005 FO 15 F031 C

C P

C o

0 C

C C

C C

0 CORE SPRAY SYSTEM PROCESS FLOW DIAGRAM IV 0

C 0

C C

V 0

C P

C C

VI 0

C 0

C C

O-FULL OPEi~

C-FULL CLOSED P-PARTIALLY OPEN GE S-25178 J

5-25178 THIS DWG.

PART OF VENDOR MANUAL N/A 10 11 12 TAB/SECT.


'--',Nt-:-/A--'------

PAGE N/A 11oN~ol~.3F38SHY.NO.l II FIGURE _------'-N-'-t-I--'--A-'------

REVISION I DATE I DATE I DATE I DATE I DATE I DATE I DATE REVISION J

I DATE 6-3-99 REV.

PER REA HT-96660.

SEE MICROFILM FOR PREVIOUS REV.

SIGNATURES.

(VENDOR REV. 8 BY SCS)

BY CHK'D I APPR.1 APPR.2 I APPR.3 I APPRA I APPR.5 BY I CHK'D I APPR.1 I APPR.2 APPR.3 I APPRA I APPR.5 BY I CHK'D I APPR.1 I APPR.2 I APPR.3 I APPR.4 APPR.5 BY I CHK'D I APPR.1 I APPR.2 I APPR.3 I APPRA I APPR.5 BY I CHK'D I APPR.1 I APPR.2 APPR.3 APPRA I APPR.5 BY I CHK'D I APPR.1 I APPR.2 I APPR.3 I APPRA I APPR.5 BY I CHK'D I APPR.1 I APPR.2 I APPR.3 I APPRA I APPR.5 BY I CHK'D I APPR.1 I APPR.2 I APPR.3 I APPR.4 I APPR.5 I

IXIXIX I

I I

XIXIX I

I I

IXIXX I

I I

IXIXIX I

I I

XXIX I

I IIXIXIX I

I I

IXIXIX KB I JWD IHNB IXIXIXIX

£9Z£Z-5 GENERAL ELECTRIC 76/£710 PROCESS O/AGRAM ft/tFJ~~~fJ<=:U;S~Y:~a:350B4

.!!W§;

I.

Till' IS TWE MA.XIMUM I\\1!lCt~

OUTl.ET 'TEMPEFV.TURE *

    • Til" IS THE MAXIMJM FLOW R....1t. PO%IBLE FOP. THl':> MODE WITII llIES;; \\oIEI\\T *EXC.I-lANG.£RS.
      • l~~~s~~~UJR~p. +~,~ J.tllAA~~~~l)~~buffi\\=~1Fl,E~~~EO OUP.I~G. THE LIFE OF THE PlJ,NT TO THE NUMBER OF C'1'CI.ES PERMITnO BY PAR~. * +IS.1 OF SECT10~,,, OF TWE ASME CODE (100 MAY-IM-UM) 2.

PO'ilITIOl.lS 31

  • 32.

I~DICATE CLE....lo,\\UP CONOITIOlo,\\S

~ITH VARIOUS R1!lCC.W It-lLET TEMPER1>,TURE':>.

~.

THE M'~IMUM REQUlf\\ED NPSH OF THE CLEAIIIUP RECIRClJL1>.TIO~

PUMP~

IS 10 FT.

4.

t~:~F~~~~~~r;.~!~~l~l~~~X~~i~~t~'~~)e;;~

A\\<lO w4-" INCI.UOE eH~t.lG.E':l It.! "'TATIC HEAl) DUE TO THE':JE M5UREO ELEVATIONti.

5.

§?~~~~~i. ';.RiCOAT Ff\\EOUEMCY SEE IW)W~TE

.......I1ITEM PROCESS

~

~. ~~~~. 'ilHONN It.! MClOE <<AM R)S\\TIOIl1 "l~\\1 1':0 'THE MJt.lIMUM REQLlIREO ~

7.

~~ T~~~~SS.FILTEP./OEMI~. &.t14.~~\\ot ANt> PRtCOAT SEQUEMCE

~

8.

PIP>>Jca OESIG,M mss. ~

TEMPE~TURE &Ivttol

&'W)1,ij 0

1<:'

FOR I~FOP.MAlION Ollll'(.

9.

FOR A8t.IORMAL. (LOW OCCU""'~E) FL.~

SEE REF." ~ 7.

REFERE~lCE DOC\\.lME\\.!TS:

MPL ITEM ND.

1.AEACTlJ'...Ti"C\\,.£ANUP....ID**_***_~

2..

IIt\\ItU PEStGlil Sl'£C, - * - **** - - - -.

&:>>1-4010 3.

RoV~ST' $YSTP '.0. "'; -. -. -- - ** (111*1020 PIPING & IN~TIUEJfT ~~ -

A4HO'O 5

FILlER/DEM'"

SYSTEM - - - - - - - - - * -

G.51-Z001

-.:']

6.

COWTlU. AOO ORr"" ~ss OIAli.-*****-* Cl'-102.0 7.

C~TROI. I'Xl DR DESIGN SPEc..--******* C.1'-40'0 I

J ITO UMI1'B" I

I

<;;,/-zoo/

REf'S (SeE NOTE 7)

'------l------- - -

~

____U!T_"-o-o-~---..~-r-----..-~.-=-

~_R~---


4

.1'-.,."'5 FE P-T~5 CAr~--'"--------l I:

~.,.J." ~

i

~*I

'Z t?~IhtAity

,..." **"'.'I.I"......" ***,..........t**,.~...M..;'()N'~1' i

~I C,*~~SE""---t""--------"""'---"'"

"-7#/ '

TO RI:.ACTOR :..

FEEDWATER Re.TURN

...._~

001..-_

RPV. INVERT ELEV.O~On)(REF.)

SEE

~OTE 4-I,

3~-...I--------"'_~~~----"---+-1

~,_---.,...t'~~--.-~---.....-..........-.---+----

l

~

RtFUEL.I~&.

t~1,"';.,;'E""4-"",o*8

~W\\..EI.E'I.

~*O" SEEM~

MODE ".." c.:SlGN BASIS Fal. HEAT E¥:CHAN6ERS AN_ SIZI""," OF THE MAIW CI.EAW-UP PUMPS' 01SCrlAR,<iE PIPlllJG.

o---------t.e.i --------

~I.LOW~8LE PIPE FRICTION pp.op~

L:JI

.. ~t'4.. tDH

-1.4 _

.....f:__"'__

IC_TI__

ON---o....0R.;.;;.;oP_C;;;.;:ON.;.;..T=P.O=:L=Lf:=O_ llP OPEIATING P!pQ£lJIU I MAIN ~s IN oPtR~TION

i. NO RH. LOAD 3 NO N~Hx LOAD "FK.TEIl-~MINUl\\l.\\lERS IN Opt.....TION

') F CV IN oPE~ATION

  • fNTIllE FLOW 1!l'OlSCIU.~GfO TOt UoWAST& OIl. CONOENSER.

8Y MoDe.,,,-

ALLOWABLE PIPE FRW:TIOIIJ DROPS MOtlE"b" tuM'IMG ~EFUEI.ING WATD. ~

SIZING. OF 6"(PASS liNE FCV LEGUm:

RSe.

PlEAc:roV'o,

...,.E.AM SPACE

?

1-1" RECl.:..t-I'C,P.AiIVE HEAT EXCI-\\,A.,t.lG.ER NP.

Hl<.

NON REG.ENE?"'ilV'!

HEAT EX.C.HANG.'C.R MODE °a" -

STARTUP OPERATION

~I~'"

TOH

_'."\\ _.

fRICTION OA,OP CON1ROL\\.EO

~p OPERAT,NG PIIOC£DUAES I. MAIN CLEM-UP PUMPS IN OPERATION

2. RHx UNDER PARTIAL LOAD
3. NRHx UNDER M~. START UP \\.OA[j
4. FILTER-DEMINERALIZERS IN OPERATION
5. Fev IN OPERATION

'.CADf SWELL AIlE DISCHARGED TO RADWASTE OR CONDENSER 8'(

"ODE "...

1.l.0WABLE PIPE' FR.IC.TION DROPS

&Y MODE'*",,-

AI.LOWA BI.E I'IP I'RICTIOI\\I [)flOPS t.aleIf' CONTJMUOUS ClEAl\\1tNa ~ REACTOR WATER DOR.lt-lG.

REFI..El.I~

NOTE 9 S25285 THIS DWG.

PART OF VENDOR MANUAL N/A Southern ComPF~Rny Services, Inc.

PLANT:

HATCH UNIT:

2 illLE:

RWCU SYSTEM PROCESS DIAGRAM VENDOR:

I~~'~:2-0000002 G.E.

S-25285 J

HA rCH r I MPL

  1. G 3/-103-0..__

"lI.OW~6LE PIl'I; FRIc:.TIO~ DRape;.

-161... TDH

__'R,",-,I__

CT...;;IO..;;.lJ..;;.OII.=o.;...p...;;c.=.O~:.;.;TIl,=C\\Ll=-:I.:.=.:El>,,--

~'" ----::8;.;..'Y__M=O=:DE__-..:..:A_"

OJE~ATI"'9 PRpqPU&E,S:

I MAIN P\\JMP5 "" OPER.ATlON Z R,H lr.

U~DC" FUU, LOAD 3 iIlRHI UNDER P~"T \\,,1.

lOAD 4

FllTE~*oeMI",eRALIz.ER It.! OPERATION 5 Fev IN OPER.ATION 6 NO BYPASS FLOw MOGf"e* OPER"T ION I.IMI TATIONS

  • Of51G/l1 I!IA~/S FOR ByPASS ORII=IC.E

""ODee' ISLOWOOWIII oPERATiON R 5 5 ~ PSIA SEe NOTes. I( 2.

NOTf: 9 PeilTlON 0 I

2.

1 5

C 1

8 9

10 II 11z.11! II~ 11511~ 111 Iia 19 20 2.1 t2. 2.' Z4 ts t6 t1 2.8 to, 30 31 132. 33 I LOW 'PM U 94 949494 94.94 94 94 70 35 35

12. 701'-r- "10 10 10 351 361 Il TEMPERAT\\RE OF 5"15 5'4-5 54-5 54 5+5 54 S45 54 ~ 100 I

15 I

100 10 85 18Q I SO PRESS. PSIA 1021:

AF': 10 1028 FLOW GPM 9696.9696 96 969~ 9696 72 36 36

12. 72.fo-- 12 It 1t 3941403 12-TEMPERATURE "'F 54 545 545 545 545545 54-5 545 !4~ 105 105.

150 '0 !06- -

105 05 10 95 1180" Jso PRESS PSIA I

I I

I I

lo2B AP=IO

'02 FLOlN GPM 110 no TlO 110 110110110 110110 Be 41 41

12. etr---Ilt IRIIt. ~161-4-87 12-TEMPERAlURE"F 54 545545545 545 545545 545 54~ lie I/O 150110 I-- -

110 110 110.I0OI180" 1110 PRESS PS/A lOla 10131182 I

I I

I I

I I

~02Q i"'4C 1&1"=10 loZ.Q FLOW GPM 1'0 1M 10410410 104104104104 18 39 39

12. 78 foI-- 78 76 l' 11481,2-TEMPEAAlURE-F 545545 54-554-554554554554551, 111 III So III 1--- III III III 1051180" '50 PRESS PSIA lola AI' <10 102 MAXIMUM...,... ~5'".... 5-...",...

': oJ""Z'S().

