PROJECT NO. PROJECT TITLE DOCUMENT TITLE Line Sizing Calculation For Liquid Services DATE DOC. NO. REV. REASON FOR
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PROJECT NO.
PROJECT TITLE
DOCUMENT TITLE
Line Sizing Calculation For Liquid Services
DATE DOC. NO.
REV.
REASON FOR REVISION CEPL-PC-001-CA-003
PREP.
CHKD.
SHEET 1 OF 6
APPD.
APPD. REV. 0
Line Sizing Calculation For Liquid Services DOC. NO. PROJECT NO. PROJECT TITLE BASIS
CEPL-PC-001-CA-003 0 0
Calculation Objective
Calculation Basis
Calculation Methodology
Assumptions
Software used
Conclusions
References
Attachments
REV. PAGE NO.
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Line Sizing Calculation For Liquid Services DOC. NO. PROJECT NO. PROJECT TITLE
CEPL-PC-001-CA-003 0 0
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SCHEMATIC:
Pipe List Phase Liquid Gas
This spreadsheet provides the sizing calculations for the pipe segment. LINE NO. P&ID NO. LINE DESCRIPTION FLUID PHASE
2.537 55.4 Liquid
T P ρ Q μ
PIPE SPEC.
1.2 kg/m3 ###
1 30 5.097 860 75 0.5159
oC kg/cm2g kg/m3 m3/h cP
Operating temperature Operating pressure Operating density Liquid flow rate Liquid viscosity
Pipe segment number
Pipe1
ϵ, Pipe roughness, mm (refer table 1)
0.045
Nominal diameter, inch
4.0
Schedule
40
Inside diameter, mm
102.26
Check valve (Swing) Check valve (Ball or piston) Butterfly valve Plug valve Globe valve (Straight pattern) VALVES Globe valve (Y- pattern) Globe valve (Angle- pattern) Ball valve Gate valve (std. bore) Gate valve (reduced bore)
Qty (nos.) Equi. Length, m
1 13.72
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
1 34.54
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
1 4.57
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
T
#NAME?
oC
Operating temperature
ρ Q μ
#NAME? #NAME? #NAME?
kg/m3 m3/s Pa.s
Operating density Lquid flow rate Liquid viscosity
Table 1
Line Sizing Calculation For Liquid Services DOC. NO. PROJECT NO. PROJECT TITLE
CEPL-PC-001-CA-003 0 0
Elbow std. 45° Elbow std. 90° Tee straight through Tee through outlet FITTINGS Std. reducer 1/2 Std. reducer 3/4 Std. enlargement 1/2 Std. enlargement 3/4
Strainer MISC. Outlet nozzle
LENGTHS
User specified equivalent length, m Straight length, m Equivalent length, m
HEIGHT
Pipe elevation increase, m
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Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
Qty (nos.) Equi. Length, m
-
125.0 52.8 -
-
-
-
60.45
Line Sizing Calculation For Liquid Services DOC. NO. PROJECT NO. PROJECT TITLE
CEPL-PC-001-CA-003 0 0
REV. PAGE NO.
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CALCULATION BASIS: The pressure loss in pipe flow is calculated using Darcy-Weisbach equation (equation 1)
Equation 1: This equation is valid for both laminar and turbulent flow regimes of any fluid with fully developed and incompressible flow. It can be used for gas services as long as there is only negligible change in gas density across the pipe length. The formula for calculating Darcy friction factor is different for laminar (equation 2) and turbulent flow (equation 3 - Haaland equation). Laminar flow meaning Reynolds number less than 2000.
Equation 2: Equation 3: The Haaland equation is used to solve directly for the Darcy–Weisbach friction factor f D for a full-flowing circular pipe. It is an approximation of the implicit Colebrook–White equation, but the discrepancy from experimental data is well within the accuracy of the data.
∆P
:
fD
:
Darcy friction factor
L
:
Length of pipe, m
V Nre
:
Velocity, m/s
Pressure drop, Pa
:
Reynolds number
ϵ/d d
:
ρ n
:
Relative roughness Inside pipe diameter, m Liquid density, kg/m3
:
Constant (n = 1 for liquid services and n= 3 for gas services )
:
Line Sizing Calculation For Liquid Services DOC. NO. PROJECT NO. PROJECT TITLE
CEPL-PC-001-CA-003 0 0
REV. PAGE NO.
