ML17335A156
| ML17335A156 | |
| Person / Time | |
|---|---|
| Site: | Cook  |
| Issue date: | 12/02/1996 |
| From: | Feliciano A INDIANA MICHIGAN POWER CO. (FORMERLY INDIANA & MICHIG |
| To: | |
| Shared Package | |
| ML17335A147 | List: |
| References | |
| NESM961021AF, NUDOCS 9808100115 | |
| Download: ML17335A156 (32) | |
Text
1 NE.014 (02/95)
NUCLEAR EMGIMEERIMG DEPARTIILIIEMT Calculation Cover Sheet Cook Nuclear Plant SECTION SHEET 1
OF Z4 CALCULATION No.
NESM961021AF SAFETY RELATED YES X
NO SYSTEM ECCS TITLE CCP NPSH RFC/MM/PM/PR/CR/TM No.
DB-12-ECCS-24 FILE LOCATION NESM Calc files INDIANA MICHIGAN POWER COMPANY UNIT No.
1&2 CALCULATED BY:
VERIFIED BY:
APPROVED BY:
DATE AT DATE I
CALCULATION DESCRIPTION: This calculation determines the NPSH available to the CCPs,and was performed as a result of DBD action item DB-12-ECCS-24.
, THOD OF VERIFICATION:
ALTERNATE CALCULATION REVISION DEsIGM REvIEM (A~
<4j+gfg' yg HO.
REASON/
FOR CHANGE Calculated By Oate verified By Date Approved By Date 9808i00iiS 9808i'7 PDR ADQCK 050003'LS H
5.
wr
)
~ I
~
~
1 I
\\
l Design Inputs Required pumo flows and CCP NPSH obtained from the various p~ mp curves are as follows:
3200 gpm (SD-12-CTS-100,Rev 0,
6.'1) 650 corn (SD DCC-NEMHlll Rev 6,
3.4.2.b.12)
- 4500 gpm (SD-12-RHR-100,Rev 0, 8.0; Centrifugal Charging Pump 550 gom (SD DCC'-NEMH111,Rev 6,
3.4 'A)
Centrifugal Charging Pump NPSH required 22 ft abs 8 550 gom Containment Spray Pump Safety Injection Pump Suction piping configuration (length, dia, fittings, etc) obta'n from the isometric drawings.
Calculation NEMP950501JEW approved 4/11/96 performed for seve e
~ accident setooints.
Note 100'f water temperature obtained from t is calculation.
3 References Containment Spray Pump Safety, Injection Pump Residual Heat Removal Pump Centrifugal Charging Pump Byron Jackson Pumo curve T-32913-:
Pacific Pump curve 34554D Ingersoll-Rand Pump curve N-3"8 Pacific Pump curve 34617I Isometric Drawings 2-SI-53 2-CS-81 2-SI-6 2-SI-43 2-CS-79 2-CS-80 Hydraulic fr'ction loss program HFLCS will be used to determine :he frictional losses thru suction piping.
HFLCS is an inho se develooed p ogram which was approved
=.or use on Feb 28, 1988..T=is program was validated and approv d in accordance witn
=he
=
requirements of GP 2.6 Software Qual'y assurance Standard in; se in la88 Description Puroose:
DBD action item DB-12-ECCS-24 "Centrifugal Charging Pump Available.
NPSH Calculation" indicated that an NPSH available calculation :or the CCPs could not be found.
The action item requested tha" a
calculation be prepared which would determine the NPSH available to the CCPs during the Injection Phase.
This calculation will determine the NPSH available to th C"Ps based on oroviding flow to two t=ains of safeguards pu;..ps (containment
- spray, safety injection, residual heat
- removal, and centrifugal charging)
+~8 M94 L~'Z(
P)
I
~ ~
~ ~
Method:
t Xn ord HFLC5 calculates the segments frictional losses and is based on the Dracy-Weisbach formula H
=
f~~
V D 2g er to obtain the frict'onal losses associated w'th the,.
suction piping the isometric drawings were used to obta'n= the piping configuration.
The sketch (pg 4
)
shows the. flow.path and branching flows to the otner safeguard pumps.
