English
 
Help Privacy Policy Disclaimer
  Advanced SearchBrowse

Item

ITEM ACTIONSEXPORT

Released

Journal Article

Intensified reactors for gas-liquid-liquid multiphase catalysis: From chemistry to engineering

MPS-Authors
/persons/resource/persons247521

Schrimpf,  Marco
Research Department Leitner, Max Planck Institute for Chemical Energy Conversion, Max Planck Society;

/persons/resource/persons237789

Esteban,  Jesus
Research Department Leitner, Max Planck Institute for Chemical Energy Conversion, Max Planck Society;

/persons/resource/persons247517

Rösler,  Thorsten
Research Department Leitner, Max Planck Institute for Chemical Energy Conversion, Max Planck Society;

/persons/resource/persons237870

Vorholt,  Andreas J.
Research Department Leitner, Max Planck Institute for Chemical Energy Conversion, Max Planck Society;

/persons/resource/persons58749

Leitner,  Walter
Research Department Leitner, Max Planck Institute for Chemical Energy Conversion, Max Planck Society;

External Resource
No external resources are shared
Fulltext (restricted access)
There are currently no full texts shared for your IP range.
Fulltext (public)
There are no public fulltexts stored in PuRe
Supplementary Material (public)
There is no public supplementary material available
Citation

Schrimpf, M., Esteban, J., Rösler, T., Vorholt, A. J., & Leitner, W. (2019). Intensified reactors for gas-liquid-liquid multiphase catalysis: From chemistry to engineering. Chemical Engineering Journal, 372, 917-939. doi:10.1016/j.cej.2019.03.133.


Cite as: https://hdl.handle.net/21.11116/0000-0006-5E33-8
Abstract
Biphasic liquid-liquid and particularly gas-liquid-liquid (GLL) environments are used in many chemical transformations performed by homogeneous catalysts where they have proven very effective for catalyst recycling, greatly improving the economy of using costly organometallic catalyst complexes such as for hydroformylation. Reacting GLL systems suffer from mass transfer limitations, for which intensified contacting is necessary to enhance the reaction rate. To tackle this issue, process intensified reactors have been designed and developed throughout the years to create large interfacial areas and high mass transfer coefficients. Apart from the classic continuously stirred tank reactor, setups like static mixer reactors, ejector loop reactors, and microreactors are promising alternatives that have gained momentum throughout the last years. This critical review covers the basic aspects of GLL mass transfer and a discussion on a number of reactions in this type of environment. More extensively, the current state of the art of contacting equipment for intensified GLL operation is described, including aspects of reactor design and correlations for different operating conditions.