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VELOCITY CRITERIA: 1 Typical allowable velocity shall be 3 m/s, as per Design Basis Memorandum.
PRESSURE DROP CRITERIA: 1 Maximum allowable pressure drop shall be 1.5 m per 1000 m pipe length, as per Design Basis Memorandum.
RESULTS: Pipe segment number
Pipe1 177.8 2.54
Total pipe length (including equivalent length, m) Velocity, m/s NRe
0.01728 83121 9.85
∆P, Pa hf, m liquid column hf, bar
0.83
hf, psi
12.05 5.00
Inlet pressure, barg Outlet pressure, barg
4.17 5.10
Inlet pressure, kg/cm2g Outlet pressure, kg/cm2g Inlet pressure, psig Outlet pressure, psig Pressure drop per 1000 m, mLc
0.85
kg/cm2
0.831
4.25 72.5 60.45 55.4
bar
CONCLUSIONS: 1 Pipe size considered is adequate w.r.to velocity criteria. 2 Pipe size considered is adequate w.r.to pressure drop criteria. REMARKS
-4.22680043 Turbulent
Turbulent
fD, Darcy friction factor
Total pressure drop
0.000148008 Laminar
432,409
Flow regime
12.05
psi
84.2
kPa
10.0
m H2O
Equivalent length of 100% open Valves
NB
D
Check valve (Swing)
0.5
0.0127
1.71
1
0.0254
3.43
Check valve (Ball or piston) 4.32 8.64
Butterfly Plug valve valve 0.25
0.57
0.51
1.14
Globe Globe valve valve (Y(Straight pattern) pattern) 4.32 2.03 8.64
4.06
Globe Ball valve valve (Anglepattern) 1.84 0.83 3.68
1.65
1.5
0.0381
5.14
12.95
0.76
1.71
12.95
6.10
5.52
2.48
2
0.0508
6.86
17.27
1.02
2.29
17.27
8.13
7.37
2.29
3
0.0762
10.29
25.91
1.52
3.43
25.91
12.19
11.05
3.43
4
0.1016
13.72
34.54
2.03
4.57
34.54
16.26
14.73
4.57
6
0.1524
20.57
51.82
3.05
6.86
51.82
24.38
22.10
6.86
8
0.2032
27.43
69.09
4.06
9.14
69.09
32.51
29.46
9.14
10
0.254
34.29
86.36
5.08
11.43
86.36
40.64
36.83
11.43
12
0.3048
41.15
103.63
6.10
13.72
103.63
48.77
44.20
13.72
14
0.3556
48.01
120.90
7.11
16.00
120.90
56.90
51.56
16.00
16
0.4064
54.86
138.18
8.13
18.29
138.18
65.02
58.93
18.29
18
0.4572
61.72
155.45
9.14
20.57
155.45
73.15
66.29
20.57
20
0.508
68.58
172.72
10.16
22.86
172.72
81.28
73.66
22.86
24
0.6096
82.30
207.26
12.19
27.43
207.26
97.54
88.39
27.43
30
0.762
102.87
259.08
15.24
34.29
259.08
121.92
110.49
34.29
32
0.8128
109.73
276.35
16.26
36.58
276.35
130.05
117.86
36.58
36
0.9144
123.44
310.90
18.29
41.15
310.90
146.30
132.59
41.15
42
1.0668
144.02
362.71
21.34
48.01
362.71
170.69
154.69
48.01
46
1.1684
157.73
397.26
23.37
52.58
397.26
186.94
169.42
52.58
48
1.2192
164.59
414.53
24.38
54.86
414.53
195.07
176.78
54.86
GPSA 13 edition SI
Comments: 90° elbow is taken as Long Radius Ellbows and Tee's are welded Enlargement and Contractions are Standard Reducers Red number are interpolated form values above/below
0% opening valves and fittings in meters Fittings
Gate valve (std. bore) 0.17
I
Elbow Gate std. 45° valve (reduced bore) 0.83 0.20
Elbow std. 90°
Tee Tee Std. Std. Std. Std. straight through reducer reducer enlargeme enlargeme through outlet 1/2 3/4 nt 1/2 nt 3/4