.. &00..

~~~~SURE TOM PSI

~... _

'NH!Q!! P!Q!' CO!iT"'QIrW 61' OfE.RATING flBOCEaJBES:

1. MAIN PUMPS IN OPERAtiON (I) j l~~~;~t~~~~ IN OPERAT~N I
5. FeY IN OPERATION L-_6'_ENT_'RE_F_LO_W..'...

S _DlSCHA

__I¥j_EC_~_*:T~~~~E~f\\-:--__'"T""I_--=_,rl SCANNED. VERIFIED BY ~

REV.

PER REA HT-96660.

SEEMICROFlLM FOR PREVIOUS REV.

SIGNATURES.

(VENDOR REV. 7 BY SCS)

HATCH 2

PFD -

CRD HYDRAULIC SYSTEM Southern ComPF~Rny Services, Inc.

[Au~AD I S25311 I

I i

D[SICiM 01""'"..~

'.: 'T[t"P

_SS l-')

t....)

(-J)

I I!SO ISO M/,..

2 ISO 1'50 W-,..

~

280 1150

~"

51!i IISO 50 DESI6N PM.UN t TE"KRATUQ.

GI'IIEN.LOW IS FOR IMf'QIt""TIQII OMLV

~ IS TIotlt aMl$.. DC.~ OF BWR5D SUPPLIED fQUlPlCNT.

PRE.SSURE-Tl"PEM1'UM. l'-T).....X FC, F 236 X lifO 8A (,,2 (CoIl-IOZO) 2.

MAXIMUM ALLOWABLE PUMP SUCTION PRESSURE SHALL BE 50 PSIG.

3.

PIPING BETWEEN LOCATION 12 &

12A SHOULD BE DESIGNED TO SAME CONDITION AS FEED WATER PIPING (BY OTHERS).

NQJlli.

1.

FOR DATA PERTAINING TO NUMBERS WITHIN HEXAGONS REFER TO PROCESS DATA REF.

5.

0001 C~

~..

J Ie 7

lm4I11. MtU'S {------t...

....,',.,,'\\,..,..

~ONOE..NSATE. ~"""'-D<"""-~-".!J STORAGE.

poT-t

~QRTlNG QOCYME.NTS:

L PIPING

~

INSTRUMENT SYMBOLS RfftRQlCE. OQQKNTS:

MPL !TEM NO.

1.

CONTROL ROO DRIYE. HVORAULIC SYS PblO -

el1-1010 CONTROL ROO DRIY£. HVORAUlIC SYS rco Cl1-1030 3.

orSIGN SPECIfiCATION -

Cl1-401'O 4

  • HYDRAUlI C CONTROL UN IT -

c11-0001 5.

PPOa:SS DATA -

(11-1010 G.E.

S-25311 THIS DWG.

PART OF VENDOR MANUAL N/A TAB/SECT.

--2N..'-t-/...!...lA I;~GGUERE ---'-'-'~;-'-':'-----------

REVISED PER ABN 99-0035-002.

RCR

z~£~z-s I

..wOE A.

NORMAL OPERATION LOCATION lA 1

4 5

SA 6

10 14 15 16 NOlES:

1, DEFlNmON Of SYMBOLS

/

INDICATES CONDITIONS FOR 0FlOWRATE.

INDICATES THE SAME CONDITION AS USTED UNDER MODE A PR INDICATES REACTOR PRESSURE NEASURED IMNEDIATELY ABOVE THE CORE PLATE INDICATES REVISED VALUE 2, MAXIMUM OPERATING TEMPERATURES llIE MAXIMUM SYSTEM OPERATING TEMPERATURES WILL NOT EXCEED 15QoF FROM LOCATIONS 1THROUGH 30 WITH THE FOLLOWING EXCEPTIONS:

LOCATION MAX. TEMP jDFI 6.0 4.2*21MChlo3*31

[2J 4.0 33 I

4,0 4.0 1.3 20 21 22 23 43.9 31**

32 4.0 12.0 12.0 2.0 30 4.0 12.0 29 2.0 52.6 PR +60 PR +60 PR+50 PH +50 PR +20 PR +20 PR t20 1421.

MAX MAX MAX 28 52.6 PR

+260 21 PR

+260 58,6 26 25 24 8.1 8.7 B.7 23 22 68.6 68.6 10.0 58,6 1438.

1430.

1430.

1427.

21 20.0 1460.

20 88.6 1460.

19 17 18

PRES, 21, 19,

!psigl

FLOW, (gallminl FLOW.

88,6 88.6 19aUninl LOCATION CONDITIONS. 1) DRNES LATCHED.

2) PRESSURE OF REACTOR AT 1035 PSIG (STEAM DOME).
FLOW, I

I 40.6

.34

.34

.34

,34 0

f 0

0 46,6 40.6 40.6(

30 30 6

< 3) WAXIWUM COOLJNG FLOW TO DRIVES. MINIWUM REQUIRED PRESSURE AT POSITION 1A IS SHOWN.

~1.:..ga_Umll_*_'l--l--+--_-I-M_A_X4-M_A_X........_MA_X-+-_M_AX-+_-+--+_-+_--I_.-...,..-_t-~)+__-+__-+_____I

4) PRESSURE AT LOCATION 16 SHALL NOT EXCEED 1510 PSIG.
PRES,

/

I PR +60 PR +15 PR +14 PH +14 PR PH I

PR +20 0

PR +20 PR +60 PR +2~

1454 97 1458 L.......:1,t;;psig*:ii:.II---I..........-.Io_........._---a._-""_---L_---L_--.L.---I._M;...;."A;.;..X"""--_-'--M_AX--I..

M_AX(~~~::--~~A.~. )

MODE ASIZES THE COOLING WATER HEADERS,

~

41llblDiH3.31-'" J'",-,,--

MODE B, ROD INSERTION 1

LOCATION tA 1

2 3

4 5

SA 6

7 8

9 10 1

  • 1
  • 13 14 15 16 11 18 19 200 546 546 280 280 200 280 280 280 23 23 24 25 27 23 24 25 27 MOOED MODE A MOOEe PROCESS DATA CRD HYDRAUUC SYSTEM 2

HATCH Southern Company Services. Inc.

FOR UNIT:

PLANT:

TITLE:

@)---,-------.

[AutoCAD I S-25312 I 23 1.74 22 1.28 I

I

/

I 1.28 11 18 19 20 21 16

165, PR +91 PR +90 23

-3.6 PR

/

I 987.

I I

/

J 126.

126, 12 90 731 MIN PR 21 90 PH PH

+260

+250 1161 MIN 4.2 a,IOK.))1 5

5 5

I I

I PH 10~lJ1415 20 PH MODE BSIZES THE DRIVE WATER HEADERS.

CONDITIONS. 1) DRIVES INSERTING,

2) PRESSURE OF REACTOR AT 1035 PSIG (STEAN DOWE). 3) MAX DRIVING FLOW TO DRIVES.

Pfl CONDITIONS. 1) SCRANWING OF DRIVES COWPLETED.

2) PRESSURE OF REACTOR AT a PSIG (STEAW DOME). 3) MAXIWUM CRD SUPPLY PUMP FLOW.

NOTE - MINIMUM ACCUMULATION PRECHARGE PRESSURE IS 565 p~g.

CONDITIONS. 1) DRIVES SCRAWMING.

2) PRESSURE OF REACTOR AT 1035 PSIG (STEAW DOME). 3) FLOW BASE ON MAXIWUM ROD VELOCITY OF 85 IN/S.

MODE CSIZES THE INSERT ~NO WITHDRAW lINES.

PR

-~---V"-'W'-7 30 31**

32 33 29 26 21 28 200.

18.

180.

180.

10.

5 2

3 4

5 5A 6

4.2.211(0;03-31"""-- ~

1141.

1141.

1063.

lDl0.

1010.

981.

APPX I

I It 30 30 6

4055.

(

7.6 1454 97 1458 t

~

26 27 28 29 3 31**

32 33

~

25

~

25 26 27 28 29 30 31 *

  • 32 33

~

25 24 24 24

PRES, 65MAX 65MAX I

65MAX 97 1141 1010

PRES, 256 94 Ipsigl MAX FLOW.

29.6 29.6 19a1fninl

FLOW,

-0.46

-0,46' 0

/

I I

0 0

6 Igal/minl PRES.

lpsigl

PRES, 6,

-4.

(psigl PRES.

Ipsigl

FLOW, 200.

200.

19a1lmin)

FLOW, IgaUmin\\

LOCATION LOCATION LOCATION FLOW.

.7

.7

.7 46.6 43,9 43.9~

30 30 6

IgalJmi\\l

~

PRES, PR+20 PR+20 PR+20 PR +20"

.. )

1454 97 1458

~I~psi'gl1_~t.i_AX N_AX__l._N_A_X..a.-~M_A_X-a-_""""'_-¥--=------L._-----L----=-----l

~

MOIlEC.

SCRAM

  • .,.......,~'-""-'...I LOCAnON IA t

2 3

4 5

SA 6

1 B

9 10 1*

13 14 15 16 17 18 19 MODE O.

SCRAM COMPlETED LOCATION lA 1

A.

CONDiiiONS USiED FOR MODE CREPRESENi iH05E CONDiiiONS WHiCH EXiSi Ai 10 ffRCENi Of inE FULL*SiROKE iNSERiiON.

3.

MOOEA A.

LOCAnON t2 - THE REACTOR RETURN LINE PRESSURE SHALL NOT EXCEED PR +50 psig WITH THE CRD COOLING WATER FlOWRATE AT 0.20 gal,'min/drive. PRESSURE IN EX*

CESS OF PH +50 psig UNDER THE ABOVE CONDITIONS WILL ADVERSELY AFFECT eRD OPERATION.

8.

LOCAnON 16 - THE MAXIMUM ACCUMULATOR CHARGING PRESSURE SHALL NOT ExceED 1510 psig, ACCUMULATOR PRESSURE IN EXCESS OF 1510 psig WILL CAUSE CRD DAMAGE DURING ASCRAM.

C.

LOCATION 20 - THE eRD COOLING WATER PRESSURE SHALL NOT BE LESS THAN PR +15 psig FOR THE CONDITIONS INDICATED.

D.

LOCATION 23 - MAXIMUM DRIVE COOLING REQUIREMENTS WilL NOT EXCEED 0.34 gal/min/drive FOR THE CONDITIONS LISTED. MINIMUM DRIVE COOLING REQUIREMENTS WILL NOT BE LESS THAN 0.20 gal/min/drive.

4.

MODE B A,

LOCAnONS t3AND 14 -INSERT VALVEF007*A CLOSES ON DRIVE INSERT SIGNAL. WITHDRAW VALVE FOO7*B CLOSES ON DRIVE WITHDRAW SIGNAL BUT DOES NOT STAY CLOSED DURING SmUNG.

B.

LOCATION 18 - THE eRD DRIVE WATER PRESSURE SHAll NOT 8E lESS THAN PR +250 psig FOR THE CONDITIONS INDICATED.

5.

MOOEC B,

THE S46°F TEMPERATUREUSTEO IN NOTE 2FOR MODE C, POSITION 23 AND 24. SHALL BE USED ONLY IN DETERMINING THE MINIMUM PlPEWALL THICKNESS IN VICINITY OF THE DRIVE HOUSING AND NOT IN DETERMINING STRESSES DUE TO THERMAL EXPANSION. IN OETERMINtNG MINIMUM WALL THICKNESS, IT MAY BE ASSUMED THAT THIS TEMPERATURE OCCURS lESS THAN 1PERCENT OF THE OPERATING UFE OF THE SYSTEM. SEE THE CRD HYDRAULIC SYSTEM DESIGN SPECIFICAnON TO DETERMINE CYCUC STRESSES DUE TO THERMAL EXPANSION.

C.

lOCATIONS 21 TO 22 - THE PRESSURE DROP FROM LOCATION 21 TO 22 SHALL NOT EXCEEO 436 psi AT 90 gal/min FOR ANY CRD.

D.

LOCATION 23 - ANEGATIVE FLOWRATE INDICATES FLOW FROM THE REACTORTHROUG~ THE DRIVE SEAL INTO THE CRD. THE MAXIMUM LEAK RATE FROM THE REACTOR CAN REACH 10 gM/minldrive, E.

LOCATIONS 24 TO 25 - THE PRESSURE DROP FROM LOCATION 24 TO 25 SHALL NOT EXCEEO 162 psi AT 29.6 gaVmin FOR ANY CRO.

F.

RESPONSE TIME OF FCV*FOO2IS SUCH THAT SCRAM IS COMPLETED BEFORE FCV*FOO2 STARTS TO CLOSE.

G.

SCRAM VENT VALVE FOlD AND DRAIN VALVE F011 CLOSE WITH ASCRAM SIGNAl.

6, MODE 0 A.

LOCATIONS 24 AND 2S - ANEGATIVE FLOWRATE HERE INDICATES ATRANSIENT CONDITION IN WHICH flOW FROM THE WITHDRAW LINE PASSES THROUGH THE CRD AND INTO THE REACTOR; DURING SCRAM THE DRIVE ACTS AS APUMP TO CHARGE THE SCRAM DISCHARGE VOLUME TO APRESSURE A80VE THAT OF THE REACTOR. IM-MEDIATELY FOLLOWING SCRAM, THE WITHDRAW LINE WILL REJECT WATER TO THE VESSel UNTIL THE LOSS OF THIS WATER REDUCES THE WITHDRAW LINE PRESSURE TO APPROXIMATELY THAT OF THE REACTOR.

B, lOCAno~ 21-THE SCRAM DISCHARGE VOLUME SHALL 8E SIZED SO THAT THE RESULTING PRESSURE AFTER l00*PERCENT STROKE IS LESS THAN 65 psig.

7.

MAXIMUM ALLOWABLE PUMP SUCTION PRESSURE SHOULD BE 50 ps~.

8.

PROCESS DIAGRAM 105D~93 SHALLSE USED WITH ANO FORM PART OF THIS PROCESS DATA, IF THERE ARE ANY CONFLICTS BETWEEN THE PROCESS DIAGRAM AND THIS PROCESS DATA. THE PROCESS DATA SHAU GOVERN.

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'(

(H.P. ALARM SETPOINT = 1480 PSIG)

-~-~~-~-~

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PART OF VENDOR MANUAL N/A TAB/SECT. _N'-'-I/'-'-A"'--

PAGE N/A I FIGURE N/A REVISION 1

I DATE 12-18-01 REVISED PER ABN 99-0035-002.

SEE MICROALM FOR PREVIOUS REV. SIGNATURES.

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tHE DOORS NIl lOCK ARE DESIGNED FOR APRESSU.

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1 By:

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05/09/2003 Vogtle Site ONLY Review:

Date:

Approval:

Date:

DOCUMENT INSERTION SHEET E. I. Hatch Nuclear Plant - Unit No.2 RHR SERVICE WATER PUMP TEST CURVES-JOHNSTON PUMP MODEL 18 DC 7 STAGE -MPL # E11-C001A1B/C/D Description Remove Insert

1.

This insertion sheet (Nothing)

In front of manual

2.

Note page referencing S-56429 for RHRSW pump (Nothing)

Behind this Document performance curves as updated per 10 CFR 21 notification Insertion Sheet Revised by SNC to Incorporate For insertion into:

553448 ABN 02-0523 Revision 0 Updated to Revision:

1 By:

AJC Appv'd:

ASK Date:

05/09/2003 Vogtle Site ONLY Review:

Date:

Approval:

Date:

DOCUMENT INSERTION SHEET E. I. Hatch Nuclear Plant - Unit No.2 RHR SERVICE WATER PUMP TEST CURVES-JOHNSTON PUMP MODEL 18 DC 7 STAGE -MPL # E11-C001A1B/C/D Description Remove Insert

1.

This insertion sheet (Nothing)

In front of manual

2.

Note page referencing S-56429 for RHRSW pump (Nothing)

Behind this Document performance curves as updated per 10 CFR 21 notification Insertion Sheet

See S-56429 for RHRSWpump performance curves as updated per 10 CFR 21 notification.

SNC REV. I See S-56429 for RHRSWpump performance curves as updated per 10 CFR 21 notification.

SNC REV. I

JOHNSTON PUMP COMPANY Nuclear Service Division GEORGIA POWER COMPANY PLANT E. I. HATCH RHR SERVICE WATER PUMP TEST CURVES JOHNSTON PUMP MODEL 18 DC - 7 STAGE SERIAL NUMBERS DATE SNRU-6504 12/12/84 SNRU-6505 03/29/85 SNRU-6519 06/28/85 SNRU-6520 10/31/85 NRW-6524 10108/86 NRW-6525 11/19/86 NRX-6531 02/13/87 NRX-6532 04/23/87 NRX-6533 06/24/87 NRX-6534 11/04/87 NC-6519 12/10/91 ND-6509 10/16/92 2601 East 34th Street 0 Chattanooga. Tennessee 37407 FAX 6151698-1447 Telephone: 6151629-1415 HOTLINE 1-800-227-2601 JOHNSTON PUMP COMPANY Nuclear Service Division GEORGIA POWER COMPANY PLANT E. I. HATCH RHR SERVICE WATER PUMP TEST CURVES JOHNSTON PUMP MODEL 18 DC - 7 STAGE SERIAL NUMBERS DATE SNRU-6504 12/12/84 SNRU-6505 03/29/85 SNRU-6519 06/28/85 SNRU-6520 10/31/85 NRW-6524 10108/86 NRW-6525 11/19/86 NRX-6531 02/13/87 NRX-6532 04/23/87 NRX-6533 06/24/87 NRX-6534 11/04/87 NC-6519 12/10/91 ND-6509 10/16/92 2601 East 34th Street 0 Chattanooga. Tennessee 37407 FAX 6151698-1447 Telephone: 6151629-1415 HOTLINE 1-800-227-2601

JOHNSTON PUMP COMPANY Nuclear Service Division January 10, 1994 Southern Nuclear Power Generating co.

P.O. Box 1295 Inverness Center Building 40 Binningharn, AL 35201 Attention: Tim Long

Reference:

NPSHa Requirements for RHR Service Water Pumps

Dear Tim:

Per your request Johnston Pump has reviewed the minimum submergence and NPSHa requirements of the Johnston Model 18DC pump used as your RHR Service Water Pump at Plant Hatch. Please review the following:

NPSHa -

29"mercury x 1.1349 x

12 12"

=

382.9 (worst case) (conversion to ft of water) (conversion to in.) (vapor pressure)

(in.water) 12

=

31.9 ft (conversion to ft)

(NPSHa)

Submergence required over the lip of the suction bell to prevent vortexing 4000 GPM = 35" 3500 GPM = 24"

+

NOTE: The eye of the impeller is 14" above the lip of the suction bell making the datum point for NPSHa 21" and 10" respectively.

At 4000 GPM - NPSHa is 31.9 feet (atmospheric pressure)

+

1. 75

= 32.7 feet of water (submergence)

The NPSHR for the 18DC Model Pump is 29 feet @ 4000 GPM and 30 feet @ 3500 GPM.

These figures were derived from Hydraulic Institute Standards for NPSH and actual test curves (see attached) of a Model18DC pump.

Please disregard any previous correspondence that may have contradicted these current figures.

.' -..... i:<

Enclosures -,

~

2601 East 34th Street 0 Chattanooga. TeMessec 37407 FAX 615/698-1447 Telephone: 6151629-1415 HOTLINE 1-800-227-2601

... ~

JOHNSTON PUMP COMPANY Nuclear Service Division January 10, 1994 Southern Nuclear Power Generating co.

P.O. Box 1295 Inverness Center Building 40 Binningharn, AL 35201 Attention: Tim Long

Reference:

NPSHa Requirements for RHR Service Water Pumps

Dear Tim:

Per your request Johnston Pump has reviewed the minimum submergence and NPSHa requirements of the Johnston Model 18DC pump used as your RHR Service Water Pump at Plant Hatch. Please review the following:

NPSHa -

29"mercury x 1.1349 x

12 12"

=

382.9 (worst case) (conversion to ft of water) (conversion to in.) (vapor pressure)

(in.water) 12

=

31.9 ft (conversion to ft)

(NPSHa)

Submergence required over the lip of the suction bell to prevent vortexing 4000 GPM = 35" 3500 GPM = 24"

+

NOTE: The eye of the impeller is 14" above the lip of the suction bell making the datum point for NPSHa 21" and 10" respectively.

At 4000 GPM - NPSHa is 31.9 feet (atmospheric pressure)

+

1. 75

= 32.7 feet of water (submergence)

The NPSHR for the 18DC Model Pump is 29 feet @ 4000 GPM and 30 feet @ 3500 GPM.

These figures were derived from Hydraulic Institute Standards for NPSH and actual test curves (see attached) of a Model18DC pump.

Please disregard any previous correspondence that may have contradicted these current figures.

.' -..... i:<

Enclosures -,

~

2601 East 34th Street 0 Chattanooga. TeMessec 37407 FAX 615/698-1447 Telephone: 6151629-1415 HOTLINE 1-800-227-2601

... ~

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B ow L PERFORMANCE

. POINT ONLY: IT IS BASED ON SHOP TESTS. WHEN HANDLING CLEAR, FRESH WATER AT 'A TEMPERATURE OF NOT OVER.5* f_ AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*157A LIQUID WAT E:'f2 SP,nA \\

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I THE CAPACITY. HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS, "'HEN HANDLING CLEAR. FRESH WATER AT A TE"'PERATURE OF NOT OVER IS' F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*117A CUSTOMER GEORGlA POWER. CO. IU"~I L~A BRit. ".AB ~I BOWlS S.S! Pl.ASnE LIQUID WA."'I EJ2. SP.GR. \\.00 DATE IO/~\\/lfjJy ". J. e. Johnston Pump Company Glendora. California 91740 ESTABLISHED 1M ""c-05(D~B SUBMERGENCE REQ'D OVER BELL TO PREVENT VORTEXES BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STDS. r 1 Ii 1'URS)NE BOWL PERFORMANCE -Z STAGE IBOc. PUMP _...... '...... 7...... 7.....,.O ___ R.P..... CURVE NOlC-OS6\\S I r ; \\. I - I-i

1' i

I THE CAPACITY. HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS, "'HEN HANDLING CLEAR. FRESH WATER AT A TE"'PERATURE OF NOT OVER IS' F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*117A CUSTOMER GEORGlA POWER. CO. IU"~I L~A BRit. ".AB ~I BOWlS S.S! Pl.ASnE LIQUID WA."'I EJ2. SP.GR. \\.00 DATE IO/~\\/lfjJy ". J. e. Johnston Pump Company Glendora. California 91740 ESTABLISHED 1M ""c-05(D~B SUBMERGENCE REQ'D OVER BELL TO PREVENT VORTEXES BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STDS. r 1 Ii 1'URS)NE BOWL PERFORMANCE -Z STAGE IBOc. PUMP _...... '...... 7...... 7.....,.O ___ R.P..... CURVE NOlC-OS6\\S I r ;

JOHN~ _ UMP COMPANY Glendora, Calif. LABORATORY* TEST DATA SHEET -(G-~Ol CURVE NO~C* OSC01B JOB NAMEM'I;(t).,,f /1 W~.e JOB NO.SA.H~ ~\\ -4* ~~. ~ CJ<< MOTOR.IS-O _L ~ .t.f.Q.....!:.lIte IMPELLERS HP Ph... Cycle Voir APM ~V,?-, ~. y" I~...2- ~.. 13 tfl II =-.&.!!F RATED CONDITION @n.:7 Q Type S'-O-M.'.riel oi *. _Ah PI II GPM~",-(JO:..O=-___. ____ _ RPM CLASS c::! FINISH _-===-VANE Hud 9~..r BOWLS J~.s. fLA,sITC SUCTION CASE,£J£ L L_ BHP M.,.,lel Coelint Typ. Sp.Gr. I,()O -___ MOTOA SERIAL NO. __ -______ _ _q1I:-~;t=--- WA TIMETER.5": 1 A.rlo Tr.n,former ~ DYNAMOMETER Impellers Rai5ed "Ale J"ruAfj HeadEL!.f_"1t/. Efl. t(Y8: ~'p.vL~. ______ ' [I F.L. Antpl __ : Voluge __ ~. I Sui. Arm + ~A'Uf~'O L. GPM =~8/"oY * -r;:-='p ORIFICE DIA. 7;oal..... E 0 EON 'ST KE I" I I 10' h H d * ' ~=I=/'='=' ;====-=-:r==V .. QjUJ=GA=rU=G=E==;===:::;=:==;===*=,;;H.A_.R_A~1 ~ltr=A=lN=De=or='r' A=le=, r"=C=I=,ure=e=" =t;:PI:;";:n~'mlln&;I. __.2_~ ___ -__ ')I.. !lI I ~.,'l' 8' i IER I LINE l_~~~iL::.... --l FEET vl WATTMETER I~ J770 RPM fjif'] U.S. 3'f. FEET W~;ER F~~

.::~

READING INPUT "::~R *. H.* I RPM I!t---.....;--T-=~;~~.. --- B.H~. 1 ~i G.P.M. TO LIz....:.: IN H.P EFF. u.s. HEA; I I

r

~1~=~=P~='t=S =t=====I==:*=""~!I=:=~=::0=t:=GA=UG=E:i=P=IP=f.=. F:F==E=E=T=i:=~~:::':':. =9=/):::_=()=*=....

==* ~-==~=F_===_4===t===IF==G=.P::.:*~:.:_=t=F=~=T= t~

5. G'~. nn i D

o 11)fJ./ 'l.. 0.70 jf1, G 3'::Ii).> \\

13',)

~) V, Y 2 ~/,.~ J il.7Q /()()O J$3 It.30). t I Y (,.10 ) I/).'~o ... /1,.90 (. ~Y,lD ~OOD '3000 MOTOR MEGOHMS ___ SUBMERGENCE ABOVE LIP OF SUCTION BELL _It. _ In. BAROMETER

  • HG WATER TEMP.

eF AIR TEMP. eF

  • ....,r.-::~:::II>>'-----

2..19,("

  • 1

'1 Vv.9 71 iA. 19('.1 J .~ FLOOR TO WATER FLOOR TO GAUGE 311

..Iu.~ *

/aD i:b. r

  • 7.;t I n.", J

?(m D D 101/..J a999 JJ'/;", Q ) /lll 1/. J ~/J8 (.)9,;'" '/77..,3 //Ti? 7 t: ~ ~I I ~ '1 J ~ f, ~ r:, I t I fi I JOHN~ _ UMP COMPANY Glendora, Calif. LABORATORY* TEST DATA SHEET -(G-~Ol CURVE NO~C* OSC01B JOB NAMEM'I;(t).,,f /1 W~.e JOB NO.SA.H~ ~\\ -4* ~~. ~ CJ<< MOTOR.IS-O _L ~ .t.f.Q.....!:.lIte IMPELLERS HP Ph... Cycle Voir APM ~V,?-, ~. y" I~...2- ~.. 13 tfl II =-.&.!!F RATED CONDITION @n.:7 Q Type S'-O-M.'.riel oi *. _Ah PI II GPM~",-(JO:..O=-___. ____ _ RPM CLASS c::! FINISH _-===-VANE Hud 9~..r BOWLS J~.s. fLA,sITC SUCTION CASE,£J£ L L_ BHP M.,.,lel Coelint Typ. Sp.Gr. I,()O -___ MOTOA SERIAL NO. __ -______ _ _q1I:-~;t=--- WA TIMETER.5": 1 A.rlo Tr.n,former ~ DYNAMOMETER Impellers Rai5ed "Ale J"ruAfj HeadEL!.f_"1t/. Efl. t(Y8: ~'p.vL~. ______ ' [I F.L. Antpl __ : Voluge __ ~. I Sui. Arm + ~A'Uf~'O L. GPM =~8/"oY * -r;:-='p ORIFICE DIA. 7;oal..... E 0 EON 'ST KE I" I I 10' h H d * ' ~=I=/'='=' ;====-=-:r==V .. QjUJ=GA=rU=G=E==;===:::;=:==;===*=,;;H.A_.R_A~1 ~ltr=A=lN=De=or='r' A=le=, r"=C=I=,ure=e=" =t;:PI:;";:n~'mlln&;I. __.2_~ ___ -__ ')I.. !lI I ~.,'l' 8' i IER I LINE l_~~~iL::.... --l FEET vl WATTMETER I~ J770 RPM fjif'] U.S. 3'f. FEET W~;ER F~~

.::~

READING INPUT "::~R *. H.* I RPM I!t---.....;--T-=~;~~.. --- B.H~. 1 ~i G.P.M. TO LIz....:.: IN H.P EFF. u.s. HEA; I I

r

~1~=~=P~='t=S =t=====I==:*=""~!I=:=~=::0=t:=GA=UG=E:i=P=IP=f.=. F:F==E=E=T=i:=~~:::':':. =9=/):::_=()=*=....

==* ~-==~=F_===_4===t===IF==G=.P::.:*~:.:_=t=F=~=T= t~

5. G'~. nn i D

o 11)fJ./ 'l.. 0.70 jf1, G 3'::Ii).> \\

13',)

~) V, Y 2 ~/,.~ J il.7Q /()()O J$3 It.30). t I Y (,.10 ) I/).'~o ... /1,.90 (. ~Y,lD ~OOD '3000 MOTOR MEGOHMS ___ SUBMERGENCE ABOVE LIP OF SUCTION BELL _It. _ In. BAROMETER

  • HG WATER TEMP.

eF AIR TEMP. eF

  • ....,r.-::~:::II>>'-----

2..19,("

  • 1

'1 Vv.9 71 iA. 19('.1 J .~ FLOOR TO WATER FLOOR TO GAUGE 311

..Iu.~ *

/aD i:b. r

  • 7.;t I n.", J

?(m D D 101/..J a999 JJ'/;", Q ) /lll 1/. J ~/J8 (.)9,;'" '/77..,3 //Ti? 7 t: ~ ~I I ~ '1 J ~ f, ~ r:, I t I fi I

>-u Z 400 200 I I" 1&1 i U i I i S*-

  • J--

I ~ I I I I I - -. *. - I*

  • I I

I T I .- -- r'-'-- - - I I., THE

CAPACITY, HEAD AND EFFICIENCY GUARANTEE IS fOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR. FRESH WATER AT A TEMPERATURE OF NOT OVER 85' F. ANO UNDER SUCTION CONDITIONS AS SPECI-fiED IN THE CONTRACT. JP-157A CUSTOMER 6 EORGlA POWER CO* REF. NO. N R.W - G25 24 -05(057 SUBMERGENCE REQ'D OVER BELL TO PREVENT VORTEXES BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STDS. i I I . ~ + " I l I t., I I I I I i I I C III a: a: -1&1 ~..J 0..1 a: L HEAD -:- CAPAC,,.':( .. --.. ~... i

... --T ------~

i! ."i II L_.... Zu ... ~ o~ 10pO I

  • 90'10 2qoc>

I IMPELLER SR.'it. 01".:...::=<-&..11,.. BOWlS S.~, PLAC\\l'E. LIQUID WA1"EJ2. SP. GR.-I\\I..!,~Q",-_____ DATE\\O*S-say ~,J,B, I EFl= le\\ E.NC.,), e."RA~E HORSE.POWE.R, i 4000 Johnston Pump Company Glendora, California 91740 ESTABLISHED 1809 i .~Obo 7000 -rURB\\WE. BOWL 7 STAGE 'BOe. _-1'-'l7c...Z.&-.;:oO=--__ ,R.P.M. I . t;!( II. \\ZOO ffi ~ f III 1/1 '\\000 ~ i

z:

III lot( ~ 800-I I I I I PERFORMANCE PUMP CURVE No-XC.-OSlO87 i i I I I. I >-u Z 400 200 I I" 1&1 i U i I i S*-

  • J--

I ~ I I I I I - -. *. - I*

  • I I

I T I .- -- r'-'-- - - I I., THE