The data obtaine from the isometric drawings was compilied on the attached "pipe Friction Calculation Data Sheets".'he totals shown o;.
these sheets is used as input to HFLC5.
where:
H-f-L-
D-V-
frictional loss in feet friction factor, dimensionless pipe length in feet pipe diamete in feet pipe velocity in feet/sec gravitational constant, 32.174 fe t/sec'he NPSH available is then determined as follows:
- NPSH,
=
H~ - Hvp-.',(
where:
- NPSH, Hp HvpA H
Hrs net positive suet'on head available in ft abs atmospheric pressure in ft vapor pressure of water static elevation difference in feet friction losses 'n feet Assumotions 1 -
RWST water level is at minimum elevation (bottom of, pi=e) and is determined as 611.25'(24" suction p'pe center line)
- 1',rad's of 24" pipe) results in 610.25'.
Th' is conse vative since in normal ECCS operation the CCPs are transfered to the rec'rc lacion sump/RHR before the RWST level reaches Lo-Lo or elevat'on 613.0'.
2 -
RWST temperature is 100'f for conservatism.
Vapor pressure at 100'f is
.94925 psia or 2.21'ased on multiply'ng by the conversion factor 2.323 ft for 100'f water.
3 -
RWST is open to atmosphere 4
For purposes of this calculation it is assumed that all safeguards pumps are operating.
That is, 2 safety injection, 2
residual heat
- removal,
. 2 containment
- spray, and 2
cent ifugal charging pumps.
N~go Rl a~t t rbC 3
I-(S~(WC
t
V (
I
==
Conclusions:==
s This result Calculation:
g2lh5+
s of this calculation indicate that the iNPSH ava'lable to the charging pumps exceeds the NPSH required by approxima=ely 7'bsolute (6.97'ast pp and 6.55'est pp) at the CCP flow of 550 gpm.
C75 P/S 77oc W2" C Yo-~ gp 5~
PP~
C~ 5>
IP csog P eA JOAN+ pa 0+0 g(o Segmen" s 1
4 3
5 6
7 8
9 10 11 12 13 Flow 17,800 16,SOO 16,500 7,500 1,100 550 550 1, 100 1, 100 550 550 550 550 11.71
~ 68
.7
.15 1.54
.21
.33 3.04
.74 1.64
.24
.56 1.26 g
(cd'&C~
Wcc.P 5AC~
~
NPSH~
=
H~
Hmz +
Hss "
Hfs H, = 33.96 ft H~,
=
.95 psia or 2.21 ft H= 610. 25 - 592. 5
=
- 17. 75 ft
(>g g as-po Ss,r s~k r<( <t"
I 0
C The friction loss for each pump is determined by adding the respective line segments to that pump.
That is for the east CCP add segments 1 thru 5
ana 7 thru 10 and for the west CCP add segments 1 thru 5 and 7 thru 9 and 11 thru 13.
H(
ECCP
= 11.71
+
.68
+.7
+.15
+ 1.54
+
.33
+ 3.04
+ *.74
- 1.64 20.53 ft Hfg WCCP
=
1 1. 71
+
. 68
+
. 7
+
~ 15
+
1. 54
+
~ 33
+
3
~ 04
+
~ 74
+
~ 24
.56
+ 1.26 20.95 ft
- NPSH, ECCP
= 33.96
- 2.21
+ 17.75
- 20.53 28.97 ft abs NPSH~
WCCP 33 96 2
e 21
+ 17
~ 75 20 95 28.55 ft abs NPSH, at 550 gpm is 22 ft Therefore, the NPSH, exceeds the NPSH, by 6.97 ft abs and 6.55 ft abs for the ECCP and WCCK'spectively.
l 0
c:icalciccpnp PIPE FRICTION CALC -
INPUT FILE IS-c:icalciccpnpsh INPUT DATA FOR THE HFLC5 SYS.
RES.
CALC.
SISTS OF THE FOLLOWING DATA:
T TEMPERTURE DEG F E - PIPE ABSOLUTE ROUGHNESS (FT.)
N FXRST PXPE SEGMENT NUMBER N1 LAST PIPE SEGMENT NUMBER QDES DESIGN FLOW THRU PXPE SEGMENT (GPM)
QMIN MXNIMUM FLOW THRU PIPE SEGMENT (GPM)
QMAX MAXIMUM FLOW THRU PIPE SEGMENT (GPM)
QDELT -
FLOW INCREMENT THRU PIPE SEGMENT (GPM)
D PIPE SEGMENT INTERNAL DIA. (IN.)
