Title: Sales Gas Pipeline Part I
1Sales 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.
2General Flow Equation
- Energy balance at steady state
3General Flow Equation
- Dividing by m and writing in differential form
- By using the enthalpy and entropy definition
4General Flow Equation
- For irreversible process
therefore - For an inclined pipe,
therefore
No Work
5General Flow Equation
- Fanning friction factor ( f )
- Wall shear stress
- Darcy or Moody friction factor (fm)
P
PdP
6General Flow Equation
- Pressure gradient in pipe
Usually negligible
Zero for horizontal pipe
7Single Phase Gas FlowReynolds Number
- Reynolds Number in Gas Pipeline
8Single Phase Gas FlowFriction Factor
- Laminar Flow (NRe lt 2100)
- Turbulent Flow (NRe gt 2100) Moody Diagram
- Smooth Wall Pipe
- Rough Wall Pipe
9Single Phase Gas FlowGeneral Equation
10Single Phase Gas Flow General Equation
- If T and zg are constant (TTav and zgzav)
C2
11Single Phase Gas Flow General Equation
Le
12Single Phase Gas Flow Average Pressure
13Single 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.
14Single 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 .
15Single 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
16Single 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.
17Single 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
18Single 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
19Single 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
20Single 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.
21Single Phase Gas Flow IGT Equation
- The IGT equation proposed by the Institute of Gas
Technology is also known as the IGT distribution
equation
22Single 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)
23Single 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