Rh‐Catalyzed Hydrogenation of CO2 to Formic Acid in DMSO‐based Reaction Media: Solved and Unsolved Challenges for Process Development
dc.contributor.author
Jens, Christian M.
dc.contributor.author
Scott, Martin
dc.contributor.author
Liebergesell, Bastian
dc.contributor.author
Westhues, Christian G.
dc.contributor.author
Schäfer, Pascal
dc.contributor.author
Franciò, Giancarlo
dc.contributor.author
Leonhard, Kai
dc.contributor.author
Leitner, Walter
dc.contributor.author
Bardow, André
dc.date.accessioned
2020-07-21T06:44:34Z
dc.date.available
2020-07-20T09:48:06Z
dc.date.available
2020-07-21T06:44:34Z
dc.date.issued
2019-01-22
dc.identifier.issn
1615-4150
dc.identifier.issn
1615-4169
dc.identifier.other
10.1002/adsc.201801098
en_US
dc.identifier.uri
http://hdl.handle.net/20.500.11850/427101
dc.description.abstract
Process concepts have been conceived and evaluated for the amine‐free homogeneous catalyzed hydrogenation of CO2 to formic acid (FA). Base‐free DMSO‐mediated production of FA has been shown to avoid the formation of stable intermediates and presumably the energy‐intensive FA recovery strategies. Here, we address the challenges in the development of an overall process: from catalyst immobilization to the FA isolation. The immobilization of the homogeneous catalyst was achieved using a multiphasic approach (n‐heptane/DMSO) ensuring high retention of the catalyst (>99%) and allowing facile separation of the catalyst‐free product phase. We show that the strong molecular interactions between DMSO and FA on the one hand shift the equilibrium towards the product side, on the other hand, lead to the formation of an azeotrope preventing a simple isolation step by distillation. Thus, we devised an isolation strategy based on the use of co‐solvents and computed the energy demands. Acetic acid was identified as best co‐solvent and its compatibility with the catalyst system was experimentally verified. Overall, the outlined process involving DMSO and acetic acid as co‐solvent has a computed energy demand on a par with state‐of‐the art amine‐based processes. However, the insufficient chemical stability of DMSO poses major limitations on processes based on this solvent.
en_US
dc.language.iso
en
en_US
dc.publisher
Wiley-VCH
en_US
dc.subject
Carbon dioxide hydrogenation
en_US
dc.subject
Biphasic catalysis
en_US
dc.subject
PC-SAFT
en_US
dc.subject
COSMO-RS
en_US
dc.subject
DMSO decomposition
en_US
dc.title
Rh‐Catalyzed Hydrogenation of CO2 to Formic Acid in DMSO‐based Reaction Media: Solved and Unsolved Challenges for Process Development
en_US
dc.type
Journal Article
dc.date.published
2018-10-04
ethz.journal.title
Advanced Synthesis & Catalysis
ethz.journal.volume
361
en_US
ethz.journal.issue
2
en_US
ethz.journal.abbreviated
Adv. Synth. Catal.
ethz.pages.start
307
en_US
ethz.pages.end
316
en_US
ethz.publication.place
Weinheim
en_US
ethz.publication.status
published
en_US
ethz.leitzahl
ETH Zürich::00002 - ETH Zürich::00012 - Lehre und Forschung::00007 - Departemente::02130 - Dep. Maschinenbau und Verfahrenstechnik / Dep. of Mechanical and Process Eng.::02668 - Inst. f. Energie- und Verfahrenstechnik / Inst. Energy and Process Engineering::09696 - Bardow, André / Bardow, André
en_US
ethz.leitzahl.certified
ETH Zürich::00002 - ETH Zürich::00012 - Lehre und Forschung::00007 - Departemente::02130 - Dep. Maschinenbau und Verfahrenstechnik / Dep. of Mechanical and Process Eng.::02668 - Inst. f. Energie- und Verfahrenstechnik / Inst. Energy and Process Engineering::09696 - Bardow, André / Bardow, André
en_US
ethz.date.deposited
2020-07-20T09:48:15Z
ethz.source
BATCH
ethz.eth
no
en_US
ethz.availability
Metadata only
en_US
ethz.rosetta.installDate
2020-07-21T06:44:45Z
ethz.rosetta.lastUpdated
2021-02-15T15:33:13Z
ethz.rosetta.versionExported
true
ethz.COinS
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