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Effect of reaction variables on CO methanation process over NiO-La2O3-MgO/Al2O3 catalyst for coal to synthetic natural gas

机译:NiO-La2O3-MgO / Al2O3催化剂制煤制合成天然气中反应变量对CO甲烷化过程的影响

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摘要

Reaction variables for methanation process were investigated using self-independently developed NiO-La2O3-MgO/Al2O3 catalyst in a big lab scale reactor. The effects of reaction parameters, such as temperature, pressure, H2/CO flow ratio and space velocity on the activity of methanation catalyst were studied. 100 % CO conversion and 95 % of selectivity of methane can be achieved at 400 °C and 3 MPa with the feed ratio of H2/ CO as 3.25:1 and space velocity of 12,000 h~(-1).The optimization reaction parameters were suggested on the basis of this work for the further development and commercialization of methanation catalyst.
机译:在大型实验室规模的反应器中,使用自主开发的NiO-La2O3-MgO / Al2O3催化剂研究了甲烷化过程的反应变量。研究了温度,压力,H2 / CO流量比和空速等反应参数对甲烷化催化剂活性的影响。 H2 / CO的进料比为3.25:1,空速为12,000h〜(-1),在400°C和3 MPa下可实现100%CO转化率和95%的甲烷选择性。在这项工作的基础上建议将甲烷化催化剂进一步开发和商业化。

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