2015
DOI: 10.1007/s40090-015-0033-0
|View full text |Cite
|
Sign up to set email alerts
|

Geometry and reactor synthesis: maximizing conversion of the ethyl acetate process

Abstract: This paper describes how experimentally generated results were used to optimize conversion of a process using adiabatic batch reactor systems. The process used in the experiment was exothermic reversible process. The experiments were conducted using Dewar Thermosflask operating under adiabatic conditions. Equilibrium conversions were determined from temperature-time information. Temperatures were determined using negative temperature coefficient thermistor. For a single batch process, the equilibrium conversio… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...

Citation Types

0
0
0

Publication Types

Select...

Relationship

0
0

Authors

Journals

citations
Cited by 0 publications
references
References 5 publications
0
0
0
Order By: Relevance

No citations

Set email alert for when this publication receives citations?