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Hydrogen production method using selectively permeable membrane reactor and selectively permeable membrane reactor
Hydrogen production method using selectively permeable membrane reactor and selectively permeable membrane reactor
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机译:使用选择性渗透膜反应器和选择性渗透膜反应器的制氢方法
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摘要
In the present invention, a raw material gas is supplied from the inlet of a reaction tube, a mixed gas containing hydrogen, carbon monoxide and carbon dioxide is generated by reforming and shift reaction, and the permeated membrane is separated from the mixed gas. A method for producing hydrogen in which hydrogen separated in a pipe is recovered from a discharge port and other gas components that do not permeate the permselective membrane are discharged from an outlet, wherein the partial pressure of carbon dioxide at the outlet is (CO2) When the partial pressure of carbon monoxide is (CO) and the equilibrium constant of the disproportionation reaction of carbon monoxide at the temperature in the reaction tube is K, the value of α defined by the following formula is 0.4 to Hydrogen is produced under the conditions of 100. α = {(CO2) / (CO) 2} / K
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机译:在本发明中,从反应管的入口供给原料气体,通过重整和变换反应生成包含氢,一氧化碳和二氧化碳的混合气体,并从该混合气体中分离出透过膜。一种氢气的制造方法,其中,从排出口回收在管道中分离出的氢气,并从出口排出未渗透该选择性渗透膜的其他气体成分,其中,该出口处的二氧化碳分压为(CO2)。一氧化碳的分压为(CO),一氧化碳在反应管中的温度歧化反应的平衡常数为K,下式定义的α值为0.4-在以下条件下产生氢气100.α= {(CO2)/(CO)2} / K
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