L - PIPE SEGMENT LENGTH (FT.)
K PIPE SEGMENT K FACTORS L/D - PIPE SEGMENT L/D FACTORS FOLLOWING IS YOUR INPUT DATA T
E N
N1 100.00
.00015 1'3 QDES.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00 QMIN 17000.00 16000.00 16000.00 7000.00 1000.00 500.00 500.00 1000.00 1000.00 500.00 500.00 500.00 500.00 QMAX 17800.00 16500.00 16500.00 7500.00 1100.00 550.00'"
550.00 1100.00 1100.00 550.00 550.00 550.00 550.00 QDELT 200.'00 500.00 500.00 500.00 100.00 50.00 50.00 100.00 100.00 50.00 50.00 50.00 50.00 D
23.250 23.250 23.250 23.250 7.981 7.981 7.981 7.981 7.981 6.065 7.981 6.065 6.065 L
221.33 6.00 7.81 6.35 13.55 8.00 8.00 12.94 1.20 19.00 15.96
- 12. 71 9.35 Tg 1.00
.00
.00
.00
.44
.00
.00
.00
.00
.00
.00
.22
.00 L/D 148'.00 20.00 20.00 20.00 80.00 53.00 93.00 235.00 60.00 133.00 52.00 20.00 113.00 FOLLOWING IS HFLCS RESULTS WATER TEMP.(F)
DENSITY(LBM/CUFT)
ABS VISCOSITY(LBM/SEC/FT)
PXPE ABS ROUGHNESS(FT)
I N
100.,00 62.00
.460533E-03
.150000E-03 PI'PE SEG NO FLOW-GPM 17000.0 17200.0 17400.0 17600.0 17800.0 1
VEL (FPS) 12.85 13.00 13.15 13.30 13.45 PiPE DIA(ID-IN)
LHD(FT)
KHD(FT) 3.54 2.56 "3. 63 2.63 3.71 2.69 3.79 2.75 3.88 2.81 23.250 LDHD(FT) 4.59 4.70 4.80 4.91
~
5 '2 TOT 10.
10.
11.
11.
11.
HD (FT) 70 95 20 45 71 PXPE SEG NO FLOW-GPM 16000.0 16500.0 E
SEG NO OW-GPM 000.0 16500.0 PIPE SEG NO PIPE DIA(ID-IN)
I 23.250 2
PIPE DIA(ID-IN) =
23.250 VEL(FPS)
LHD(FT)
KHD(FT)
LDHD(FT) 12.09
.09
.00
.55
- 12. 47
.09
.00
.59 3
PIPE DIA(ID-IN) =
- 23. 250 VEL(FPS)
LHD(FT)
KHD (FT)
LDHD(FT) 12.09
.11
.00
.SS 12.47
.12
.00
.59 TOT TOT HD (FT) 64 68 HD (FT) 66 70 r(, lOZl 4>
~f~
1M' >i 8
.1 g(
F~~OW-GPM 7000.0 7500.0 VEL(FPS) 5.29 5.67 LHD(FT)
'KHD(FT)
.02
.00
.02
.00 LDHD(FT)
.11
.13 TOT HD (FT)
.13
.15 SEG NO W-GPM 000.0 1100.0 PIPE SEG NO FLOW-GPM 500.0 550.0 PIPE SEG NO FLOW-GPM 500.0 550.0 PIPE SEG NO FLOW-GPM 1000.0 1100.0 PiPE SEG NO FLOW-GPM 1000.0 1100.0 PIPE SEG NO FLOW-GPM 500.0 550.0 E
SEG NO FLOW-GPM 500.0 550.0 PIPE SEG NO FLOW-GPM 500.0 550.0 11 VEL(FPS)
- 3. 21
- 3. 53 12 VEL(FPS) 5.55 6.11 PIPE DlA(ID-IN) =
7.,981 LHD(FT)
KHD(FT)
LDHD(FT)
.06
.00
.14
.08
.00
.17 PIPE DIA(ID-IN) =
6.065 LHD (FT)
