pump head calculation

S:\MPI\Mp435\Sheet1\document.xls\NDDate: 03 December 2004 of 14

Meinhardt Philippines Inc.

Calculation/Sketch

LCBI, RVSI, ICOS TOOL HOOK-UP INST'N. MP435Project Project No. Sheet of

Designed by ND Date 03 DECEMBER 2004 Circ: FN/OR/AGR/ND /File

25th Flr., Chatham House116 Valero cor. Herrera Sts.Salcedo Village, Makati City1227 PhilippinesTel. (632) 887-1391Fax (632) 887-1172E-mail [email protected]

S:\MPI\Mp435\Sheet1\document.xls\NDDate: 03 December 2004 of 14

S:\MPI\Mp435\PCW pipe cap\document.xls\NDDate: 03 December 2004 of 14


Calculation/Sketch



I BASIS OF DESIGN RATING 150 psig @ 200 degrees F

PIPING Copper, seamless, Type L, ANSI B31.3, type ACR tubing, hard drawn, conforming to B-280, class: IED.

FITTINGS Wrought copper, ANSI B16.22, socket joint, B-75.

FLANGES Copper, socket joint, Class 125 FF

UNIONS Copper, socket joint, brass ring nut

BOLTING Machine bolts, A307 Gr B, with heavy hex nuts, plated

SOLDER Silver brazing B260 melting range 640°C to 705°C, Aircosil 15 or Silphos.

GASKETS Full face, 1/8" thick, Viton Class 125, old ANSI.

VALVES BA-5 – Bronze body, bronze ball trim, RTFE seats, TFE seals and packing, design pressure-400psi @ 150°F, three piece body construction, threaded end connection“Apollo 82-10, Watts B-6800 or Kitz”.

BA-6 – Bronze body, bronze ball trim, RTFE seats and TFE2 seals to be removed during soldering, TFE packing, design pressure-400psi and temperature depends on solder used, three piece body construction, solder end connection “Apollo 82-20X, Watts B-6801 or Kitz”.

INSULATION Pipe insulation shall have a maximum “k” factor of 0.23 at 75 degrees F mean temperature with a maximum service temperature of 250 degrees F. Insulation shall be tube elastomeric rubber insulation. Butt joints shall be sealed with pressure tape of type and as the insulation jacket to provide a continuous vapor seal. Manufacturer’s: Armaflex, Flex Therm or Intel approved equivalent. Insulation thickness (3/4”Ø and below – 3/4”, 1”Ø through 3”Ø - 1”, 4”Ø and larger – 1 1/2”).

II REFERENCESSTANDARD 1310

SECTION 15060

SECTION 15061

SECTION 15181-A

CAPITOLINE by Lee Kendrick




Calculation/Sketch




ENGINEERING COOKBOOK by James Meats

III GUIDE FOR PIPE SIZINGTHE MAXIMUM ALLOWABLE FRICTION LOSS OR VELOCITY IS < 5 FEET / 100 FEET LENGTH OR < 9 FEET / SECOND WHICHEVER IS MORE RESTRICTIVE.

IV PROCESS COOLING WATER SYSTEM CALCULATION

1 EXISTING:EXISTING PCW MAIN LINE = 6 INCHES DIAMETEREXISTING CONNECTED LOAD = 19 UNITS TEX OVENWHERE:

FLOW REQUIREMENT PER TOOL = 12.5 GPMTHEREFORE, THE TOTAL LOAD OF EXISTING 6 INCHES DIAMETER PCW MAIN LINE IS:

= 12.5 x 19 = 237.5 GPM

2 ADDITIONAL:FLOW REQUIREMENT PER TOOL = 40 GPM EACH FOR Ch. #1 & Ch. #2

= 80 GPMNO. OF TOOLS = 2 UNITS LCBITOTAL REQUIRED WATER FLOW, GPM

= 80 x 2 = 160.0 GPM

EXISTING PCW BRANCH LINE = 2 INCHES DIAMETERWHERE:

THE INSIDE DIAMETER OF 2 INCHES IS 2.067 THEREFORE, THE AVAILABLE FLOW FOR EXISTING TAPPING POINT IS 50 GPM AND

THE REQUIRED POC'S ARE 4 NOS., SEE CALCULATIONS BELOW:

Q =V x

0.41

Q =4.8 x 4.272

0.41 = 50 GPM

3 CHECK IF THE 6 INCHES DIAMETER PCW MAIN LINE COULD CARRY THE EXISTING ANDADDITIONAL LOAD

= 237.5 + 160.0 = 397.5 GPM

d =GPM x 0.41

V

=397.5 x 0.41

9 = 4.255 OR 6"Ø

THEREFORE, THE 6 INCHES DIAMETER COULD CARRY THE 397.5 GPM.

