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Selectively permeable membrane reactor and hydrogen production method using a selectively permeable membrane reactor
Selectively permeable membrane reactor and hydrogen production method using a selectively permeable membrane reactor
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机译:选择性渗透膜反应器和使用选择性渗透膜反应器的制氢方法
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摘要
In the hydrogen production process of the present invention, A [ml / min], the amount of hydrogen that has not passed through the selectively permeable membrane (non-permeated hydrogen amount of hydrogen separated by passing through the permselective membrane (permeated hydrogen amount) when as B [ml / min] amount), the value of the hydrogen recovery is defined by the following equation becomes a 60~99%, (CO 2), one the partial pressure of carbon dioxide at the outlet of the reaction tube When the (CO) and the partial pressure of carbon oxides, and to K the equilibrium constant for the disproportionation of carbon monoxide in the reaction tube temperature, under the condition that the value defined by the following equation α is 0.6 or more I do the production of hydrogen. Hydrogen recovery rate = 100 × {A / (A + B)} α ={(CO 2) / (CO) 2} / K
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