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Techno economic evaluation of co2 utilization processes hydrogenation, bi and tri reforming of co2 into methanol production

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Cấu trúc

  • 0-TITLE PAGE

  • 1-Acceptance page

  • 2-Abstract (English)

  • 3-Thai Abstract

  • 4-Acknowledgements

  • 5-Table of Contents

  • 6-Thesis

  • 7-References

  • 8-Appendix

    • A. Appendix A CO2 Conversion Process Flowsheet and Steam Tables Implemented by Aspen Plus 8.6

      • A.1 Hydrogenation of CO2 into Methanol

      • A.2 Bi-reforming of CO2 into Methanol

      • A.3 Tri-reforming of CO2 into Methanol

    • B. Appendix B Economic Evaluation For Each Process

      • B.1 Hydrogenation of CO2 into Methanol

        • B.1.1 Hydrogenation of CO2 into Methanol for the Base Case Design

          • B.1.1.1 Raw Material, Product and Utilities Prices

          • B.1.1.2 Raw Materials and Product Annual Prices

          • B.1.1.3 Annual Utility Cost

          • B.1.1.4 Equipment Sizing and Purchase Cost

          • B.1.1.5 Capital Cost Analysis

          • B.1.1.6 Production Cost Analysis

          • B.1.1.7 Profitability Assumptions

        • B.1.2 Hydrogenation of CO2 into Methanol for the Optimized and Alternative Case Designs

          • B.1.2.1 Raw Materials and Product Annual Prices

          • B.1.2.2 Annual Utility Cost

          • B.1.2.3 Equipment Sizing and Purchase Cost

          • B.1.2.4 Capital Cost Analysis

          • B.1.2.5 Production Cost Analysis

          • B.1.2.6 Production Cost Analysis

      • B.2 Bi-reforming of CO2 into Methanol

        • B.2.1 Bi-reforming of CO2 into Methanol for the Base Case Design

          • B.2.1.1 Raw Material, Product and Utilities Prices

          • B.2.1.2 Raw Materials and Product Annual Price

          • B.2.1.3 Annual Utility Cost

          • B.2.1.4 Equipment Sizing and Purchase Cost

          • B.2.1.5 Capital Cost Analysis

          • B.2.1.6 Production Cost Analysis

          • B.2.1.7 Profitability Assumptions

        • B.2.2 Bi-reforming of CO2 into Methanol for the Optimized Case

          • B.2.2.1 Raw Materials and Product Annual Price

          • B.2.2.2 Annual Utility Cost

          • B.2.2.3 Equipment Sizing and Purchase Cost

          • B.2.2.4 Capital Cost Analysis

          • B.2.2.5 Production Cost Analysis

        • B.2.3 Bi-reforming of CO2 into Methanol for the Alternative Case

          • B.2.3.1 Raw Materials and Product Annual Price

          • B.2.3.2 Annual Utility Cost

          • B.2.3.3 Equipment Sizing and Purchase Cost

          • B.2.3.4 Capital Cost Analysis

          • B.2.3.5 Production Cost Analysis

      • B.3 Tri-reforming of CO2 into Methanol

        • B.3.1 Tri-reforming of CO2 into Methanol for the Base Case

          • B.3.1.1 Raw Material, Product and Utilities Prices

          • B.3.1.2 Raw Materials and Product Annual Price

          • B.3.1.3 Annual Utility Cost

          • B.3.1.4 Equipment Sizing and Purchase Cost

          • B.3.1.5 Capital Cost Analysis

          • B.3.1.6 Production Cost Analysis

          • B.3.1.7 Profitability Assumptions

        • B.3.2 Tri-reforming of CO2 into Methanol for the Optimized Case

          • B.3.2.1 Raw Materials and Product Annual Price

          • B.3.2.2 Annual Utility Cost

          • B.3.2.3 Equipment Sizing and Purchase Cost

          • B.3.2.4 Capital Cost Analysis

          • B.3.2.5 Production Cost Analysis

        • B.3.3 Tri-reforming of CO2 into Methanol for the Alternative Case

          • B.3.3.1 Raw Materials and Product Annual Price

          • B.3.3.2 Annual Utility Cost

          • B.3.3.3 Equipment Sizing and Purchase Cost

          • B.3.3.4 Capital Cost Analysis

          • B.3.3.5 Production Cost Analysis

    • C. Appendix C Calculation of Indirect CO2 Emission

  • 9-Curriculum Vitae

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