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HERO ID
4641888
Reference Type
Journal Article
Title
Equilibrium conversion, selectivity and yield optimization of the simultaneous liquid-phase etherification of isobutene and isoamylenes with ethanol over Amberlyst (TM) 35
Author(s)
Soto, R; Fite, C; Ramirez, E; Bringue, R; Cunill, F
Year
2016
Is Peer Reviewed?
Yes
Journal
Fuel Processing Technology
ISSN:
0378-3820
Volume
142
Page Numbers
201-211
DOI
10.1016/j.fuproc.2015.09.032
Web of Science Id
WOS:000367107300023
Abstract
A prospective study on the product distribution at chemical equilibrium for the simultaneous liquid-phase etherification of isobutene and isoamylenes with ethanol over Amberlyst (TM) 35 is presented. Experiments were performed isothermally in a 200 cm(3) stirred tank batch reactor operating at 2.0 MPa. Initial molar ratios of alcohol/olefins and isobutene/isoamylenes ranged both from 05 to 2, and temperature from 323 to 353 K. Reactants equilibrium conversion, selectivities and yields toward products were clearly affected by the experimental conditions. Experimental etherification yields have been modeled using the response surface methodology (RSM), combined with the stepwise regression method to include only the statistically significant variables into the model. The multiobjective optimization (MOO) of etherification yields has been carried out numerically, by means of the desirability function approach, and graphically, by using the overlaid contour plots (OCP). Optimal conditions for the simultaneous production of ethyl tert-butyl ether (ETBE) and tert-amyl ethyl ether (TAEE) have been found to be at low temperatures (323 to 337 K) and initial molar ratio alcohol/olefins close to 0.9 and isobutene/isoamylenes close to 0.5. (C) 2015 Elsevier B.V. All rights reserved.
Keywords
Ethyl tert-butyl ether (ETBE); Tert-amyl ethyl ether (TAEE); Simultaneous etherification; Equilibrium conversion; Selectivity; Yield optimization
Tags
IRIS
•
tert-Amyl ethyl ether (TAEE)
Initial Litsearch 6/2018
WOS
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