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Catalytic pyrolysis and partial oxidation of methane and liquefied petroleum gas (LPG) were studied using a novel wire-mesh reactor (WMR) and a quartz tubular reactor. A non-porous nickel mesh was used as a catalyst to avoid the complexity of internal pore diffusion. The catalyst activities were stable even for the pyrolysis of pure methane and LPG when short gas-catalyst contact times were used....
Direct catalytic oxidation of CH 4 with air was studied using a wire-mesh reactor and a quartz tube reactor. Two types of nickel-containing catalysts (nickel and Monel 400 alloy) in the form of wire-mesh were used. The wire-mesh reactor features the minimisation of the thermally induced gas-phase reactions by rapidly quenching the products leaving the mesh catalyst surface. The wire-mesh reactor...
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