Catalytic pyrolysis of biomass is a promising method to convert biomass feedstock into high-
value products. However, coke formation on catalysts causes the severe deactivation and …

Abstract Global supply of 1, 3-butadiene (abbreviated as BD) is faced with a problem such
as variation in chemical feedstock in recent years. Many research efforts have been made to …

The kinetics of propane dehydrogenation to produce propene over a Cr2O3/Al2O3 catalyst
has been investigated over the temperature range of 525–575° C at atmospheric pressure …

A complete kinetic model of propane dehydrogenation to produce propene over a Pt–Sn–
K/Al2O3 catalyst was obtained. This has been investigated over the temperature range of …

Coke formation is one of the major obstacles in the development of catalytic pyrolysis of
biomass. The experiments were carried out on poplar wood chips using the biochar-based …

Steam reforming of methanol over a Cu/ZnO/Al2O3 catalyst has been investigated over the
temperature range of 493–573K at atmospheric pressure in a fixed bed reactor. A series of …

This work aims at providing insight into the deactivation mechanism of Pd-based
membranes in propane dehydrogenation processes. Thermogravimetric analysis (TGA) …

The gas-phase hydrogenation of ethyne, propyne, and propadiene was investigated over
partially reduced Ni–Al mixed oxides derived from takovite, a hydrotalcite-type compound …

Coke formation rates under propane dehydrogenation reaction conditions on a used
monolithic Pt/γ-Al2O3 catalyst have been experimentally determined in a thermogravimetric …

The effect of the support (here silica and silica-alumina) and of the composition of Ni-based
hydrogenation catalysts, elaborated by sol–gel method, on their physico-chemical …