CAPACITY, HEAD AND EFFICIENCY GUARANTEE IS fOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR. FRESH WATER AT A TEMPERATURE OF NOT OVER 85' F. ANO UNDER SUCTION CONDITIONS AS SPECI-fiED IN THE CONTRACT. JP-157A CUSTOMER 6 EORGlA POWER CO* REF. NO. N R.W - G25 24 -05(057 SUBMERGENCE REQ'D OVER BELL TO PREVENT VORTEXES BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STDS. i I I . ~ + " I l I t., I I I I I i I I C III a: a: -1&1 ~..J 0..1 a: L HEAD -:- CAPAC,,.':( .. --.. ~... i

... --T ------~

i! ."i II L_.... Zu ... ~ o~ 10pO I

  • 90'10 2qoc>

I IMPELLER SR.'it. 01".:...::=<-&..11,.. BOWlS S.~, PLAC\\l'E. LIQUID WA1"EJ2. SP. GR.-I\\I..!,~Q",-_____ DATE\\O*S-say ~,J,B, I EFl= le\\ E.NC.,), e."RA~E HORSE.POWE.R, i 4000 Johnston Pump Company Glendora, California 91740 ESTABLISHED 1809 i .~Obo 7000 -rURB\\WE. BOWL 7 STAGE 'BOe. _-1'-'l7c...Z.&-.;:oO=--__ ,R.P.M. I . t;!( II. \\ZOO ffi ~ f III 1/1 '\\000 ~ i

z:

III lot( ~ 800-I I I I I PERFORMANCE PUMP CURVE No-XC.-OSlO87 i i I I I. I

JOHN~ *.. L1MF COMPANY Glendora. Calif LABORATORY TEST DATA SHEET CURVE NO. ______ JOB No.N,( au -{, 3.!L_----.:~ JOB NAMEMJ..<'I,!./A- /11U£".e '-D. (~U) _L~Il_£,--MOTOR.!S"O _=L- ~ .ffQ...:l:1.6LC IMPELLEflS HI' Ph... Cyel. VolI AP... 1.* I I, J. I~ 2-8~-:c. >f FIILL + -I/. r£r-RATED CONDITION @n?O Typ. 5'10. ....'.ri.' Oi *. _klt.1.. GPM_YLC()~()~O~ _______ -_--MOTOR SEHIAL NO. __ -______ _ WATTMETER So' I A.llo Tr.nl'orm.r ClASS_4_-_FINISH VANE Hlld 9s-r BOWLS....s,S. fL,fSI7"C SUCTION CASE ~£ L L_ BHP ...... rl.1 Coa"", Typ. Sp. Gr. /,()O ~ ~ DYNAMOMETER I Sui. GPM=608,,"oY

  • ...;KP ORIFICE DIA. 7.. 0;:t2--

Arm Elf.. f.l. AmpI ___ : VOllilg. __ Impellers Railed ()itJC _.fftRm Head~(~'1L/' +~A't!f~' OL. HEAD READINGS TAKEN Illelor *. AIle" Disella/lle Hnd I F==/~L==" =r====-;r===G=A=U=G=~L=_==r====;="=I=r====jj'W=8=)wS=-A=T=TZ=Mi=IE'=T=EI =Re=R:;=:==r===i==r=I===r====t=p,=r=lo=rrr=*,.:=1I0=';='.:..=,,;=t ~'-. -'~--A-p~~a~e ~,, ci'.] U.S. y.~~A~~'-::.-.-1 F~~T

11 TOTAL 11-------4 INPUT MOTOR I

,t------.---~~~.LT-- BHJ'. M \\ G P M P!.I FEU WATER FeR HEAD READING H.P EfF B.H.P RPM EFF. US HEAD ~ '~;i~ -...=! 'I~:D G:::Ol ~~ F~~T ~_ 1D-;- -., GP~ F~~T I "G*/. on I.. t========F====tl==== F--:=:-::=t:==i:-==t==-==i==f:!~,====t=== -=--== :.==t=====1I===~~==-- =- IlV.¥' ,900 '/7.7 ~90 D D l'IlL"e; ~~~'-~~~--~~~~- "L 0.70 5'09 10L', 1"5 L/. !. 102.<;.} . I J.z. '0 /tJ~ 0 y (,.10 ".1Y,lO 3000 lJl,O IJv~.(.,. }) '(

  • 0

-z. 7l d." /" ) /);:0 "l. YLt~ .1:..£".0 IrD. L MOTOR MEGOHMS ___ SUBMERGENCE ABOVE LIP OF SUCTION BELL _. U. _ In. BAROMETER -HG WATER TEMP. OF AIR TEMP. \\ OF ) { \\ 6.. { ( ,5 ) S(JI ,~¥I , Jv9 G 'lJcl) .*n 0 ~ Ii" .1Vr-FLOOR TO WATER _~ FLOOR TO GAUGE _~'---=-- ILL lao I l~ IJb'J:) ~ 7/. c) ,., lot, )7C.( 1..22Q. ~t(.. 1/01.1/ I i I t . 'i c ~ )y'!.; S'~7 7/,0 3D "L 1 /I.z '(.1 I ~ , I,

  • f

../ (}fJ,1t

  • ~?:I IS-V, VI'ii"?I" ct<), 'I

'/0'23. /Ob7.YI 11 -?---. I* T'II.d b~ Oil' 1£)_7 -ft ! / It' /)./

  • I

, 1 Wiln'lSId by .' ;/ /" ,~ L 'I~- ' I I' I( II

l' (

\\- P 1/.-. ~ l

  • ('.

.~. I,'* / :./ rmili.tf 1111 '1" 1( ., L_,-(.A.. l _ ~ (.", /.,!.,.- = R =2.DJ/ '1L:ll. R'=~.cYf5~T) JOHN~ *.. L1MF COMPANY Glendora. Calif LABORATORY TEST DATA SHEET CURVE NO. ______ JOB No.N,( au -{, 3.!L_----.:~ JOB NAMEMJ..<'I,!./A- /11U£".e '-D. (~U) _L~Il_£,--MOTOR.!S"O _=L- ~ .ffQ...:l:1.6LC IMPELLEflS HI' Ph... Cyel. VolI AP... 1.* I I, J. I~ 2-8~-:c. >f FIILL + -I/. r£r-RATED CONDITION @n?O Typ. 5'10. ....'.ri.' Oi *. _klt.1.. GPM_YLC()~()~O~ _______ -_--MOTOR SEHIAL NO. __ -______ _ WATTMETER So' I A.llo Tr.nl'orm.r ClASS_4_-_FINISH VANE Hlld 9s-r BOWLS....s,S. fL,fSI7"C SUCTION CASE ~£ L L_ BHP ...... rl.1 Coa"", Typ. Sp. Gr. /,()O ~ ~ DYNAMOMETER I Sui. GPM=608,,"oY

  • ...;KP ORIFICE DIA. 7.. 0;:t2--

Arm Elf.. f.l. AmpI ___ : VOllilg. __ Impellers Railed ()itJC _.fftRm Head~(~'1L/' +~A't!f~' OL. HEAD READINGS TAKEN Illelor *. AIle" Disella/lle Hnd I F==/~L==" =r====-;r===G=A=U=G=~L=_==r====;="=I=r====jj'W=8=)wS=-A=T=TZ=Mi=IE'=T=EI =Re=R:;=:==r===i==r=I===r====t=p,=r=lo=rrr=*,.:=1I0=';='.:..=,,;=t ~'-. -'~--A-p~~a~e ~,, ci'.] U.S. y.~~A~~'-::.-.-1 F~~T

11 TOTAL 11-------4 INPUT MOTOR I

,t------.---~~~.LT-- BHJ'. M \\ G P M P!.I FEU WATER FeR HEAD READING H.P EfF B.H.P RPM EFF. US HEAD ~ '~;i~ -...=! 'I~:D G:::Ol ~~ F~~T ~_ 1D-;- -., GP~ F~~T I "G*/. on I.. t========F====tl==== F--:=:-::=t:==i:-==t==-==i==f:!~,====t=== -=--== :.==t=====1I===~~==-- =- IlV.¥' ,900 '/7.7 ~90 D D l'IlL"e; ~~~'-~~~--~~~~- "L 0.70 5'09 10L', 1"5 L/. !. 102.<;.} . I J.z. '0 /tJ~ 0 y (,.10 ".1Y,lO 3000 lJl,O IJv~.(.,. }) '(

  • 0

-z. 7l d." /" ) /);:0 "l. YLt~ .1:..£".0 IrD. L MOTOR MEGOHMS ___ SUBMERGENCE ABOVE LIP OF SUCTION BELL _. U. _ In. BAROMETER -HG WATER TEMP. OF AIR TEMP. \\ OF ) { \\ 6.. { ( ,5 ) S(JI ,~¥I , Jv9 G 'lJcl) .*n 0 ~ Ii" .1Vr-FLOOR TO WATER _~ FLOOR TO GAUGE _~'---=-- ILL lao I l~ IJb'J:) ~ 7/. c) ,., lot, )7C.( 1..22Q. ~t(.. 1/01.1/ I i I t . 'i c ~ )y'!.; S'~7 7/,0 3D "L 1 /I.z '(.1 I ~ , I,

  • f

../ (}fJ,1t

  • ~?:I IS-V, VI'ii"?I" ct<), 'I

'/0'23. /Ob7.YI 11 -?---. I* T'II.d b~ Oil' 1£)_7 -ft ! / It' /)./

  • I

, 1 Wiln'lSId by .' ;/ /" ,~ L 'I~- ' I I' I( II

l' (

\\- P 1/.-. ~ l

  • ('.

.~. I,'* / :./ rmili.tf 1111 '1" 1( ., L_,-(.A.. l _ ~ (.", /.,!.,.- = R =2.DJ/ '1L:ll. R'=~.cYf5~T)

'LrJl r II) j ...... u.u... \\ CIRTlfllD IY: I 11. I\\. >'""'" CU.TOUl/! GEORGiA POWER CO. C It (u/b. ?- Q 11/"2...* J'VL J. 1-l- I-14.p~ 11~C~'~ pr- ~ ~p ~ '\\ Ir 1-I- THE

CAPACITY, HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

YIMEN HANDLING CLEAR. FRESH WATER AT A TEMPERATURE OF NOT OVER IS' F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. 1-- RII'. No.NR,w-CDS'2S ~~ 1+- 1- -~-I- +1H I*- 1-- 1--. -H-"HH-H-+-t-J-. 1-1-,1-+1 I-+- I-1-1-1 1-+++++ I-tr,h b,~.. 1_ ~ : Ii r\\ b J. "JiLllCl~ ~I~ "'N"'~I IMPELLER 8~i. DIA.\\'~ %-. r;.r-BOWLS S.S. PLA"'1'e. 1 J L10UID 'VIA1'f.= R SP.OR. '.0 Johnston Pump Company Glendora, California 91740 DATE \\\\~\\~'!"BY " .~.e, * ~- ESTABLISHED 1101 "Tc..- OS70\\ SUBMEROENCE REQ'D OVER BELL TO PREVENT VORTEXES BASED ON SUMP DESION PER HYDRAULIC INS~ITUTE.aTDS. f-1- TUR..B \\ N E BowLpERFORMANCE 7 STAOE \\8 DC PUMP \\770 R.P.M. . CURVENO"TOOS70\\ 'LrJl r II) j ...... u.u... \\ CIRTlfllD IY: I 11. I\\. >'""'" CU.TOUl/! GEORGiA POWER CO. C It (u/b. ?- Q 11/"2...* J'VL J. 1-l- I-14.p~ 11~C~'~ pr- ~ ~p ~ '\\ Ir 1-I- THE

CAPACITY, HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

YIMEN HANDLING CLEAR. FRESH WATER AT A TEMPERATURE OF NOT OVER IS' F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. 1-- RII'. No.NR,w-CDS'2S ~~ 1+- 1- -~-I- +1H I*- 1-- 1--. -H-"HH-H-+-t-J-. 1-1-,1-+1 I-+- I-1-1-1 1-+++++ I-tr,h b,~.. 1_ ~ : Ii r\\ b J. "JiLllCl~ ~I~ "'N"'~I IMPELLER 8~i. DIA.\\'~ %-. r;.r-BOWLS S.S. PLA"'1'e. 1 J L10UID 'VIA1'f.= R SP.OR. '.0 Johnston Pump Company Glendora, California 91740 DATE \\\\~\\~'!"BY " .~.e, * ~- ESTABLISHED 1101 "Tc..- OS70\\ SUBMEROENCE REQ'D OVER BELL TO PREVENT VORTEXES BASED ON SUMP DESION PER HYDRAULIC INS~ITUTE.aTDS. f-1- TUR..B \\ N E BowLpERFORMANCE 7 STAOE \\8 DC PUMP \\770 R.P.M. . CURVENO"TOOS70\\

JOHNSTON ~.., ~OMPANY Glendor., Canl, LABORATORY TEST DATA SHEET CURVE NO.\\C.~057C> I JOB NO M<w:"'!!i~ ~""~"11" JOB NAMEMI..(I,!.I,f /1 14JE".e io. RATED CONDITION 0.121Q RPM OPM yPOO ~~tD) I , 't,'" " *.t' LAt MOTOR1S"0 _:1_ k.L.rf!1l.. g*J'ItE'IMrEllERS Jtl}(j ,~~ *. **pJr"LL+ "J.~F _.;;:..u.--.- H' Ph... C,el. Volt fiPit' I ',pI ~ U... rl.1 011... " PI", Hlld 95"..r IH' ________________ __ Sp.Or, /,00 MOTOR SEfUAl NO. CLAIS_4-'INISH vANE -'-r#--"--WAT--'TM'ETER..5':, ....,. "0 [) : r BOWLS..$,5,. ,. fLA~/rr SUCTION CASE ~£ L L _ ..0..;"-:--- 7 UII".' COlli,.. --VYP. A.llo tranaformer Arm Impelleu R.lsed (JAJC I HtRM Head~t~1t/. +~,f't!M**t. HEAD READINU'S TAKEN 18110rl, AII.rt Dllch.,.e Hlld ttl. _______. ____ _ F.L. AmpI __ .: VoIlIg, __ _ , ~ ~ DYNAMOMETER Scal. GPM='D8, "oY

  • VAP ORIFICE DIA. '7... oa~ -

.== .=-=-"*:==:-==-==-" I/,.. GAUGE 8\\S.bSb,,"ZI eR.' ,,,'o,mlnt:I. __._L ___.. ___ 'I'!l1 'NE df.ES;JL. FEEl Vi rn.F_".Ct] U.S. a".-. Of 'It PSI FEU WATER Fon G.P.M. U flPIN ~ OF TO;c'E-INeUE! ~

  • 'IEAD GAUGE PIPF.

OF H<1==:I====I=== __ f=::== __ _ TOTAL WATTMETER ~O.. 'L It-__ 'J~_..,;..=_~.?'?Q ___ ** _RPM .INPUT MOTOA 0 W lOTAl D.H.P. HEAD READING H.P lFF I.H.P RPM EFf. U.s. HEAD fI F IENET G.P.M IN SP. 0,. ._ ~=Y=O~Dtt===~===. __==~'=='_=F~~~=====i,======~=FE=E=T~~~~~~L~~~n'jn~i t-..c.-D-t--_=--O_.L..I !~/_rJ'Jt.LLI':.Llk--t-==S"~,'l.L.-..t_-_-t~j~]:;L..:'" ~~Ii __ -.......:;,l.~'I..t..... 'l_-t-'l..:..o';;{~ 9".... 1.._ -f_...... c,~' lV~/~LI/'......

3'-t-........

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.90D IJf~.jtgCC? .... r.~ Y'9~ 'i('1.'I."l MOTOn MEGOHMS SUBMEnGENCE ABO-Y-E -U-P -- OF SUCTION BELL _It. _' _ In. BAROtAETER HG WMERlEMP. of AIIlTEMP.* of T.P.l. P. 2.9' FLOOR TO WATER Z-FLOOR TO GAUGE --'~Q __. ,r

  • ";;2' I~ '.3

,'100 'Y'I.3 ~i'~., 1).1 ~~ i',,'oo.o lj,/~" I I I!"~,? ,900 I/Jr.~Itf<iP 7l.,"\\.. '~tl '17>iY Jfj71.' i I 1220

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~t1 nt., ' ~ Vtu? ~.;" I JOHNSTON ~.., ~OMPANY Glendor., Canl, LABORATORY TEST DATA SHEET CURVE NO.\\C.~057C> I JOB NO M<w:"'!!i~ ~""~"11" JOB NAMEMI..(I,!.I,f /1 14JE".e io. RATED CONDITION 0.121Q RPM OPM yPOO ~~tD) I , 't,'" " *.t' LAt MOTOR1S"0 _:1_ k.L.rf!1l.. g*J'ItE'IMrEllERS Jtl}(j ,~~ *. **pJr"LL+ "J.~F _.;;:..u.--.- H' Ph... C,el. Volt fiPit' I ',pI ~ U... rl.1 011... " PI", Hlld 95"..r IH' ________________ __ Sp.Or, /,00 MOTOR SEfUAl NO. CLAIS_4-'INISH vANE -'-r#--"--WAT--'TM'ETER..5':, ....,. "0 [) : r BOWLS..$,5,. ,. fLA~/rr SUCTION CASE ~£ L L _ ..0..;"-:--- 7 UII".' COlli,.. --VYP. A.llo tranaformer Arm Impelleu R.lsed (JAJC I HtRM Head~t~1t/. +~,f't!M**t. HEAD READINU'S TAKEN 18110rl, AII.rt Dllch.,.e Hlld ttl. _______. ____ _ F.L. AmpI __ .: VoIlIg, __ _ , ~ ~ DYNAMOMETER Scal. GPM='D8, "oY

  • VAP ORIFICE DIA. '7... oa~ -

.== .=-=-"*:==:-==-==-" I/,.. GAUGE 8\\S.bSb,,"ZI eR.' ,,,'o,mlnt:I. __._L ___.. ___ 'I'!l1 'NE df.ES;JL. FEEl Vi rn.F_".Ct] U.S. a".-. Of 'It PSI FEU WATER Fon G.P.M. U flPIN ~ OF TO;c'E-INeUE! ~

  • 'IEAD GAUGE PIPF.

OF H<1==:I====I=== __ f=::== __ _ TOTAL WATTMETER ~O.. 'L It-__ 'J~_..,;..=_~.?'?Q ___ ** _RPM .INPUT MOTOA 0 W lOTAl D.H.P. HEAD READING H.P lFF I.H.P RPM EFf. U.s. HEAD fI F IENET G.P.M IN SP. 0,. ._ ~=Y=O~Dtt===~===. __==~'=='_=F~~~=====i,======~=FE=E=T~~~~~~L~~~n'jn~i t-..c.-D-t--_=--O_.L..I !~/_rJ'Jt.LLI':.Llk--t-==S"~,'l.L.-..t_-_-t~j~]:;L..:'" ~~Ii __ -.......:;,l.~'I..t..... 'l_-t-'l..:..o';;{~ 9".... 1.._ -f_...... c,~' lV~/~LI/'......

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.90D IJf~.jtgCC? .... r.~ Y'9~ 'i('1.'I."l MOTOn MEGOHMS SUBMEnGENCE ABO-Y-E -U-P -- OF SUCTION BELL _It. _' _ In. BAROtAETER HG WMERlEMP. of AIIlTEMP.* of T.P.l. P. 2.9' FLOOR TO WATER Z-FLOOR TO GAUGE --'~Q __. ,r

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,'100 'Y'I.3 ~i'~., 1).1 ~~ i',,'oo.o lj,/~" I I I!"~,? ,900 I/Jr.~Itf<iP 7l.,"\\.. '~tl '17>iY Jfj71.' i I 1220

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I r I i 1 1 6 THE

CAPACITY, HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR. FRESH WATER AT A TEMPERATURE OF NOT OVER 15' F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*'S7A !.j. i I ............ *-*... I-:- * * -** **,*~:-..,-. 1".-'-" . I:' I ' I ' j

  • j 1000 2.000 BOWLS S.s. pv..cne, LIOUID WA.i eg SP. OR \\.0 DATE'2-\\3--87 BY \\\\.J.e.

3000 I .... -:. ~-'-:-I-..... '-i _.. I I I L '.i.. . J i + I i i ~ I :. j I ~_. _.................. -1.

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STAGE IBDC PERFORMANCE PUMP ESTABLISHED 180t \\770 R.P.M. CURVE No-rC~OS72 \\ i L I f t ! i I II I C-OS72...\\* SUBMERGENCE REO'D OVER Bell TO PREVENT VORh~"S BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STDS. i I i\\MC I I (!),---~. . L ~RE::F.~N:O=. N:=R..='X==G=5~;!>:::\\========::J i i L. i I .. - * - * * --r-**-~

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CAPACITY, HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR. FRESH WATER AT A TEMPERATURE OF NOT OVER 15' F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*'S7A !.j. i I ............ *-*... I-:- * * -** **,*~:-..,-. 1".-'-" . I:' I ' I ' j

  • j 1000 2.000 BOWLS S.s. pv..cne, LIOUID WA.i eg SP. OR \\.0 DATE'2-\\3--87 BY \\\\.J.e.

3000 I .... -:. ~-'-:-I-..... '-i _.. I I I L '.i.. . J i + I i i ~ I :. j I ~_. _.................. -1.

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..., I'.. ~!. I I.. ~l I * ~ .. :.... " r'".. '800 111 1000 : i I Johnston Pump Company Glendora, 'California 91740

f\\.lS2B1N E: BQ\\Wk 7

STAGE IBDC PERFORMANCE PUMP ESTABLISHED 180t \\770 R.P.M. CURVE No-rC~OS72 \\ i L I f t ! i I II

JOHNSTON PllOIr lMPANY Glendd. LABORATORY TEST DATA SHEET CURVE NO. -rc.- 05]2. \\ JOB NO.Allb<-I,Sll. __ JOB NAME ~£oR..I;I" I'ow{/{. (!o, .L' IMPELLERS ItAa 2- /fL4>- 13 'IFIll' + -41'& ~RATED CONDITION @.JJ70 R~M Type Slag. "blerial Oia. *' ., p..... GPM_'I:...:O~p...;:;O,---______ _ -.. --MOTOR SERIAL NO.. __ -=::::::'== __ CLASS

4.

FINISH VANE Head 9~) BOWLS :51; srI-. hA$/~ SUCTION CASE.gEl'- BHP Material C.. a\\inv Tvpe Sp. Gr. /.D D WATTMETER S-! I Ratio . Transformer Impeller5 Raised _-=o:....:~::~C~_._Jj!!~1 HeadY.t1 IL NJI,/:-t '1if,a:~ <! ~L. ~ ~ DYNAMOMETER --:-:--:-_ Scale EfI. ____________ I F.L. Amps_.. _.. Vollage __ Arm GPM= kOS.bOY *....;KP ORIFICE DIA. 7,O;u." HEAD Af:ADINliS TAKEN ~fterl Discharge Head

====~======T=======~~==~==r-='=.=,.r=======~r===9====r==~==~===9F===========~======~ I GAUGE I LN '4;;116 he ~ PetlormBnte_._ ** L.. ___ Slage JI- .. p. LINE I!i. 1'iL. FEET vl WATTMETER I (.)I t.?,?Q. RPM I I OF FEB I WATER Of TO HEAD iGAUGE U. S. I PSI G.P.M. I....., 1-N,,,5. o o 29 FeR _II,.. PIPF. TOTAL HEAD IN FEET READING , L'l r f) ?h ~D9 I Vl/. D lIn.. £. J3 9.2..

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.k.. I 0 lO.¥O ,,,,,90 }OOO 1!"03 V

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t.i.JO 3boD MOTOR MEGOHMS SUBMERGENCE ABO-V-E-L-'P--

OF SUCTION BELL _ fl. _In. BAROMETER

  • HG WATER TEMP.

of AIR TEMP. of T.P.L _______ _ 111.) .1.'1S'

  • JO I FLOOR TO WATER _..1..'....,2,--_-

FLOOR TO GAUGE ---",.,./'~DIC.. __ - --t,.'-+1--- ~<<4 I INPUT H.P. MOTOR EfF B.H.p. RPM J 220 = R =/. ~9rr ca-r1 ~~"JL EFF. D TOTAL U.s. HEAD G.P.M. IN FEET S.H.P. Sn. Gr. II)"ff.1J /091.. i' Certified by ______________ PAM ... _ _.... of.... __ paqes I JOHNSTON PllOIr lMPANY Glendd. LABORATORY TEST DATA SHEET CURVE NO. -rc.- 05]2. \\ JOB NO.Allb<-I,Sll. __ JOB NAME ~£oR..I;I" I'ow{/{. (!o, .L' IMPELLERS ItAa 2- /fL4>- 13 'IFIll' + -41'& ~RATED CONDITION @.JJ70 R~M Type Slag. "blerial Oia. *' ., p..... GPM_'I:...:O~p...;:;O,---______ _ -.. --MOTOR SERIAL NO.. __ -=::::::'== __ CLASS

4.

FINISH VANE Head 9~) BOWLS :51; srI-. hA$/~ SUCTION CASE.gEl'- BHP Material C.. a\\inv Tvpe Sp. Gr. /.D D WATTMETER S-! I Ratio . Transformer Impeller5 Raised _-=o:....:~::~C~_._Jj!!~1 HeadY.t1 IL NJI,/:-t '1if,a:~ <! ~L. ~ ~ DYNAMOMETER --:-:--:-_ Scale EfI. ____________ I F.L. Amps_.. _.. Vollage __ Arm GPM= kOS.bOY *....;KP ORIFICE DIA. 7,O;u." HEAD Af:ADINliS TAKEN ~fterl Discharge Head

====~======T=======~~==~==r-='=.=,.r=======~r===9====r==~==~===9F===========~======~ I GAUGE I LN '4;;116 he ~ PetlormBnte_._ ** L.. ___ Slage JI- .. p. LINE I!i. 1'iL. FEET vl WATTMETER I (.)I t.?,?Q. RPM I I OF FEB I WATER Of TO HEAD iGAUGE U. S. I PSI G.P.M. I....., 1-N,,,5. o o 29 FeR _II,.. PIPF. TOTAL HEAD IN FEET READING , L'l r f) ?h ~D9 I Vl/. D lIn.. £. J3 9.2..

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t.i.JO 3boD MOTOR MEGOHMS SUBMERGENCE ABO-V-E-L-'P--

OF SUCTION BELL _ fl. _In. BAROMETER

  • HG WATER TEMP.

of AIR TEMP. of T.P.L _______ _ 111.) .1.'1S'

  • JO I FLOOR TO WATER _..1..'....,2,--_-

FLOOR TO GAUGE ---",.,./'~DIC.. __ - --t,.'-+1--- ~<<4 I INPUT H.P. MOTOR EfF B.H.p. RPM J 220 = R =/. ~9rr ca-r1 ~~"JL EFF. D TOTAL U.s. HEAD G.P.M. IN FEET S.H.P. Sn. Gr. II)"ff.1J /091.. i' Certified by ______________ PAM ... _ _.... of.... __ paqes I JOHNSTON PllOIr lMPANY Glendd. LABORATORY TEST DATA SHEET CURVE NO. -rc.- 05]2. \\ JOB NO.Allb<-I,Sll. __ JOB NAME ~£oR..I;I" I'ow{/{. (!o, .L' IMPELLERS ItAa 2- /fL4>- 13 'IFIll' + -41'& ~RATED CONDITION @.JJ70 R~M Type Slag. "blerial Oia. *' ., p..... GPM_'I:...:O~p...;:;O,---______ _ -.. --MOTOR SERIAL NO.. __ -=::::::'== __ CLASS

4.

FINISH VANE Head 9~) BOWLS :51; srI-. hA$/~ SUCTION CASE.gEl'- BHP Material C.. a\\inv Tvpe Sp. Gr. /.D D WATTMETER S-! I Ratio . Transformer Impeller5 Raised _-=o:....:~::~C~_._Jj!!~1 HeadY.t1 IL NJI,/:-t '1if,a:~ <! ~L. ~ ~ DYNAMOMETER --:-:--:-_ Scale EfI. ____________ I F.L. Amps_.. _.. Vollage __ Arm GPM= kOS.bOY *....;KP ORIFICE DIA. 7,O;u." HEAD Af:ADINliS TAKEN ~fterl Discharge Head

====~======T=======~~==~==r-='=.=,.r=======~r===9====r==~==~===9F===========~======~ I GAUGE I LN '4;;116 he ~ PetlormBnte_._ ** L.. ___ Slage JI- .. p. LINE I!i. 1'iL. FEET vl WATTMETER I (.)I t.?,?Q. RPM I I OF FEB I WATER Of TO HEAD iGAUGE U. S. I PSI G.P.M. I....., 1-N,,,5. o o 29 FeR _II,.. PIPF. TOTAL HEAD IN FEET READING , L'l r f) ?h ~D9 I Vl/. D lIn.. £. J3 9.2..

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t.i.JO 3boD MOTOR MEGOHMS SUBMERGENCE ABO-V-E-L-'P--

OF SUCTION BELL _ fl. _In. BAROMETER

  • HG WATER TEMP.

of AIR TEMP. of T.P.L _______ _ 111.) .1.'1S'

  • JO I FLOOR TO WATER _..1..'....,2,--_-

FLOOR TO GAUGE ---",.,./'~DIC.. __ - --t,.'-+1--- ~<<4 I INPUT H.P. MOTOR EfF B.H.p. RPM J 220 = R =/. ~9rr ca-r1 ~~"JL EFF. D TOTAL U.s. HEAD G.P.M. IN FEET S.H.P. Sn. Gr. II)"ff.1J /091.. i' Certified by ______________ PAM ... _ _.... of.... __ paqes I

SUBMERGENCE REQ'D OVER BELL TO PREVENT BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE.STDS. CERTIFIED BY: \\6.LL.ao":"'-~II!!!:!.-III!!!!!~L-. __ DATE 1\\.-11,;J In CUSTOMERGEORG\\~ PQWER CO* . f i REF. No.NR.;?<- <0632 ./

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CAPACITY, HEAD AND GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE OF NOT OVER 15" F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*167A BOWLS '5.f>, e M\\-re LIQUID =sU.. *,-U::'1C!. SP. GR. ).0 DATE4-t~P>7BY \\\\~.'B' I ! I ~ . t I I '4Q?D' j. '. ;. ~ I ., -i u.s. GALLONS PER MI Johnston Pump Company Glendora. California 91740 ESTABLISHEQ 18011 ,70q>O: i. _71.-_5TAGE.....;':....S=:;,..'DC.=..;:=-_____ PUMP _..Ll 7..!.....LZ;-:IoQ~ __ R.P."'. CURVE Note... 0 5750 i, I SUBMERGENCE REQ'D OVER BELL TO PREVENT BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE.STDS. CERTIFIED BY: \\6.LL.ao":"'-~II!!!:!.-III!!!!!~L-. __ DATE 1\\.-11,;J In CUSTOMERGEORG\\~ PQWER CO* . f i REF. No.NR.;?<- <0632 ./

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CAPACITY, HEAD AND GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE OF NOT OVER 15" F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*167A BOWLS '5.f>, e M\\-re LIQUID =sU.. *,-U::'1C!. SP. GR. ).0 DATE4-t~P>7BY \\\\~.'B' I ! I ~ . t I I '4Q?D' j. '. ;. ~ I ., -i u.s. GALLONS PER MI Johnston Pump Company Glendora. California 91740 ESTABLISHEQ 18011 ,70q>O: i. _71.-_5TAGE.....;':....S=:;,..'DC.=..;:=-_____ PUMP _..Ll 7..!.....LZ;-:IoQ~ __ R.P."'. CURVE Note... 0 5750 i, I SUBMERGENCE REQ'D OVER BELL TO PREVENT BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE.STDS. CERTIFIED BY: \\6.LL.ao":"'-~II!!!:!.-III!!!!!~L-. __ DATE 1\\.-11,;J In CUSTOMERGEORG\\~ PQWER CO* . f i REF. No.NR.;?<- <0632 ./

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CAPACITY, HEAD AND GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS.

WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE OF NOT OVER 15" F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. JP*167A BOWLS '5.f>, e M\\-re LIQUID =sU.. *,-U::'1C!. SP. GR. ).0 DATE4-t~P>7BY \\\\~.'B' I ! I ~ . t I I '4Q?D' j. '. ;. ~ I ., -i u.s. GALLONS PER MI Johnston Pump Company Glendora. California 91740 ESTABLISHEQ 18011 ,70q>O: i. _71.-_5TAGE.....;':....S=:;,..'DC.=..;:=-_____ PUMP _..Ll 7..!.....LZ;-:IoQ~ __ R.P."'. CURVE Note... 0 5750 i, I

} 'I I 7 YlHNST( MP COMPANY LABORATORY TEST DATA SHEET CURVE NO."Tc-oS7SQ JOB NO.A1R:><-"S3: Glendora. Calif. JOB NAME ~£DI!I;,I~ PvvJE.'" l!.o. J (ito) ~RATED CONDITION @ L~~ MOTOR -' !"o..1_ ~:cle* ttL- "-ftl{ IMPELLERS IfA_l! __ 2- ~L~ 13ff~u. + -4.!~ 17~O RPM HP Ph... Voll RPM Type Stag~ Mat.,ial Oia.-'.. -' p.... GPMYl'OO MOTOR SERIAL NO. CLASS_~ __ FINISH VANE Head 9~~ ~-:L S"U (lQQ! ~ BOWLS :51; S'TL. fJ.A$i~ SUCTION CASE £ E I. L BHP WATTMETER Material C"aling' Type RatiO T,ansforme, Sp. Gr.I.DQ ~ -~ Ell. oJJC Head iA& I" ~J/,f."" ~ DYNAMOMETER - Impellers Raised F.l. Ampl __. ' Voluge Scale Arm r,f18£~ <!~(. GPM-LoS.boY

  • VKP ORIFICE DIA. 7,04" HEAD A~. ADINliS TAKEN ~ller) Discharge Head J~..