KHD(FT)
LDHD(FT)
.20
.10
.16
.24
.13
.19 5
PIPE DIA(XD-IN) =
7.981 VEL(FPS)
LHD (FT)
KHD(FT)
LDHD(FT) 41
.20
.28
~
.79 7.05
.24 34
.96 6
PIPE DIA(ID-IN) =
7.981 VEL(FPS)
LHD (FT)
KHD(FT)
LDHD(FT) 3.21
.03
.00
.14 3.53
.04
.00
.17 7
PIPE DIA(ID-IN) =
7.981 VEL (FPS)
LHD(FT)
KHD (FT)
LDHD(FT) 3.21
.03
.00
.25 3.53
.04
.00
.30 8
PIPE DIA(ID-IN) =
7.981 VEL(FPS)
LHD(FT)
KHD(FT)
LDHD(FT) 6.41
.19
.00 2.34 7.05 '23
.00
- 2. 81 9
PIPE DIA(ID-IN) =
- 7. 981 VEL(FPS)
LHD(FT)
KHD(FT)
LDHD(FT) 6.41
.02
.00
.60 7.05
.02
.00
.72 10 PIPE DIA(XD"IN) =
6.065 VEL(FPS)
LHD(FT)
KHD(FT)
LDHD(FT) 5.55
.30
.00 1.06 6.11
.36
.00 1.28 TOT HD (FT) 1.28 1.54 TOT HD (FT)
.17
.21 TOT HD (FT)
.28
.33 TOT HD (FT) 2.53 3.04 TOT HD (FT)
Q J 74 TOT HD (FT) 1.36 1.54 TOT HD (FT)
.20
.24 TOT HD (FT)
. 47
.56 PIPE SEG NO FLOW-GPM 500.0 550.0 13 PIPE DIA(ID-IN) =
6.065 VEL(FPS)
LHD(FT)
KHD(FT)
LDHD(FT) 5.55
.15
.00
.90 6.11
.18
.00 1.09 TOT HD (FT) 05 26
R(((i. 5/94
(
PIPE FRICTION CALCULATION DATASHEETS w 9 ~I oZIR I SHEET <
OF Z PLANT C~ ~ 4 STEM.
AI~/ P~+ r4 UNIT:
E SEGMENTTO(IE FROM
~ I Qo ~
(Z.i~"
i
~ i>
5 ~
I P
,".(r <.a>>
DWG.REF.: '4-5
~ - ~- <<- Z 7-5(-CO FLUID TEMP (4F):
~
PIPE ABS. ROUGHNESS (FT):
I>EEIGN FLOW:
MINIMUMFLOW: ~d~ >
MAXIMUMFLOW WIPE LO. (IN}:>'I PIPE EL:
PIPE SEGMENT NUMBER
'/9-"'9
> OFLOWINCREMENT: ~(=}< +
IJ 5//- g TOEL: <~~- ~
~-'TRAIGHT PIPE LENGTHS FITTINGS NUMBER
'K OR L/D z L/D I
I ~
,'I
-7 gI I
~(
0 lt
~ 0 GATE VALVE GLOBE VALVE BUT1'ERFLY VALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH w MITRE BENDS w LATERAL+ OUTLET
- LATERAL'NLET w STRAIGHT RUN LATERAL PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND 4 PIPE EXIT SHARP EDGE
/
w ORIFICF (Q =.61) w SUDDEN CONTRACTION
+
4 SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
13 340 40 135 30 50 20 50 20 60 1.2 (1WOSe) 1.0 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RF/0
.5(1-lP)
(1-(3~)'91.4 d l(j2
/o >
33.>, '53 4 ITEMS ARE'K"VALUES ONLY B = dlD RF = RECOVERY FACTOR
+ BASED ON SMALLER PIPE DIAMETER
g
~
~
Ryv.5/94 IPE FRICTION CALCuLATION DATASHEETS
+~m gI /oZ// >
SHEET OF PLANT~cPo ~
YSTEM.
CC. ~
F',
5 I-c~~C E SEGMFNTTQ 5 FROM; 4rC g
P.