QT

QT

d2

QT



Calculation/Sketch




S:\MPI\Mp435\PCW loop2 friction loss\document.xls\NDDate: 03 December 2004

of 14


Calculation/Sketch

LCBI, RVSI, ICOS TOOL HOOK-UP INSTALLATION MP435Project Project No. Sheet of 8


PUMP HEAD CALCULATIONS - CV1 PCW LOOP 2

A B C D E F G H I J K L M N O P Q R

PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,

fps VALVES & FITTINGS

CU

MU

LA

TIV

E,

ft.

REMARKS

TYPE QTY. PER SECTION

TOTAL

PCW SUPPLY SIDE1-2 1 1250 8 2.0 6.56 2.4 8.01 2 13 26 175 0.16 4.20 4.36 4.36

PUMP SECTION

Flow Thru 0 13 0

Branch Tee 1 40 40

Flexible Connector 1 8.5 8.5

Reducer 1 8.5 8.5

Check Valve 1 80 80

Butterfly Valve 1 12 12

SUB-TOTAL 175

2-3 2 1250 14 3.2 10.496 0.2 2.61 Flow Thru 1 23 23 23 0.02 0.05 0.07 4.42

SUB-TOTAL 23

3-4 3 2500 14 1.7 5.576 0.7 5.23 Branch Tee 1 68 68 68 0.04 0.48 0.52 4.94

SUB-TOTAL 68

4-5 4 3750 14 3.0 9.84 1.5 7.84 1 23 23 46 0.15 0.69 0.84 5.78

Flow Thru 1 23 23

SUB-TOTAL 46

5-6 5 2500 14 1.9 6.232 0.7 5.23 Flow Thru 1 23 23 23 0.04 0.16 0.20 5.98

SUB-TOTAL 23

6-7 6 1250 14 3.33 10.9224 0.2 2.61 1 23 23 62 0.02 0.12 0.15 6.13

Flow Thru 1 23 23

FR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.

TOTAL PRESSURE LOSS, FT.

EQUIVALENT LENGTH, ft.

