Add to ORKGDehydration of 1-butanol over the catalytic membrane was carried out in a tubular membrane reactor. The main products were 1-butene and trans- and cis-2-butene. From experiments it can be found that operating conditions had an obvious influence on conversion of 1-butanol and the active sites on the membrane surface had a remarkable effect on the selectivity of 1-butene
Optimising catalyst and membrane performance and performing a fundamental analysis on the dehydrogen...
In a high‐temperature catalytic membrane reactor, a plug‐flow reactor is combined with a gas‐separat...
A chromium incorporated mesoporous silicate structured Cr/MCM-41 type catalyst was synthesized follo...
The dehydrogenation of isobutane on a commercial chromia-alumina catalyst was studied using a conven...
A catalytic membrane reactor (CMR) was applied in order to enhance the selectivity in the hydrogenat...
Isobutane dehydrogenation to isobutene has been investigated experimentally and by modelling for a m...
International audience—A two-stage method was developed for the synthesis of 1,3-butadiene by dehydr...
Butenes are considered as important olefinic building block to produce fuels/fuel additives and comm...
The oxidative dehydrogenation of ethane to ethylene was studied in a conventional fixed bed reactor ...
The reactions of methanol over catalytically active alumina membranes are described in this paper. A...
Phosphate catalytic systems (B-PO4, Al-PO4, Ca-Ni-PO4) were tested in transformation of 1-butanol, p...
The operation of a packed-bed membrane reactor (PBMR) was analyzed in comparison to a conventional f...
A catalytic membrane reactor with a Au–Pd catalyst, impregnated at the inner side of the membrane, w...
International audienceA new two-step dehydration-dehydrogenation catalytic process for the productio...
The potential of using various types and configurations of membranes in reactors attracts already a ...
Optimising catalyst and membrane performance and performing a fundamental analysis on the dehydrogen...
In a high‐temperature catalytic membrane reactor, a plug‐flow reactor is combined with a gas‐separat...
A chromium incorporated mesoporous silicate structured Cr/MCM-41 type catalyst was synthesized follo...
The dehydrogenation of isobutane on a commercial chromia-alumina catalyst was studied using a conven...
A catalytic membrane reactor (CMR) was applied in order to enhance the selectivity in the hydrogenat...
Isobutane dehydrogenation to isobutene has been investigated experimentally and by modelling for a m...
International audience—A two-stage method was developed for the synthesis of 1,3-butadiene by dehydr...
Butenes are considered as important olefinic building block to produce fuels/fuel additives and comm...
The oxidative dehydrogenation of ethane to ethylene was studied in a conventional fixed bed reactor ...
The reactions of methanol over catalytically active alumina membranes are described in this paper. A...
Phosphate catalytic systems (B-PO4, Al-PO4, Ca-Ni-PO4) were tested in transformation of 1-butanol, p...
The operation of a packed-bed membrane reactor (PBMR) was analyzed in comparison to a conventional f...
A catalytic membrane reactor with a Au–Pd catalyst, impregnated at the inner side of the membrane, w...
International audienceA new two-step dehydration-dehydrogenation catalytic process for the productio...
The potential of using various types and configurations of membranes in reactors attracts already a ...
Optimising catalyst and membrane performance and performing a fundamental analysis on the dehydrogen...
In a high‐temperature catalytic membrane reactor, a plug‐flow reactor is combined with a gas‐separat...
A chromium incorporated mesoporous silicate structured Cr/MCM-41 type catalyst was synthesized follo...