I |
Introduction |
1 |
|
1 |
Objective Study |
1 |
2 |
General Considerations |
1 |
II |
Membrane Process Design |
2 |
|
1 |
Operating Conditions and Economic Parameters |
2 |
2 |
Membrane Process Configurations |
3 |
|
A |
Membrane Process without Recycle |
3 |
B |
Membrane Process with Recycle |
3 |
III |
Optimization Methodology |
4 |
|
1 |
Problem Formulation and Analysis |
4 |
2 |
Optimization Methods |
5 |
IV |
Results and Discussions |
6 |
|
1 |
Membrane Process without Recycle |
6 |
|
A |
Processing Costs for Base-Case Conditions |
6 |
|
1 |
Single permeation stage with H2S - selective
membranes |
6 |
2 |
Single Permeation stage with CO2 - and H2S
- selective membranes |
7 |
3 |
Permeation stage(s) with CO2 - and H2S -
selective membranes |
8 |
4 |
Adjustment of CO2 and H2S concentrations
in retentate |
10 |
5 |
Components of Total Processing Costs |
10 |
B |
Effects of Operating and Economic Parameters on
Processing Cost |
11 |
|
1 |
Effect of Flow Rate |
11 |
2 |
Effect of Wellhead Price of Natural Gas |
11 |
3 |
Effect of Membrane Module Cost |
12 |
4 |
Effect of Feed Pressure |
12 |
2 |
Membrane Process with Recycle |
13 |
3 |
Comparison of Membrane Process with Adsorption |
15 |
|
REFERENCES |
16 |
TABLES |
24 |
FIGURES |
26 |