Abstract Process Economics Program Report 269 SUPERCRITICAL CO2: A GREEN SOLVENT

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Abstract Process Economics Program Report 269 SUPERCRITICAL CO2: A GREEN SOLVENT ( abstract-process-economics-program-report-269-supercritical- )

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TABLES 2.1 Cost Estimate of Supercritical Extraction Processes ............................................ 2-6 2.2 Comparison of FEP Production Processes ........................................................... 2-9 2.3 Comparison of Capital Investment Costs for FEP Processes............................... 2-10 2.4 Comparison of Production Costs for FEP Processes ........................................... 2-10 2.5 Comparison of Production Costs for Polycarbonate Processes ........................... 2-11 3.1 Commercial and Potential Applications for Supercritical CO2............................... 3-5 3.2 Commercial Scale Supercritical CO2 Extraction Plants and Processes ............... 3-8 4.1 Critical Conditions of Different Solvents................................................................ 4-2 4.2 Typical Physical Properties of Gas, Supercritical Fluid and Liquid....................... 4-2 5.1 Supercritical CO2 Applications in Chemical Reactions.......................................... A-3 5.2 Several Enzymatic Reactions Tested in scCO2 Medium ...................................... 5-11 5.3 Hydroformylation of Octene Using Supercritical CO2 Design Bases and Assumptions............................................................................ 5-17 5.4 Hydroformylation of Octene Using Supercritical CO2 Stream Flows......................................................................................................... 5-18 5.5 Hydroformylation of Octene Using Supercritical CO2 Major Equipment ................................................................................................... 5-19 5.6 Hydroformylation of Octene Using Supercritical CO2 Total Capital Investment........................................................................................ 5-23 5.7 Hydroformylation of Octene Using Supercritical CO2 Production Costs ................................................................................................... 5-24 5.8 Comparison of Hydroformylation Production Processes ...................................... 5-26 5.9 Comparison of Costs for Nonyl Aldehyde Production Processes......................... 5-27 6.1 Supercritical CO2 Applications in Extractions ........................................................ A-8 6.2 Advantages of Using Supercritical CO2 Extraction for Natural Products .............. 6-5 6.3 Supercritical CO2 Extraction Process with Low Pressure Recycling Design Bases and Assumptions............................................................................ 6-12 6.4 Supercritical CO2 Extraction Process with High Pressure Recycling Design Bases and Assumptions............................................................................ 6-13 6.5 Cost Estimate of Supercritical Extraction Processes ............................................ 6-14 © SRI Consulting xi PEP Report 269

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