I GAUGE I D"¥ PI: :P 1 r Flit Perlormanl:e . ___ Z.. _. Stage LINE .. 'm... FEET v l WATTMETER (~

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RPM 0 t°-;rEI I OF 2g TOTAL INPUT MOTOR £b/IJL U.S. I READING TOTAL B.H.P. I PSI FEET I WATER Fen HEAD H.P. ErF B.H.P. RPM EFf. 01 G.P.M. _II,.. IN U.s. HEAD Of TO 4ID> Sp. Gr. APIN 'lb G.P.M. IN HE.o.O I GAUGE FEET INCHES PIPE X:= YDl OF HG FEET /'DO -F-~ ~~/.D ~~~13 IJ3V,O ,Yeo IY/Y,O 0 0 11/t*1I- ~r - l..~D /Lt.,,, ((t 5' 0 D i9("I.r 1f7T T D 'Jb ~o9 IYY'O :r:n-, (. \\ - 1Ji.l , 1.., 0 II/t/,~ ,fjco I3t.J r_y'? 3~dl /0/7 JJ V9r Y l!l>J~ '~I .J()~,¥ y8"S-- S?, /1.. 1'(,,3

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  • 62

..., v}-..ll ~A/J ~b.J/S} WATER TEMP. OF ~D. ~~ R'=1,9C)/o FLOOR TO GAUGE AIR TEMP. OF .S'o!" Cerlil i,d bV TPI .., <1"7 q } 'I I 7 YlHNST( MP COMPANY LABORATORY TEST DATA SHEET CURVE NO."Tc-oS7SQ JOB NO.A1R:><-"S3: Glendora. Calif. JOB NAME ~£DI!I;,I~ PvvJE.'" l!.o. J (ito) ~RATED CONDITION @ L~~ MOTOR -' !"o..1_ ~:cle* ttL- "-ftl{ IMPELLERS IfA_l! __ 2- ~L~ 13ff~u. + -4.!~ 17~O RPM HP Ph... Voll RPM Type Stag~ Mat.,ial Oia.-'.. -' p.... GPMYl'OO MOTOR SERIAL NO. CLASS_~ __ FINISH VANE Head 9~~ ~-:L S"U (lQQ! ~ BOWLS :51; S'TL. fJ.A$i~ SUCTION CASE £ E I. L BHP WATTMETER Material C"aling' Type RatiO T,ansforme, Sp. Gr.I.DQ ~ -~ Ell. oJJC Head iA& I" ~J/,f."" ~ DYNAMOMETER - Impellers Raised F.l. Ampl __. ' Voluge Scale Arm r,f18£~ <!~(. GPM-LoS.boY

  • VKP ORIFICE DIA. 7,04" HEAD A~. ADINliS TAKEN ~ller) Discharge Head J~..

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RPM 0 t°-;rEI I OF 2g TOTAL INPUT MOTOR £b/IJL U.S. I READING TOTAL B.H.P. I PSI FEET I WATER Fen HEAD H.P. ErF B.H.P. RPM EFf. 01 G.P.M. _II,.. IN U.s. HEAD Of TO 4ID> Sp. Gr. APIN 'lb G.P.M. IN HE.o.O I GAUGE FEET INCHES PIPE X:= YDl OF HG FEET /'DO -F-~ ~~/.D ~~~13 IJ3V,O ,Yeo IY/Y,O 0 0 11/t*1I- ~r - l..~D /Lt.,,, ((t 5' 0 D i9("I.r 1f7T T D 'Jb ~o9 IYY'O :r:n-, (. \\ - 1Ji.l , 1.., 0 II/t/,~ ,fjco I3t.J r_y'? 3~dl /0/7 JJ V9r Y l!l>J~ '~I .J()~,¥ y8"S-- S?, /1.. 1'(,,3

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  • 62

..., v}-..ll ~A/J ~b.J/S} WATER TEMP. OF ~D. ~~ R'=1,9C)/o FLOOR TO GAUGE AIR TEMP. OF .S'o!" Cerlil i,d bV TPI .., <1"7 q

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THE CAPACITY. HEAD AND GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS. WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE 01' NOT OVER as* F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. '" f....,. CUSTOMER G E.ORG\\ A. S,S.PLbC\\TE. ,¥1,p..-reR. SPoOR 1.0 DATE G,*2.£\\.WBY \\\\.\\)B POWER.. Johnston Pump Company Glendora, California 91740 ESTABLISHED 1101 SUBMERGENCE REO'D OVER BEll TO PREVENT VORTEXES BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STBS. I..,, I ! ~ .,-UR.Sl blE BOW L PERFORMANCE 7 STAGE \\ 8, DC. PUMP \\770 R.P.M. CURVE No"IC.-OS7BO I ~;. : - **-*-f~ I

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THE CAPACITY. HEAD AND GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS. WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE 01' NOT OVER as* F. AND UNDER SUCTION CONDITIONS AS SPECI. FlED IN THE CONTRACT. '" f....,. CUSTOMER G E.ORG\\ A. S,S.PLbC\\TE. ,¥1,p..-reR. SPoOR 1.0 DATE G,*2.£\\.WBY \\\\.\\)B POWER.. Johnston Pump Company Glendora, California 91740 ESTABLISHED 1101 SUBMERGENCE REO'D OVER BEll TO PREVENT VORTEXES BASED ON SUMP DESIGN PER HYDRAULIC INSTITUTE STBS. I..,, I ! ~ .,-UR.Sl blE BOW L PERFORMANCE 7 STAGE \\ 8, DC. PUMP \\770 R.P.M. CURVE No"IC.-OS7BO I

.~ ) 't I 7 JOHNstON PUMP COMPANY , Glendora. Calif. LABORATORY TEST DATA SHEET CUhVI: NO.,c:.-C)S790 JOB NO. )Jtx-Gas:n.: JOB NAME ~£DJ!..t..I,. I'ljuJEIt.. ~o I LI6 "'0) IMPELLERS It~ 2-- dL.. 1-" ~RATED CONDITION@ 17-,.0 MOTOR -It'o..l_ JWL. Y1L. (-ftlf 13 t FJl.1.t + -iC"T~ RP¥ GPM YOf2 0 HP Ph... Cycl. Vol! RPM Type SIege Mal.,ial Dia.*& " p..... MOTOR SERIAL NO. CLASS ~- FINISH VANE Heed 9~~ -:;Fib WATTMETER S:, ~lD.Q! ~ BOWLS $1; S'Ti.. tJA$/~ SUCTION CASE ~£l t. BHP Ma,.,ial C"a"", Type Ratio T,an.lo,m., Sp.Gr.I.DD ~ oJJr ~:':i Head i.J.4 I, "'.}I.I,-I Eft. ~ DYNAMOMETER - Impellers Raised F.L. Ampl __,. Voluge Scale Arm "f]I18£.t. (f~L. GPM= LoS, ~o Y

  • VKP ORIFICE DIA. 7, oAA" HEAD READINGS TAKEN ~Iterl Discharge Held

.lp.. GAUGE li¥ PI: '" Ie afl Perlormanc:e ___ -L_ Suge LINE __ ' t;rI __ FEET 'V1 WATTMETER (~ t.."7 ?.fJ. RPM I OWE I OF 2, TOTAL INPUT MOTOR 4~~l... U.S. TOTAL B.H.P. PSI FEET WATER FeR HEAD READING H.P. EfF S.H.P. APM EFf. E:i G.P.M. 1(,.. IN U.S, HEAD OF TO ~ ~ Sfl, Gr. APIN G.P.M. IN -+WC I. HE~D I GAUGE PIPE FEET INCHES X:t '101 OF HG FEET .1.00

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  • VKP ORIFICE DIA. 7, oAA" HEAD READINGS TAKEN ~Iterl Discharge Held

.lp.. GAUGE li¥ PI: '" Ie afl Perlormanc:e ___ -L_ Suge LINE __ ' t;rI __ FEET 'V1 WATTMETER (~ t.."7 ?.fJ. RPM I OWE I OF 2, TOTAL INPUT MOTOR 4~~l... U.S. TOTAL B.H.P. PSI FEET WATER FeR HEAD READING H.P. EfF S.H.P. APM EFf. E:i G.P.M. 1(,.. IN U.S, HEAD OF TO ~ ~ Sfl, Gr. APIN G.P.M. IN -+WC I. HE~D I GAUGE PIPE FEET INCHES X:t '101 OF HG FEET .1.00

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'c.- CUSTOMER GEORGlA poweR co. i-':'~*H':":" .;.~ ~.* ---I"r"" **1,*L...... '.'. ~..,-:.. -,. '.;. r~~~(II:t::~;**~ : *r~~:;~~.:- I*---*-f-*... --*~.')I *}IIJ~.... -~*-:..*~--+-*--.. *-*.----901C7~' -"'-'~-"'-"'--r- ' -""';"" ~~ ~..... -...... SUBMERGENCe REO'O OVER BELL TO PREVENT BASEO ON SUMP DESIGN PER HYDRAULIC INSTlTl4TE STDS. --. -, - --~7--- ----*--*---t*-.. ---I---...***-+*~**--.-,*.. -* -~I-.-.. -*-*~*-.- ,--.I-.. r'*"-*'-'--"l***.... _J_* 1.-._._*.r_'~.!...:.J-* __.l._, -.... 00 800-

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THE CAPACITY. HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS. WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE OF NOT OVER 85* F. AND UNDER SUCTION CONOITIONS AS SPECI. FlED IN THE CONTRACT. BOWlS 5,S,.E\\,ACITe lIOUIO Wbje.li2.., SP.GR '.0 DATEn*/te*s7BY \\\\.~,~ Johnston Pump Company Glendora, California 91740 ESTABLISHED 1909 J].lRB) l'.lE.. BDWL 7 STAGE) B DC:.. _-J,.\\...L7...J7:.....:0~ __ R.P.M. PERFORMANCE PUMP CURVE NO TC -OS 673 -I 'c.- CUSTOMER GEORGlA poweR co. i-':'~*H':":" .;.~ ~.* ---I"r"" **1,*L...... '.'. ~..,-:.. -,. '.;. r~~~(II:t::~;**~ : *r~~:;~~.:- I*---*-f-*... --*~.')I *}IIJ~.... -~*-:..*~--+-*--.. *-*.----901C7~' -"'-'~-"'-"'--r- ' -""';"" ~~ ~..... -...... SUBMERGENCe REO'O OVER BELL TO PREVENT BASEO ON SUMP DESIGN PER HYDRAULIC INSTlTl4TE STDS. --. -, - --~7--- ----*--*---t*-.. ---I---...***-+*~**--.-,*.. -* -~I-.-.. -*-*~*-.- ,--.I-.. r'*"-*'-'--"l***.... _J_* 1.-._._*.r_'~.!...:.J-* __.l._, -.... 00 800-

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THE CAPACITY. HEAD AND EFFICIENCY GUARANTEE IS FOR THE DESIGNATED POINT ONLY: IT IS BASED ON SHOP TESTS. WHEN HANDLING CLEAR, FRESH WATER AT A TEMPERATURE OF NOT OVER 85* F. AND UNDER SUCTION CONOITIONS AS SPECI. FlED IN THE CONTRACT. BOWlS 5,S,.E\\,ACITe lIOUIO Wbje.li2.., SP.GR '.0 DATEn*/te*s7BY \\\\.~,~ Johnston Pump Company Glendora, California 91740 ESTABLISHED 1909 J].lRB) l'.lE.. BDWL 7 STAGE) B DC:.. _-J,.\\...L7...J7:.....:0~ __ R.P.M. PERFORMANCE PUMP CURVE NO TC -OS 673 -I

) 'I I t JOHNSTON~uMPCOMPANY Glendora. Calif. LABORATORY TEST DATA SHEET ('to) CURVE No.,.c.-05B7~ JOB NO. tJ&.?( -6:"-~i JOB NAME ~£Oe.tltf PuwEIL ('!o , ~ I "I * .L., IMPEllERS IfJ~ ~RATED CONDITION @ 17';0 LA~ MOTOR -I $"0 -1_ k.L Y.J.L f-fetl L-'~L~ J3TfJiu+ -It- '1& RPM Typ. Stag. Mat.rlal OiA.*' ' J P ',... YlJl2 0 HP Pha.. Cycl. Volt RPM GPM MOTOR SERIAL NO. CLASS ~ - FINISH VANE 9~~ Hud -:F"-;L SU LlQQ: S-BOWLS.$1; sri-. f..LAs/~ SUCTIONCASE £EiL DHP WATTMETER Mat.ria. C.... \\inll

    • Type R.lio Tr.n,lorm.r Sp.Gr.I.DQ

~ oJJC Jr~:~ Head LA& I L ~ Jl,1:-t Ell. ~ DYNAMOMETER - Impellers Raised F.L. Amps __.. Voluge Seal. Arm '11I18£1! (uc., GPM= /"O~. 4.0 Y

  • VAP ORIFICE D/A. 7, oU II HEAD RI:ADINliS TAKEN ~llerl Discharge Head

.J.Iz-" I GAUGE I FEET l1¥Fh.r' : ,~ Pedormanl:e _Z Suge LINE It; I'SL. VZ WATTMETER (~ !'?'?"Q. RPM fO~EI OF 29 TOTAL INPUT MOTOR ~~~L. U.S. TOTAL D.H.P. PSI FHT WATER FeR HEAD READING H.P. EfF D.H.P. RPM EFF. ~ G.P.M. Jl,., IN U.S. HEAD OF TO oGD> Sn. Gr. APIN G.P.M. IN .we ' to HEA.D I GAUGE FEET INCHES PIPE x= YD~ OFHG FEET /'00 0 0 I~<,O 30'} I". ~.- 'lS7,$' . *l.r~ ng,cl ,tJOO )1l.D ~90 0 0 flit)',?... 9?1,L 1l.. 2l:J ~() It IY'I,<" 33.1.~ \\ - 1 YO, t, , )..71 )yr,3 9lJO }3D.~ ~"1,~ ID/I,., H 5"""/",3 lo39,~ 1 0,10

z.?O JoDO

/l '1..0 i"JD v.tt "]I/,'} .l!'~ IS"/, L .{JDD 1]/',' ~ 5"'7,~ 199;- (2. 'II, L iof</.1/ I £" I D )S"03 JJ/f. r 1.') L.D I , I "L.~ 1... $I JDb JI, '1./ ,cue 11)],7 ~J )1..,; 2 c/y $' 111..~.-r /173,k, l!~~.1) / (,1") v 'O*¥O

lOOO JbY,O 1'}0. ?... L.g I~ "tV?,1-

, lit nD.~,IJ O'b )5l,v ~y) 'B'I,lJ .3 ~/'11 9~YcJ I z.IPo, ~ 't..90 ~~D1- ~Y,D } $' 'I, D \\ , 3 "Z..o },' ,lIS-I/. 'i,9 '1trJ 1~2,C s>S'] ~l,1., 1,/99J ~6b, 't /1.D78*

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~.r,r-II~/? ,:tt.3 1~/,7 ,c100 illS !r;~ 109,., " 1/~3 '1"'I,~ Ie'S I/, I.. ~ MOTOR MEGOHMS "y SUBMERGENCE ABOVE LIP Telltd b'~ :;P4f;... Dlleb'-l-1r 2 OF SUCTION BELL _It. _In.

0 R =J,~5s S-

~y FLOOR TO WATER Mtl l77Q BAROMETER "HG c,;-S'1 Wilnessed by WATER TEMP. OF /t.a R'=l,?~t.D AIRTEMP.

  • FLOOR TQ G'(uGE rr

_ _____ _ _ OF fI'" rr I."g' ~r&ili.d by I ) 'I I t JOHNSTON~uMPCOMPANY Glendora. Calif. LABORATORY TEST DATA SHEET ('to) CURVE No.,.c.-05B7~ JOB NO. tJ&.?( -6:"-~i JOB NAME ~£Oe.tltf PuwEIL ('!o , ~ I "I * .L., IMPEllERS IfJ~ ~RATED CONDITION @ 17';0 LA~ MOTOR -I $"0 -1_ k.L Y.J.L f-fetl L-'~L~ J3TfJiu+ -It- '1& RPM Typ. Stag. Mat.rlal OiA.*' ' J P ',... YlJl2 0 HP Pha.. Cycl. Volt RPM GPM MOTOR SERIAL NO. CLASS ~ - FINISH VANE 9~~ Hud -:F"-;L SU LlQQ: S-BOWLS.$1; sri-. f..LAs/~ SUCTIONCASE £EiL DHP WATTMETER Mat.ria. C.... \\inll

    • Type R.lio Tr.n,lorm.r Sp.Gr.I.DQ

~ oJJC Jr~:~ Head LA& I L ~ Jl,1:-t Ell. ~ DYNAMOMETER - Impellers Raised F.L. Amps __.. Voluge Seal. Arm '11I18£1! (uc., GPM= /"O~. 4.0 Y

  • VAP ORIFICE D/A. 7, oU II HEAD RI:ADINliS TAKEN ~llerl Discharge Head

.J.Iz-" I GAUGE I FEET l1¥Fh.r' : ,~ Pedormanl:e _Z Suge LINE It; I'SL. VZ WATTMETER (~ !'?'?"Q. RPM fO~EI OF 29 TOTAL INPUT MOTOR ~~~L. U.S. TOTAL D.H.P. PSI FHT WATER FeR HEAD READING H.P. EfF D.H.P. RPM EFF. ~ G.P.M. Jl,., IN U.S. HEAD OF TO oGD> Sn. Gr. APIN G.P.M. IN .we ' to HEA.D I GAUGE FEET INCHES PIPE x= YD~ OFHG FEET /'00 0 0 I~<,O 30'} I". ~.- 'lS7,$' . *l.r~ ng,cl ,tJOO )1l.D ~90 0 0 flit)',?... 9?1,L 1l.. 2l:J ~() It IY'I,<" 33.1.~ \\ - 1 YO, t, , )..71 )yr,3 9lJO }3D.~ ~"1,~ ID/I,., H 5"""/",3 lo39,~ 1 0,10

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, lit nD.~,IJ O'b )5l,v ~y) 'B'I,lJ .3 ~/'11 9~YcJ I z.IPo, ~ 't..90 ~~D1- ~Y,D } $' 'I, D \\ , 3 "Z..o },' ,lIS-I/. 'i,9 '1trJ 1~2,C s>S'] ~l,1., 1,/99J ~6b, 't /1.D78*

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~.r,r-II~/? ,:tt.3 1~/,7 ,c100 illS !r;~ 109,., " 1/~3 '1"'I,~ Ie'S I/, I.. ~ MOTOR MEGOHMS "y SUBMERGENCE ABOVE LIP Telltd b'~ :;P4f;... Dlleb'-l-1r 2 OF SUCTION BELL _It. _In.

0 R =J,~5s S-

~y FLOOR TO WATER Mtl l77Q BAROMETER "HG c,;-S'1 Wilnessed by WATER TEMP. OF /t.a R'=l,?~t.D AIRTEMP.

  • FLOOR TQ G'(uGE rr

_ _____ _ _ OF fI'" rr I."g' ~r&ili.d by I

o o ~. ,-.' /' 1000 1500 JOHNSTON PUM'"' r:OMPANY BROOKSHIIlli~ TEXAS CUSTOMER: GEORGIA POWER COMPANY JOB #: NC-6519 SIN: NC-6519 POF #: 66170 TC #:06566 1780 RPM 2000 2500 3000 3S00 ~ooo .soo 5000 5500 . Reviewed By O'lgr# c;:e./~ Title Et.'~L4.a.,.. - 6000 6500 7000 I

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1 1 I I I., o o ~. ,-.' /' 1000 1500 JOHNSTON PUM'"' r:OMPANY BROOKSHIIlli~ TEXAS CUSTOMER: GEORGIA POWER COMPANY JOB #: NC-6519 SIN: NC-6519 POF #: 66170 TC #:06566 1780 RPM 2000 2500 3000 3S00 ~ooo .soo 5000 5500 . Reviewed By O'lgr# c;:e./~ Title Et.'~L4.a.,.. - 6000 6500 7000 I

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TC 110.:.. , rc-o~m 1IC-6m JOOIISron MP a:lPAIlT PElFOWIlCE TEST SET-UP AIID TEST DATA snm !lOTOIII.P./U.II.: 150 I &80 ," '- mtAL. ~.Q.: WIIIElITS: TEST rnrm ASSDlBLY 11m A TEST DISCl.HtlD AIID COLUWt At lEOOCED 51 USING A TEST LAB IlOTOl. 'P4TS aiOU I: roF-66110 Pillet/v: 3/GO/U0 JOB JlUKBE1: NC-6m WOTOI S/H: JOO 01 LAB IIOT01: LAB CUST.: GEOlGtA !'(mEl OliPAIIT UOC /7 WODEL/suc£s: ' fKt. IftA.: mnlKTEl HO,: It l3.15O' Olrle( DIAXtTEl: 1.0tt IF/eL.:

,1.

fliP.KAT[lIAL: TEST LINE SIZE: 16 P1ESSUIE GAGE: 300 .063' / 'C' om - C13600! C1ATAlIOOOA P.O.NO. ~,',. T! - 9H6 BOIfL IIATElIAL: SJ.351 - CF311 !IIP.ADJUS11IY.lIT: TlIO TUlliS TESTED AS PEl PIOC!IXlll KO.: Jp-TP-Om m, Il(IL roltlKG: SUCTION: PLASltE 1111 BELL DESIGN g.P.11. i G.P,II.: 1710 ~ooo m.o IIOII OIDEl HO.:' '.' ~ TEST D. READ: TEST roL.: TEST COIISTAIITS;; fLOlf: nWl: pm DIUPSI GAGE: 1I0r01 EFFlCIEIICT; 100%: 1st: i SOl: WATEl TO F1.OO1: FLOOl ro CAGE: un 16' IIIW PIESSUU: DlSat. UWl TUPElED COLUlIlI PIPE 601.60~ 1.31 16.000 UEAD: B,II,P.: 'EFFICIY.lIet: U % IlC1.fL SPECIFIC GlAYITT 1: 1,00 SPECIFIC GlAYITT %: " 0,00 ITIll HO.: FLUID: APPLICATlOH: DID USU: SITE: GEOlG IA roll Jl rolP.oo GEOIGIA POKE! COYPAliT Zl IKOIKS 60 tHOlES TAlE SIIUT-OFF(TES/KO): YES Z 3 1 a 9 10 11 13 DElTl 'P' i 10.80 i 0.80 i 1.10 i 2.10 i l.oo 5.00 i 6.10 i 10.&0 i 13.50 i 16.~0 i 10.50 i 24.30 i 21.50 i I GILLOHS P£1 KIHutE I 2000 I m I 194 1 1000 I lZIl un 1 1503 I zOOO I me I ZSOz I me I 3000 1 3249 1-GAGE/nc l£ADINC

103.90 14l.60 1 Il6.60: Ill.90 I 121.00 Itt.lO I 111.00 I 103.10 I 92.60 I 11.30 I 10.zo I 51.00 I 42.50 l--r.r lEEf OF 1l£AD 1 nUl 331.1: m.ss I JOU9: 193.11 m.n I m.ss I m.5S I m.n I m.ao I m.nl 133.911 91.n!-,r GIG! £LEV.COIl. I' 6.15 6.151 6.15 1 6.15 1 6.15 ti.15 1 6.15 1 6.151 6.15 I 6.151 6.151 6.151 i.15 I-
  • i~1Tl "£AD LOSs I o.n 0.01 I 0.01 I 0.04 I 0.06 0.01 1 0.09 I 0.16 I 0.20 I 0.25 I 0.30 I D.n I D.n t TOtAL JlEXb I 146.9%

m.n 1 m.ll :1 m.n 1 300.11 t m.S1! m.n 1 m.n 1 nus! 191.10 I 169.%1 I lU.nl lo~3i l-rr lIft lEADING I 123.10 105.60 I 106.10 I 109.50 I 114.10 1 116.10 I m.lO I 123.10 I m.l0 1 120.90 I, m.30 I lIUO I 10"00 I' INPUT n.p. I 165.12 141.55 I 143.16 I 146.18 I 15t.95 I 156.51 I 151.45 I 165.15 I 164.41 I 162.06 I -158.51 I 151.21 I 142.09 I~ 1IOT01 EFFicIENCY I MOO 0.900 I 0.900 1 o.m I 0.900 1 0.900 1 D.900 I 0.900 I 0.900 1 0.900 I 0.900 I 0.980 1 D.900 10 n.n.p. 149.24 121.40 I 128.85 I 132.10 I 131.65 I 110.91 I 111.60 I 148.63: 141.03 I 145.16 I 141.11 I 131.05 I 111.1& (--"r tESt U.K.: m B9S I m 1, i90 I 8891 m I m 1 ill I au I m I m I 1191 89D I~ YOLTS(ID.oHLY) 0 I 0 !., 0 I 0 I 0 I 0 I 0 I G\\ 0 I 0 I 0 I 0 1 0 1-lIIPS(IEP.oHLy): 0 I 0 I 0 1 0 I 0 I 0 I 0 : q 0 : 0 I 0: 0 I 0 1-YlnwlOH IN wIts 0.00 I 0.00 I 0.00 I 0.00 I 0.00 1 0.00 I 0.00 I 0.00 1 0.00 I 0.00 I 0.00 I 0.00 I 0.00 1-PElF.WTEIl.U.Il.:, 1110 I 1180 I 1110 I 1180: 1180 1 1110 I 1180 I 1m I 11&0 I 1110 I 1110 I 1110 I 1m I~ GXLLOHS PEl II I RDfE: I 4005! 1083 I 1m I 1000 1 W1 1 2125 1 3010: 4009 1 nu I 5015 1 55[1 I Coot I ml 1-;- toUL DW IN FEET:I m.1911331.13In14.91 I 114S.91 Ilm.n I mo.n I mo.19 1 990.21 I 111.40 I m.111 m.n I 565.611 m.ll 111ft D.n.p.@ 1.0 s ** GI*:1 1191.92 I 1002.11 I 1013.&0 I 10SS.lt I 110t.95 I 1131.10 I Iltt.&' I 1191.11 I 1191.1' I 1114.11 I 1115.&3 I II'D.II I I013.DC I~ B.n.p.@ JOB Sf.Cl.11 1191.9% 11002.2111013.60 11056.1411104.951 ml.l0 I mUG: 1191.11 I lIU.IS I nU.ll I ms.nlllOo*l1 l 1013.0C l-sf B.n.p.8 JOB SP.Gi.I: 0.00: 0.00: 0.00 I 0.00 I 0.00 I 0.00 I 0.00 I 0.00 I 0.00 I 0.00 1 0.00 f 0.000 1 0.001 1"- £FPlcIEHcY: I o.m 1 o.m I 0.501 1 0.595 1 0.S10 I D.m I o.m 1 o.m 1 0.141 I 0.144 I "0.125 I 0.110 I O.m 1-'- 1 1 1 1 1 I 1 17-1 I I 1_ .iSTED DY: LLJOD COTTON C!lTIFIED DY: EllllllODllGlJ}l:I7I---- IlTlleiSED BT: DATE or TEST: OEema 10, lS91 ,.' ;.j\\ TC 110.:.. , rc-o~m 1IC-6m JOOIISron MP a:lPAIlT PElFOWIlCE TEST SET-UP AIID TEST DATA snm !lOTOIII.P./U.II.: 150 I &80 ," '- mtAL. ~.Q.: WIIIElITS: TEST rnrm ASSDlBLY 11m A TEST DISCl.HtlD AIID COLUWt At lEOOCED 51 USING A TEST LAB IlOTOl. 'P4TS aiOU I: roF-66110 Pillet/v: 3/GO/U0 JOB JlUKBE1: NC-6m WOTOI S/H: JOO 01 LAB IIOT01: LAB CUST.: GEOlGtA !'(mEl OliPAIIT UOC /7 WODEL/suc£s: ' fKt. IftA.: mnlKTEl HO,: It l3.15O' Olrle( DIAXtTEl: 1.0tt IF/eL.:

,1.

fliP.KAT[lIAL: TEST LINE SIZE: 16 P1ESSUIE GAGE: 300 .063' / 'C' om - C13600! C1ATAlIOOOA P.O.NO. ~,',. T! - 9H6 BOIfL IIATElIAL: SJ.351 - CF311 !IIP.ADJUS11IY.lIT: TlIO TUlliS TESTED AS PEl PIOC!IXlll KO.: Jp-TP-Om m, Il(IL roltlKG: SUCTION: PLASltE 1111 BELL DESIGN g.P.11. i G.P,II.: 1710 ~ooo m.o IIOII OIDEl HO.:' '.' ~ TEST D. READ: TEST roL.: TEST COIISTAIITS;; fLOlf: nWl: pm DIUPSI GAGE: 1I0r01 EFFlCIEIICT; 100%: 1st: i SOl: WATEl TO F1.OO1: FLOOl ro CAGE: un 16' IIIW PIESSUU: DlSat. UWl TUPElED COLUlIlI PIPE 601.60~ 1.31 16.000 UEAD: B,II,P.: 'EFFICIY.lIet: U % IlC1.fL SPECIFIC GlAYITT 1: 1,00 SPECIFIC GlAYITT %: " 0,00 ITIll HO.: FLUID: APPLICATlOH: DID USU: SITE: GEOlG IA roll Jl rolP.oo GEOIGIA POKE! COYPAliT Zl IKOIKS 60 tHOlES TAlE SIIUT-OFF(TES/KO): YES Z 3 1 a 9 10 11 13 DElTl 'P' i 10.80 i 0.80 i 1.10 i 2.10 i l.oo 5.00 i 6.10 i 10.&0 i 13.50 i 16.~0 i 10.50 i 24.30 i 21.50 i I GILLOHS P£1 KIHutE I 2000 I m I 194 1 1000 I lZIl un 1 1503 I zOOO I me I ZSOz I me I 3000 1 3249 1-GAGE/nc l£ADINC

103.90 14l.60 1 Il6.60: Ill.90 I 121.00 Itt.lO I 111.00 I 103.10 I 92.60 I 11.30 I 10.zo I 51.00 I 42.50 l--r.r lEEf OF 1l£AD 1 nUl 331.1: m.ss I JOU9: 193.11 m.n I m.ss I m.5S I m.n I m.ao I m.nl 133.911 91.n!-,r GIG! £LEV.COIl. I' 6.15 6.151 6.15 1 6.15 1 6.15 ti.15 1 6.15 1 6.151 6.15 I 6.151 6.151 6.151 i.15 I-
  • i~1Tl "£AD LOSs I o.n 0.01 I 0.01 I 0.04 I 0.06 0.01 1 0.09 I 0.16 I 0.20 I 0.25 I 0.30 I D.n I D.n t TOtAL JlEXb I 146.9%

m.n 1 m.ll :1 m.n 1 300.11 t m.S1! m.n 1 m.n 1 nus! 191.10 I 169.%1 I lU.nl lo~3i l-rr lIft lEADING I 123.10 105.60 I 106.10 I 109.50 I 114.10 1 116.10 I m.lO I 123.10 I m.l0 1 120.90 I, m.30 I lIUO I 10"00 I' INPUT n.p. I 165.12 141.55 I 143.16 I 146.18 I 15t.95 I 156.51 I 151.45 I 165.15 I 164.41 I 162.06 I -158.51 I 151.21 I 142.09 I~ 1IOT01 EFFicIENCY I MOO 0.900 I 0.900 1 o.m I 0.900 1 0.900 1 D.900 I 0.900 I 0.900 1 0.900 I 0.900 I 0.980 1 D.900 10 n.n.p. 149.24 121.40 I 128.85 I 132.10 I 131.65 I 110.91 I 111.60 I 148.63: 141.03 I 145.16 I 141.11 I 131.05 I 111.1& (--"r tESt U.K.: m B9S I m 1, i90 I 8891 m I m 1 ill I au I m I m I 1191 89D I~ YOLTS(ID.oHLY) 0 I 0 !., 0 I 0 I 0 I 0 I 0 I G\\ 0 I 0 I 0 I 0 1 0 1-lIIPS(IEP.oHLy): 0 I 0 I 0 1 0 I 0 I 0 I 0 : q 0 : 0 I 0: 0 I 0 1-YlnwlOH IN wIts 0.00 I 0.00 I 0.00 I 0.00 I 0.00 1 0.00 I 0.00 I 0.00 1 0.00 I 0.00 I 0.00 I 0.00 I 0.00 1-PElF.WTEIl.U.Il.:, 1110 I 1180 I 1110 I 1180: 1180 1 1110 I 1180 I 1m I 11&0 I 1110 I 1110 I 1110 I 1m I~ GXLLOHS PEl II I RDfE: I 4005! 1083 I 1m I 1000 1 W1 1 2125 1 3010: 4009 1 nu I 5015 1 55[1 I Coot I ml 1-;- toUL DW IN FEET:I m.1911331.13In14.91 I 114S.91 Ilm.n I mo.n I mo.19 1 990.21 I 111.40 I m.111 m.n I 565.611 m.ll 111ft D.n.p.@ 1.0 s ** GI*:1 1191.92 I 1002.11 I 1013.&0 I 10SS.lt I 110t.95 I 1131.10 I Iltt.&' I 1191.11 I 1191.1' I 1114.11 I 1115.&3 I II'D.II I I013.DC I~ B.n.p.@ JOB Sf.Cl.11 1191.9% 11002.2111013.60 11056.1411104.951 ml.l0 I mUG: 1191.11 I lIU.IS I nU.ll I ms.nlllOo*l1 l 1013.0C l-sf B.n.p.8 JOB SP.Gi.I: 0.00: 0.00: 0.00 I 0.00 I 0.00 I 0.00 I 0.00 I 0.00 I 0.00 I 0.00 1 0.00 f 0.000 1 0.001 1"- £FPlcIEHcY: I o.m 1 o.m I 0.501 1 0.595 1 0.S10 I D.m I o.m 1 o.m 1 0.141 I 0.144 I "0.125 I 0.110 I O.m 1-'- 1 1 1 1 1 I 1 17-1 I I 1_ .iSTED DY: LLJOD COTTON C!lTIFIED DY: EllllllODllGlJ}l:I7I---- IlTlleiSED BT: DATE or TEST: OEema 10, lS91 ,.' ;.j\\

N N 0 Z ~ .-I U ~ .-I. .\\ ~.) .-I ~ \\0 jS) fti to) - ~ : ~ ~ .. ' i ! ~ I r ,0 '. ~ 0 John~' Pump Com~ny Brookshire, T exos. Customer: Georgia Power. Company Job i:NO-6509 S/N:NRX-6533 POfj:66224 TC 1:06784 1780 RPM t8CO .I' 1+.!-h=H-.' \\ l 1..u..+/- I!:H 4-l." LJ..!..1.J..H+H--q*q-~iu' II ~+ UI' L.t-H-.f-tt'.lll.I*+-H-! ~:III +=ttt~" LL H.Ll f1#' 1...Ll..!. ~~ LL'.J _ll 0 - ~ I" IT+I.!.l...!LLJ.:rD:.t...!..:t ~H='::n~-' : 1'1 I I I) '1. _ur C[Li.1.uiTl 1"1 II U.L~mt-*1 il...D._.,iIl.C ffi..l*,I I -' ".!.8i'l!.L. ';iI.f t I.~ ; t+/- r- ,, " -U-l-t- ' 'I T I I TiT' i-!, " W. ..!. U. 1 , I it I TfT'I-I' ,,IT 'I I I,r", , It I I r, ~I-I' "!Ii I T~ i"tij, I'.,-. '- I ,+rr ~ (IT ' n& I I i ..~ ""'i"-........-----,,or" ~ I I ~J _LU."!'""" I I: r-1700 . I I I I I

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-4 1.70 2.70 784 1000 131.10 1:13.70 310.01 3D... ! U3 5.13.- 0.02 0.04 Gz.c.at 314.72 1011.80 1011.110 142.00 146.112 o.aoo 0.000 nUl 132.23 8110 aao 1780 1780 1587 2002 1200.41 1%111.71 1028.85 1081.38 1028.15 10Gl.~1 0.00 0.00 0.501 0.801 FluId: Waler Job I: No-IISOO AppRuUon: End U.. r: sa.: a.org'. Power Comp.ny POF I: _.;;.ftft;;.;;2~2,-,,4 ______ _ Ceor;la Pow.r Company Chaltanoo;_ P.O.';TE - 10234 Take 8hU! - Off (Yu 1 No): Yes 0 7 II D 10 11 t2 13 U 4.00 11.00 11.10 10.80 13.50 18.110 20.50 Z4.~ 21.50 0.00 1217 1:101 150:1

