Shale Gas to Ethylene (G2): Difference between revisions

From processdesign
Jump to navigation Jump to search
Line 30: Line 30:
==Appendix A: Shale Gas Composition==
==Appendix A: Shale Gas Composition==


[[File:Shalecomp.PNG|thumb|upright=5|left|'''Table A.1:''' Barnett Shale Gas Composition]]
[[File:Shalecomp.PNG|frame|none|upright=5|'''Table A.1:''' Barnett Shale Gas Composition]]


==Appendix B: Process Flow Diagram==
==Appendix B: Process Flow Diagram==

Revision as of 19:01, 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

Appendix B: Process Flow Diagram

Appendix C: HYSYS Diagram

Appendix D: Equipment List

Appendix E: Stream Information

Appendix F: Economic Analysis