~ r 4'., r m~
gc DWG. REF.:
FLUIDTEMP ('F):
DESIGN FLOW:
WIPE I,D. (IN):~'I 4 PIPE ABS. ROUGHNESS (FT):
PIPE SEGMENT NUMBER
'I!INIMUM FLOW: /oo o AilAXIMUMFLOW. g7o Og SFLOWINCREMENT /Oo Q PIPE EL:O'E<
lO TO EL:
STRAIGHT PIPE LENGTHS FITTINGS NUMBER
'K OR L/D x L/D GATE VALVE GLOBE VALVE BNTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW
'90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH w MITRE BENDS
- LATERAL+ OUTLET
- LATERAL'NLET
- STRAIGHT RUN LATERAL
- PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND w PIPE EXIT SHARP EDGE
- ORIFICE(Q =.61) w SUDDEN CONTRACTION
+
w SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
13 340 40 135 30 50 20 26 50 20 60 1.2 (1WOse) 1.0 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RF/6
.5(1-P)
(1-0')'91.4 d /
2 e ITEMS ARE "K"VALUES ONLY B = d/D RF = RECOVERY FACTOR 8zu
+ BASED ON SMALLERPIPE DIAMETER
Rov. 5/94 PIPE FRICTION CALCULATION DATASHEETS
&PIE.Q~ PQ fQ j f A+
SHEET ii~
OF YSTEM:
Cc 4'
SEGMENT TO a FROM: I"- ~
.1< pt i'4
~r X~ ~P C-;
UNIT:
DWG. RFF.:
FLUIDTEMP ('F):
'QESIGN FLOW:
IPE I.D. (IN):
5 i PIPE ABS. ROUGHNESS (Fl)'IPE SEGMENT NUMBER
'INIMUM FLOW:/0 4 l3 MAXIMUMFLOW. /Pn< Q
'FLOW INCREMENT. ~
c sl
<7.a )
PIPEEL:
5~~
) "
TO EL:
STRAIGHT PIPE LENGTHS FITTINGS NUMBER "KOR L/D z LID GATE VALVE GLOBE VALVE
,BUTTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW
'I80'LOSE RETURN STD. TEE RUN STD. TEE BRANCH
- MITRE BENDS
- LATERAL+ OUTLET LATERAL'NLET
- STRAIGHT RUN LATERAL
- PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND
- PIPE EXIT SHARP EDGE
- ORIFICE (Cg =,61)
- SUDDEN CONTRACTION
+
~ SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
340 40 135 30 50 20 16 26 50 20 60 1.2 (1wose) 1.0 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RF/8
.5(1-fP)
(1-0')'91.4 d /
2 rats
~ ITEMS ARE"K"VALUES ONLY 0 = cM)
RF = RECOVERY FACTOR U7
+ BASED ON SMALLERPIPE DIAMETER
,r Rov 5/94' C
SYSTEM:
PE SEGMENT TO Ec FROM:
PIPE FRICTION CALCULATION DATASHEETS I
> ~~
Q P
~
C ro p pcJ~+g/ag/ Al SHEET
/'~.
OF Z~
RBE UNIT:
DWG. REF.:
FLUIDTEMP ('F):
ESIGN FLOW; WIPE LD. (IN): -i~ ~
5
~
Cc PIPEABS.ROUGHNESS(FI):
PIPESEGMENTNUMBER
%WNIMUMFLOW /O OO QAXIMUMFLOWIo.o!Can OFLOWINCREMENT, r'do 6 25.'P, )
PIPEEL:
>FT-I i<<TOEI-:
STRAIGHT PIPE LENGTHS 6-<jr FACINGS GATE VALVE GLOBE VALVE BUTTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH NUMBER K OR L/D 13 340 40 135 30 50 20 16 26 50 20 60 x L/D
- MITRE BENDS LATERAL/ OUTLET w LATERAL/ INLET
" >> STRAIGHT RUN LATERAL
- PIPE EMR PROJ. INWD.
SHARP EDGE WELL ROUND w PIPE EXITSHARP EDGE
- ORIFICE ((g =.61) w SUDDEN CONTRACTION
+
w SUDDEN INCREASE
+
w VALVE,MISCELLANEOUS MISC.
1.2 (1WoSe) 1.0 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RF/8
.5(1-P)
(1- 0')
891.4 d /6(,'
TALE e ITEMS ARE "K VALUES ONLY 8 -" dlD RF = RECOVERY FACTOR
+ BASED ON SMALLERPIPE DIAMETER
1 1
0 0
~ I 0
~
0
~
0 0
0 \\ ~
I I
~
e
~
I I
~
~
I I ~
~
P
~
~ 1 0
~
~
~
~
Aov.$94 PIPE FRICTION CALCULATION DATASHEETS
,~ C Qmcjio /02IAI SHEET
~ ~
OF PLANT VSTEM:
E SEGMENT TO 4 FROM:
DWG. REF.:
2" -
- "I UNIT:,
2.
