Book contents
- Green Catalysis and Reaction Engineering
- Cambridge Series in Chemical Engineering
- Green Catalysis and Reaction Engineering
- Copyright page
- Dedication
- Contents
- Preface
- Acknowledgments
- 1 Sustainability Challenges of the Chemical Industry
- 2 Multiphase Catalytic Processes and Sustainability Challenges
- 3 Ethylene Production from Diverse Feedstocks and Energy Sources
- 4 Ethylene Epoxidation in Gas-Expanded Liquids with Negligible CO2 Formation as a Byproduct
- 5 Spray Reactor-Based Terephthalic Acid Production as a Greener Alternative to the Mid-Century Process
- 6 Sustainability Assessments of Hydrogen Peroxide-Based and Tertiary Butyl Hydroperoxide-Based Propylene Oxide Technologies
- 7 Separation of Propane/Propylene Mixture by Selective Propylene Hydroformylation in Gas-Expanded Liquids
- 8 A Greener Higher Olefin Hydroformylation Process
- 9 Solid Acid-Catalyzed Olefin/Isoparaffin Alkylation in Supercritical Carbon Dioxide
- 10 Epilogue
- Index
- References
8 - A Greener Higher Olefin Hydroformylation Process
Published online by Cambridge University Press: 15 September 2022
- Green Catalysis and Reaction Engineering
- Cambridge Series in Chemical Engineering
- Green Catalysis and Reaction Engineering
- Copyright page
- Dedication
- Contents
- Preface
- Acknowledgments
- 1 Sustainability Challenges of the Chemical Industry
- 2 Multiphase Catalytic Processes and Sustainability Challenges
- 3 Ethylene Production from Diverse Feedstocks and Energy Sources
- 4 Ethylene Epoxidation in Gas-Expanded Liquids with Negligible CO2 Formation as a Byproduct
- 5 Spray Reactor-Based Terephthalic Acid Production as a Greener Alternative to the Mid-Century Process
- 6 Sustainability Assessments of Hydrogen Peroxide-Based and Tertiary Butyl Hydroperoxide-Based Propylene Oxide Technologies
- 7 Separation of Propane/Propylene Mixture by Selective Propylene Hydroformylation in Gas-Expanded Liquids
- 8 A Greener Higher Olefin Hydroformylation Process
- 9 Solid Acid-Catalyzed Olefin/Isoparaffin Alkylation in Supercritical Carbon Dioxide
- 10 Epilogue
- Index
- References
Summary
Higher olefin hydroformylation with syngas to produce linear aldehydes uses cobalt-based catalyst complexes, which requires rather high temperatures (>180°C) and pressures (~20 MPa). Further, it entails substantial solvent usage to recover and recycle the cobalt complex. Rh-based catalysts are known to operate at milder conditions (<100°C and a few MPa) and are much more active and selective toward the linear aldehyde. However, Rh is three orders of magnitude more expensive than cobalt and requires near-quantitative recovery for economic viability. A new 1-octene hydroformylation process that uses carbon-dioxide expanded liquid (CXL) as solvent medium and a nanofiltration membrane to substantially retain the Rh-catalyst complex in the reactor was demonstrated by researchers at the University of Kansas Center for Environmentally Beneficial Catalysis to outperform the cobalt-based process, with capital investment being 30% lower than the Co-based process. Gate-to-gate life cycle assessments show that the CXL process is environmentally friendlier than the conventional process in most impact categories such as ecotoxicity, greenhouse gas emissions and smog formation.
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- Green Catalysis and Reaction EngineeringAn Integrated Approach with Industrial Case Studies, pp. 167 - 188Publisher: Cambridge University PressPrint publication year: 2022