lOaD 2238 2502 2758 3000 324D 0

1211.00 128.00 121.00 105.50 117.30 8S.00 74.00 113.110 50.70 152.30 2011.3. 291.00 2711.51 243.71 224.7S 108.43 170.114 140.02 117.12 351 ** ' 5.&3 5.113 5.83 $.113 1i.13 '.113 5.83 1:1.13 5.83 lI.n 0.011 0.07 0.00 0.18 0.20 0.25 0.30 O.:UI 0.42 0.00 305.27 20a.o7 285.43 240.70 230.70 zOU1 177.07 153.11 123~7 357.85 1H.IIO 110.10 11UO 123.DO 124.110 124.00 121.10 11UO 112.40 00.20 154.02 1!1.31 100.19 18$.00 167.~3 1011.22 H13.27 151.'5 1110.01 132.1& 0.000 0.1100 0.1100 0.1100 0.1100 0.1100 0.1100 0.1100 0.000 0.000 131.82 1U.4I 144.17 14UI 150.01 1411.80 1411.04 142.110 13UO 11UI SIt ua 881 au 1547 817 1&7 all 880 allo 1780 11"10 1780 17.0 1710 1710 1780 1710 1710 1780 2~37 2721 3013 40011 4417 6021 6530 11014 05015 0 1223.'2 11V3.ZZ 1"8.81 100UD 0211.43 823.51 71:1.00 1115.11 4U,58 H:l0.50 1112.70 1147.58 1181.15 1203.V2 1217.74 12011.07 1187.62 1151.4-4 10aUII 1157.~3 1112.70 1147.50 11111.111 1203.02 1217.74 t208.t7 1"7.'2 11S1.U 10ea.411 1157.43 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 O.Dn. 0.7111 0.752 0.'44 6.lII! i? 0.884 O.IOSI D.'11 0.748 0.000 [, c ertHIad By: Ernle Rodr'gu~ II ~ Data Of Tell: October 10, 111112 i '. ~.-. '. .... \\: r RCV BY:XEROX TELECOPIER 7~1~ ~1~-16-92 2: 14PM QCT,-16-92 FRI 13:08 J

  • G.

.INC. 6156981447:** 3 P.03 ~ TO No.: Job Number: Cu.lom.r: Modell SI.o.e: Imp. 01 ** : TIlF / CL: Imp. MAtlrlal: Bowl MAlltlal: Bowl CoaUn;: Sucllon: T.d D. Hud: T.. t Col.: T.al Constants; Flow: H ** d: JOHNSTON PUMP COMPANY PERFORMANCE TEST SET -UP AND TEST DATA SHEET Te-Oll784 ND-IISOII G.Ot;.. Powe, Compllny 1I0e/7 13.750 .08~ I'C* Btonze st. SII. Plnlt. e.1 Lab 1 S" H.P. Dllch. Head LAb Tapper Column 1101.1104 2.31 Molal H.P.I R.P.M.: PH/CY IV: Molar SIN: Job OR Lab Motol: Wattmeter No.: Orllct Dlamet.r: T.. t JI"I Blu: Pr *** ute GA;e: Imp ell., AdJualmenl: DESIGN @ A.P.M.: a.p.M.: Hnd: S.H.P.: EflIclency: Specific GravIty 1: Bp.clfic GrAvity 2: 1501 no

! 1 OO/HO lab 62 7.02Z 18 300 Two Turn.

1780 4000 Q55.00 S~ " Bowl 1.00 0.00 Commlnta: Taellhe Bowl Anlmbly onlv al rlduced apud wilh

  • TI.t Lab Diu/\\' Hud and ColUmn ullna _ T.. t Lab Molal.

ReVIewed ay;f. ~ ~'e /tJ -1'-, nu *. ~. .

  • c::!.

~ 7?'La-, Teat Procedure I:JP-TP-OOeo Rn. III 4 SerIal #: NRX - IIS33 rIp, 01 ** Gal,l': 18.000 Item No.: Molar Elf.: 100 %: 75 %: 50,,: Walar To FloOf: Fl T G oor 0 Auge: T ** t PoInt I Q.. 9~on. Pit Minute ~~.a.. d'na ~!!!:1.. d Gao. Elev.Corr. Velocity Head LOll Tot.! Htad. Walt AudIno: tnpllt H.P. Molor Efficl.ncy S.H.P. Tnt A.P.M.: Valla: (R.f.Only) AmP' (Ref.OnM: VibraUon In Mill: Rated ft.,..M.: aallon. Per MInute: l!!.' Head In F ** l: 8' - '5' 1.0 Sp.Gr. ' ~ b.@ Sp.Gr.1: 8.H.P.!i S~.Qr.2: T.II.d By:

  • Wln.... d By:

.;..;10;...INCHES 00 INCHE S 1 2 10.10 0.10 2000 11-44 105.00 144.30 242.55

133.33 80S 3 11.83 -..

0.10 0.01 2~1.64 330.1 I 1ZUO !~~.30 108.00 141.15 0.1100 0.1100 1411.48 127.04 8&1 aDo 17110 1780 4014 10lD 1000.110 1351.71 1207.011 101 D.30 1207.00 1018.30 0.00 0.00 0.140 0.3111 Darryl Clark Jr.

t

-4 1.70 2.70 784 1000 131.10 1:13.70 310.01 3D... ! U3 5.13.- 0.02 0.04 Gz.c.at 314.72 1011.80 1011.110 142.00 146.112 o.aoo 0.000 nUl 132.23 8110 aao 1780 1780 1587 2002 1200.41 1%111.71 1028.85 1081.38 1028.15 10Gl.~1 0.00 0.00 0.501 0.801 FluId: Waler Job I: No-IISOO AppRuUon: End U.. r: sa.: a.org'. Power Comp.ny POF I: _.;;.ftft;;.;;2~2,-,,4 ______ _ Ceor;la Pow.r Company Chaltanoo;_ P.O.';TE - 10234 Take 8hU! - Off (Yu 1 No): Yes 0 7 II D 10 11 t2 13 U 4.00 11.00 11.10 10.80 13.50 18.110 20.50 Z4.~ 21.50 0.00 1217 1:101 150:1

lOaD 2238 2502 2758 3000 324D 0

1211.00 128.00 121.00 105.50 117.30 8S.00 74.00 113.110 50.70 152.30 2011.3. 291.00 2711.51 243.71 224.7S 108.43 170.114 140.02 117.12 351 ** ' 5.&3 5.113 5.83 $.113 1i.13 '.113 5.83 1:1.13 5.83 lI.n 0.011 0.07 0.00 0.18 0.20 0.25 0.30 O.:UI 0.42 0.00 305.27 20a.o7 285.43 240.70 230.70 zOU1 177.07 153.11 123~7 357.85 1H.IIO 110.10 11UO 123.DO 124.110 124.00 121.10 11UO 112.40 00.20 154.02 1!1.31 100.19 18$.00 167.~3 1011.22 H13.27 151.'5 1110.01 132.1& 0.000 0.1100 0.1100 0.1100 0.1100 0.1100 0.1100 0.1100 0.000 0.000 131.82 1U.4I 144.17 14UI 150.01 1411.80 1411.04 142.110 13UO 11UI SIt ua 881 au 1547 817 1&7 all 880 allo 1780 11"10 1780 17.0 1710 1710 1780 1710 1710 1780 2~37 2721 3013 40011 4417 6021 6530 11014 05015 0 1223.'2 11V3.ZZ 1"8.81 100UD 0211.43 823.51 71:1.00 1115.11 4U,58 H:l0.50 1112.70 1147.58 1181.15 1203.V2 1217.74 12011.07 1187.62 1151.4-4 10aUII 1157.~3 1112.70 1147.50 11111.111 1203.02 1217.74 t208.t7 1"7.'2 11S1.U 10ea.411 1157.43 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 O.Dn. 0.7111 0.752 0.'44 6.lII! i? 0.884 O.IOSI D.'11 0.748 0.000 [, c ertHIad By: Ernle Rodr'gu~ II ~ Data Of Tell: October 10, 111112 i '. ~.-. '. .... \\: r

t>68SS-S I UNIT I ~o 2 TIlA\\lEUI'l(; WATER SCREENS - G£NERAL AllRmGEllENT [)R,\\Vf.~ 1 & 2 rv.TCH 6O~6~I7 5-55894 TAIIJS'cT. Nt.! PM;[ Nt.! THIS DWr;. PART or VENDOR MANUAL NjA N**S. o A1X18 0036 _1~_2 BASKET pETAl1 REX F G (02_<E1'l) Southern Nuclear Operating Campany. Inc. __.M_ Edwin I Hatch Nuclear Plant =~ -L:""'~ rfiH1J. ......'"':""'.='1:...., L.2...i I~h'ii ~ SECTION C C

.l............lt....",,'
!!...~J""~

~~..,~~~-n~..... iIi,p,p.....:.r::o~" PO ~'-_.".. ~__......,uo._ =~~-"._-- =:;"::Jti~::"'_ DR'YF CHAIN >t***,....,. COMPONENTS: ~idf~m jM;~~'="":&.. ~~::;;;~~ ........... ",(lJOlDo.) flUoR SPL\\.SH HSG. ANCHOR BOlT DETAk-VlEW D Q ___~r _--T-j T SEl CO'..lAA.J FRONT ELEVATION 2 1/'~*. F\\lOT')l-WT S.S. ./Sroooy Slt£\\U L.H. SIDE ELEVATION ... 01<...... ""--......,_ VOl> ~ DEW

Revised by SNC per Document No.: 5-56429 ABN H00330 Version 1.0 Document Ver.:

3.0 Vendor

JOHNSTON PUMP CO. By: BgT Checked: MWD Approved: WLN Date: 03/08/2007 DOCUMENT INSERTION SHEET E. I. Hatch Nuclear Plant - Unit No. 1 /2 RHR SERVICE WATER PUMP PERFORMANCE CURVES Description Remove

1.

This insertion sheet Existing Sheet(s)

2.

Letter from OEM dated July 21, 1986 -

Subject:

RHRSW, N/A PSW, Stand By Service Water Pumps, Submergence Requirements

3.

Attachment to Letter Dated July 21, 1986,

Subject:

Pump N/A Submergence of Plant Service Water Pumps... Document Insertion Sheet.dot Procedure: CM-003/CM-004 Insert Front of Manual SNC Ver.3.0 (pdf page 2) SNC Ver.3.0 (pdf page 3) Revised by SNC per Document No.: 5-56429 ABN H00330 Version 1.0 Document Ver.:

3.0 Vendor

JOHNSTON PUMP CO. By: BgT Checked: MWD Approved: WLN Date: 03/08/2007 DOCUMENT INSERTION SHEET E. I. Hatch Nuclear Plant - Unit No. 1 /2 RHR SERVICE WATER PUMP PERFORMANCE CURVES Description Remove

1.

This insertion sheet Existing Sheet(s)

2.

Letter from OEM dated July 21, 1986 -

Subject:

RHRSW, N/A PSW, Stand By Service Water Pumps, Submergence Requirements

3.

Attachment to Letter Dated July 21, 1986,

Subject:

Pump N/A Submergence of Plant Service Water Pumps... Document Insertion Sheet.dot Procedure: CM-003/CM-004 Insert Front of Manual SNC Ver.3.0 (pdf page 2) SNC Ver.3.0 (pdf page 3)

~oa""P NucJI!aI' ~ /JtfII.dDrt 2601 EaSt 34th SUeel ~ Tennessee 57407 Phone: (615) 629-]41S 0 TC'X: 81~573-5m {P1S-I~Yl July 21. 1986 SOUTHER" COMPA"Y SERVICES Post Off;ce Box 2625 SirDlingha ** Alabama 35202 AmrITIOH: Mr. Willi.. ~rner streJEC.T: RHRSW. PSW. Stand 8y Service Water Punps. Sublllergence Requi rements R£fERENCE: letter dated July 21. 1986 Pl~Bse refer to the attached sheet ~hen adjusting the submergence of the referenced pumps. If 1 c~n be of further assistance please do not hesitiate to call. Best Regards. JOHHSTOH PUMP C(JotPAHY ~~ Ger~ld D. Harrelson Nuclear Account Manager cc: JPCO Distribution Till long J Fa, 5-56429 SNC Ver.3.0 ~oa""P NucJI!aI' ~ /JtfII.dDrt 2601 EaSt 34th SUeel ~ Tennessee 57407 Phone: (615) 629-]41S 0 TC'X: 81~573-5m {P1S-I~Yl July 21. 1986 SOUTHER" COMPA"Y SERVICES Post Off;ce Box 2625 SirDlingha ** Alabama 35202 AmrITIOH: Mr. Willi.. ~rner streJEC.T: RHRSW. PSW. Stand 8y Service Water Punps. Sublllergence Requi rements R£fERENCE: letter dated July 21. 1986 Pl~Bse refer to the attached sheet ~hen adjusting the submergence of the referenced pumps. If 1 c~n be of further assistance please do not hesitiate to call. Best Regards. JOHHSTOH PUMP C(JotPAHY ~~ Ger~ld D. Harrelson Nuclear Account Manager cc: JPCO Distribution Till long J Fa, 5-56429 SNC Ver.3.0

en

  • 01 en

~ N CO en z (") (I) Co.) o \\ GEORGIA P(}.. _~ COMPANY PlANT E.l. HATCH

SUBJECT:

Pu~ Submergence of Plant Service Water Pumps RHR Service Water Pumps Stand-BY Service Water Pumps J\\)1f/' *.. July 21. 1986 SERVICE ~ Plant Service Water 24 fe-3 Stg. Wi GC-27S1-54 NE-3565-68 ~

  • 8500 g
  • 275 1 SUBMERGENCE REQUIRED OVER SUCTION BELL 48" W/O Suction Umbrella RHR Serv 1 ce Wa ter 18 DC-7 Stg.

GC-2755-58 NE-3561-64 Stand-By Service Water 12 EMC-3 St9. NG-2273

  • DESIGN CONDITIONS

, REDUCED FL~ 17000

  • 4000 13500
  • 700

'327'

  • 955' "036 1231.5 40" W/O Suction Urlbrel1a 32" WID Suction Umbrella 24" WI Suction Untrel1a 35" 24" IHE REDUCED FLOW AND SUBMERGENCE REFERENCED ABOVE SHOUtD HOT REDUCE THE SERVICE tlFE OF YOUR PUMPS.

FURTHER REDUCTION IN SUBMERGENCE PERIODICALLY SHOULD NOT CAUSE CATAsTROPHlt FAILURE SUT WILL REDUCE THE SERVICE LIFE SCIENTIFICALLY. en

  • 01 en

~ N CO en z (") (I) Co.) o \\ GEORGIA P(}.. _~ COMPANY PlANT E.l. HATCH

SUBJECT:

Pu~ Submergence of Plant Service Water Pumps RHR Service Water Pumps Stand-BY Service Water Pumps J\\)1f/' *.. July 21. 1986 SERVICE ~ Plant Service Water 24 fe-3 Stg. Wi GC-27S1-54 NE-3565-68 ~

  • 8500 g
  • 275 1 SUBMERGENCE REQUIRED OVER SUCTION BELL 48" W/O Suction Umbrella RHR Serv 1 ce Wa ter 18 DC-7 Stg.

GC-2755-58 NE-3561-64 Stand-By Service Water 12 EMC-3 St9. NG-2273

  • DESIGN CONDITIONS

, REDUCED FL~ 17000

  • 4000 13500
  • 700

'327'

  • 955' "036 1231.5 40" W/O Suction Urlbrel1a 32" WID Suction Umbrella 24" WI Suction Untrel1a 35" 24" IHE REDUCED FLOW AND SUBMERGENCE REFERENCED ABOVE SHOUtD HOT REDUCE THE SERVICE tlFE OF YOUR PUMPS.

FURTHER REDUCTION IN SUBMERGENCE PERIODICALLY SHOULD NOT CAUSE CATAsTROPHlt FAILURE SUT WILL REDUCE THE SERVICE LIFE SCIENTIFICALLY.

See S-53448 for original RHRSWpump performance curves SNC REV. 2 See S-53448 for original RHRSWpump performance curves SNC REV. 2

c JOHNSTON PUMP COMPANY Nuclear Service Division September 18, 2000 Southern Nuclear Operating Company Nuclear Administration 40 Inverness Center Parkway Birmingham, AI 35202 Attention: Rozell Harris This letter is to inform you of a possible condition with respect to the pump(s) supplied to you pursuant to Purchase Order Numbers shown on NCR Attachment which may require a report to the Nuclear Regulatory Commission under 10 C.F.R. Part 21. At this point we are continuing our evaluations, and we may determine that there is in fact no deviation from the applicable procurement specifications. Moreover, we have substantial experience and expertise with pumps of this type, and based on what we know to date it may very well be that this condition would not create a substantial safety hazard. N~vertheless, in accordance with 10 C.F.R. \\21.21 (b), we request your assistance in making these determinations I I, The condition involves the hydraulic testing that was performed at our Test Laboratory'. T~t re..sults suggest that the pump flow may have been overstated _by a factor of up to 3.8%. We are continuing to evaluate the matter, but enclosed with this letter are corrected pump curves. Your cooperation is appreciated inasmuch as a definitive determination whether a Part 21 report is required cannot be made without more detailed knowledge of your system and license requirements. We would appreciate a response by 12 October 2000. Please contact Mr. Tommy Craig, Quality Assurance Manager, with your response or any questions. We are committed to the highest quality standards, therefore we respectfully request your assistance in this matter. Sincerely Edward Hang President Johnston Pump Company o rf ')) 2601 East 34th Street 0 Chattanooga, Tennessee 37407 FAX 423/698-1447 Telephone: 423/629-1415 HOTLINE 1-800-227-2601 c JOHNSTON PUMP COMPANY Nuclear Service Division September 18, 2000 Southern Nuclear Operating Company Nuclear Administration 40 Inverness Center Parkway Birmingham, AI 35202 Attention: Rozell Harris This letter is to inform you of a possible condition with respect to the pump(s) supplied to you pursuant to Purchase Order Numbers shown on NCR Attachment which may require a report to the Nuclear Regulatory Commission under 10 C.F.R. Part 21. At this point we are continuing our evaluations, and we may determine that there is in fact no deviation from the applicable procurement specifications. Moreover, we have substantial experience and expertise with pumps of this type, and based on what we know to date it may very well be that this condition would not create a substantial safety hazard. N~vertheless, in accordance with 10 C.F.R. \\21.21 (b), we request your assistance in making these determinations I I, The condition involves the hydraulic testing that was performed at our Test Laboratory'. T~t re..sults suggest that the pump flow may have been overstated _by a factor of up to 3.8%. We are continuing to evaluate the matter, but enclosed with this letter are corrected pump curves. Your cooperation is appreciated inasmuch as a definitive determination whether a Part 21 report is required cannot be made without more detailed knowledge of your system and license requirements. We would appreciate a response by 12 October 2000. Please contact Mr. Tommy Craig, Quality Assurance Manager, with your response or any questions. We are committed to the highest quality standards, therefore we respectfully request your assistance in this matter. Sincerely Edward Hang President Johnston Pump Company o rf ')) 2601 East 34th Street 0 Chattanooga, Tennessee 37407 FAX 423/698-1447 Telephone: 423/629-1415 HOTLINE 1-800-227-2601

JUHN::; I UN t"UMt-' I;UMt-'AN Y. NONCONFORMANCE REPORT NCR I DESCRIPTION PAGE 1 OF 2 DATE JOB NUMBER i SHOP ORDER NO. I PART NO. I PART NAME ~ N/A I N/A I N/A ~/l8/00 SEE ATTACHED i : I MATERIAL TYPE

PATTERN NO.

I LAST OPER. COMPo QTY. N/A N/A SEE I N/A ATTACHED SUPPLIER P.O. NO. I CORRECTIVE ACTION REQ'D. JOHNSTON PUMP COMPANY BROOKSHIRE, TEXAS SEE ATTACHED I 00-009 LOCATION 0 MACHINE SHOP 0 RECEIVING CJ STORAGE 0 WELDING 0 HYDRO at SUPPLIER 0 PAINT D ASSEMBLY SHIPPING 0 OTHER w DETAILS OF NONCONFORMANCE: INCORRECT HYDRAULIC PERFORMANCE TEST RESULTS OF 3.8% ON FLOW, TO JOHNSTON PUMP PURCHASE ORDER REQUIREMENTS ./i INSPECTO~~~" '?~.I'/oO DATE v DISPOSITION ~NITIAL DISPOSITION: [j REWORKJ 0 REPLACE ARTS, xx MRB ~ ~fl/~" q;j~o po- ~bd'-- f~/;:"p(/ PROJECT ENGINEER DATE QA ENGINEER DATE / I I MRB DISPOSITION: o USE*AS*IS 0 REPAIR 0 REWORK 0 ~CRAP 0 RTS CORRECTED HYDRAULIC CURVES TO BE REVIEWED BY ENGINEERING AND COMPARED TO COMMENTS: CUSTOMER SPECIFICATION AND/OR PURCHASE ORDER REQUIREMENTS.

1)

CORRECTED CURVES TO THE LATEST DESIGN REQUIREMENTS, ACCEPT AS-IS. SEE CURVES ATTACHED

2)

CORRECTED CURVES WHERE PERFORMANCE DOES NOT MEET DESIGN REQUIREMENTS. THESE CONDITION REQUIRE FINAL REVIEW AND CUSTOMER ACCEPTANCE AS-IS. SEE ATTACHED CURVES. NOTE: PLEASE 'ACKNO~~EDGE ACCEPTANCE BX SIGNATURE AND RETURN OF THIS NONCONFORMANCE. /U-p:(;- ?-!/:-tflP t:.,~ ~#~~P MANAG~ ENGR. DATE QUAL lASSUR.~ DATE CUSTOMER/ANI DATE MANUFACTURING INSTRUCTIONS OPER' I DEPT. WP: HP OPERATION PROC. TOOLING A B C MANF. QC NO. NO. I NO. 005 I ENG IA REVIEW TEST CURVES I, I I I I ~~, I I I I I I I I I i I I I I I I form 10... *1 PRODUCTION CONTROL COST DEP I. JUHN::; I UN t"UMt-' I;UMt-'AN Y. NONCONFORMANCE REPORT NCR I DESCRIPTION PAGE 1 OF 2 DATE JOB NUMBER i SHOP ORDER NO. I PART NO. I PART NAME ~ N/A I N/A I N/A ~/l8/00 SEE ATTACHED i : I MATERIAL TYPE

PATTERN NO.

I LAST OPER. COMPo QTY. N/A N/A SEE I N/A ATTACHED SUPPLIER P.O. NO. I CORRECTIVE ACTION REQ'D. JOHNSTON PUMP COMPANY BROOKSHIRE, TEXAS SEE ATTACHED I 00-009 LOCATION 0 MACHINE SHOP 0 RECEIVING CJ STORAGE 0 WELDING 0 HYDRO at SUPPLIER 0 PAINT D ASSEMBLY SHIPPING 0 OTHER w DETAILS OF NONCONFORMANCE: INCORRECT HYDRAULIC PERFORMANCE TEST RESULTS OF 3.8% ON FLOW, TO JOHNSTON PUMP PURCHASE ORDER REQUIREMENTS ./i INSPECTO~~~" '?~.I'/oO DATE v DISPOSITION ~NITIAL DISPOSITION: [j REWORKJ 0 REPLACE ARTS, xx MRB ~ ~fl/~" q;j~o po- ~bd'-- f~/;:"p(/ PROJECT ENGINEER DATE QA ENGINEER DATE / I I MRB DISPOSITION: o USE*AS*IS 0 REPAIR 0 REWORK 0 ~CRAP 0 RTS CORRECTED HYDRAULIC CURVES TO BE REVIEWED BY ENGINEERING AND COMPARED TO COMMENTS: CUSTOMER SPECIFICATION AND/OR PURCHASE ORDER REQUIREMENTS.

1)

CORRECTED CURVES TO THE LATEST DESIGN REQUIREMENTS, ACCEPT AS-IS. SEE CURVES ATTACHED

2)

CORRECTED CURVES WHERE PERFORMANCE DOES NOT MEET DESIGN REQUIREMENTS. THESE CONDITION REQUIRE FINAL REVIEW AND CUSTOMER ACCEPTANCE AS-IS. SEE ATTACHED CURVES. NOTE: PLEASE 'ACKNO~~EDGE ACCEPTANCE BX SIGNATURE AND RETURN OF THIS NONCONFORMANCE. /U-p:(;- ?-!/:-tflP t:.,~ ~#~~P MANAG~ ENGR. DATE QUAL lASSUR.~ DATE CUSTOMER/ANI DATE MANUFACTURING INSTRUCTIONS OPER' I DEPT. WP: HP OPERATION PROC. TOOLING A B C MANF. QC NO. NO. I NO. 005 I ENG IA REVIEW TEST CURVES I, I I I I ~~, I I I I I I I I I i I I I I I I form 10... *1 PRODUCTION CONTROL COST DEP I.

c c c NONCONFORMANCE ATTACHMENT NCR-2033 Page 2 of2 Georgia Power Company JIP Job Customer Purchase Customer Nwnber Order Number Specification 94JC1500S 60139820000 SS-2105-6 94JC1501S 60139820000 SS-2105-6 94JC1502S 60] 39820000 SS-2105-6 94JC1503S 60178650000 SS-2105-6 94JC1504S 60178650000 SS-2]05-6 96JC1500S 60244490000 SS-2105-6 96JC1501S 60244490000 SS-2105-6 96JC1503S 60270210000 SS-21 05-6 98JC1504S 6034852 SS-2105-6 98JC1509S 6038116 SS-2105-6 99JC1508S 604]879 S8-2105-6 Result Legend: S = Satisfactory to Customer Specification U = Does not meet Customer Specification Results S U U S S U S U U U U JIP Order No. TE-] 1325 TE-11347 TE-11326 TE-11605 TE-11606 TE-12935 TE-13141 TE-13241 TE-14341 TE-14868 TE-15559 Comments c c c NONCONFORMANCE ATTACHMENT NCR-2033 Page 2 of2 Georgia Power Company JIP Job Customer Purchase Customer Nwnber Order Number Specification 94JC1500S 60139820000 SS-2105-6 94JC1501S 60139820000 SS-2105-6 94JC1502S 60] 39820000 SS-2105-6 94JC1503S 60178650000 SS-2105-6 94JC1504S 60178650000 SS-2]05-6 96JC1500S 60244490000 SS-2105-6 96JC1501S 60244490000 SS-2105-6 96JC1503S 60270210000 SS-21 05-6 98JC1504S 6034852 SS-2105-6 98JC1509S 6038116 SS-2105-6 99JC1508S 604]879 S8-2105-6 Result Legend: S = Satisfactory to Customer Specification U = Does not meet Customer Specification Results S U U S S U S U U U U JIP Order No. TE-] 1325 TE-11347 TE-11326 TE-11605 TE-11606 TE-12935 TE-13141 TE-13241 TE-14341 TE-14868 TE-15559 Comments

r ~ D:: ~ 0 0-W f/) D:: 0 :C. W ~ ~ m Johnston P.,-., Company Brooksh',_. texas Customer: Georgia Power Company Job # 94JC1500S SIN: SNRU 6504 POF#: 66303 TC#: 07365 Rev. # 1* n() 1770 RPM 1900~-;;;'-;:~-r~~~~~~~~~--____ ~ ____ T-____ ~ __ ~~~ __ ~ ____ ~ ____ ~ __ ~-,r;;;-:T95.0 --:*-t*-~-*~ * - .. *~--:--t*.. ~* -

  • - *!**-!-**~-*t-*.. ~-.~... :-.. ~.-

-*t**1-*-t--~-- ::t::t:::::t: :::t::t::t::!:: :::::t::::::t:: ::!::t:t:t:: ::t::~:::::t: :::!:::~::t::!:: ::t:~:::t::t:: ::::::::t:::::: ::t:::::!::t:

: ;::~ : :~: :~:: ::~::~::;::~:: ::;::~ : :;::~:: ::~::~: : ~::~:: ::f::~::~::~:.. ~--~-. ;**i-- -.+-.;... ~-.~. -

.-~.-~.--}... ;... -*l** ~.. i* *':*....... ~.... ~... ;.. i**..... :,.. ;.-.~ -. ;.. -.. ;.-~. -.:... a;' e. -. ;. - ~... i o... :....... 0;" -l* -;.... i-.. ~:~:~~::~::~:: ::~::~::~::~:.: ::~::~::!::~:: :::--~-.~.--:.-. --~.-:.. :.. ~... -:::~::~~:~~~ :~~::~~:~ : ~~:~ :~::~~~~~~ ~ ~~~~ : ~~~~~~~~: : ~~~ -90.0 ..*........*.... _..*..*.......*..*.. _..*.. *:I%BOWL EFFICIENCYI~***** * *****..*..*...*..*..........*..*..............*...

~::~: : !::~:: ::;:;~: :f::::: ::~ : :~::~::t:: ::. ~

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500

~::~::~:: :}.~:::::~:: ::~::~::::~: Bowl Mill Coating: SA351-CF8M I Plasite 7122
:~::~:::::~:: ::;::~::~::~:: ::~:::::;::;:: ::~:::~;;t~~ ~;~;~:: ::;::;.. ;.. ;.. 25.0
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400 ";";"~'~¥1".. ~.. ;.. ;.. ;.... ~.. ~... ~.. ~. Certified By: Ernie Rodrlg;7I-uez AUU{jgust 23, 1994 .. ;.. ;.. ;.. **~**~**~**f*.......... ;.... ;.. ~i~- ... ~.~ ~ ... ;.. ;.. 20.0 ..*..*..,......*..*..*..*....,.. ~..*..*. Rev.1: Performance co du measurement ..*..*..... *****~******:ICORRECTED HEAD - CAPACITY W*.....,....*.......... :;:: 300

~:::::~:::.: ::::~::~::!:: ::~::~:::::: error. R.H.D.

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500