FLUIDTEMP ('F):
DESIGN FLOW:
OIPEI.D.(IN): ~I PIPE ABS. ROUGHNESS (FT):
PIPE SEGMENT NUMBER
'IIINIMUM FLOW:
C~ O WAXIMUMFLOW: /3< O FLOW INCREMENT:
7 7$
PIPE El TO EL:
STRAIGHT PIPE LENGTHS 11 I/
il IZ
'I u -&
FtT1lNGS GATE VALVE GLOBE VALVE BNTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH w MITRE BENDS
~ LATERAL/ OUTLET w LATERAL'NLET w STRAIGHT RUN LATERAL
- PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND w PIPE EXITSHARP EDGE w ORIFICE (Q =,61) w SUDDEN CONTRACTION
+
w SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
NUMBER
'K OR L10 13 340 40 135 30 50 I
20 26 50 20 60 1.2 (1wose) 1.0 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RFi8
.5(1-P)
(1-O'P 891.4 d /Q 2 xK x UD
~ ITEMS ARE "K"VALUES ONLY B = d/D RF = RECOVERYFACTOR
+ BASED ON SMALLERPIPE DIAMETER
E
heV. S/94 o
PIPE FRICTION CALCULATION DATASHEETS OF PLANT c o au-BY +~
DATE 4 <~<<4 YSTEM:
f' P
W~ a+Q I
CF I C UNIT:
2 E SEGMENTTO8t FROM ': <<" ~
~r c
~i ~r c.
q I-ru
~Pr/
DWG. REF.:
FLUIDTEMP ('F):
ESIGN FLOW:
4 IPE I.O. (IN): - '-I" PIPE ABS. ROUGHNESS (FT):
PIPE SEGMENT NUMBER
'IIINIMUM FLOW:
~
IIIAXIMUMFLOW:~IO CFLOW INCREMENT:
- 7. ch I
PIPE EL: ~>~
TO EL:
STRAIGHT PIPE LENGTHS FITTINGS NUMBER
'K OR LID z L/D GATE VALVE GLOBE VALVE BUTTERFLYVALVE SWING CHECK 90'TD.'ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEF RUN STD. TEE BRANCH
<<MITRE BENDS w LATERAL+ OUTLET LATERAL'NLET
- STRAIGHT RUN LATERAL
- PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND w PIPE EXITSHARP EDGE
- ORIFICE(Q =.61)
- SUDDEN CONTRACTION
+
- SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
340 40 135 30 50 20 16 50 20 60 1.2 (1wose) 1.0 0.5 O.I5 0.78 0.50 0.04 1.0 2.69 RF/8
.5(1-fP)
(1-GE) 891.4 d 1 2
w ITEMS ARE "K"VALUESONLY 8 = d/D RF = RECOVERY FACTOR UT
+ BASED ON SMALLER PIPE DIAMETER
4
RIEV; 5/94 PIPE FRICTION CALCULATION DATASHEETS
~~/~ g tOS~ 2f ~<
SHEET >>
OF. ~
PLANT BY <<-
DATE ~~solve SYSTEM
~
C
~
~
~
~
SEGMENT TO DWG. REF.:
Cf
~MD pg a FROM: <<.~ ~
2-C
-7T UNIT:
FLUIDTEMP ('F):
DESIGN FLOW:
WIPE I.D. (IN):~N'IPE ABS. ROUGHNESS (FT):
PIPE SEGMENT NUMBER
'MINIMUM FLOW.
y o O
'MAXIMUMFLOW. /gg ~
CIFLOW INCREMENT.
7-'fh'IPEEL: < ~" ~"
TO EL:
STRAIGHT PIPE LENGTHS FITllNGS NUMBER "K OR L/D x L/D e /
/cr "/>>'ATEVALVE GLOBE VALVE BUTTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH.
w MITRE BENDS w LATERAL+ OUTLET w LATERAL+ INLET
<<STRAIGHT RUN LATERAL
- PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND
- PIPE EXIT SHARP EDGE
- ORIFICE (Cg =.61) w SUDDEN CONTRACTION
+
N SUDDENINCREASE
+
- VALVE,MISCELLANEOUS MISC.