PER FITTING

90o Long Radius Elbow





of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


Reducer 1 16 16

SUB-TOTAL 62

7-8 7 1250 8 4.6 15.088 2.4 8.01 2 13 26 98.5 0.36 2.36 2.73 8.85

FILTER SECTION

Branch Tee 1 40 40

Reducer 1 8.5 8.5


SUB-TOTAL 98.5

PCW Filter 20 28.85

8-9 8 3750 14 16.0 52.48 1.5 7.84 6 23 138 161 0.79 2.42 3.20 32.06

Flow Thru 1 23 23

SUB-TOTAL 161

9-10 9 2500 14 2.6 8.528 0.7 5.23 Flow Thru 1 23 23 23 0.06 0.16 0.22 32.28

SUB-TOTAL 23

10-11 10 1250 14 2.6 8.528 0.2 2.61 1 23 23 39 0.02 0.08 0.10 32.37

Reducer 1 16 16

SUB-TOTAL 39

11-12 11 1250 8 5.0 16.4 2.4 8.01 4 13 52 124.5 0.39 2.99 3.38 35.75

Flow Thru 0 13 0

Branch Tee 1 40 40

Reducer 1 8.5 8.5






HEAT EXCHANGER SECTION


of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


SUB-TOTAL 124.5

Plate Heat Exchanger 20 55.75

12-13 12 2500 14 2.6 8.528 0.7 5.23 Flow Thru 1 23 23 23 0.06 0.16 0.22 55.97

SUB-TOTAL 23

13-14 13 3750 14 61.0 200.08 1.5 7.84 10 23 230 269 3.00 4.04 7.04 63.01

Flow Thru 1 23 23

Reducer 1 16 16

SUB-TOTAL 269

14-15 14 2475 10 15.0 49.2 2.8 10.15 4 16 64 119 1.38 3.33 4.71 67.72

Flow Thru 1 16 16

Reducer 1 20 20


SUB-TOTAL 119

15-16 15 2200 10 27.8 91.184 2.3 9.02 Flow Thru 1 16 16 36 2.10 0.83 2.93 70.64

Reducer 1 20 20

SUB-TOTAL 36

16-17 16 397.5 6 44.25 145.14 1.1 4.53 5 10 50 250 1.60 2.75 4.35 74.99

Flow Thru 1 10 10


Balancing Valve 1 170 170

SUB-TOTAL 250

HEAT EXCHANGER SECTION





of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


17-18 17 347.5 6 0.9 2.952 0.9 3.96 Flow Thru 1 10 10 10 0.03 0.09 0.12 75.11

SUB-TOTAL 10

18-19 18 310 6 3.1 10.168 0.7 3.53 Flow Thru 1 10 10 10 0.07 0.07 0.14 75.25

SUB-TOTAL 10

19-20 19 272.5 6 5.0 16.4 0.55 3.10 Flow Thru 1 10 10 10 0.09 0.06 0.15 75.39

SUB-TOTAL 10

20-21 20 235 6 1.5 4.92 0.39 2.68 Flow Thru 1 10 10 21 0.02 0.08 0.10 75.50

Reducer 1 11 11

SUB-TOTAL 21

21-22 21 235 4 3.5 11.48 3 6.02 Flow Thru 1 6.7 6.7 6.7 0.34 0.20 0.55 76.04

SUB-TOTAL 6.7

22-23 22 195 4 5.5 18.04 2.3 5.00 Flow Thru 1 6.7 6.7 6.7 0.41 0.15 0.57 76.61

SUB-TOTAL 6.7

23-24 23 145 4 1.3 4.1 0.9 3.72 Flow Thru 1 6.7 6.7 10.5 0.04 0.09 0.13 76.74

Reducer 1 3.8 3.8

SUB-TOTAL 10.5

24-25 24 145 3 2.5 8.2 3.5 6.61 Flow Thru 1 5 5 5 0.29 0.18 0.46 77.20

SUB-TOTAL 5

25-26 25 105 3 1.0 3.28 2.6 4.78 Flow Thru 1 5 5 5 0.09 0.13 0.22 77.42

SUB-TOTAL 5

26-27 26 80 3 3.0 9.84 1.65 3.64 Flow Thru 1 5 5 5 0.16 0.08 0.24 77.66


of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


SUB-TOTAL 5

27-28 27 40 3 3.0 9.84 0.45 1.82 Branch Tee 1 5 5 5 0.04 0.02 0.07 77.73

SUB-TOTAL 5

28-29 28 40 2 17.0 55.76 3.2 4.10 12 3.3 39.6 121.4 1.78 3.88 5.67 83.40

LCBI SECTION

Flow Thru 3 3.3 9.9

Reducer 1 1.6 1.6


Ball Valve 1 2.3 2.3

3 Way Ball Valve 2 24 48

Wye Strainer 1 14 14

SUB-TOTAL 121.4

PCW RETURN SIDE29-28 29 40 2 17.0 55.76 3.2 4.10 12 3.3 39.6 66.7 1.78 2.13 3.92 87.32

