Run Parameters for a Continuous Hydrogenation Process Using ACMC-Pd To Replace Commercial Batch Reactor Processes-Reference-Cited by-同舟云学术

Run Parameters for a Continuous Hydrogenation Process Using ACMC-Pd To Replace Commercial Batch Reactor Processes

Published:2018-11-20 Issue:12 Volume:22 Page:1622-1627
ISSN:1083-6160
Container-title:Organic Process Research & Development
language:en
Short-container-title:Org. Process Res. Dev.

Author:

Gulotty Robert J.¹^ORCID,Rish Stephanie¹,Boyd Andrew¹,Mitchell Lee¹,Plageman Scott¹,McGill Corinne¹,Keller Joseph²,Starnes Jeter³,Stadalsky John³,Garrison George³

Affiliation:

1. Applied Catalysts, Applied Ceramics Inc., 5555 Pleasantdale Road, Doraville, Georgia 30340, United States

2. Supported Catalysts, 19191 Sterling Drive, Abingdon, Virginia 24211, United States

3. Santolubes Manufacturing LLC, 2155 West Croft Circle, Spartanburg, South Carolina 29302, United States

Publisher

American Chemical Society (ACS)

Subject

Organic Chemistry,Physical and Theoretical Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.oprd.8b00286

Reference28 articles.

1. The segmented two-phase flow monolithic catalyst reactor. An alternative for liquid-phase hydrogenations

2. Monoliths in Heterogeneous Catalysis

3. Monolithic Catalysts as an Alternative to Slurry Systems: Hydrogenation of Edible Oil

4. Parillo, D. J.; Boehme, R. P.; Brockhuis, R. R.; Machado, R. M. Use of a monolith catalyst for the hydrogenation of dinitrotoluene to toluenediamine. U.S. Patent 6,005,143, Dec 21, 1999.

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