The process of methanol dehydrogenation over nanostructured copper-containing catalyst
was simulated using a two-dimensional non-isothermal stationary mathematical model of …

Dehydrogenation of methanol was performed over copper-silica catalyst. Methyl formate
decomposition to carbon monoxide and hydrogen was considered as a main side reaction …

A two-dimensional non-isothermal stationary mathematical model of the catalytic membrane
reactor for the process of methanol dehydrogenation is described. Copper supported on the …

The catalytic oxidation of methanol was investigated employing a tubular wall reactor to
elucidate reaction kinetics and a membrane reactor to record performance. The membrane …

The kinetics of methanol dehydrogenation over copper catalyst supported on silica–
montmorillonite composite was studied. The samples of the catalyst were prepared by …

The modeling of ethylbenzene dehydrogenation in a catalytic membrane reactor has been
carried out for porous membrane by means of two-dimensional, non-isothermal stationary …

This research demonstrated thepossibility of achieving conversions above the
originalequilibrium conversion based on the feed conditions by combining the selective …

The two-dimensional non-isothermal stationary mathematical model of the catalytic
membrane reactor for the process of propane dehydrogenation has been developed. The …

A packed-bed catalytic ceramic membrane reactor (PBCMR) was used for the isobutane
dehydrogenation reaction. The experimental results have shown that through the use of the …

In this theoretical work the CO2 conversion into methanol in both a traditional reactor (TR)
and a membrane reactor (MR) is considered. The purpose of this study was to investigate …