13 340 40 135 50 20 16 26 50 20 60 1.2 (1WOSe) 1.0 0.5 0.15 0.78 0.50 o.oa 1.0 2.69 RF/8
.5(1-fP)
(1-G~P 891.4 d /Q 2
~ ITEMS ARE'K"VALUES ONLY 8 -"d/D RF = RECOVERY FACTOR
+ BASED ON SMALLERP!PE DIAMETER
~
AMV.Ss~
~
~
l PIPE FRICTION CALCULATION DATASHEETS
~~ /Col<~'t E
"'NEZr 1<
OF PLANT BY~ DATE /at>wrg YSTEM:
Ii 0
E SEGMENT TO8c FROM' F
OWG.REF.:
2-cg-V9 UNIT:
FLUIDTEMP ('F):
DESIGN FLOW:
4 IPEI.D.(IN): <>
PIPE ABS. ROUGHNESS (Fl):
PIPE SEGMENT NUMBER IIIINIMUMFLOW:
I CIEAXIMUMFLOW: ~BC C OFLOW INCREMENT:
~. ~ci PIPEEL'>>"'~ ~"-
TUEL: +F+
STRAIGHT PIPE LENGTHS FITTINGS NUMBER K OR LID x L/D GATE VALVE GLOBE VALVE BUTTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH w MITRE BENDS w LATERAL/ OUTLET
- LATERAL/ INLET w STRAIGHT RUN LATERAL
- PiPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND w PIPE EXIT SHARP EDGE
- ORIFICE ((g =..61) w SUDDEN CONTRACTION
+
w SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
13 340 40 135 30 50 20 16 26 50 20 1.2 (1Wose) 1.0 0.5 0.15 0.78 0.50 o.o4 1.0 2.69 RF/6
.5(1-6')
(1-GE) 891.4 d IC 2 ALS P5
~ fTEMS ARE "K"VALUES ONLY S = d/D RF = RECOVERY FACTOR
+ BASED ON SMALLERPfP E DlAMETER
1
~ '.
Rov. b/94
~
~
PIPE FRICTION CALCULATION DATASHEETS
~~a qC iOZ/AC SHEET '
OF PLANT~~
BY ~
DATE r~au<C YSTEM:
E SEGMENTTO8L FROM
~ I- <'";,."
c<
P% a F
cc r o Mc., 'aha DWG. REF.:
4-C~
FLUID TE5I!P ('F):
DESIGN FLOW: li WIPE I.D. (IN): +
~-
r-'
c~
PIPE ABS, ROUGHNESS (FT):
PIPE SEGMENT NUMBER'INIMUM FLow: r 0MIUUMUMFLow: / 'FLow INUREMENT:
. 04$
PIPEEL:
SPC - ~"/r-TOEL:
meP-C STRAIGHT PIPE LENGTHS
>I rFWa 7
/
I rF 0
/
I FITTINGS GATE VALVE GLOBE VALVE BUTTERFLYVALVE
'WING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH
- MITRE BENDS w LATERAL/ OUTLET w LATERAL'NLET
- STRAIGHT RUN LATERAL
- PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND w PIPE EXIT SHARP EDGE
- ORIFICE (Cg =.61)
- SUDDEN CONTRACTION
+
w SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
NUMBER K OR UD 13 340 40 30 50 3
20 26 50 20
/
60 1.2 (1WOSe) 1.0 0.5 0.15 0.78 0,50 0.04 1.0 2.69 RF/8
.5(1-fP)
(1-O'P 891,4 d /(j 2 x L/D ALS U e ITEMS ARE "K"VALUES ONLY 8 =d/D RF = RECOVERY FACTOR 33
+ BASED ON SMALLERPIPE DIAMETER ~
ROVE 5/94
~ I PIPE FRICTION CALCULATION DATASHEETS
~m~ fCIO2/I'r.
SHEET~
QF TEM:
C C
P F-0 UNIT:
SEGMENTTOa FROM:
I=<~ r
~ e
~~
V>> -
yF i~
DWG. REF.:
2-c S
FLUIDTEMP ('F):
DESIGN Fl OW:
WIPE I.D. (IN):
PIPE ABS. ROUGHNESS (FT):
PIPE SEGMENT NUMBER
'MINIMUM FLOW:
/ ~+
MAXIMUMFLOW: 7 +
OFLOW INCREMENT:
3 PIPE EL
+~ ~
~
TO EL:
STRAIGHT PIPE LENGTHS FITTINGS NUMBER K OR L/D x L/D GATE VALVE GLOBE VALVE BUTTERFLYVALVE SWING CHECK 90'TD. ELBOW 90'.R. ELBOW 90'.R. ELBOW 45'TD. ELBOW 45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH
~ MITRE BENDS
~ LATERAL/ OUTLET LATERAL'NLET
~ STRAIGHT RUN LATERAL
~ PIPE ENTR PROJ. INWD.
