10L. Capacity (Two-Phase-Modified Flanigan Calculation For Flow
Lines) Back to Main
This page is used to determine gas flow rate of a two-phase flow. The relationship between gas flow rate, diameter and pressure drop is represented by the Panhandle A equation (Table 10.1). Two corrections are made for two-phase flow.
1. The value of outlet pressure () is
adjusted for the pressure loss due to uphill and downhill flow of two phases,
including the effect of holdups.
2. The efficiency term (E) is correlated to
reflect measured system performance based on gas velocity and liquid-gas ratio.
As thus,
the modified Panhandle A equation becomes
(Equation
10.61)
Where: = gas rate at
P = absolute pressure
= mean absolute temperature of line
= temperature, standard conditions
d = inside diameter of pipe
L = pipe length
g =
gas relative density
= mean compressibility factor
= two-phase efficiency, can be found in
Figure 10.11
K = constant Metric
, English 435.87
=
(10.62)
Where: = additive correction to Panhandle A
A = constant Metric 0.00981, English 0.0069
= liquid density
= gas density
H = head
= uphill heads
= downhill heads
= empirical head factor (Figure 10.10)
(Equation 10.63, used
with Figure 10.10 to find Eh)
For
more information, please refer to page 363-366 in the book Gas Processing and
Conditioning Volume 1. To carry out the capacity calculation the Inlet
pressure, Pipe length, Uphill heads, Gas relative density, Liquid density, Mean
line temperature, Outlet pressure, Pipe inside diameter, Downhill heads, Mean
line compressibility, and Liquid to gas ratio of the two phase solution must be
entered into their entry spaces. To do so use the mouse to click the curser in
their entry spaces and input the data. Once this has been done, select Run to execute the solution.
Inlet
pressure is the pressure of the solution as it enters the system.
Pipe
length
L
Y
X
Where: Y
= distance from the bottom of the pipeline to the top of the pipeline in
the vertical direction.
X = distance from the beginning of the pipeline to the end of
the pipeline in the horizontal direction.
L = pipe length
Uphill
heads is the sum of the changes in elevation in the uphill direction.
Downhill
heads is the sum of the changes in elevation in the downhill direction. (Page
262, Volume 1)
Gas
relative density is the molecular weight of the gas divided by the molecular
weight of air or the density of the gas divided by the density of air at
atmospheric pressure.
(1.2)
Mean
line temperature is defined in Equation 10.41:
Outlet
pressure is the pressure of the solution as it leaves the system.
The
inside diameter of the pipe is the length from one inner edge of the pipe to
another inner edge of the pipe on the exact opposite side.
Mean
line compressibility is a measure of the average deviation of the actual
relation from the ideal-gas equation state (PV = nRT.) If the gas compositions are known,
Compressibility Factor can be calculated using screen 3C.
Liquid
to gas ratio is the amount of liquid within the mixture in respect to the gas.