~::~::~:: :}.~:::::~:: ::~::~::::~: Bowl Mill Coating: SA351-CF8M I Plasite 7122
:~::~:::::~:: ::;::~::~::~:: ::~:::::;::;:: ::~:::~;;t~~ ~;~;~:: ::;::;.. ;.. ;.. 25.0
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400 ";";"~'~¥1".. ~.. ;.. ;.. ;.... ~.. ~... ~.. ~. Certified By: Ernie Rodrlg;7I-uez AUU{jgust 23, 1994 .. ;.. ;.. ;.. **~**~**~**f*.......... ;.... ;.. ~i~- ... ~.~ ~ ... ;.. ;.. 20.0 ..*..*..,......*..*..*..*....,.. ~..*..*. Rev.1: Performance co du measurement ..*..*..... *****~******:ICORRECTED HEAD - CAPACITY W*.....,....*.......... :;:: 300

~:::::~:::.: ::::~::~::!:: ::~::~:::::: error. R.H.D.

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c c ( JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: TC-07365 ROY. 0 Job Number: 94JC1500S eu.. tomer: Georgie Power Company Modell Stages: 180C 17 Test Imp. Die {in): 13.75 (With Wing Tips) Job Imp. Oia [in): TBF I Ct..:.063" I'e-Imp. Material: SA.351-CFBM Bowl Msterial: SA.351-CFBM Bowl Coating: P1asite 7122 Suction: Bell* 1.0. Coated Test D. Hud: Lab 16" H.P. Discharge Head Test Col.: Lab T epperec:t Column Pipe Test Constants; Flow: 635.226 Head: 2.31 Pipe Cia. a Gage lin): water To Floor pn): Floor To Gauge rill): psi tap on Bowl or heed eoWt 16 12 60 Motor H.P. I R.P.M.: 150 I 880 PH/CY/V: 3160/480 Motor SIN: 1118661 Job OR Lab Motor: Lab Wattmeter No.: 112 Test line Size [in): 16" Orfic:e Diameter [111): 7.0209 Pressure Gage [p&I): o* 300 Impeller Adjustment: Two Turns DESIGN Q R.P.M.: 1nO G.P.M.: 4000 Head [It): 955 S.H.P.: Elficiency: 0.00 Specific GrMy 1: Specific GrMy 2: Item No.: Fluid: Application: End IJaer. Georgia Pcwer Company SIte: Tag: Take Shut* 011 (Yes I No): YES Wllter Temperature: 0 Tat Point. 1 2 3 ~ 5 6 7 Della "P" {inHgl 10.1 0.7 3.0 7.3 8.2 9.2 10.1 Gallons Per Minute 2019 531 1100 1716 1819 1927 2019 G8ge R.adtna ['*I 105.0 1~6.5 133.7 116.0 : 112.5 109.0 105.0 Headjftl 2~2.6 338. ~ 308.8 268.0 259.9 251.B 242.6 aage EIev.CoIT. [It 6.00 6.00 6.00 6.00 6.00 6.00 6.00 Velocity Heed loll [It) 0.2 0.0 0.0 0.1 0.1 0.1 0.2 ToIIII Heed 1ft) 248.7 344. ~ 31<4.9 27<4.1 266.0 257.9 248.7 Watt Reading [kW) 119.8 97.2 105.7 116.0 117.6 118.9 119.3 InputH.P. 160.6 130.3 141.7 155.5 157.6 159. ~ 159.9 Motor EIIiciency 0.9 0.9 0.9 0.9 0.9 0.9 0.9 B.H.P. 144.5 117.3 127.5 139.9 141.9 143.4 143.9 Teat RP.M.: 888.0 891.0 890.0 888.0 888.0 888.0 888.0 ORIGINAL TEST DATA Rated R.P.M.: 1no 1no 1no 1nO 1no 1no 1no G811on1 Per Minute: 402<C 1056 2188 3<421 3626 3840 4024 Total 0iIeharge Head [II): 988.1 1359.2 1245.5 1088.9 1056.8 1024.8 988.1 B.H.P.G 1.0 Sp.Gr.: 1144.6 11111.3 1003.1 1108.3 1123.5 1138.0 1139.8 B.H.P.Q Sp.Gr.1: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bowl EJIIcIency: 0.8n 0.394 0.686 0.849 0.861 0.875 0.881 B 12.0 2200 96.5 222.9 6.00 0.2 229.1 118.5 158.8 0.9 143.0 888.0 1nO 4386 910.2 1132.1 0.00 0.891 Comments: Test the bawl assembly only using a test lab discharge head and column pipe at reduced speed with II test Lab Motor Serial Number: SNRU 6504 Jab Numt-: 84JC15OO5 Chattanooga P.O. Number: TE*11325 Cultorner P.O. Number. -=-:-~=~ POF Number: SJC 66303 Project Manager: ___ _ 9 10 11 12 15.0 1B.0 21.0 24.0 2460 2S5 2811 3112 83.0 73.3 62.5 SO.5 191.7 169.31 144. ~ 116.7 6.00 6.00 6.00 6.00 0.2 0.3 0.3 0.4 198.0 175.6 1SO.7 123.0 116.7 11<C.S1 111.5 106.8 156.4 154.0 1~9. 5 143.2 0.9 0.9 0.9 0.9 140.8 138.6 13<4.5 128.8 888.0 888.0 889.0 889.0 1no 1nO 1nO 1nO 4904 5372 5798 6196 786.5 697.7 597.4 487.7 1115.0 1097.8 1081.7 1016.9 0.00 0.00 0.00 0.00 0.874 0.862 0.82~ 0.7SO 13 28.0 3361 31.5 72.8 6.00 0.4 79.2 97.2 130.3 0.9 117.3 890.0 1nO 6685 313.3 922.4 0.00 0.573 1~ 0.0 0 152.0 351.1 6.00 0.0 357.1 87.5 117.3 0.9 105.6 8112.0 1nO 0 1406.1 824.8 0.00 0.000 NEW DATA BASED ON FlOW CORRECTION Rated RP.M.: 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 0aII0na Per Minute: 3873 10111 2106 3293 3490 3696 3873 4221 4720 5170 5578 59113 6434 0 TcUI DIIchaIge Haad [It): 988.1 1359.2 1245.5 1088.9 1056.8 102~.8 988.1 910.2 786.5 697.7 587.4 487.7 313.3 1406.1 B.H.P.G 1.0 Sp.Gr.: 1144.& 1119.3 1003.1 1108.3 1123.5

  • 1136.0 1139.8 1132.1 1115.0 1097.8 1061.7 1016.11 922.<4 824.8 B.H.P.G Sp.Gr.1:

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. ~~~~0.~37_9~_0_.~~~_0~ .8~1~7~~0~.829~~_0~.842~~_0~.84B~~~0.857~~_0~.~~1~_0~1.~~~~0~.7_~~~0~.7=22~~0~.~~~~0~.000~-J II..- T estad By : Darryl CIIIrk Jr. CertiIIed By: ErnIe Rodriguez.v.L\\.....) WItn5Ied By. __________ Date r:I Test :.,;.";;;:V::;"=23;,:..' 1.;,;;8$4.;:..;... ____ _ c c ( JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: TC-07365 ROY. 0 Job Number: 94JC1500S eu.. tomer: Georgie Power Company Modell Stages: 180C 17 Test Imp. Die {in): 13.75 (With Wing Tips) Job Imp. Oia [in): TBF I Ct..:.063" I'e-Imp. Material: SA.351-CFBM Bowl Msterial: SA.351-CFBM Bowl Coating: P1asite 7122 Suction: Bell* 1.0. Coated Test D. Hud: Lab 16" H.P. Discharge Head Test Col.: Lab T epperec:t Column Pipe Test Constants; Flow: 635.226 Head: 2.31 Pipe Cia. a Gage lin): water To Floor pn): Floor To Gauge rill): psi tap on Bowl or heed eoWt 16 12 60 Motor H.P. I R.P.M.: 150 I 880 PH/CY/V: 3160/480 Motor SIN: 1118661 Job OR Lab Motor: Lab Wattmeter No.: 112 Test line Size [in): 16" Orfic:e Diameter [111): 7.0209 Pressure Gage [p&I): o* 300 Impeller Adjustment: Two Turns DESIGN Q R.P.M.: 1nO G.P.M.: 4000 Head [It): 955 S.H.P.: Elficiency: 0.00 Specific GrMy 1: Specific GrMy 2: Item No.: Fluid: Application: End IJaer. Georgia Pcwer Company SIte: Tag: Take Shut* 011 (Yes I No): YES Wllter Temperature: 0 Tat Point. 1 2 3 ~ 5 6 7 Della "P" {inHgl 10.1 0.7 3.0 7.3 8.2 9.2 10.1 Gallons Per Minute 2019 531 1100 1716 1819 1927 2019 G8ge R.adtna ['*I 105.0 1~6.5 133.7 116.0 : 112.5 109.0 105.0 Headjftl 2~2.6 338. ~ 308.8 268.0 259.9 251.B 242.6 aage EIev.CoIT. [It 6.00 6.00 6.00 6.00 6.00 6.00 6.00 Velocity Heed loll [It) 0.2 0.0 0.0 0.1 0.1 0.1 0.2 ToIIII Heed 1ft) 248.7 344. ~ 31<4.9 27<4.1 266.0 257.9 248.7 Watt Reading [kW) 119.8 97.2 105.7 116.0 117.6 118.9 119.3 InputH.P. 160.6 130.3 141.7 155.5 157.6 159. ~ 159.9 Motor EIIiciency 0.9 0.9 0.9 0.9 0.9 0.9 0.9 B.H.P. 144.5 117.3 127.5 139.9 141.9 143.4 143.9 Teat RP.M.: 888.0 891.0 890.0 888.0 888.0 888.0 888.0 ORIGINAL TEST DATA Rated R.P.M.: 1no 1no 1no 1nO 1no 1no 1no G811on1 Per Minute: 402<C 1056 2188 3<421 3626 3840 4024 Total 0iIeharge Head [II): 988.1 1359.2 1245.5 1088.9 1056.8 1024.8 988.1 B.H.P.G 1.0 Sp.Gr.: 1144.6 11111.3 1003.1 1108.3 1123.5 1138.0 1139.8 B.H.P.Q Sp.Gr.1: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bowl EJIIcIency: 0.8n 0.394 0.686 0.849 0.861 0.875 0.881 B 12.0 2200 96.5 222.9 6.00 0.2 229.1 118.5 158.8 0.9 143.0 888.0 1nO 4386 910.2 1132.1 0.00 0.891 Comments: Test the bawl assembly only using a test lab discharge head and column pipe at reduced speed with II test Lab Motor Serial Number: SNRU 6504 Jab Numt-: 84JC15OO5 Chattanooga P.O. Number: TE*11325 Cultorner P.O. Number. -=-:-~=~ POF Number: SJC 66303 Project Manager: ___ _ 9 10 11 12 15.0 1B.0 21.0 24.0 2460 2S5 2811 3112 83.0 73.3 62.5 SO.5 191.7 169.31 144. ~ 116.7 6.00 6.00 6.00 6.00 0.2 0.3 0.3 0.4 198.0 175.6 1SO.7 123.0 116.7 11<C.S1 111.5 106.8 156.4 154.0 1~9. 5 143.2 0.9 0.9 0.9 0.9 140.8 138.6 13<4.5 128.8 888.0 888.0 889.0 889.0 1no 1nO 1nO 1nO 4904 5372 5798 6196 786.5 697.7 597.4 487.7 1115.0 1097.8 1081.7 1016.9 0.00 0.00 0.00 0.00 0.874 0.862 0.82~ 0.7SO 13 28.0 3361 31.5 72.8 6.00 0.4 79.2 97.2 130.3 0.9 117.3 890.0 1nO 6685 313.3 922.4 0.00 0.573 1~ 0.0 0 152.0 351.1 6.00 0.0 357.1 87.5 117.3 0.9 105.6 8112.0 1nO 0 1406.1 824.8 0.00 0.000 NEW DATA BASED ON FlOW CORRECTION Rated RP.M.: 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 0aII0na Per Minute: 3873 10111 2106 3293 3490 3696 3873 4221 4720 5170 5578 59113 6434 0 TcUI DIIchaIge Haad [It): 988.1 1359.2 1245.5 1088.9 1056.8 102~.8 988.1 910.2 786.5 697.7 587.4 487.7 313.3 1406.1 B.H.P.G 1.0 Sp.Gr.: 1144.& 1119.3 1003.1 1108.3 1123.5

  • 1136.0 1139.8 1132.1 1115.0 1097.8 1061.7 1016.11 922.<4 824.8 B.H.P.G Sp.Gr.1:

0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 ~. ____ ~BowI~~B~ma.~

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~0~

. ~~~~0.~37_9~_0_.~~~_0~ .8~1~7~~0~.829~~_0~.842~~_0~.84B~~~0.857~~_0~.~~1~_0~1.~~~~0~.7_~~~0~.7=22~~0~.~~~~0~.000~-J II..- T estad By : Darryl CIIIrk Jr. CertiIIed By: ErnIe Rodriguez.v.L\\.....) WItn5Ied By. __________ Date r:I Test :.,;.";;;:V::;"=23;,:..' 1.;,;;8$4.;:..;... ____ _

~:~. n o S()() 1000 1500 2000 2500 3000 3500 40()() U.S. GALLONS PER MINUTE 45(10 5000 ssoo nn CiCIOI) (,501) 7000 ~:~. n o S()() 1000 1500 2000 2500 3000 3500 40()() U.S. GALLONS PER MINUTE 45(10 5000 ssoo nn CiCIOI) (,501) 7000

JOHNSTON PUMP *COMPANY PERFORMANCE TEST SET -up AND TeST DATA SHEET C NO.: Numb.,: Cuatom.,: e el/Stag.a: Dla.: /Cl.: Imp. Mat.,IaI: Bowl M...,IaI: Bowl CoeIing: Suction: Teat O. Head: Teat Col.: T.at Conatants; Flow: Head: TC-07385 R.v.I:O 114JC1500S Georgi. Power Comp.ny laDC / 7 13.750 'With "Wing Tip.' .083" / *C* SA351-CFIM SA351-CFIM Plaslta 7122 Bal - 1.0. Co.ted l.b,.,. H.P. Oi.charg. Head lab T.ppered Column Pip. 835.228 2.31 Pipe Oi *. @ Gag.: 18.000 Motor Eft. : 100,,: 75 %: 50": Water To Floor: loor 0 F T Ga ug.: Teat Point # O... *p* ~, na Per Minute .R_dlng .. MtofH_d Ga ** EJev.Corr. -CTelocity Head lou Total Head Watt R.. dlng: Input H.P.*. Motor Effici.ncy B.H.P. Teat R.P.M.: Volta: (Ref.Only) Amp. (R.f.Only) : VIbration in Mil.: Rated R.P.M.: GaIIona Per MinUte: Total Head in Feat: 12 INCHES ---INCHES 80 1 2 10.10 0.70 2019 531 105.00 148.50 242.55 331.42 11.00 IS.OO 0.18 0.01 248.71 34..... 3 I 1111.80 87.20 180.5111 130.2l1 O.lIOO 0.1100 144.53 117.27 as8 Ul I I 1770 1770 4024 1056 988.1 1359.2 B.H.P.@ 1.0 sp.Gr.J 1 144.6 919.3 3 3.00 1100 133.70 301.15 '.00 0.05 314.18 105.70 141.'111 0.11100 127.52 ilia 1770 2188 1245.5 1003.1 4 7.30 1718 118.00 21S7.911 11.00 0.12 274.08 118.00 155.50 O.lIOO Motor H.P./ R.P.M.: PH I CY IV: Motor S, N: Job OR lab Motor: Wattm.ter No.: Or1ic. Diamat.,: Tut Ina Siz.: Pr... ur. Gag.: Impell., AdJustm.nt: DESIGN @ R.P.M.: G.P.M.: H.ad: B.H.P.: Effici.ncy: Sp.citlc Gravity 1: Specific Gravity 2: Item No.: Fluid: Ap!'Ii... tla": 150/110 3/80 '410 LAB

  1. 2 7.0208 18 300 Two Turn.

1770 4000 1155.00 1.00 0.00 Comments: T.at the bowl **** mbly only uaing

  • t ** t lab di.charg. head.nd column pip. at reduced.peed with
  • tat lab motol.

I Test Procedure #: JP-TP-0069 Rev.#j Serial #: SNRU 6504 Job #: 94JC1500S End u *.,Georgia Power Company Sit.: POF#: ~6~6~3~O~3~ __________ __ Chattanooga P.0.#:TE -11325 Tak. Shut - Off (y ** ' No): YES 5 IS 7 I II 10 t1 12 I 13 14 1.20 8.20 10.10 12.00 15.00 11.00 21.00 24.00 21.00 0.00 i 2011 31121 1118 1927 2018 2200 241S0 2885 3381 0 112.50 108.00 105.00 88.50 13.00 73.30 112.50 50.50 31.50 152.00 250." 251.70 242.55 222.112 "1.73 1IS0.32 144.31 118.1S11 72.77 351.12 IS.OO IS.OO 8.00 8.00 8.00 8.00 8.00 I 8.00 IS.OO 11.00 0.13 0.15 0.11S 0.10 0.24 0.211 0.33 0.38 0.451 0.00 2IU'.01 I 257.8" 2"8.71 228.11 187.117 175.81 150.71 123.04 70.21 I 357.12 117.80 118.110 1111.30 118.50 118.70 114.110 111.501 108.80 87.20 I 87.50 I 157.114 159.31 158.82 151.85 15.... 3 154.02 ,41U8 143.18 130.20 117.2111 O.lIoo 0.1100 O.lIOO 0.1100 0.000 O.lIOO 0.1100 0.1100 0.800 0.900 1311.lI51 141.88 143.45 143.113 142.118 I 140.711 138.1S2 134.52 128.15 117.27 105.58 8a8 aas 888 8as sa8 888 881 as8 188 11110 I 192 I I I I I I I I I 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 ' 3421 3626 3840 4024 4386 4904 5372 5802 6196 66851 0 1088.9 1056.8 1024.8 988.1 910.2 786.5 697.7 598.8 487.7 313.311406.1 1108.3 1123.5 1136.0 1139.8 1132.1 1115.0 1097.8 1065.3 1016.9 I 922.4. 824.8 B.H.P.@Sp.Gr.l : It 144.6 919.3 1003.1 111 08.3 1123.5 1136.0 1139.8' 1132.1 1115.0 1097.8 1065.3 1016.91 922.4; 824.8 B.H.P.@ Sp.Gr.2: I 0.0 0.0 0.0 0.01 0.0 0.0 0.01 0.0 0.0 0.0 0.0 0.01 0.0 0.0 ( ncv: 0.877 0.394 0.6861 0.849 0.861 0.875 0.881 0.891 0.8.24, hO.862 0.824 i 0.7501 0.573 0.000 ~ad Sy : Da":tl C kark Jr. C attifIad By : Erni. ROdriau~ ~.

  • **** d By :

Oat. Of T ** t: August 23. 1ee4. \\ JOHNSTON PUMP *COMPANY PERFORMANCE TEST SET -up AND TeST DATA SHEET C NO.: Numb.,: Cuatom.,: e el/Stag.a: Dla.: /Cl.: Imp. Mat.,IaI: Bowl M...,IaI: Bowl CoeIing: Suction: Teat O. Head: Teat Col.: T.at Conatants; Flow: Head: TC-07385 R.v.I:O 114JC1500S Georgi. Power Comp.ny laDC / 7 13.750 'With "Wing Tip.' .083" / *C* SA351-CFIM SA351-CFIM Plaslta 7122 Bal - 1.0. Co.ted l.b,.,. H.P. Oi.charg. Head lab T.ppered Column Pip. 835.228 2.31 Pipe Oi *. @ Gag.: 18.000 Motor Eft. : 100,,: 75 %: 50": Water To Floor: loor 0 F T Ga ug.: Teat Point # O... *p* ~, na Per Minute .R_dlng .. MtofH_d Ga ** EJev.Corr. -CTelocity Head lou Total Head Watt R.. dlng: Input H.P.*. Motor Effici.ncy B.H.P. Teat R.P.M.: Volta: (Ref.Only) Amp. (R.f.Only) : VIbration in Mil.: Rated R.P.M.: GaIIona Per MinUte: Total Head in Feat: 12 INCHES ---INCHES 80 1 2 10.10 0.70 2019 531 105.00 148.50 242.55 331.42 11.00 IS.OO 0.18 0.01 248.71 34..... 3 I 1111.80 87.20 180.5111 130.2l1 O.lIOO 0.1100 144.53 117.27 as8 Ul I I 1770 1770 4024 1056 988.1 1359.2 B.H.P.@ 1.0 sp.Gr.J 1 144.6 919.3 3 3.00 1100 133.70 301.15 '.00 0.05 314.18 105.70 141.'111 0.11100 127.52 ilia 1770 2188 1245.5 1003.1 4 7.30 1718 118.00 21S7.911 11.00 0.12 274.08 118.00 155.50 O.lIOO Motor H.P./ R.P.M.: PH I CY IV: Motor S, N: Job OR lab Motor: Wattm.ter No.: Or1ic. Diamat.,: Tut Ina Siz.: Pr... ur. Gag.: Impell., AdJustm.nt: DESIGN @ R.P.M.: G.P.M.: H.ad: B.H.P.: Effici.ncy: Sp.citlc Gravity 1: Specific Gravity 2: Item No.: Fluid: Ap!'Ii... tla": 150/110 3/80 '410 LAB

  1. 2 7.0208 18 300 Two Turn.

1770 4000 1155.00 1.00 0.00 Comments: T.at the bowl **** mbly only uaing

  • t ** t lab di.charg. head.nd column pip. at reduced.peed with
  • tat lab motol.

I Test Procedure #: JP-TP-0069 Rev.#j Serial #: SNRU 6504 Job #: 94JC1500S End u *.,Georgia Power Company Sit.: POF#: ~6~6~3~O~3~ __________ __ Chattanooga P.0.#:TE -11325 Tak. Shut - Off (y ** ' No): YES 5 IS 7 I II 10 t1 12 I 13 14 1.20 8.20 10.10 12.00 15.00 11.00 21.00 24.00 21.00 0.00 i 2011 31121 1118 1927 2018 2200 241S0 2885 3381 0 112.50 108.00 105.00 88.50 13.00 73.30 112.50 50.50 31.50 152.00 250." 251.70 242.55 222.112 "1.73 1IS0.32 144.31 118.1S11 72.77 351.12 IS.OO IS.OO 8.00 8.00 8.00 8.00 8.00 I 8.00 IS.OO 11.00 0.13 0.15 0.11S 0.10 0.24 0.211 0.33 0.38 0.451 0.00 2IU'.01 I 257.8" 2"8.71 228.11 187.117 175.81 150.71 123.04 70.21 I 357.12 117.80 118.110 1111.30 118.50 118.70 114.110 111.501 108.80 87.20 I 87.50 I 157.114 159.31 158.82 151.85 15.... 3 154.02 ,41U8 143.18 130.20 117.2111 O.lIoo 0.1100 O.lIOO 0.1100 0.000 O.lIOO 0.1100 0.1100 0.800 0.900 1311.lI51 141.88 143.45 143.113 142.118 I 140.711 138.1S2 134.52 128.15 117.27 105.58 8a8 aas 888 8as sa8 888 881 as8 188 11110 I 192 I I I I I I I I I 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 ' 3421 3626 3840 4024 4386 4904 5372 5802 6196 66851 0 1088.9 1056.8 1024.8 988.1 910.2 786.5 697.7 598.8 487.7 313.311406.1 1108.3 1123.5 1136.0 1139.8 1132.1 1115.0 1097.8 1065.3 1016.9 I 922.4. 824.8 B.H.P.@Sp.Gr.l : It 144.6 919.3 1003.1 111 08.3 1123.5 1136.0 1139.8' 1132.1 1115.0 1097.8 1065.3 1016.91 922.4; 824.8 B.H.P.@ Sp.Gr.2: I 0.0 0.0 0.0 0.01 0.0 0.0 0.01 0.0 0.0 0.0 0.0 0.01 0.0 0.0 ( ncv: 0.877 0.394 0.6861 0.849 0.861 0.875 0.881 0.891 0.8.24, hO.862 0.824 i 0.7501 0.573 0.000 ~ad Sy : Da":tl C kark Jr. C attifIad By : Erni. ROdriau~ ~.

  • **** d By :

Oat. Of T ** t: August 23. 1ee4. \\

n a 500 Johnston p~ Company rlj BrookstJ. texas Customer: Georgia Power Company Job # 94JC1503S SIN: SNRU 8519 POF#: 66328 TC#: 07495 Rev. # 1 1000 1500 2000 2500 3000 3500 4000 4500 u.s. GALLONS PER MINUTE ()n 5000 5500 6000 6500 7000 n a 500 Johnston p~ Company rlj BrookstJ. texas Customer: Georgia Power Company Job # 94JC1503S SIN: SNRU 8519 POF#: 66328 TC#: 07495 Rev. # 1 1000 1500 2000 2500 3000 3500 4000 4500 u.s. GALLONS PER MINUTE ()n 5000 5500 6000 6500 7000

n 100 o 500 1000 1500 2000 2500 3000 3500 4000 4500 U.S. GALLONS PER MINUTE n() 5000

  • 5500 6000 6500 7000 n

100 o 500 1000 1500 2000 2500 3000 3500 4000 4500 U.S. GALLONS PER MINUTE n() 5000

  • 5500 6000 6500 7000

1..... c c c c JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: TC-07495 Re ** O Job Number: I14JC1503S Customer: Georgi. p __ Company Modell Stages: I soc I 7 Test Imp. Cia (in): 13 3/. Job Imp. Cia (in): TBF I CL.:.0113" I *C* Imp. Mateflal: SA ~'"CF8M Bowl Material: SA ~'*CF8M Bowl CoIIIIng:,.,.. 7122 Suctlon: Bel* 1.0. Co_ Test D. Head: Lob 10* H.P. DiochIrge Heed Test Col.: Lob T __ CokInIn Pipe Test Constants; Flow: 635.226 Head: 2.31 Pipe Cia. CD Gage (in]: 10.000 Water To Floor (in): m :m:m~nw<: Motor H.P. I R.P.M.: 150 1880 PHICY/V: 31601480 Motor SIN: 1118661 Job OR Leb Motor: Lab Wattmeter No.:.2 Test line Size (in): IS" Orfice Diameter (in): 7.0209 "'-n Gage (psi): O* 300 ImpeAer Adjustment: Two Turns DESIGN ~ R.P.M.: 1770 G.P.M.: 4000 Head [ft): 955 B.H.P.: Etficiency: Specific GnMty 1: Specific Gravity 2: Item No.: Fluid: Application: Comments: T.., the _I-'My only uoino. ,., t.b dilcharoe he.. Mld column pipe., reduced ~ with.. 1 __ llib M0101' Serial Number: SNRU 6519 Job Number: 94JC1503S Chattanooga P.O. Number:....;,T;;;,.e*...;.,11.;.;;605;.;;.;;... __ Floor To Gauge lin): 60 End User: "-oil _ c:on.p.ny Customer P.O. Number: POF Number: -:SJC663:-::==28~--- SIte: psi tap on Bowl or head~. Tag: Take Shut* 0Ir (Va' No): YES Project t.\\1IIIIIger: __ Water T.mperature: __ _ Tnt PoInt. 1 2 3 5 6 7 8 9 10 11 12 Delta.F" PnHg) 10.10 0.70 3.00 7.30 8.20 9.20 10.10 12.00 15.00 ".00 21.00 2 *. 00 GIIIIona Per Minute 2019 531 1100 1716 1819 1927 2019 2200 2460, 2S5 25111 3112 Gage Reeding IpeI) 105.5 .0 132.5., 116.0 113.0 108.5 105.5 97.5 85.5 7$.0 S3.5 54.5 Head (Ill 243.71 332.64 306.08 267.96 261.03 250.64 243.71 225.23 197.51 173.25 146.69 125.90 Gage E1w.COIr. Iftl 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.110 5.50 Velocity Heed Loa (It) 0.18 0.01 0.05 0.12 0.13 0.15 0.18 0.18 0.24 0.28 0.33 0.38 T ot8I Head 1ft) 249.37 338.15 311.62 273.58 266.66 256.28 249.37 230.92 203.24 178.04 152.52 131.78 Watt Reeding [kW) 121.7 87.S 10UI 118.4 120.1 121.5 121.7 121.2 119.8 118.1 114.7 110.5 Input H.P. 163.1 130.8 145.6 158.7 161.0 162.9 163.1 162.5 160.6 158.3 153.8 148.1 Motor EIIIcIency 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 B.H.P. 146.8 117.7 131.0 142.8 144.9 146.6 146.8 146.2 144.5 142.5 138.4 133.3 Tnt RP.M.: 888 891 889 888 888 888 888 888 888 888 889 888 Rated RP.M.: 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 GaIona Per Minute: <<124 1056 2191 3421 3626 3840 4024 4386 4904 53n 5796 6196 Total DI8chIrge Heed (Ill:

go.7 1334.4 1235.3 1086.9 10!59.4 1018.2
go.7 917.4 807.5 711.3 804.8 522.4 B.H.P.Q 1.0 Sp.Gf.

1162.7 923.1 1034.1 1131.2 1147.4 1160.8 1162.7 1157.9 1144.6 1128.3 1092.1 1052.2 B.H.p.e Sp.Gr.l: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 8.H.P.ClSp*Gr.2: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bowl EJriciency: 0.866 0.385 0.661 0.830 0.845 0.851 0.866 0.878 0.874 0.855 0.810 o.m T nted By : Darryl Clark oW. CertIfied By: Ernie Rodrigue] K ~ ~ By : ________ _ Date of Test: Fetrwry 15, 1l1li5 13 28.00 3361 37.0 85.47 5.50 o.e 81.42 102.1 136.9 0.900 123.2 no 1770 6685 361.6 SI68.9 0.00 0.00 0.630 1..... c c c c JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: TC-07495 Re ** O Job Number: I14JC1503S Customer: Georgi. p __ Company Modell Stages: I soc I 7 Test Imp. Cia (in): 13 3/. Job Imp. Cia (in): TBF I CL.:.0113" I *C* Imp. Mateflal: SA ~'"CF8M Bowl Material: SA ~'*CF8M Bowl CoIIIIng:,.,.. 7122 Suctlon: Bel* 1.0. Co_ Test D. Head: Lob 10* H.P. DiochIrge Heed Test Col.: Lob T __ CokInIn Pipe Test Constants; Flow: 635.226 Head: 2.31 Pipe Cia. CD Gage (in]: 10.000 Water To Floor (in): m :m:m~nw<: Motor H.P. I R.P.M.: 150 1880 PHICY/V: 31601480 Motor SIN: 1118661 Job OR Leb Motor: Lab Wattmeter No.:.2 Test line Size (in): IS" Orfice Diameter (in): 7.0209 "'-n Gage (psi): O* 300 ImpeAer Adjustment: Two Turns DESIGN ~ R.P.M.: 1770 G.P.M.: 4000 Head [ft): 955 B.H.P.: Etficiency: Specific GnMty 1: Specific Gravity 2: Item No.: Fluid: Application: Comments: T.., the _I-'My only uoino. ,., t.b dilcharoe he.. Mld column pipe., reduced ~ with.. 1 __ llib M0101' Serial Number: SNRU 6519 Job Number: 94JC1503S Chattanooga P.O. Number:....;,T;;;,.e*...;.,11.;.;;605;.;;.;;... __ Floor To Gauge lin): 60 End User: "-oil _ c:on.p.ny Customer P.O. Number: POF Number: -:SJC663:-::==28~--- SIte: psi tap on Bowl or head~. Tag: Take Shut* 0Ir (Va' No): YES Project t.\\1IIIIIger: __ Water T.mperature: __ _ Tnt PoInt. 1 2 3 5 6 7 8 9 10 11 12 Delta.F" PnHg) 10.10 0.70 3.00 7.30 8.20 9.20 10.10 12.00 15.00 ".00 21.00 2 *. 00 GIIIIona Per Minute 2019 531 1100 1716 1819 1927 2019 2200 2460, 2S5 25111 3112 Gage Reeding IpeI) 105.5 .0 132.5., 116.0 113.0 108.5 105.5 97.5 85.5 7$.0 S3.5 54.5 Head (Ill 243.71 332.64 306.08 267.96 261.03 250.64 243.71 225.23 197.51 173.25 146.69 125.90 Gage E1w.COIr. Iftl 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.110 5.50 Velocity Heed Loa (It) 0.18 0.01 0.05 0.12 0.13 0.15 0.18 0.18 0.24 0.28 0.33 0.38 T ot8I Head 1ft) 249.37 338.15 311.62 273.58 266.66 256.28 249.37 230.92 203.24 178.04 152.52 131.78 Watt Reeding [kW) 121.7 87.S 10UI 118.4 120.1 121.5 121.7 121.2 119.8 118.1 114.7 110.5 Input H.P. 163.1 130.8 145.6 158.7 161.0 162.9 163.1 162.5 160.6 158.3 153.8 148.1 Motor EIIIcIency 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 B.H.P. 146.8 117.7 131.0 142.8 144.9 146.6 146.8 146.2 144.5 142.5 138.4 133.3 Tnt RP.M.: 888 891 889 888 888 888 888 888 888 888 889 888 Rated RP.M.: 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 GaIona Per Minute: <<124 1056 2191 3421 3626 3840 4024 4386 4904 53n 5796 6196 Total DI8chIrge Heed (Ill:

