“…This makes it possible to measure the intrinsical reaction kinetics of the etherification. The apparent activation energy measured is in accordance with the results found by Collignon et al [23] in the etherification of methanol and iso-butene over zeolite BEA. They measured apparent activation energies between 94 and 158 kJ/mol, depending on the SiO 2 :Al 2 O 3 ratio of the zeolite BEA used.…”
Section: Effect Of the Temperaturesupporting
confidence: 81%
“…In the synthesis of methyl-tert butyl ether (MTBE) from methanol and iso-butene zeolite BEA showed a comparable activity to the current commercial ion-exchange resin Amberlyst-15 [21][22][23]. Other zeolite catalysts (i.e.…”
The etherification of 1-octanol catalysed by zeolite BEA was investigated. The kinetics were determined in an open system with almost no water present. The influence of the catalyst particle size, catalyst concentration, temperature, and alcohol concentration was investigated. The apparent activation energy measured for the etherification was 149.8 kJ/mol. The 1-octanol showed an inhibiting effect on the reaction rate, i.e. when the concentration of 1-octanol increased the initial reaction rate decreased. This effect can be explained by a Langmuir-Hinshelwood like mechanism in which an adsorbed alcohol needs an empty neighbouring site to form an active intermediate and split of water. The influence of water on the kinetics was investigated using a closed autoclave set-up. Water showed a strong inhibiting effect on the initial reaction rate of the etherification of 1-octanol.
“…This makes it possible to measure the intrinsical reaction kinetics of the etherification. The apparent activation energy measured is in accordance with the results found by Collignon et al [23] in the etherification of methanol and iso-butene over zeolite BEA. They measured apparent activation energies between 94 and 158 kJ/mol, depending on the SiO 2 :Al 2 O 3 ratio of the zeolite BEA used.…”
Section: Effect Of the Temperaturesupporting
confidence: 81%
“…In the synthesis of methyl-tert butyl ether (MTBE) from methanol and iso-butene zeolite BEA showed a comparable activity to the current commercial ion-exchange resin Amberlyst-15 [21][22][23]. Other zeolite catalysts (i.e.…”
The etherification of 1-octanol catalysed by zeolite BEA was investigated. The kinetics were determined in an open system with almost no water present. The influence of the catalyst particle size, catalyst concentration, temperature, and alcohol concentration was investigated. The apparent activation energy measured for the etherification was 149.8 kJ/mol. The 1-octanol showed an inhibiting effect on the reaction rate, i.e. when the concentration of 1-octanol increased the initial reaction rate decreased. This effect can be explained by a Langmuir-Hinshelwood like mechanism in which an adsorbed alcohol needs an empty neighbouring site to form an active intermediate and split of water. The influence of water on the kinetics was investigated using a closed autoclave set-up. Water showed a strong inhibiting effect on the initial reaction rate of the etherification of 1-octanol.
“…The main advantage of the zeolite catalysts is their well-known better thermal stability compared with ion-exchange resins. Improved ether selectivities have been reported with zeolites but the activities have remained at a lower level than with the resins [94,95]. Improved ether selectivities have been reported with zeolites but the activities have remained at a lower level than with the resins [94,95].…”
The sections in this article are
Scope
Introduction and History of Tertiary Ethers
Chemistry
Main Etherification Reactions
Most Important Side Reactions
Thermodynamics of Ether Reactions
Kinetic Models
Other Ethers
Heavier Ethers
C
8
Alkenes
Higher Alcohols
Polyfunctional Ethers
Catalysts
Acidic Ion‐Exchange Resins
Zeolites and Modified Zeolites
Other Acidic Catalysts
Catalyst Deactivation
Raw Materials and Products
Typical Raw Materials
Feed Stream Treatment
Ether Products
Hydrocarbon Products
Processes
Operating Conditions
Processes for
MTBE
Production
Conventional
MTBE
Units
Reactive Distillation in
MTBE
Production
Processes for
ETBE
Production
Conversion of
MTBE
Plants for
ETBE
Production
Processes for
TAME
Production
Multipurpose Processes for Production of Ethers
Diesel Ethers
Dimethyl Ether
Properties of Dimethyl Ether
Processes for Dimethyl Ether Production
Di‐
n
‐Pentyl Ether
The Future
“…At 90°C the conversion degree of methanol and isobutene decreased slightly to 38% whereas the MTBE selectivity reached 98%. The MTBE yield of 37% reached by cloverite is remarkably high, but does not meet the higher values of about 50% of the commercial Amberlyst-15 catalysts or of zeolite beta [30,31]. However, compared to other zeolite types (HY, ZSM-5, ZSM-12 [32], mordenite, omega) cloverite shows a distinctly higher MTBE yield.…”
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