Shale Gas to Ethylene (G2): Difference between revisions
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=Appendices= | =Appendices= | ||
==Appendix A: Shale Gas Composition== | ==Appendix A: Shale Gas Composition== | ||
[[File:Shalecomp.PNG|frame|left|'''Table A.1:''' Barnett Shale Gas Composition]] | |||
==Appendix B: Process Flow Diagram== | ==Appendix B: Process Flow Diagram== | ||
==Appendix C: HYSYS Diagram== | ==Appendix C: HYSYS Diagram== | ||
Revision as of 23:59, 13 March 2015
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