Sales Gas Pipeline Part I - PowerPoint PPT Presentation

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Sales Gas Pipeline Part I

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... therefore: No Work General Flow Equation Fanning friction factor ( f ): ... Usually negligible Zero for horizontal pipe Single Phase Gas Flow Reynolds Number ... – PowerPoint PPT presentation

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Title: Sales Gas Pipeline Part I


1
Sales Gas PipelinePart I
  • Ref.1 Brill Beggs, Two Phase Flow in Pipes,
    6th Edition, 1991. Chapter 1.
  • Ref.2 Menon, Gas Pipeline Hydraulic, Taylor
    Francis, 2005, Chapter 2.

2
General Flow Equation
  • Energy balance at steady state

3
General Flow Equation
  • Dividing by m and writing in differential form
  • By using the enthalpy and entropy definition

4
General Flow Equation
  • For irreversible process
    therefore
  • For an inclined pipe,
    therefore

No Work
5
General Flow Equation
  • Fanning friction factor ( f )
  • Wall shear stress
  • Darcy or Moody friction factor (fm)

P
PdP
6
General Flow Equation
  • Pressure gradient in pipe

Usually negligible
Zero for horizontal pipe
7
Single Phase Gas FlowReynolds Number
  • Reynolds Number in Gas Pipeline

8
Single Phase Gas FlowFriction Factor
  • Laminar Flow (NRe lt 2100)
  • Turbulent Flow (NRe gt 2100) Moody Diagram
  • Smooth Wall Pipe
  • Rough Wall Pipe

9
Single Phase Gas FlowGeneral Equation
10
Single Phase Gas Flow General Equation
  • If T and zg are constant (TTav and zgzav)

C2
11
Single Phase Gas Flow General Equation
Le
12
Single Phase Gas Flow Average Pressure
13
Single Phase Gas Flow Erosional Velocity
Higher velocities will cause erosion of the pipe
interior over a long period of time. The upper
limit of the gas velocity is usually calculated
approximately from the following equation
Usually, an acceptable operational velocity is
50 of the above.
14
Single Phase Gas Flow Pipeline Efficiency
In Practice, even for single-phase gas flow, some
water or condensate may be present. Some solids
may be also present. Therefore the gas flow rate
must be multiply by an efficiency factor (E). A
pipeline with E greater than 0.9 is usually
considered clean .
15
Single Phase Gas Flow Non-Iterative Equations
  • Several equations for gas flow have been derived
    from General Equation. These equations differ
    only in friction factor relation assumed

Gas Transmission Pipline 1. AGA equation 2.
Weymouth equation 3. Panhandle A equation 4.
Panhandle B equation
Gas Distribution Pipeline 1. IGT equation 2.
Spitzglass equation 3. Mueller equation 4.
Fritzsche equation
16
Single Phase Gas Flow AGA Equation
  • The transmission factor is defined as
  • First, F is calculated for the fully turbulent
    zone. Next, F is calculated based on the smooth
    pipe law. Finally, the smaller of the two values
    of the transmission factor is used.

17
Single Phase Gas Flow Weymouth Equation
  • The Weymouth equation is used for high pressure,
    high flow rate, and large diameter gas gathering
    systems.
  • The Weymouth friction factor is

18
Single Phase Gas Flow Panhandle A Equation
  • The Panhandle A Equation was developed for use in
    large diameter natural gas pipelines,
    incorporating an efficiency factor for Reynolds
    numbers in the range of 5 to 11 million. In this
    equation, the pipe roughness is not used.
  • The Panhandle A friction factor is

19
Single Phase Gas Flow Panhandle B Equation
  • The Panhandle B Equation is most applicable to
    large diameter, high pressure transmission lines.
    In fully turbulent flow, it is found to be
    accurate for values of Reynolds number in the
    range of 4 to 40 million.
  • The Panhandle B friction factor is

20
Single Phase Gas Flow Gas Transmission Equations
  • A. Comparison of the calculated Output Pressure
    by AGA, Colebrook, Weymouth and Panhandle
    equations Figure 2.5
  • B. Comparison of the calculated Flow rate by AGA,
    Colebrook, Weymouth and Panhandle equations
    Figure 2.6
  • We therefore conclude that the most conservative
    flow equation that predicts the highest pressure
    drop is the Weymouth equation and the least
    conservative flow equation is Panhandle A.

21
Single Phase Gas Flow IGT Equation
  • The IGT equation proposed by the Institute of Gas
    Technology is also known as the IGT distribution
    equation

22
Single Phase Gas Flow Spitzglass Equation
  • The Spitzglass equation originally was used in
    fuel gas piping calculations. This equation has
    two version
  • A. Low pressure (less than 1 psig)
  • B. High pressure (more than 1 psig)

23
Single Phase Gas Flow Mueller and Fritzsche
Equation
  • The Mueller equation is
  • The Fritzsche formula, developed in Germany in
    1908, has found extensive use in compressed air
    and gas piping
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