The paper investigates the effects of an additional mesoporous structure on the physicochemical, textural, and catalytic properties of a Mo/HZSM-5 catalyst for methane dehydroaromatization. The mesoporous structure was generated by adding carbon black P354 during the synthesis of a ZSM-5 zeolite; this carbon was removed during the subsequent calcination of the sample. The catalyst consisted of 0.5–1.0 mm pellets that were prepared by molding a zeolite powder into tablets followed by their grinding and sifting through sieves. The paper describes the results of an investigation into the methane dehydroaromatization kinetics, as well as relevant data obtained by X-ray fluorescence, IR spectroscopy, X-ray diffraction, low- temperature nitrogen ...
The active site requirements for methane dehydroaromatization by Mo/HZSM-5 were investigated by empl...
Two dealumination methods were used to modify the framework composition of the HZSM-5 zeolite. The s...
The effect of Mo/HZSM-5 pretreatment at 973 K in inert (He), oxidizing (artificial air), and carburi...
The structures of Mo/HZSM-5 catalysts with different molybdenum loadings were characterized and the ...
The influence of mesoporosity and silylation on the physico-chemical and catalytic properties of Mo/...
Non-oxidative dehydroaromatization is arguably the most promising process for the direct upgrading o...
The active site requirements for methane dehydroaromatization by Mo/HZSM-5 were investigated by empl...
The catalytic performance of the bifunctional catalyst Mo/HZSM-5 for methane dehydroaromatization (...
Methane, the main component of natural gas, is an interesting source of chemicals and clean liquid f...
The structures of Mo/HZSM-5 catalysts with various molybdenum loadings were studied by means of XRD,...
Methane, the main component of natural gas, is an interesting source of chemicals and clean liquid f...
The catalytic dehydrocondensation of methane to aromatics such as benzene and naphthalene was studie...
The deactivation of Mo/HZSM-5 during the non-oxidative methane aromatization (MDA) reaction that yie...
The conversion of methane into benzene, toluene and naphthalene at the reaction temperature of 750 В...
The active site requirements for methane dehydroaromatization by Mo/HZSM-5 were investigated by empl...
Two dealumination methods were used to modify the framework composition of the HZSM-5 zeolite. The s...
The effect of Mo/HZSM-5 pretreatment at 973 K in inert (He), oxidizing (artificial air), and carburi...
The structures of Mo/HZSM-5 catalysts with different molybdenum loadings were characterized and the ...
The influence of mesoporosity and silylation on the physico-chemical and catalytic properties of Mo/...
Non-oxidative dehydroaromatization is arguably the most promising process for the direct upgrading o...
The active site requirements for methane dehydroaromatization by Mo/HZSM-5 were investigated by empl...
The catalytic performance of the bifunctional catalyst Mo/HZSM-5 for methane dehydroaromatization (...
Methane, the main component of natural gas, is an interesting source of chemicals and clean liquid f...
The structures of Mo/HZSM-5 catalysts with various molybdenum loadings were studied by means of XRD,...
Methane, the main component of natural gas, is an interesting source of chemicals and clean liquid f...
The catalytic dehydrocondensation of methane to aromatics such as benzene and naphthalene was studie...
The deactivation of Mo/HZSM-5 during the non-oxidative methane aromatization (MDA) reaction that yie...
The conversion of methane into benzene, toluene and naphthalene at the reaction temperature of 750 В...
The active site requirements for methane dehydroaromatization by Mo/HZSM-5 were investigated by empl...
Two dealumination methods were used to modify the framework composition of the HZSM-5 zeolite. The s...
The effect of Mo/HZSM-5 pretreatment at 973 K in inert (He), oxidizing (artificial air), and carburi...