SHARP EDGE WELL ROUND PIPE EXITSHARP EDGE
~ ORIFICE(Q =.61)
~ SUDDEN CONTRACTION
+
~ SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
13 340 40 135 30 20 26 50
/
20 60 12 (1wose) 1.0 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RF/6
.5(1-P)
(1-PP 891.4 d /
2 ALS U e ITEMS ARE "K"VALUES ONLY B = d/D RF = RECOVERY FACTOR p 5'2
+ BASED ON SMALLERPIPE DIAMETER
P P
P
~
~
a
~
~
~
e
~
~
a
~ I a ~
II '
~ P 0
)
~
)
e 0
~
0
~
~ ~
~
~
~
~ ~
~
~
~
~
~
~
~
a
~
ReVi M/94
'(
lg PIPE FRICTION CALCULATION DATASHEETS V~~ 5(. la Wl~
OF >
PLANT~~
TEM:
r C SEGMENT TO 4 DWG. REF.:
FLUIDTEMP ('F):
DESIGN FLOW:
PIPE I.D. (IN):
UNIT:
. Z.
FROM gcP>>
l
)v gpss
~pc'cgf~l
~ w (4
C C C
c.
<A I
3-C s-F'I PIPE ABS. ROUGHNESS (FT):
PIPE SEGMENT NUMBER'3 IIIINIMUMFLOW:
~
IIUCIMUMFLOW:
F FLOW INCREMENT:
g.o 6g PIPE EL.
gg T. ~/~~
TO EI-.
S F2-C STRAIGHT PIPE LENGTHS FLINGS NUMBER
'K OR VD zK x VD GATE VALVE z
-'LOBE VALVE BNTERFLYVALVE SWING CHECK 90'TD. ELBOV/
90',R. ELBOW 90'.R. ELBOW 45'TD. ELBOV/
45'.R. ELBOW 180'LOSE RETURN STD. TEE RUN STD. TEE BRANCH
- MITRE BENDS w LATERAL+ OUTLET w LATERAL'NLET w STRAIGHT RUN LATERAL PIPE ENTR PROJ. INWD. ~
SHARP EDGE WELL ROUND
<<PIPE EXITSHARP EDGE
- ORIFICF (Cg =.61) w SUDDEN CONTRACTION
+
w SUDDEN INCREASE
+
- VALVE,MISCELLANEOUS MISC.
13 340 40 135 30 50 20 16 50 20
/
60 12 (1-cose)
'I.O 0.5 0.15 0.78 0.50 0.04 1.0 2.69 RF/8
.5(1-P)
(1-HAPP 891A d/
2
?
ALS U e ITEMS ARE"K"VALUES ONLY 8 = d/D RF = RECOVERY FACTOR
+ BASED ON SMALLERPIPE DIAMETER
r ~w
\\
w
~
~
e NE 015 (02/95)
NESN DONALD C.
COOK NUCLEAR PLANT Section DESIGN VERIFICATION CHECKLIST - CALCULATIONS Calculation Number NESM961021AF Rev 0.
l'I /27 Basis
, C0 IC Sinai:ore of Ver fier Da"=
1.0 Mere the inputs correctly selected, incorporated and documented into the calculation?
Yes ~
N/A v'4 co~
n~~l, 2.0 Are assumptions necessary to perform the calculation adequately described and reasonable?
Basis:
0 a Ovo v
~ t(
SO Are the applicable codes.
standards and regulatory requirements ident-fied and
. equi rements for desicn I
met?
Yes i~l/A >
Basis:
(l 0
V a ('
W'o 4.0 Mas an appropri'ate design method used?
Basis:
i
'~
~.~
dc~
f Yes N/A 5.0 's the output reasonable compared to input?
Basis:
U Yes N/A 6.0 Are the results numerically correct?
Basis:
~
4 4
i Yes V N/A Page 1 of 1