Kinetics of liquid phase synthesis of methyl tert-butyl ether from tert-butyl alcohol and methanol catalyzed by ion exchange resin

1993 ◽  
Vol 25 (10) ◽  
pp. 825-831 ◽  
Author(s):  
Mohammed H. Matouq ◽  
Shigeo Goto
Keyword(s):  
Liquid Phase ◽  
Exchange Resin ◽  
Ion Exchange Resin ◽  
Butyl Alcohol ◽  
Methyl Tert Butyl Ether ◽  
Butyl Ether ◽  
Phase Synthesis ◽  
Tert Butyl ◽  
Tert Butyl Alcohol ◽  
Kinetics Of

Liquid-phase synthesis of isopropyl tert-butyl ether by addition of 2-propanol to isobutene on the oversulfonated ion-exchange resin Amberlyst-35

2007 ◽  
Vol 323 ◽  
pp. 38-50 ◽  
Author(s):  
Marc Pera-Titus ◽  
Marta Bausach ◽  
Javier Tejero ◽  
Montserrat Iborra ◽  
Carles Fité ◽  
...  
Keyword(s):  
Liquid Phase ◽  
Ion Exchange ◽  
Exchange Resin ◽  
Ion Exchange Resin ◽  
Butyl Ether ◽  
Phase Synthesis ◽  
Tert Butyl

Kinetics of Gas Phase Synthesis of Ethyl-tert-butyl Ether (ETBE) on H3PW12O40/MCM-41 Catalyst

2018 ◽  
Vol 69 (11) ◽  
pp. 3042-3047
Author(s):  
Song Il Kong ◽  
Anca Borcea ◽  
Diana Cursaru ◽  
Dragos Ciuparu
Keyword(s):  
Partial Pressure ◽  
Gas Phase ◽  
Butyl Alcohol ◽  
Butyl Ether ◽  
Phase Synthesis ◽  
Tert Butyl ◽  
Tert Butyl Alcohol ◽  
Different Temperatures ◽  
Kinetics Of ◽  
Mcm 41

The mechanism and kinetics of gas phase synthesis of ethyl-tert-butyl ether (ETBE) in the reaction between tert-butyl alcohol (TBA) and ethanol (EtOH) were investigated performing the reaction in a continuous flow quartz reactor at different temperatures and atmospheric pressure, using a heteropoliacid catalyst with 30wt% loading, dispersed on MCM-41. The Eley-Rideal reaction mechanism was previously proposed based on experimental observations that showed the rate of ETBE increased when partial pressure of tert-butyl alcohol increased, and the partial pressure of ethanol decreased, without significant effects on product selectivity. The kinetic model based on the Eley-Rideal mechanism was proposed and successfully employed to model accurately the experimental data at three different temperatures. The apparent activation energy and the frequency factor of the etherification reaction were 39.42 kJ/mol and 1.69 x 108 mol/kg . h . bar, respectively.

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