Shale Gas to Ethylene (G2)
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Contents
1
Executive Summary
2
Introduction
3
Technical Approach
4
Design Summary
4.1
Overview
4.2
HYSYS Simulation
4.3
Acid Gas Removal
4.4
Dehydration
4.5
Fractionation Train
4.6
Hydrogenation Reactor
4.7
Ethylene Splitter
4.8
Steam Cracking
4.9
Process Optimization
5
Process Alternatives
5.1
Acid Gas Removal
5.2
Dehydration
5.3
Fractionation Train
5.4
Separation of Methane and Hydrogen
5.5
Hydrogenation Reactor
5.6
Steam Cracking
6
Economic Analysis
6.1
Capital Costs
6.2
Energy Usage
6.3
Fixed and Variable Costs
6.4
Overall Economic Feasibility
6.5
Sensitivity Analysis
7
Conclusion and Recommendations
8
References
9
Appendices
9.1
Appendix A: Shale Gas Composition
9.2
Appendix B: Process Flow Diagram
9.3
Appendix C: HYSYS Diagram
9.4
Appendix D: Equipment List
9.5
Appendix E: Stream Information
9.6
Appendix F: Economic Analysis
Executive Summary
Introduction
Technical Approach
Design Summary
Overview
HYSYS Simulation
Acid Gas Removal
Dehydration
Fractionation Train
Hydrogenation Reactor
Ethylene Splitter
Steam Cracking
Process Optimization
Process Alternatives
Acid Gas Removal
Dehydration
Fractionation Train
Separation of Methane and Hydrogen
Hydrogenation Reactor
Steam Cracking
Economic Analysis
Capital Costs
Energy Usage
Fixed and Variable Costs
Overall Economic Feasibility
Sensitivity Analysis
Conclusion and Recommendations
References
Appendices
Appendix A: Shale Gas Composition
Table A.1:
Barnett Shale Gas Composition
Appendix B: Process Flow Diagram
Figure B.1:
PFD
Appendix C: HYSYS Diagram
Appendix D: Equipment List
Appendix E: Stream Information
Appendix F: Economic Analysis
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