Abstract

A series of MoO3/Al2O3 catalysts with different amounts (molar ratio of CA/Mo = 0, 1, 1.5, and 2) of citric acid (CA) prepared by simultaneous impregnation were evaluated for sulfur-resistant methanation. Based on the evaluation results, catalytic activity increased accompanied with the rise of citric acid amount. Combine with the analysis of N2-physisorption, XRD, H2-TPR, XPS, and TEM, the catalyst saturated loading capacity improved, resulting in increasing dispersion of Mo species on Al2O3 surface clearly. According to H2-TPR result, the Mo oxide precursors can be more easily sulfureted when citric acid is added. Moreover, based on the Raman analysis, increasingly tetrahedrally coordinated Mo6+ species with high methanation performance are generated after citric acid treatment. These factors probably together accelerate MoO3/Al2O3 catalytic activity growth for methanation.

Highlights

  • With the energy shortage and contamination crisis on the environment [1], the efficient and clean use of coal resources has become increasingly significant

  • All samples showed typical and similar IV curves, with hysteresis loops according to the IUPAC classification system

  • After adding citric acid into catalysts, the Brunauer–Emmett–Teller (BET) surface area, the average pore volume, and the pore size of all catalyst samples are smaller than the Al2 O3 support

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Summary

Introduction

With the energy shortage and contamination crisis on the environment [1], the efficient and clean use of coal resources has become increasingly significant. The production of synthetic natural gas (SNG). Methanation is an essential process for SNG production. Ni-based catalyst can be used for a methanation reaction [3,4], but it is extremely sensitive to sulfur and only occurs as the molar ratio of H2 /CO is no less than 3:1. Considering its good performance in water-gas shift (WGS) reactions [5], Mo-based catalysts can exhibit good methanation activity at relatively low H2 /CO. The chemical equation for sulfur-resistant methanation on Mo-based catalyst can be expressed in the following equation [6]

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