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A new process for synthesis gas by co-gasifying coal and natural gas

机译:煤与天然气共气化制合成气的新工艺

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Production of synthesis gas with coal and natural gas co-gasification is a new process based on coupling of methane steam-reforming and coal gasification. The process concept is discussed in this paper. Experiments are earned out in a laboratory fixed-bed gasifying reactor to investigate the effect of feedstock on composition, ratio of hydrogen to carbon monoxide, concentrations of hydrogen and carbon monoxide in the produced raw synthesis gas. Preliminary experimental results indicate that the effect of steam flow rate on component, ratio of hydrogen to carbon monoxide and concentrations of hydrogen and carbon monoxide of the raw synthesis gas is slight, while the effect of oxygen flow rate is pronounced. When the ratio of oxygen to methane in feedstock is below 1, the ratio of hydrogen to carbon monoxide is greater than 1 and the total concentration of hydrogen and carbon monoxide is above 90 percent. Comparison of experimental results with calculated results shows that the composition of raw synthesis gas is near equilibrium.
机译:煤与天然气共气化生产合成气是基于甲烷蒸汽重整与煤气化耦合的新工艺。本文讨论了过程概念。在实验室固定床气化反应器中进行了实验,以研究原料对组成,氢气与一氧化碳之比,所产生的粗合成气中氢气和一氧化碳浓度的影响。初步实验结果表明,蒸汽流速对原料气,原料合成气中氢,一氧化碳的比例以及氢和一氧化碳的浓度的影响很小,而氧气流速的影响则很明显。当原料中氧气与甲烷的比例小于1时,氢气与一氧化碳的比例大于1,氢气和一氧化碳的总浓度大于90%。实验结果与计算结果的比较表明,原料合成气的组成接近平衡。

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