2000
DOI: 10.1016/s0920-5861(00)00326-6
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Recovery of dilute acetic acid through esterification in a reactive distillation column

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Cited by 98 publications
(48 citation statements)
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“…The energy consumption of the RD process is only half of the conventional batch one. Also the size of the plant could be drastically reduced [66,67].…”
Section: Reactive Distillationmentioning
confidence: 99%
“…The energy consumption of the RD process is only half of the conventional batch one. Also the size of the plant could be drastically reduced [66,67].…”
Section: Reactive Distillationmentioning
confidence: 99%
“…In this section we present a few possible column configurations for the recovery process. Some of these configurations are based on the work by Saha et al (2000). Configurations 1-6 shown in Fig.…”
Section: Alternate Designs For Acetic Acid Recovery By Rd Columnmentioning
confidence: 99%
“…Another very promising option is reactive distillation, where acetic acid is reacted off with a suitable alcohol in order to produce a valuable ester product at the one end of the column and the aqueous stream free of organic impurities at the other end of the column. In particular, esterification with n-butanol was proposed for this purpose (Saha et al 2000). In that work, however, by trial and error experiments a maximum of up to 58% acetic acid conversion was achieved with a 100% excess of butanol in feed.…”
Section: Introductionmentioning
confidence: 99%
“…This contribution proposes a dynamic reactive distillation column model taking into account the potential liquid phase splitting, very useful in practical studies on the intricate nonlinear process dynamic behavior (including steady state multiplicities, bistability and self sustained nonlinear oscillations). The algorithm is successfully tested on a benchmark example for acetic acid (AcH) recovery [3].…”
Section: Introductionmentioning
confidence: 99%