0.25
0.25
0.83
0.09
0.30
0.36
0.10
0.33
1.65
0.41
0.51
0.51
1.65
0.19
0.30
0.72
0.20
0.50
2.48
0.61
0.76
0.76
2.48
0.30
0.30
1.22
0.30
0.66
3.30
0.81
1.02
1.02
3.30
0.30
0.30
1.52
0.30
0.99
4.95
1.22
1.52
1.52
4.95
0.61
0.30
2.44
0.61
1.32
6.60
1.63
2.03
2.03
6.60
0.91
0.30
3.05
0.91
1.98
9.91
2.44
3.05
3.05
9.91
1.22
0.30
4.27
1.22
2.64
13.21
3.25
4.06
4.06
13.21
1.52
0.61
5.79
1.52
3.30
16.51
4.06
5.08
5.08
16.51
1.83
0.61
7.32
2.13
3.96
19.81
4.88
6.10
6.10
19.81
2.13
0.61
8.53
2.44
4.62
23.11
5.69
7.11
7.11
23.11
2.61
0.61
10.14
2.86
5.28
26.42
6.50
8.13
8.13
26.42
2.98
0.61
11.59
3.27
5.94
29.72
7.32
9.14
9.14
29.72
3.36
0.61
13.04
3.68
6.60
33.02
8.13
10.16
10.16
33.02
3.73
0.61
14.49
4.09
7.92
39.62
9.75
12.19
12.19
39.62
4.47
0.61
17.39
4.90
9.91
49.53
12.19
15.24
15.24
49.53
5.59
0.61
21.74
6.13
10.57
52.83
13.00
16.26
16.26
52.83
5.96
0.61
23.18
6.54
11.89
59.44
14.63
18.29
18.29
59.44
6.71
0.61
26.08
7.35
13.87
69.34
17.07
21.34
21.34
69.34
7.83
0.61
30.43
8.58
15.19
75.95
18.69
23.37
23.37
75.95
8.57
0.61
33.33
9.40
15.85
79.25
19.51
24.38
24.38
79.25
8.95
0.61
34.78
9.81
API 14E
Miscellaneous
Outlet nozzle
Strainer
0.41
3.18
0.81
6.35
1.22
9.53
1.63
12.70
2.44
19.05
3.25
25.40
4.88
38.10
6.50
50.80
8.13
63.50
9.75
76.20
11.38
88.90
13.00
101.60
14.63
114.30
16.26
127.00
19.51
152.40
24.38
190.50
26.01
203.20
29.26
228.60
34.14
266.70
37.39
292.10
39.01
304.80
GPSA 13 edition SI
INSIDE DIAMETER (MM)
Sch/Spec \ NB
0.5
0.75
1
1.5
2
3
4
6
8
10
12
14
16
18
STANDARD STD
15.76
20.96
26.64
40.98
52.48
77.92
102.26
154.08
202.74
254.56
304.84
336.55
387.35
437.95
XS
13.87
18.88
24.31
38.14
49.23
73.66
97.18
146.35
193.70
247.60
298.40
330.20
381.00
431.60
XXS
6.36
11.05
15.21
27.98
38.15
58.42
80.06
124.41
174.65
-
-
-
-
-
10
-
22.48
20
-
30 40 60 80
15.76 13.83
21.87 20.96 18.88
-
-
-
-
-
-
-
-
-
342.90
393.70
444.30
-
-
-
-
-
-
206.40
260.30
311.10
339.75
390.55
441.15
26.64 24.31
40.93 38.14
52.48 49.23
77.93 73.66
100
-
-
-
-
-
-
120
-
-
-
-
-
-
140
-
-
-
-
-
-
-
-
205.03
257.40
307.04
336.55
387.35
434.75
102.26
154.08
202.74
254.46
303.18
333.35
381.00
428.45
-
-
198.48
247.60
295.25
325.42
373.08
418.90
97.18 92.05 -
146.35
193.70
242.82
288.85
317.50
363.52
409.35
-
188.92
236.47
280.92
307.95
354.03
398.28
139.75
182.57
230.12
273.00
300.02
344.47
387.15 377.65
-
177.85
222.20
266.65
292.10
333.55
160
11.75
15.57
20.70
34.03
42.82
66.65
87.33
131.77
173.08
215.85
257.15
284.18
325.42
366.52
5S
18.00
23.40
30.10
45.00
57.00
84.68
110.08
162.76
213.56
266.19
315.88
347.68
398.02
448.62
10S
17.08
22.48
27.86
42.76
54.76
82.80
108.20
161.49
211.58
264.62
314.66
346.05
396.85
447.44
40S
15.76
20.96
26.64
40.93
52.48
77.93
102.26
154.08
202.74
254.46
304.75
-
-
-
80S
13.83
18.88
24.31
38.14
49.23
73.66
97.18
146.35
193.70
247.60
298.40
-
-
-
Misc.