go.7 1334.4 1235.3 1086.9 10!59.4 1018.2
go.7 917.4 807.5 711.3 804.8 522.4 B.H.P.Q 1.0 Sp.Gf.

1162.7 923.1 1034.1 1131.2 1147.4 1160.8 1162.7 1157.9 1144.6 1128.3 1092.1 1052.2 B.H.p.e Sp.Gr.l: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 8.H.P.ClSp*Gr.2: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bowl EJriciency: 0.866 0.385 0.661 0.830 0.845 0.851 0.866 0.878 0.874 0.855 0.810 o.m T nted By : Darryl Clark oW. CertIfied By: Ernie Rodrigue] K ~ ~ By : ________ _ Date of Test: Fetrwry 15, 1l1li5 13 28.00 3361 37.0 85.47 5.50 o.e 81.42 102.1 136.9 0.900 123.2 no 1770 6685 361.6 SI68.9 0.00 0.00 0.630

- n Johnston ~mp Company Drool lre, Texas Customer: Georgia Power Company Job ##: 94JC1503S, SIN: SNRU-6519, POF66328 TC##:07495 Rev. ##:0 1770 RPM ()() o 500 1000 lSOO 2000 2500 3000 3500 4000 4500 5000 5500 6000 6500 7000 -l -I -w-- _1-1 --1-- i =.,........................... .......................... +-........ :( ~:~ '"............. + ...............1... +-...... t....... 1****1................ J............... **It** ***l****,**+***,*** ****1****1****... :1......,... 1 *. 1 *.. * ** \\J;........ 1****1 ***"- ~ ~ -....I.... ~~~..................... _.....It............. L..LJJ........... 1...... ***:i:**.I..*.I..**I............ ***f**I...*........ J.~ **:I:***!...*L:\\:... ~ ..... ~.. +.+... ~... ****:**.I..**I* * *~t:**.... I.... l.... !... !...... l....!... +....... - co ' 300 -.............. /.................... _....................................... Bowl Assembly Pcrfonnlnce Tcsl(Lab Molor)

      • t***.. ++... '.... 1... ****I****J****.... 1* ** *.... I... +.. !.. +.. ***+**,****j***T** -

! 5 - "'j-'" "'"1:1.......,............................ -..... ****t**t**... '"...... !8OC -7 Stage 06rmF Class *C* ... ~... ****f**+ *+***I..*..*. ;.... 1.*.* ;... *1*.. *.... '.... I.. +. '...... ;.... !.... j.... I.... -

::: :::: ::::1/. :::. :::: :.:. :::: ::::.::: :::: :::.:::.:::.:::.::: ~ ::: ::: ::: ::: ::: :::
1::: :::L l=::I::::t::: ::::1::::1::::/::::1:::: ::::1::::1::':/::1::: ::::I::::t::: ::::J:::: -

200 -........................................................... +.........,....... Imp.MII.: SA351-CF8M at 13.750" Oia. (Wilh Wing Tips) **'1'" **f*******+*+**....1..+.. +... 1 **...*** ' ** ** 1.** 1.. +...... I **** I *.* I.* ::f.+ 10 _ *******. 1". **** *** **** **** **** **** **** ****

  • ************ *** -/-****** I *** f..........
      • f***......... 1.... 1.... 1........ 1...., *..* 1 **.. '.*.....* 1.... 1.... 1.... 1........ I..** !.... I**.. I****I-
  • .*.*.*. '# *.......*.....****.*************** ******************T**... "'r--.......

BowIMI1./COIting: SA3S1-CFBMJ / PLasilc .*. 4... .. ~.... !.... !................. 1..* '1"..........,....,.... 1...+..... J. *. J **** I****t**+ 1000 ~ ~~ :~; :; ~ ~ ~~: ~ ~ ~;: :; ~:;' ~.: ; ~ ::: c.";r~ By. &d. Rodri8.;iF~:"~ 15, 19Os 1:ll;lllll! ~I~'f~ 0 5 I II . {:I

  • 1 I

"*......................... **!*.. *I***{.................. ~ .... *.. *4 .. ** ~+ I=-. o 500 1000 ISOO 2000 2500 3000 3500 4000 4500 5000 5500 GOOO (,500 7000 U. S. OALLONS PER MINUTE - n Johnston ~mp Company Drool lre, Texas Customer: Georgia Power Company Job ##: 94JC1503S, SIN: SNRU-6519, POF66328 TC##:07495 Rev. ##:0 1770 RPM ()() o 500 1000 lSOO 2000 2500 3000 3500 4000 4500 5000 5500 6000 6500 7000 -l -I -w-- _1-1 --1-- i =.,........................... .......................... +-........ :( ~:~ '"............. + ...............1... +-...... t....... 1****1................ J............... **It** ***l****,**+***,*** ****1****1****... :1......,... 1 *. 1 *.. * ** \\J;........ 1****1 ***"- ~ ~ -....I.... ~~~..................... _.....It............. L..LJJ........... 1...... ***:i:**.I..*.I..**I............ ***f**I...*........ J.~ **:I:***!...*L:\\:... ~ ..... ~.. +.+... ~... ****:**.I..**I* * *~t:**.... I.... l.... !... !...... l....!... +....... - co ' 300 -.............. /.................... _....................................... Bowl Assembly Pcrfonnlnce Tcsl(Lab Molor)

      • t***.. ++... '.... 1... ****I****J****.... 1* ** *.... I... +.. !.. +.. ***+**,****j***T** -

! 5 - "'j-'" "'"1:1.......,............................ -..... ****t**t**... '"...... !8OC -7 Stage 06rmF Class *C* ... ~... ****f**+ *+***I..*..*. ;.... 1.*.* ;... *1*.. *.... '.... I.. +. '...... ;.... !.... j.... I.... -

::: :::: ::::1/. :::. :::: :.:. :::: ::::.::: :::: :::.:::.:::.:::.::: ~ ::: ::: ::: ::: ::: :::
1::: :::L l=::I::::t::: ::::1::::1::::/::::1:::: ::::1::::1::':/::1::: ::::I::::t::: ::::J:::: -

200 -........................................................... +.........,....... Imp.MII.: SA351-CF8M at 13.750" Oia. (Wilh Wing Tips) **'1'" **f*******+*+**....1..+.. +... 1 **...*** ' ** ** 1.** 1.. +...... I **** I *.* I.* ::f.+ 10 _ *******. 1". **** *** **** **** **** **** **** ****

  • ************ *** -/-****** I *** f..........
      • f***......... 1.... 1.... 1........ 1...., *..* 1 **.. '.*.....* 1.... 1.... 1.... 1........ I..** !.... I**.. I****I-
  • .*.*.*. '# *.......*.....****.*************** ******************T**... "'r--.......

BowIMI1./COIting: SA3S1-CFBMJ / PLasilc .*. 4... .. ~.... !.... !................. 1..* '1"..........,....,.... 1...+..... J. *. J **** I****t**+ 1000 ~ ~~ :~; :; ~ ~ ~~: ~ ~ ~;: :; ~:;' ~.: ; ~ ::: c.";r~ By. &d. Rodri8.;iF~:"~ 15, 19Os 1:ll;lllll! ~I~'f~ 0 5 I II . {:I

  • 1 I

"*......................... **!*.. *I***{.................. ~ .... *.. *4 .. ** ~+ I=-. o 500 1000 ISOO 2000 2500 3000 3500 4000 4500 5000 5500 GOOO (,500 7000 U. S. OALLONS PER MINUTE

\\ JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: Jo.r""'IIb... : Cu\\......r: Modell Stag.,: Im~. : TB Imp. .terial: Bowl Material: Bowl Coating: Suction: Test D. H.. d: T.at Col.: Test Constants; Flow: Head: TC-07485 Rev. #:0 04JC1503S Georgia Power Company 18DC I 7 13.750 (With *Wing TIpe, .083* I "C" SA351-CF8M SA351-CF8M Plu1te7122 Bel - 1.0. Coated Lab 18" H.P. Discharge Haad Lab Tappered Column Pip. 835.2211 2.31 Pip. 0Ia. @ Gage: 111.000 Motor Eft. : 100 %: 75 %: 50 %: Watw To Floor: Floor To GaUg.: Teat Point II Della 'P" "'_L _lOW Mlnut.

{

,ding FMtOfHead Gag. EIev.Cort. Velocity H.. d Loss Total H.. d WaltR.. ding: InputH.P. MCItAIr EtIcIency S.H.P. Teet RP.M.: Vola: (Ref. Only) Amp. (R".Only): Vlbndlon In MI.: RIItM RP.M.: GIIIIona 'w Minute: rallll H_1n feet: 8.HP"'.0 Sp.Qr. B.HP" Sp.Gr.1: B.HP" Sp.Gr.2: ~- Mtn... ecI By: 8 INCHES HE 80 INC S 1 2 3 10.10 0.70 3.00 2018 531 1100 105.50 144.00 132.50 243.71 332.04 301.01 11.50 I.ID 5.SO 0.10 0.01 0.05 248.37 331.15 311.02 121.70 87.00 101.00 103.14 130.83 145.51 0.Il00 0.Il00 0.Il00 140.82 I 117.75 131.02 aaa 881 .ag 1770 1770 1770 4024 1056 2191 990.7 1334.4 1235.3 1162.7 923.1 1034.1 1162.7 923.1 1034.1 0.0 0.0 0.0 0.866 0.385 0.661 D!!!l! CIuk Jr. 4 7.30 1710 110.00 207." II.SO 0.12 273.51 111.40 158.71 0.Il00 Motor H.P. I R.P.M.: 150/880 PH/CY/V: 31&0/480 Motor SIN : Job OR Lab Motor: LAB Comments: Test the bowla".mbly only using. t.st lab discharge head and columr. Wattmeter No.:

  1. 2 Ortice Diameter:

7.0208 T ** t lin. Siz.: 18 Pr.asur. Gage: 300 Imp'" Adjustment Two Tums DESIGN @ R.P.M.: 1no G.P.M.: 4000 Haad: 855.00 B. H. P ~ Efficiency: Specific Gravity 1: 1.00 Specific Gravity 2: 0.00 Item No.: Fluid: Application: End userGeorgia Power Company Site: Take Shut - Off (Y ** I No): YES 5 8 7 I 8 1.20 8.20 10.10 12.00 15.00 1118 1827 2018 2200 2450 113.00 101.50 105.50 87.50 15.50 201.03 250.04 243.71 225.23 187.51 15.S0 5.SO 11.50 11.50 5.50 0.13 0.15 O.HI 0.18 0.24 288.00 2511.21 248.37 230.82 203.24 120.10 121.50 121.70 121.20 118.80 1110.88 182.87 183.14 182.47 100.58 0.Il00 0.Il00 0.Il00 0.Il00 0.Il00 pipe at reduced spHd with a test lab motor. I Test Procedure #: JP-TP-0069 Rev.#51 Serial II: SNRU-6519 Job II: 94JC1503S POF II: 66328 ~~~-------- Ch&ttanpoga P.O.1I:TE-11605 10 11 12 13 14 11.00 21.00 24.00 n.oo 0.00 2085 2811 3112 1301 0 75.00 03.SO./ 54.50 37.00 150.00 173.25 140.08 121.00 '5.47 340.50 5.50 5.50 5.1D S.ID 5.50 0.28 0.33 0.31 0.45 0.00 178.04 152.52 131.78 81.42 352.00 111.10 114.70 110.50 102.10 85.00 151.31 153.75 148.12 130.80 113.84 0.Il00 0.Il00 0.Il00 0.Il00 0.Il00 142.'" I 144.is8 I I I I 14$.58 14$.12 1441.22 144.53 142.48 138.38 133.31 123.1' 102.55 aaa aaa aaa 181 aaa aaa aaa 888 lie uo H2 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 3421 3626 3840 4024 4386 4904 5372 5796 6196 6685 0 1086.9 1059.4 1018.2 990.7 917.4 807.5 711.3 6041.6 522.4 361.6 1386.0 1131.2 1147.4 1160.8 1162.7 1157.9 1144.6 1128.3 1092.1 1052.2 968.9 801.2 1131.2 1147.4 1160.S 1162.7 1157.9 1144.6 112S.3 1092.1 1052.2 968.9 801.2 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.830 0.845 0.851 0.866 0.878 0.814 /17.855 0.810 0.777 0.630 0.000 CwtIhd 8y: Emie Rodrigu~ /.#' Dat. Of Test: February 15. 1885 \\ JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: Jo.r""'IIb... : Cu\\......r: Modell Stag.,: Im~. : TB Imp. .terial: Bowl Material: Bowl Coating: Suction: Test D. H.. d: T.at Col.: Test Constants; Flow: Head: TC-07485 Rev. #:0 04JC1503S Georgia Power Company 18DC I 7 13.750 (With *Wing TIpe, .083* I "C" SA351-CF8M SA351-CF8M Plu1te7122 Bel - 1.0. Coated Lab 18" H.P. Discharge Haad Lab Tappered Column Pip. 835.2211 2.31 Pip. 0Ia. @ Gage: 111.000 Motor Eft. : 100 %: 75 %: 50 %: Watw To Floor: Floor To GaUg.: Teat Point II Della 'P" "'_L _lOW Mlnut.

{

,ding FMtOfHead Gag. EIev.Cort. Velocity H.. d Loss Total H.. d WaltR.. ding: InputH.P. MCItAIr EtIcIency S.H.P. Teet RP.M.: Vola: (Ref. Only) Amp. (R".Only): Vlbndlon In MI.: RIItM RP.M.: GIIIIona 'w Minute: rallll H_1n feet: 8.HP"'.0 Sp.Qr. B.HP" Sp.Gr.1: B.HP" Sp.Gr.2: ~- Mtn... ecI By: 8 INCHES HE 80 INC S 1 2 3 10.10 0.70 3.00 2018 531 1100 105.50 144.00 132.50 243.71 332.04 301.01 11.50 I.ID 5.SO 0.10 0.01 0.05 248.37 331.15 311.02 121.70 87.00 101.00 103.14 130.83 145.51 0.Il00 0.Il00 0.Il00 140.82 I 117.75 131.02 aaa 881 .ag 1770 1770 1770 4024 1056 2191 990.7 1334.4 1235.3 1162.7 923.1 1034.1 1162.7 923.1 1034.1 0.0 0.0 0.0 0.866 0.385 0.661 D!!!l! CIuk Jr. 4 7.30 1710 110.00 207." II.SO 0.12 273.51 111.40 158.71 0.Il00 Motor H.P. I R.P.M.: 150/880 PH/CY/V: 31&0/480 Motor SIN : Job OR Lab Motor: LAB Comments: Test the bowla".mbly only using. t.st lab discharge head and columr. Wattmeter No.:

  1. 2 Ortice Diameter:

7.0208 T ** t lin. Siz.: 18 Pr.asur. Gage: 300 Imp'" Adjustment Two Tums DESIGN @ R.P.M.: 1no G.P.M.: 4000 Haad: 855.00 B. H. P ~ Efficiency: Specific Gravity 1: 1.00 Specific Gravity 2: 0.00 Item No.: Fluid: Application: End userGeorgia Power Company Site: Take Shut - Off (Y ** I No): YES 5 8 7 I 8 1.20 8.20 10.10 12.00 15.00 1118 1827 2018 2200 2450 113.00 101.50 105.50 87.50 15.50 201.03 250.04 243.71 225.23 187.51 15.S0 5.SO 11.50 11.50 5.50 0.13 0.15 O.HI 0.18 0.24 288.00 2511.21 248.37 230.82 203.24 120.10 121.50 121.70 121.20 118.80 1110.88 182.87 183.14 182.47 100.58 0.Il00 0.Il00 0.Il00 0.Il00 0.Il00 pipe at reduced spHd with a test lab motor. I Test Procedure #: JP-TP-0069 Rev.#51 Serial II: SNRU-6519 Job II: 94JC1503S POF II: 66328 ~~~-------- Ch&ttanpoga P.O.1I:TE-11605 10 11 12 13 14 11.00 21.00 24.00 n.oo 0.00 2085 2811 3112 1301 0 75.00 03.SO./ 54.50 37.00 150.00 173.25 140.08 121.00 '5.47 340.50 5.50 5.50 5.1D S.ID 5.50 0.28 0.33 0.31 0.45 0.00 178.04 152.52 131.78 81.42 352.00 111.10 114.70 110.50 102.10 85.00 151.31 153.75 148.12 130.80 113.84 0.Il00 0.Il00 0.Il00 0.Il00 0.Il00 142.'" I 144.is8 I I I I 14$.58 14$.12 1441.22 144.53 142.48 138.38 133.31 123.1' 102.55 aaa aaa aaa 181 aaa aaa aaa 888 lie uo H2 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770 3421 3626 3840 4024 4386 4904 5372 5796 6196 6685 0 1086.9 1059.4 1018.2 990.7 917.4 807.5 711.3 6041.6 522.4 361.6 1386.0 1131.2 1147.4 1160.8 1162.7 1157.9 1144.6 1128.3 1092.1 1052.2 968.9 801.2 1131.2 1147.4 1160.S 1162.7 1157.9 1144.6 112S.3 1092.1 1052.2 968.9 801.2 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.830 0.845 0.851 0.866 0.878 0.814 /17.855 0.810 0.777 0.630 0.000 CwtIhd 8y: Emie Rodrigu~ /.#' Dat. Of Test: February 15. 1885

1900 1800 1700 1600 1500 g c 1400 l:i J: 1300 ~ 1200 CD ~ 1100 e 1000 ~ ~ 900 800 0 0.. W 700 U) a::: 0 600 J: ~ 500 ~ CD 400 300 200 100 0 I n ...,........... ~............................... --.. - -.:... '.!-...:... -.. ~--~-.. :.-!.......:..... :.-.. ~... !...... !... ~-.:.-.. :.-... :.. :--:....:.. --1-- --I--i-- --~--I--f--I-- ---:.. -~--I--I-- --l--~---:---~-- --I--I--{--+-

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  • ............ 4..... _

.. ~ 85.0 45_0 ~ 0 40.0 m ~ 0 35_0 30.0 25.0 20.0 15_0 10_0 5_0 0_0 o 500 1000 1500 2000 2500 3000 3500 4000 4500 5000 5500 6000 6500 7000 U.S. GALLONS PER MINUTE 1900 1800 1700 1600 1500 g c 1400 l:i J: 1300 ~ 1200 CD ~ 1100 e 1000 ~ ~ 900 800 0 0.. W 700 U) a::: 0 600 J: ~ 500 ~ CD 400 300 200 100 0 I n ...,........... ~............................... --.. - -.:... '.!-...:... -.. ~--~-.. :.-!.......:..... :.-.. ~... !...... !... ~-.:.-.. :.-... :.. :--:....:.. --1-- --I--i-- --~--I--f--I-- ---:.. -~--I--I-- --l--~---:---~-- --I--I--{--+-

    • eo........ _ _...... _................. _.................................. _

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r-JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: TC47UO Rev. 1 Job Number: 96JC1S01S Cuetomer: GeorgIa Power Company Modell stages: 180C 17 Teat Imp. CIa pn): 13.75 (With WIng Tips) Job Imp. Dia pn): TBF I CL: J)(;y' '.r::' Imp. Material: SA 351-CF8M Bowl Material: SA 351-CF8M Bowl CoatIng: Plasite 7122 SuctIon: Bel - 1.0. Coaled Test D. Heed: Lab 16" H.P. DIscharge Head Teet Col.: Lab Tappered Column Pipe Teet Conetanb; Flow: 635.226 Head: 2.31 PIpe CIa. Q Gege pn): 16 WatM To Floor (In): 6 Floor To Gauge pn)~ 60 Motor H.P. I RP.M.: lSO 1880 PH/CY/V: 31601~ Motor SIN: 1118661 Job OR lab Motor. Lab Wattmeter No.:.2 Test Une SIze [Ill]: 16" 0rIIce DIameter pn]: 7.0209 Pressure Gage (psIl: a -300 Impeller Adjustment: Two Tums DESIGN 0 RP.M.: 1770 G.P.M.: 4000 Head [It]: 955 B.H.P.: EIIiciency: 0.00 SpecitIc Gravity 1: Specific GrIMly 2: Item No.: Fluid: AppIIcEicn: End User: Geo!gia Power Company Site: Tag: Take Shut - orr (Yes 1 No): YES Water Temperature: 0 Teet Point. 1 2 3 4 5 6 7 8 Della "P' PnHQ) 10.1 0.7 3.0 7.3 8.2 9.2 10.1 12.0 Gallona Per Minute 2019 531 1100 1716 1819 1927 2019 2200 Gage Reeding [~ 106.5 148.3 134.5 116.0 113.0 109.5 106.0 97.5 Heed [It I 246.0 342.6 310.7 268.0 261.0 252.9 244.9 225.2 Gage EIev.Corr. [It I 5.SO 5.S) ~SO 5.SO 5.S) 5.SO 5.SO 5.SO VeIodty Heed L..oa lft) 0.2" 0.0 0.0 0.1 0.1 0.1 0.2 0.2 Tot.! Heed lft) 251.7 348.1 318.2 273.6 268.7 258.8 250.5 230.9 Watt Reading (kW) 120.5 102.0 106.0 116.8 118.0 119.2 120.0 119.2 Input H.P. 161.5 136.7 144.8 156.6 158.2 159.8 160.9 159.8 Motor EIIIctency 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 B.H.P. 145.4 123.1 130.3 14D.9 142.4 143.8 144.8 143.8 T..tR.P.M.: 888.0 890.0 889.0 888.0 888.0 887.0 887.0 887.0 ORIGiNAl TEST DATA Rat.d R.P.M.: 1770 1770 1770 1770 1770 1770 1770 1770 GaIIona Per Minute: 4024 1057 2191 3421 362e 3845 <1028 4391 Tot.! DIIdwge Heed lftl: 999.9 1376.7 1253.8 1088.9 1059.4 1029.7 997.8 919.5 B.H.P.Q 1.0 Sp.Gr.: 1151.3 968.0 1028,4 1115.9 1127.4 1142.7 1150.4 1142.7 B.H.P.G Sp.Gr.1: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bawl EIIIcIency: 0.883 0.380 0.674 0.841 0.860 0.875 0.882 0.892 HeN DATA BASED ON A.CNI CORRECTION Rated R.P.M.: 1770 1770 1770 1770 1770 1770 1770 1770 GdonI Per Minute: 3873 1017 2108 3293 3490 3700 3877 4226 Total HMdlft): 999.9 1376.7 1253.6 1088.9 1059.4 1029.7 997.6 919.5 B.H.P. 1.0 Sp.Gr.: 1151.3 988.0 1028.4 1115.9 1127.4 1142.7 1150.4 1142.7 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bawl EIIIcIency: 0.849 0.3<<1 0.1!49 0.810 0.828 0.842 0.849 0.859 Comments: Test the baoNI-.embIy only using a test lab cn.c:t.rge heed and column pipe at I8duced speed with a test lab Motor Serial Number: NRW-6525 Job Number: 96JC1S01S Chattanooga P.O. Number: TE*13141 Customer P.O. Number: -::-:-:::-==-:- POF Number: SJC 66554 Project Manager: __ 9 10 11 12 lS.0 18.0 21.0 24.0 2460 2695 2911 3112 85.0. 75.0 85.5 55.0 196.4 173.3 . 151.3 127.1 5.SO 5.~ 5.S) 5.50 0.2 0.3 0.3 0.4 202.1 1711.0 157.1 132.11 116.9 115.0 112.3 108.0 156.7 154.2 1SO.5 144.8 0.9 0.9 0.9 0.9 141.0 138.7 135.5 130.3 887.0 887.0 888.0 889.0 1770 1770 1770 1770 4909 5378 5802 8196 13 28.0 3361 38.0 67.8 5.SO 0.4 93.7 99.2 133.0 0.9 119.7 890.0 1770 8685 804.7 712.11 &24.3 527.0 370.7 1120.6 1102.4 1072.9 1028.4 941.4 0.00 0.00 0.00 0.00 0.00 0.890 0.878 0.853 0.802 0.6115 1770 1770 1770 1770 1770 4725 5176 5584 5983 6434 804.7 712.9 824.3 527.0 370.7 1120.6 1102.4 1on9 1028.4 1141.4 0.00 0.00 0.00 0.00 0.00 0.857 0.845 0.821 o.m 0.&40 Tested By: Ray DumesniI CertIIed By : Ernie Rodriguez WiIneAed By : 911~ K~() Date or Test: ~a.11116 Rev;.1: Perfarmenc:e COIT'8Cted due to ~ 8ITOI'. RH.O. 14 0.0 0 15S.0 38Q.4 5.50 0.0 385.11 93.1 124.8 0.9 112.3 891.0 1770 a 1443.8 880.5 0.00 o.CXIO 1770 0 1443.8 880.5 0.00 o.CXIO c c r-JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No.: TC47UO Rev. 1 Job Number: 96JC1S01S Cuetomer: GeorgIa Power Company Modell stages: 180C 17 Teat Imp. CIa pn): 13.75 (With WIng Tips) Job Imp. Dia pn): TBF I CL: J)(;y' '.r::' Imp. Material: SA 351-CF8M Bowl Material: SA 351-CF8M Bowl CoatIng: Plasite 7122 SuctIon: Bel - 1.0. Coaled Test D. Heed: Lab 16" H.P. DIscharge Head Teet Col.: Lab Tappered Column Pipe Teet Conetanb; Flow: 635.226 Head: 2.31 PIpe CIa. Q Gege pn): 16 WatM To Floor (In): 6 Floor To Gauge pn)~ 60 Motor H.P. I RP.M.: lSO 1880 PH/CY/V: 31601~ Motor SIN: 1118661 Job OR lab Motor. Lab Wattmeter No.:.2 Test Une SIze [Ill]: 16" 0rIIce DIameter pn]: 7.0209 Pressure Gage (psIl: a -300 Impeller Adjustment: Two Tums DESIGN 0 RP.M.: 1770 G.P.M.: 4000 Head [It]: 955 B.H.P.: EIIiciency: 0.00 SpecitIc Gravity 1: Specific GrIMly 2: Item No.: Fluid: AppIIcEicn: End User: Geo!gia Power Company Site: Tag: Take Shut - orr (Yes 1 No): YES Water Temperature: 0 Teet Point. 1 2 3 4 5 6 7 8 Della "P' PnHQ) 10.1 0.7 3.0 7.3 8.2 9.2 10.1 12.0 Gallona Per Minute 2019 531 1100 1716 1819 1927 2019 2200 Gage Reeding [~ 106.5 148.3 134.5 116.0 113.0 109.5 106.0 97.5 Heed [It I 246.0 342.6 310.7 268.0 261.0 252.9 244.9 225.2 Gage EIev.Corr. [It I 5.SO 5.S) ~SO 5.SO 5.S) 5.SO 5.SO 5.SO VeIodty Heed L..oa lft) 0.2" 0.0 0.0 0.1 0.1 0.1 0.2 0.2 Tot.! Heed lft) 251.7 348.1 318.2 273.6 268.7 258.8 250.5 230.9 Watt Reading (kW) 120.5 102.0 106.0 116.8 118.0 119.2 120.0 119.2 Input H.P. 161.5 136.7 144.8 156.6 158.2 159.8 160.9 159.8 Motor EIIIctency 0.9 0.9 0.9 0.9 0.9 0.9 0.9 0.9 B.H.P. 145.4 123.1 130.3 14D.9 142.4 143.8 144.8 143.8 T..tR.P.M.: 888.0 890.0 889.0 888.0 888.0 887.0 887.0 887.0 ORIGiNAl TEST DATA Rat.d R.P.M.: 1770 1770 1770 1770 1770 1770 1770 1770 GaIIona Per Minute: 4024 1057 2191 3421 362e 3845 <1028 4391 Tot.! DIIdwge Heed lftl: 999.9 1376.7 1253.8 1088.9 1059.4 1029.7 997.8 919.5 B.H.P.Q 1.0 Sp.Gr.: 1151.3 968.0 1028,4 1115.9 1127.4 1142.7 1150.4 1142.7 B.H.P.G Sp.Gr.1: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bawl EIIIcIency: 0.883 0.380 0.674 0.841 0.860 0.875 0.882 0.892 HeN DATA BASED ON A.CNI CORRECTION Rated R.P.M.: 1770 1770 1770 1770 1770 1770 1770 1770 GdonI Per Minute: 3873 1017 2108 3293 3490 3700 3877 4226 Total HMdlft): 999.9 1376.7 1253.6 1088.9 1059.4 1029.7 997.6 919.5 B.H.P. 1.0 Sp.Gr.: 1151.3 988.0 1028.4 1115.9 1127.4 1142.7 1150.4 1142.7 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bawl EIIIcIency: 0.849 0.3<<1 0.1!49 0.810 0.828 0.842 0.849 0.859 Comments: Test the baoNI-.embIy only using a test lab cn.c:t.rge heed and column pipe at I8duced speed with a test lab Motor Serial Number: NRW-6525 Job Number: 96JC1S01S Chattanooga P.O. Number: TE*13141 Customer P.O. Number: -::-:-:::-==-:- POF Number: SJC 66554 Project Manager: __ 9 10 11 12 lS.0 18.0 21.0 24.0 2460 2695 2911 3112 85.0. 75.0 85.5 55.0 196.4 173.3 . 151.3 127.1 5.SO 5.~ 5.S) 5.50 0.2 0.3 0.3 0.4 202.1 1711.0 157.1 132.11 116.9 115.0 112.3 108.0 156.7 154.2 1SO.5 144.8 0.9 0.9 0.9 0.9 141.0 138.7 135.5 130.3 887.0 887.0 888.0 889.0 1770 1770 1770 1770 4909 5378 5802 8196 13 28.0 3361 38.0 67.8 5.SO 0.4 93.7 99.2 133.0 0.9 119.7 890.0 1770 8685 804.7 712.11 &24.3 527.0 370.7 1120.6 1102.4 1072.9 1028.4 941.4 0.00 0.00 0.00 0.00 0.00 0.890 0.878 0.853 0.802 0.6115 1770 1770 1770 1770 1770 4725 5176 5584 5983 6434 804.7 712.9 824.3 527.0 370.7 1120.6 1102.4 1on9 1028.4 1141.4 0.00 0.00 0.00 0.00 0.00 0.857 0.845 0.821 o.m 0.&40 Tested By: Ray DumesniI CertIIed By : Ernie Rodriguez WiIneAed By : 911~ K~() Date or Test: ~a.11116 Rev;.1: Perfarmenc:e COIT'8Cted due to ~ 8ITOI'. RH.O. 14 0.0 0 15S.0 38Q.4 5.50 0.0 385.11 93.1 124.8 0.9 112.3 891.0 1770 a 1443.8 880.5 0.00 o.CXIO 1770 0 1443.8 880.5 0.00 o.CXIO

JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET eNO.: TC-07890 Rev. #:0 Job Number: 98JC1501S C tomer: Georgia Power Company eI / Stages18DC / 7 Imp. Dla.: ,,,,, (WIth "Wing Tips") TBF I CL.: .063" I *C" Imp. Material:SA351-CF8M Bowl Material SA351-CF8M Bowl Coating:Plasite 7122 Suction: Bell-I.D. Coated Test D. HeadLab 16" H.P. Discharge Head Test Col.: Lab Tappered Column Pipe Test Constants; Row: 635.2 Heed: 2.31 Pipe Di *. @ (lJI,,/I, Motor Eff. : 100 %: 75 %: 50 %: Water To Flo 6 INCHES C' To Gau--SO-INCHES Point' 1 2 3 Delta "p. 10.10 0.70 *3.00 Gallons Per M 2019 531 1100 Gage Reeding,,,,, ",,,,,,,, Feet of Heed "", ",,, ",,, Gage Elev;Co 5.50 5.50 5.50 VeJocltyHead 0.18 0.01 0.05 Total Heed "", " "", Watt Reeding:,,,,, "", "'" Input H.P.,,,,, II'"~ ",,, Motor Efflcierl ~.900 0.900 0.900 S.H.P. TestR.P.M.: 888 890 889 VoIt8: (Ref. Only) Amos IRef.Only): VIbration in Mils: Rated R.P.M.: 1770 1770 1770 Gallons Per M #### #### #### Total Heed in =11### #### #1## S.H.P.* 1.0 #### #### #### C~@SP.G #### #### #### B...* Sp.G 0.0 0.0

0.0 Efficiency

Tested By: Ray Dumesml 4 7.30 1716 5.50 0.12 0.900 888 1770 0.0 Motor H.P.' R.P.M.: 150/880 PH, CY I V: 3 I 60, 480 Motor SIN: Job OR Lab Motor: LAB Wattmeter No.: '2 Ortice Diameter: 7.021 Test line Size: 16 Pressure Gage: 300 Impeller Adjustment: Two Turns DESIGN @ R.P.M.: 1770 G.P.M.: 4000 Head: B.H.P.: Efficiency: Specific Grllvity 1: 1.00 Specific Gravity 2: 0.00 Item No.: Auid: Application: File Name = 66554 CommTest the bowl assembly only us test lab discharge heed and colu pipe at reduced speed with lites motor. ITest Procedure #: JP-TP-0069 Rev.N Serial' NRW-6525 Job': 96JC1501S End usGeorgia Power Company POF': 111# Site: Chattanooga P. TE-13141 Teke Shut - Off (Yes YES j 5 6 7 8 9 10 11 12 13 14 8.20 9.20 10.10 12.00 15.00 18.00 21.00 24.00 2~.00 0.00 1819 1927 2019 2200 2460 2895 2911 3112 3381 0 "", ",,,,,,,, 97.50 85.00 75.00 65.50 55.00 38.00 ",,, 87.78,,,,, 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 0.13 0.15 0.18 0.19 0.24 0.29 0.33 0.38 0.45 0.00 93.73 "", "", ",,, "", "",,,,,, "",,,,,,.",,, 99.20 93.10 ",,,,,,,, ",,, ",,, ",,,,,,,, ",,, II'"~ II'"~ " 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 "", ",,, "", III'" ",,, '/III' "'" "'" "",,,,,, 888 887 887 887 887 887 888 889 890 891 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770

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CertifIed By: ErnIe Rodnguez JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET eNO.: TC-07890 Rev. #:0 Job Number: 98JC1501S C tomer: Georgia Power Company eI / Stages18DC / 7 Imp. Dla.: ,,,,, (WIth "Wing Tips") TBF I CL.: .063" I *C" Imp. Material:SA351-CF8M Bowl Material SA351-CF8M Bowl Coating:Plasite 7122 Suction: Bell-I.D. Coated Test D. HeadLab 16" H.P. Discharge Head Test Col.: Lab Tappered Column Pipe Test Constants; Row: 635.2 Heed: 2.31 Pipe Di *. @ (lJI,,/I, Motor Eff. : 100 %: 75 %: 50 %: Water To Flo 6 INCHES C' To Gau--SO-INCHES Point' 1 2 3 Delta "p. 10.10 0.70 *3.00 Gallons Per M 2019 531 1100 Gage Reeding,,,,, ",,,,,,,, Feet of Heed "", ",,, ",,, Gage Elev;Co 5.50 5.50 5.50 VeJocltyHead 0.18 0.01 0.05 Total Heed "", " "", Watt Reeding:,,,,, "", "'" Input H.P.,,,,, II'"~ ",,, Motor Efflcierl ~.900 0.900 0.900 S.H.P. TestR.P.M.: 888 890 889 VoIt8: (Ref. Only) Amos IRef.Only): VIbration in Mils: Rated R.P.M.: 1770 1770 1770 Gallons Per M #### #### #### Total Heed in =11### #### #1## S.H.P.* 1.0 #### #### #### C~@SP.G #### #### #### B...* Sp.G 0.0 0.0

0.0 Efficiency

Tested By: Ray Dumesml 4 7.30 1716 5.50 0.12 0.900 888 1770 0.0 Motor H.P.' R.P.M.: 150/880 PH, CY I V: 3 I 60, 480 Motor SIN: Job OR Lab Motor: LAB Wattmeter No.: '2 Ortice Diameter: 7.021 Test line Size: 16 Pressure Gage: 300 Impeller Adjustment: Two Turns DESIGN @ R.P.M.: 1770 G.P.M.: 4000 Head: B.H.P.: Efficiency: Specific Grllvity 1: 1.00 Specific Gravity 2: 0.00 Item No.: Auid: Application: File Name = 66554 CommTest the bowl assembly only us test lab discharge heed and colu pipe at reduced speed with lites motor. ITest Procedure #: JP-TP-0069 Rev.N Serial' NRW-6525 Job': 96JC1501S End usGeorgia Power Company POF': 111# Site: Chattanooga P. TE-13141 Teke Shut - Off (Yes YES j 5 6 7 8 9 10 11 12 13 14 8.20 9.20 10.10 12.00 15.00 18.00 21.00 24.00 2~.00 0.00 1819 1927 2019 2200 2460 2895 2911 3112 3381 0 "", ",,,,,,,, 97.50 85.00 75.00 65.50 55.00 38.00 ",,, 87.78,,,,, 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 5.50 0.13 0.15 0.18 0.19 0.24 0.29 0.33 0.38 0.45 0.00 93.73 "", "", ",,, "", "",,,,,, "",,,,,,.",,, 99.20 93.10 ",,,,,,,, ",,, ",,, ",,,,,,,, ",,, II'"~ II'"~ " 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 0.900 "", ",,, "", III'" ",,, '/III' "'" "'" "",,,,,, 888 887 887 887 887 887 888 889 890 891 1770 1770 1770 1770 1770 1770 1770 1770 1770 1770

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CertifIed By: ErnIe Rodnguez

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( ( ' c c JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No,: TC,075O!> Rov, 0 Job Number. M./C1504S Customer. ~oio P __ Compony Modell Stages: I BOe I 7 Test Imp, Dill [in): 13 314 CWith Wing Tiool Job Imp, Dia (In): TBF I CL:,oe;r '"CO Imp. Materiel: SA 351*CfBM Bowl Material: SA 351*CfIM Bowl Coating: _ 7122 suction: Sol* to. ~ Test D. Head: lob Ie" H.P. Diochergo Hood Test Col.: lob T_od CoMM Pioo Test Constants; Flow: 635.226 Head: 2.31 Pipe Dia. e Gage rm): le.OOO Water To Floor lin): ::nnW:1G':i!:::: Molor H.P, I RP,M,: 150 1880 PH/CY IV: 3/60/480 Motor SIN: 1118661 Job OR Lab Motor: Lab Wattmeter No,: 112 Test line SIze [in): 16" Orfice Diameter [in): 7.0209 Pressure Gage [psij: 0 - 300 Irnpeler ~ : Two Tums DESIGN 0 RP,M.: 1770 G,P.M.: 4000 Head [ft): 955 B.H.P.: EIIiciency: Specific: Gravity 1: Specific Gravity 2: Item No.: Fluid: Application: Comments: T.I tho _1_bIy only uoina 0 1.1 lob "'_go hood end coUmn ptpe. et reduced.~ with... t le Motor Sen.! Number: NRX 11534 Job Numb... : "':9:"::4~JC=':':5:::04~S--- Chattanooga P.O. Number:... T.,;;;E;...-I""I",,606;;.;;... __ _ Floor To Gauge [in): 60 End User: '"-oio P __ Compony Customer P.O. Number: ~==.,,-__ _ Site: POF Number: SJC 66329 Tag: Take Shut - 011 (Yes I No): YES Project Manager: __ Water Temperature: __ _ Test Point; 1 2 3 4 5 6 7 8 9 10 11 12 Delta "P" rlt1Ho) 10.10 0.70 3.00 7.30 '.20 '.20 10.10 12.00 15.00 ".00 21.00 24.00 Gallons Per Minute 2019 53' "00 '7'6 '819 '927 2019 2200 2460 2895 29" 31'2 Gage Reading [psi] lee.O 149.5 133.5 115.5 112.5 109.0 lee.O 98.0 88.6 77.0 87.0 58.5 Heed [1t) 244.86 345.35 308.39 266.8' 259.88 251.79 244.86 226.38 199.82 '7'1.87 154.n '30.52 G8ae s.v.COIr. [1t).' 8.33 6.33 6.33 8.33 8.33 6.33 8.33 6.33 8.33 8.33 8.33 8.33 Velocity Heed Lou_[1t) 0.16 0.01 0.05 0.'2 0.13 0.15 0.16 0.19 0.24 0.28 0.33 0.38 T oIaI Heed [1t) 251.35 351.69 314.n 273.25 266.34 258.27 251.35 232.90 206.39 '84.49 161.44 137.23 Watt Reeding [kW) 121.5 103.2 108.2 117.1 118.7 120.3 121.0 121.1 119.2 118.1 115.3 1 I 1.2 InputH.P. '62.9 '38.3 145.0 157.0 '59.1 161.3 '62.2 162.3 159.8 158.3 154.6 149.1 Motor EII\\ciency 0.900 0.900 0.800 0.900 0.800 0.800 0.900 0.800 0.800 0.800 0.800 0.800 S.H.P. '46.6 124.5 130.5 '4'.3 143.2 145.1 146.0 146.1 143.8 '42.5 139.1 134.2 Test RP.M.: 888 891 880 888 888 888 888 888 889 888 889 889 Rated R.P.M.: lnO 1770 Ina lno lno 1770 lno Ina Ina lno 1no. Ina Gallons Per Minute: 4024 1056 2188 3417 3626 3840 4024 4386 4B98 5372 5798 15196 Tolal Oisc:harge Heed [1tJ: 998.6 1387.9 1245.0 1083.2 1058.2 1026.1 998.6 925.3 818.1 733.0 640.0 544.0 S.H.p.e 1.0 Sp.Gr.: 1160.8 976.0 1026.8 1115.0 1134.1 1149.3 1156.0 1157.0 1135.0 1128.3 1097.9 1058.8 a.H.p.e Sp.Gr.l: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 S.H.p.e Sp.Gr.2: 0.00 0.00 0.00 0.00 1i.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bowl EIIiciency: 0.874 0.379 0.670 0.838 0.854 0.866 0.878 0.886 0.892 0.881 0.853 0.804 r_ed By : Ray [)gnesnW WIMAed By : ________ DIlle cJ Teat:.,;.MM:II..=..;..1.,;.1I;.... 1.;;,;1185:..:-____ 13 21.00

336, 40.0 92.40 6.33 0.45 99.'8 102.9 137.9 0.800 124.1 890 1no e885 392.3 976.5 0.00 0.00 0.878 J

( ( ' c c JOHNSTON PUMP COMPANY PERFORMANCE TEST SET-UP AND TEST DATA SHEET TC No,: TC,075O!> Rov, 0 Job Number. M./C1504S Customer. ~oio P __ Compony Modell Stages: I BOe I 7 Test Imp, Dill [in): 13 314 CWith Wing Tiool Job Imp, Dia (In): TBF I CL:,oe;r '"CO Imp. Materiel: SA 351*CfBM Bowl Material: SA 351*CfIM Bowl Coating: _ 7122 suction: Sol* to. ~ Test D. Head: lob Ie" H.P. Diochergo Hood Test Col.: lob T_od CoMM Pioo Test Constants; Flow: 635.226 Head: 2.31 Pipe Dia. e Gage rm): le.OOO Water To Floor lin): ::nnW:1G':i!:::: Molor H.P, I RP,M,: 150 1880 PH/CY IV: 3/60/480 Motor SIN: 1118661 Job OR Lab Motor: Lab Wattmeter No,: 112 Test line SIze [in): 16" Orfice Diameter [in): 7.0209 Pressure Gage [psij: 0 - 300 Irnpeler ~ : Two Tums DESIGN 0 RP,M.: 1770 G,P.M.: 4000 Head [ft): 955 B.H.P.: EIIiciency: Specific: Gravity 1: Specific Gravity 2: Item No.: Fluid: Application: Comments: T.I tho _1_bIy only uoina 0 1.1 lob "'_go hood end coUmn ptpe. et reduced.~ with... t le Motor Sen.! Number: NRX 11534 Job Numb... : "':9:"::4~JC=':':5:::04~S--- Chattanooga P.O. Number:... T.,;;;E;...-I""I",,606;;.;;... __ _ Floor To Gauge [in): 60 End User: '"-oio P __ Compony Customer P.O. Number: ~==.,,-__ _ Site: POF Number: SJC 66329 Tag: Take Shut - 011 (Yes I No): YES Project Manager: __ Water Temperature: __ _ Test Point; 1 2 3 4 5 6 7 8 9 10 11 12 Delta "P" rlt1Ho) 10.10 0.70 3.00 7.30 '.20 '.20 10.10 12.00 15.00 ".00 21.00 24.00 Gallons Per Minute 2019 53' "00 '7'6 '819 '927 2019 2200 2460 2895 29" 31'2 Gage Reading [psi] lee.O 149.5 133.5 115.5 112.5 109.0 lee.O 98.0 88.6 77.0 87.0 58.5 Heed [1t) 244.86 345.35 308.39 266.8' 259.88 251.79 244.86 226.38 199.82 '7'1.87 154.n '30.52 G8ae s.v.COIr. [1t).' 8.33 6.33 6.33 8.33 8.33 6.33 8.33 6.33 8.33 8.33 8.33 8.33 Velocity Heed Lou_[1t) 0.16 0.01 0.05 0.'2 0.13 0.15 0.16 0.19 0.24 0.28 0.33 0.38 T oIaI Heed [1t) 251.35 351.69 314.n 273.25 266.34 258.27 251.35 232.90 206.39 '84.49 161.44 137.23 Watt Reeding [kW) 121.5 103.2 108.2 117.1 118.7 120.3 121.0 121.1 119.2 118.1 115.3 1 I 1.2 InputH.P. '62.9 '38.3 145.0 157.0 '59.1 161.3 '62.2 162.3 159.8 158.3 154.6 149.1 Motor EII\\ciency 0.900 0.900 0.800 0.900 0.800 0.800 0.900 0.800 0.800 0.800 0.800 0.800 S.H.P. '46.6 124.5 130.5 '4'.3 143.2 145.1 146.0 146.1 143.8 '42.5 139.1 134.2 Test RP.M.: 888 891 880 888 888 888 888 888 889 888 889 889 Rated R.P.M.: lnO 1770 Ina lno lno 1770 lno Ina Ina lno 1no. Ina Gallons Per Minute: 4024 1056 2188 3417 3626 3840 4024 4386 4B98 5372 5798 15196 Tolal Oisc:harge Heed [1tJ: 998.6 1387.9 1245.0 1083.2 1058.2 1026.1 998.6 925.3 818.1 733.0 640.0 544.0 S.H.p.e 1.0 Sp.Gr.: 1160.8 976.0 1026.8 1115.0 1134.1 1149.3 1156.0 1157.0 1135.0 1128.3 1097.9 1058.8 a.H.p.e Sp.Gr.l: 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 S.H.p.e Sp.Gr.2: 0.00 0.00 0.00 0.00 1i.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 Bowl EIIiciency: 0.874 0.379 0.670 0.838 0.854 0.866 0.878 0.886 0.892 0.881 0.853 0.804 r_ed By : Ray [)gnesnW WIMAed By : ________ DIlle cJ Teat:.,;.MM:II..=..;..1.,;.1I;.... 1.;;,;1185:..:-____ 13 21.00

336, 40.0 92.40 6.33 0.45 99.'8 102.9 137.9 0.800 124.1 890 1no e885 392.3 976.5 0.00 0.00 0.878 J
  • ~ n o

500 o 500 Johnston Pu"",,Company Brookshi( }rexas Customer: Georgia Power Company Job II: 94JC1504S, SIN: NRX 6534, POF66329 TCII:0750S Rev. #:0 1770 RPM f)n 1000 1500 2000 2500 3000 3500 4000 4500 5000 5500 6OQO 6500 I I I II~I I I I ILLI~ ~III I I I II I I I 1/ I I 1000 1500 2000 2500 3000 3500 4000 4500 50(JO 550() 60()O 6500 U. S. OAI.LONS PER MJNUTH 7000 7000 --1

  • ~ n o

500 o 500 Johnston Pu"",,Company Brookshi( }rexas Customer: Georgia Power Company Job II: 94JC1504S, SIN: NRX 6534, POF66329 TCII:0750S Rev. #:0 1770 RPM f)n 1000 1500 2000 2500 3000 3500 4000 4500 5000 5500 6OQO 6500 I I I II~I I I I ILLI~ ~III I I I II I I I 1/ I I 1000 1500 2000 2500 3000 3500 4000 4500 50(JO 550() 60()O 6500 U. S. OAI.LONS PER MJNUTH 7000 7000 --1

JOHNSTON PUMP COMPANY PERFORMANCE TEST SET -UP AND TEST DATA SHEET

u.tomer:

-e Stag ** : Ia.: '"'BF/CL.: mp.... erIaJ: 5ow1....... : 3ow1 Codng: Suction: rest D. Head: rot Col.: Tnt Con.tants; Flow: \\ Head: TC-07505 Rev. #:0 84JC1504S G.orgia Pow., Company 18DC / 7 13.750 lWlth "Wma Tip., .083 0 / "Co SA351-CF8M SA351-CFIM Plaalt.7122 B.. - LD. C_ted Lab 1 eo H.P. Di.charg. H.. d Lab Tapp.,ed Column Pipe 835.228 2.31 Pip. Dla. @ ~g.: 18.000 100 %: 75 %: 50 %: Water To Floor: Floor To ~uge : Test Paint # C~o I. p., Minute G:i". R.. din~ FaetGfH.. d Gag. !lev.Corr. Velocity He.d Loss Total Head Watt Reading: Input H.P. Motor Efllciency S.H.P. Test R.P.M.: Volts: (Ret.Only) Amp. (Ret.Only): VIbration in Mil.: Rated R.P.M.: Gallons Per Minute: 18 INCHES --';";"',*N ES 80 CH 1 2 10.10 0.70 20'8 531 1 De.OO 1411.50 244.88 345.~5 8.33 8.33 0.18 0.01 251.35 351.88 121.50 103.20 182.87 138.34 0.1100 0.1100 I 124.50 I '.8.58 I 888 801 I i I I 1770 1770 4024 1056 Total H.. d in Feet: I 998.6 1387.9 S.H.P.@ 1.0 Sp.Gr.: 1160.8 976.0 3 3.00 1100 133.50 308.38 8.33 0.05 314.77 108.20 145.04 0.000 130.54 880 1770 2168 1245.0 1026.8 4 7.30 1718 115.50 288.81 8.33 0.12 273.25 117.10 158.117 0.1100 141.27 888 1770 3417 1083.2 1115.0 S.H.P.@ Sp.Gr.l : 11160.8 ! 976.0 1026.811115.0 B.H.P.Ci Sp.Gr.2: I 0.0 ! 0.0 0.0

0.0 Qancy

I 0.874 1 0.379 0.670 ! 0.838 t.d Sy: Ra~ Oum ** nil Motor H.P./R.P.M.: 150 1880 PH/CY IV: 3180/480 Motor SIN: Job OR Lab Motor: Wattmet., No.: Orftce Diameter: LAB

  1. 2 7.0208 Comment.: T e.t the bowl.... mbly only u.ing a t ** t lab di.charge h.. d IIIId column pip. at reduced.peed with a test lab motor.

Test Ine SIze: 18 Prnaure Gag.: 300 Imp..., AdJustment Two Tum. DESIGN @ R.P.M.: lno G.P.M.: 4000 H.. d: 855.00 B.H.P.: Eftlciency: Sp ecitc Gravity 1: 1.00 Specilc Gravity 2: 0.00 Item No.: Fluid: Application: End UserGeorgia Power CompatlY Site: Take Shut - Of! (V ** I No): YES 5 8 7 8 8 8.20 8.20 10.10 12.00 15.00 1818 lD27 2018 2200 2480 112.50 log.00 108.00 88.00 88.50 258.88 251.7t 244.88 228.38 18t.82 8.33 8.33 8.33 8.33 8.33 0.13 0.15 0.18 0.18 0.24 288.34 258.27 251.35 232.QO 208.311 118.70 120.30 121.00 121.10 118.20 158.12 181.28 182.20 182.33 158.711 0.800 0.1100 0.800 0.1100 0.1100 143.20 145.13 145.118 148.10 143.81 888 888 888 888 880 1770 1770 1770 1770 1770 3626 3840 4024 4386 4898 10582 1026.1 998.6 925.3 818.1 1134.1 1149.3 1156.0 1157.0 1135.0 1134.1 1149.3 1156.0 1157.0 1135.0 0.0 0.0 0.0, - 0.0 0.0 0.854 0.866 0.878 0.886 0.892 Certi1ied By : Ernie Rodri!ilu.z'. Oata Of T ** I: March 18. 1 l1li5 I Test Procedure II: Jp-TP-0069 Rev.lIst Serial,: NRX 6534 Job # : 94JC1S04S rC~~: ~e~63~o~2=9=-__________ ___ Challanooga p.o.#:TE-11606 10 11 12 13 14 18.00 '21.00 24.00 28.00 0.00 2885 Ul1 3112 3381 0 noo tR.OO -- 58.50 40.00 158.50 177.87 154.77 130.52 112.40 381.52 8.33 8.33 8.33 8.33 8.33 0.20 0.33 0.38 0.45 0.00 184.48 tel.44 137.23 l1li.18 387.85 118.10 115.30 111.20 102.80 117.80 158.31 154.58 '.II.De 137.84 130.83 0.800 0.1100 0.000 0.000 O.toO 142.48 1311.10 134.18 124.1. 1~7.75 880

180, 800 801 I

1770 1770 1770 1770 1770 53721 5796 6196 6685 0 733.0 640.0 544.0 392.3 1451.6 1128.3 1097.9 1058.8 976.5 923.1 1128.3 1097.9 1058.8 976.5 923.1 0.0 0.0 0.0 0.0 O.oj 0.881 0.853 0.804 ! 0.678 0.000 JOHNSTON PUMP COMPANY PERFORMANCE TEST SET -UP AND TEST DATA SHEET

u.tomer:

-e Stag ** : Ia.: '"'BF/CL.: mp.... erIaJ: 5ow1....... : 3ow1 Codng: Suction: rest D. Head: rot Col.: Tnt Con.tants; Flow: \\ Head: TC-07505 Rev. #:0 84JC1504S G.orgia Pow., Company 18DC / 7 13.750 lWlth "Wma Tip., .083 0 / "Co SA351-CF8M SA351-CFIM Plaalt.7122 B.. - LD. C_ted Lab 1 eo H.P. Di.charg. H.. d Lab Tapp.,ed Column Pipe 835.228 2.31 Pip. Dla. @ ~g.: 18.000 100 %: 75 %: 50 %: Water To Floor: Floor To ~uge : Test Paint # C~o I. p., Minute G:i". R.. din~ FaetGfH.. d Gag. !lev.Corr. Velocity He.d Loss Total Head Watt Reading: Input H.P. Motor Efllciency S.H.P. Test R.P.M.: Volts: (Ret.Only) Amp. (Ret.Only): VIbration in Mil.: Rated R.P.M.: Gallons Per Minute: 18 INCHES --';";"',*N ES 80 CH 1 2 10.10 0.70 20'8 531 1 De.OO 1411.50 244.88 345.~5 8.33 8.33 0.18 0.01 251.35 351.88 121.50 103.20 182.87 138.34 0.1100 0.1100 I 124.50 I '.8.58 I 888 801 I i I I 1770 1770 4024 1056 Total H.. d in Feet: I 998.6 1387.9 S.H.P.@ 1.0 Sp.Gr.: 1160.8 976.0 3 3.00 1100 133.50 308.38 8.33 0.05 314.77 108.20 145.04 0.000 130.54 880 1770 2168 1245.0 1026.8 4 7.30 1718 115.50 288.81 8.33 0.12 273.25 117.10 158.117 0.1100 141.27 888 1770 3417 1083.2 1115.0 S.H.P.@ Sp.Gr.l : 11160.8 ! 976.0 1026.811115.0 B.H.P.Ci Sp.Gr.2: I 0.0 ! 0.0 0.0

0.0 Qancy

I 0.874 1 0.379 0.670 ! 0.838 t.d Sy: Ra~ Oum ** nil Motor H.P./R.P.M.: 150 1880 PH/CY IV: 3180/480 Motor SIN: Job OR Lab Motor: Wattmet., No.: Orftce Diameter: LAB

  1. 2 7.0208 Comment.: T e.t the bowl.... mbly only u.ing a t ** t lab di.charge h.. d IIIId column pip. at reduced.peed with a test lab motor.

Test Ine SIze: 18 Prnaure Gag.: 300 Imp..., AdJustment Two Tum. DESIGN @ R.P.M.: lno G.P.M.: 4000 H.. d: 855.00 B.H.P.: Eftlciency: Sp ecitc Gravity 1: 1.00 Specilc Gravity 2: 0.00 Item No.: Fluid: Application: End UserGeorgia Power CompatlY Site: Take Shut - Of! (V ** I No): YES 5 8 7 8 8 8.20 8.20 10.10 12.00 15.00 1818 lD27 2018 2200 2480 112.50 log.00 108.00 88.00 88.50 258.88 251.7t 244.88 228.38 18t.82 8.33 8.33 8.33 8.33 8.33 0.13 0.15 0.18 0.18 0.24 288.34 258.27 251.35 232.QO 208.311 118.70 120.30 121.00 121.10 118.20 158.12 181.28 182.20 182.33 158.711 0.800 0.1100 0.800 0.1100 0.1100 143.20 145.13 145.118 148.10 143.81 888 888 888 888 880 1770 1770 1770 1770 1770 3626 3840 4024 4386 4898 10582 1026.1 998.6 925.3 818.1 1134.1 1149.3 1156.0 1157.0 1135.0 1134.1 1149.3 1156.0 1157.0 1135.0 0.0 0.0 0.0, - 0.0 0.0 0.854 0.866 0.878 0.886 0.892 Certi1ied By : Ernie Rodri!ilu.z'. Oata Of T ** I: March 18. 1 l1li5 I Test Procedure II: Jp-TP-0069 Rev.lIst Serial,: NRX 6534 Job # : 94JC1S04S rC~~: ~e~63~o~2=9=-__________ ___ Challanooga p.o.#:TE-11606 10 11 12 13 14 18.00 '21.00 24.00 28.00 0.00 2885 Ul1 3112 3381 0 noo tR.OO -- 58.50 40.00 158.50 177.87 154.77 130.52 112.40 381.52 8.33 8.33 8.33 8.33 8.33 0.20 0.33 0.38 0.45 0.00 184.48 tel.44 137.23 l1li.18 387.85 118.10 115.30 111.20 102.80 117.80 158.31 154.58 '.II.De 137.84 130.83 0.800 0.1100 0.000 0.000 O.toO 142.48 1311.10 134.18 124.1. 1~7.75 880

180, 800 801 I

1770 1770 1770 1770 1770 53721 5796 6196 6685 0 733.0 640.0 544.0 392.3 1451.6 1128.3 1097.9 1058.8 976.5 923.1 1128.3 1097.9 1058.8 976.5 923.1 0.0 0.0 0.0 0.0 O.oj 0.881 0.853 0.804 ! 0.678 0.000

8 7 6 5 4 3 1. GRAVER TO SUPPLY AlL PIPING ANO EQJIPM 9fT WITHIN THE ~lMrtS [A 8JEXCEPT WHERE STATED TO TO A B BE FURNISHED BY OTHERS. EC(JJPMENT 001510£ THESE LIMITS iO 8£ ruRHISHED BY GRAVER ONLY WHEN DESIGNATED (SG). (80)- BY OTHERS. Z. ALL PIPING AND £()JIPHENT WITHIN THE LIMITS CTO :JTO BE ASSEMBlED FOR SHIPMENT* ~- G:~ NEk: ~~ ~:5 2N2\\* F2~5A ..........-----.........-~ ~~ !~--'-~~...=...-.I- _.- -... I I t I I 3. LEGEND: SEE ORAWINC R-1J898* ~----~--, 4

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DIAGRAM 2.. H~ 2.G029.. 0 0 RADWASTE SYS, P~I 0 5HT: 4 .3.S"1441b... 0 .. MAKE-UP DEMINERALllER SYSTEM FLOW DIAGRAM SYMBOLS

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PLANT, HATCH UNIT' 1

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3. f"(:q THE TVI'[ O~'TRAOISDUCERt~ncIiOR"IlANSMliTER)

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