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Design, Use and Results from Combinatorial Steady-State Reactors for the Optimization of Highly Selective Heterogeneous Catalysts in Liquid Systems

Published online by Cambridge University Press:  01 February 2011

James L Spivack
Affiliation:
Combinatorial Chemistry Laboratory, GE Global Research Center, Niskayuna, NY, USA.
Jimmy Webb
Affiliation:
Cyclics Corporation, Schenectady, NY, USA.
William P Flanagan
Affiliation:
Combinatorial Chemistry Laboratory, GE Global Research Center, Niskayuna, NY, USA.
Cheryl Sabourin
Affiliation:
Combinatorial Chemistry Laboratory, GE Global Research Center, Niskayuna, NY, USA.
Ralph May
Affiliation:
Union College, Schenectady, NY, USA.
Lamyaa Hassib
Affiliation:
Combinatorial Chemistry Laboratory, GE Global Research Center, Niskayuna, NY, USA.
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Abstract

A reactor was designed, built and successfully operated that allowed the simultaneous running of 96 independent reactions at steady-state. Since the problem involved the attainment of 98% in selectivity from a starting point of 93%, very precise reproducibility in selectivity was required. Because selectivity varies with time in a batch reactor, and since commercial reactors for this process are continuous, continuous reactors operated at steady-state were required. Longterm standard deviation in selectivity of <0.2% was attained. Information feedback from so many reactors allowed study of variation in catalyst composition, liquid retention times, space velocity, temperature and other variables to be accomplished in relatively short time. Comparison between heterogeneous and homogeneous catalysis in the same reactors gave insight into the underlying mechanisms determining activity and selectivity. Results from 200 uL reactors scaled very well to laboratory and pilot plant sizes.

Type
Research Article
Copyright
Copyright © Materials Research Society 2004

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References

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