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LINE SIZING
www.oilgascourse.com
1
DESIGN OF PIPING
 MATERIAL
 DESIGN PRESSURE
 INSIDE DIAMETER
2
www.oilgascourse.com
FACTORS FOR CHOOSING MATERIAL
 TEMPERATURE
 PRESSURE
 FLUIDA
3
www.oilgascourse.com
 Diameter of Pipe
4
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LINE SIZING
 LIQUID SIZING
 GAS SIZING
 MULTIPHASE SIZNG
5
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SIZING CRITERIA - GENERAL
Considerations:
o Type of fluid
o Fluid velocity and pressure drop (always consider
operation windows, minimum, normal and
maximum)
o Application to associated equipment
o Reference design code API 14E
www.oilgascourse.com
6
LIQUID LINE
7
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SIZING CRITERIA - LIQUID LINE
1. Fluid velocity range 3-15 ft/s (below erosion)
2. Pressure drop (dP) per 100 ft < 4 psi
www.oilgascourse.com
8
Inside Diameter
depend on schedule
of pipe
 Source : API 14E
REYNOLD NUMBER
 Source : API 14E 9
www.oilgascourse.com
 Source : GPSA 12th Ed
10
www.oilgascourse.com
IF turbulent use moody diagram
SIZING CRITERIA - LIQUID LINE
Moody Friction Factor
Diagram
www.oilgascourse.com
11
CHEN (4000 TO 4(10)8 AND ROUGHNESS
0.05 TO 5 .10-7
Colebrook Equation fromFriction Factor Diagram
(Slide 8)
12
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Source : GPSA 12th Ed
13
www.oilgascourse.com
SIZING CRITERIA - LIQUID LINE
Pump Suction Piping
1. One or two pipe sizes larger than pump suction nozzle
2. Short with minimum elbow and pipe fittings
3. Use eccentric reducer near pump inlet nozzle
4. Typical velocities:
www.oilgascourse.com
14
 Source : API 14E
QUIZ 1 LIQUID SIZING
15
www.oilgascourse.com
MULTIPHASE
LINE
16
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SIZING CRITERIA – TWO PHASE LINE
1. Minimum Velocity 10 ft/s (For Minimize Slugging
Separation Equipment)
C=100; Continuous service
C=125; Intermittent service
C=150-200; for solids free and corrosion controller
www.oilgascourse.com
17
 Source : API 14E
SIZING CRITERIA – TWO PHASE LINE
Avoid slug flow regime
www.oilgascourse.com
18
19
www.oilgascourse.com
20
www.oilgascourse.com
QUIZ 2 MULTIPHASE
SIZING
21
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GAS LINE
22
www.oilgascourse.com
23
www.oilgascourse.com
SIZING CRITERIA – GAS LINE
1. Maximum velocity 60 ft/s (Noise problem)
2. Pressure drop (Norsok Standard)
- dP per 100 ft < 0.5 psi (P < 500 psig)
- dP per 100 ft 0.5 psi-1.2 psi (500 < P < 2000 psig)
3. Velocity calculation
www.oilgascourse.com
24
QUIZ 3 GAS LINE SIZING
25
www.oilgascourse.com
THANK YOU
26
www.oilgascourse.com

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