LCBI SECTION

Flow Thru 2 3.3 6.6

Reducer 1 1.6 1.6


Ball Valve 3 2.3 6.9

Flow Meter 1 6 6

SUB-TOTAL 66.7

28-27 28 40 3 3.0 9.84 0.45 1.82 Branch Tee 1 5 5 5 0.04 0.02 0.07 87.38

SUB-TOTAL 5




of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


27-26 27 80 3 3.0 9.84 1.65 3.64 Flow Thru 1 5 5 5 0.16 0.08 0.24 87.63

SUB-TOTAL 5

26-25 26 105 3 1.0 3.28 2.6 4.78 Flow Thru 1 5 5 5 0.09 0.13 0.22 87.84

SUB-TOTAL 5

25-24 25 145 3 2.5 8.2 3.5 6.61 Flow Thru 1 5 5 5 0.29 0.18 0.46 88.31

SUB-TOTAL 5

24-23 24 145 4 1.3 4.1 0.9 3.72 Flow Thru 1 6.7 6.7 10.5 0.04 0.09 0.13 88.44

Reducer 1 3.8 3.8

SUB-TOTAL 10.5

23-22 23 195 4 5.5 18.04 2.3 5.00 Flow Thru 1 6.7 6.7 6.7 0.41 0.15 0.57 89.01

SUB-TOTAL 6.7

22-21 22 235 4 3.5 11.48 3 6.02 Flow Thru 1 6.7 6.7 6.7 0.34 0.20 0.55 89.55

SUB-TOTAL 6.7

21-20 21 235 6 1.5 4.92 0.39 2.68 Flow Thru 1 10 10 21 0.02 0.08 0.10 89.65

Reducer 1 11 11

SUB-TOTAL 21

20-19 20 272.5 6 5.0 16.4 0.55 3.10 Flow Thru 1 10 10 10 0.09 0.06 0.15 89.80

SUB-TOTAL 10

19-18 19 310 6 3.1 10.168 0.7 3.53 Flow Thru 1 10 10 10 0.07 0.07 0.14 89.94

SUB-TOTAL 10

18-17 18 347.5 6 0.9 2.952 0.9 3.96 Flow Thru 1 10 10 10 0.03 0.09 0.12 90.06


of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


SUB-TOTAL 10

17-16 17 397.5 6 44.25 145.14 1.1 4.53 5 10 50 80 1.02 0.56 1.58 91.63

Flow Thru 1 10 10


SUB-TOTAL 80

16-15 16 2200 10 27.8 91.184 2.3 9.02 Flow Thru 1 16 16 36 2.10 0.83 2.93 94.56

Reducer 1 20 20

SUB-TOTAL 36

15-14 15 2475 10 15.0 49.2 2.8 10.15 4 16 64 119 1.38 3.33 4.71 99.27

Flow Thru 1 16 16

Reducer 1 20 20


SUB-TOTAL 119

14-30 14 3750 14 36.5 119.72 1.5 7.84 8 23 184 328 1.80 4.92 6.72 105.98

Flow Thru 2 23 46

Reducer 3 16 48


SUB-TOTAL 328

Air Separator 20.00 125.98

30-31 30 2500 14 4.3 14.104 0.7 5.23 Flow Thru 1 23 23 46 0.10 0.32 0.42 126.40

Reducer 1 23 23




AIR SEPARATOR SECTION


of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


SUB-TOTAL 46

31-1 31 1250 8 3.2 10.496 0.2 8.01 2 13 26 218 0.02 0.44 0.46 126.86

PUMP SECTION

Flow Thru 1 13 13

Branch Tee 0 40 0

Flexible Connector 1 8.5 8.5

Reducer 1 8.5 8.5

Wye Strainer 1 150 150


SUB-TOTAL 218

SUB-TOTAL 126.86

ADD 5% 6.34

TOTAL FRICTION LOSS 133.20


DOUBLE SUCTION HORIZONTAL SPLIT-CASE PROCESS COOLING WATER PUMP WITH 1250 GPM x 3 UNITS x 190 FT. TDH CAPACITY (2 UNITS ON DUTY & 1 UNIT STANDBY)


of 14


Calculation/Sketch





PIP

E R

UN

SE

CT

ION

FL

OW

, G

PM

PIP

E D

IAM

ET

ER

, in

.

ST

RA

IGH

T R

UN

, m

.

ST

RA

IGH

T R

UN

, ft

.

VE

LO

CIT

Y,


CU

MU

LA

TIV

E,

ft.

REMARKS


TOTALFR

ICT

ION

LO

SS

, ft

.H20

/100

ft. l

eng

th

EQ

. LG

TH

OF

V

AL

VE

S &

FIT

TIN

GS

, ft

.

PIP

ES

FR

ICT

ION

L

OS

S, f

t.

VA

LV

ES

& F

ITT

ING

S

FR

ICT

ION

LO

SS

, ft. TOTAL

PRESSURE LOSS, ft.



PER FITTING


pump head calculation

Documents