(43b) Single-Step Conversion of Methane to Liquid Hydrocarbon Fuels with a Layered Composite Catalyst | AIChE

(43b) Single-Step Conversion of Methane to Liquid Hydrocarbon Fuels with a Layered Composite Catalyst

Authors 

Zhao, X. - Presenter, University of South Florida
Cimenler, U., University of South Florida
Weber, D., University of South Florida
Joseph, B., University of South Florida
Kuhn, J., University of South Florida
Combination of steam reforming and Fischer-Tropsch Synthesis (FTS) is a potential process to convert methane directly to liquid hydrocarbon fuels. In this study, the combination of zeolite membrane coated composite steam reforming catalyst and FTS catalyst was used for a single-step conversion of methane to hydrocarbons. The layered reforming catalyst (zeolite membrane coated NiMg/Ce0.6Zr0.4O2) consisted of an outer layer of H-β zeolite encapsulating an inner reforming catalyst core. The layered reforming catalyst was synthesized using a double physical coating method. The layered reforming catalyst has been utilized for methane steam reforming and the methane conversion could reach ~ 30%. The methane conversion decreased with the increase of the zeolite shell thickness, which is proportional to the zeolite amount added [1]. The layered composite catalyst and Fe/SBA-15 catalyst were loaded in a micro fixed-bed glass U-tube. Methane and steam were used as reactants. The primary results show a high methane conversion (> 20%) and hydrocarbons were produced. The operation conditions including methane-to-steam molar ratio, temperature, and gas hourly space velocity (GHSV) will be optimized to produce more hydrocarbons.

[1] Cimenler, Ummuhan, Babu Joseph, and John N. Kuhn. "Effect of Zeolite Membrane Shell Thickness on Reactant Selectivity for Hydrocarbon Steam Reforming Using Layered Catalysts." Energy & Fuels 30, no. 7 (2016): 5300-5308.