Wall thickness (in) STD
0.109
0.113
0.133
0.145
0.154
0.216
0.237
0.280
0.322
0.365
0.375
0.375
0.375
0.375
XS
0.147
0.154
0.179
0.200
0.218
0.300
0.337
0.432
0.500
0.500
0.500
0.500
0.500
0.500
XXS
0.294
0.308
0.358
0.400
0.436
0.600
0.674
0.864
0.875
10
-
20 30 40 60 80
-
-
-
-
-
-
-
-
-
-
-
-
-
-
0.250
0.250
-
0.095
-
-
-
-
-
-
0.277
0.307
0.322
0.147
0.113 0.154
0.133 0.179
0.145 0.200
0.154 0.218
0.216 0.300
100
-
-
-
-
-
-
120
-
-
-
-
-
-
140
-
-
0.109
-
-
-
-
-
-
0.237 0.337 0.438 -
0.280 0.432 0.562 -
-
-
0.083
-
-
-
0.250
0.250
0.250
0.250
0.312
0.312
0.312
0.330
0.375
0.375
0.438
0.365
0.406
0.438
0.500
0.562
0.406
0.500
0.562
0.594
0.656
0.750
0.500
0.594
0.688
0.750
0.844
0.938
0.594
0.719
0.844
0.938
1.031
1.156
0.719
0.844
1.000
1.094
1.219
1.375
0.812
1.000
1.125
1.250
1.434
1.562
160
0.188
0.219
0.250
0.281
0.344
0.438
0.531
0.719
0.906
1.125
1.312
1.406
1.594
1.781
5S
0.065
0.065
0.065
0.065
0.065
0.083
0.083
0.109
0.109
0.134
0.156
0.156
0.165
0.165
10S
0.083
0.083
0.109
0.109
0.109
0.120
0.120
0.134
0.148
0.165
0.180
0.188
0.188
0.188
40S
0.109
0.113
0.133
0.145
0.154
0.216
0.237
0.280
0.322
0.365
0.375
-
-
-
80S
0.147
0.154
0.179
0.200
0.218
0.300
0.337
0.432
0.500
0.500
0.500
-
-
-
20
24
30
List 1
List 2
List 3 Unit
List 4 Unit
0.5
STD
kg/s
oC
XS XXS 10 20 30 40 60 80 100 120 140 160 5S 10S 40S 80S Misc.
kg/h
K
kg/min lb/h lb/s lb/min m3/h m3/s m3/min LPH LPM LPS USGPM UKGPM USBWPD UKBWPD USBPD UKBPD
oF oR
36
488.95
591.30
0.75
482.60
584.60
-
-
495.30
597.30
488.95
590.95
482.60
581.45
477.82
575.05
466.75
560.77
455.63
548.07
442.93
532.23
431.80
517.95
419.10
505.25
407.97
490.42
498.45
598.92
496.93
597.30
-
-
-
-
1 1.5 2 3 4 6 8 10 12 14 16 18 20 24 30 36 36
0.375
0.368
0.500
0.500
0.250
-
ND 0.5 0.75
0.250
1 1.5
0.375
0.375
0.500
0.562
2
0.594
0.688
3
0.812
0.969
4
1.031
1.219
6
1.281
1.531
8
1.500
1.812
10
1.750
2.062
12
1.969
2.344
14
0.188
0.218
16
0.218
0.250
18
-
-
20
-
-
24
OD (in) OD (mm) 0.840 21.3 1.05 26.7 1.315 33.4 1.900 48.3 2.375 60.3 3.500 88.9 4.500 114.3 6.625 168.3 8.625 219.1 10.750 273.0 12.750 323.8 14.000 355.6 16.000 406.4 18.000 457.0 20.000 508.0 24.000 610.0
List 5 Unit
List 6 Unit
barg
kg/m
bara
3
psig psia kPag kPaa kg/cm2g
3
lb/ft
List 7A
List 8 Unit
Pipe1
Pa.s P
List 7B Pipe2 List 7C Pipe3 List 7D Pipe4 List 7E Pipe5
kg/ms Ns/m2 mPa.s cP St cm2/s m2/s cSt mm2/s