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Optimal design and operation of methane steam reforming in a porous ceramic membrane reactor for hydrogen production

机译:制氢用多孔陶瓷膜反应器中甲烷蒸汽重整的优化设计和运行

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Multi-objective optimization is performed for methane steam reforming in a porous ceramic membrane reactor using nitrogen and steam as sweep gases. The non-dominated sorting genetic algorithm (NSGA) is applied in solving the optimization problems. The Pareto optimal solutions have been obtained for the simultaneous maximization of the hydrogen production rate and the recovery yield, and for the simultaneous maximization of the hydrogen production rate and minimization of the sweep gas flow rate or the membrane area. The comparisons of the membrane reactor performances for nitrogen and steam as sweep gases at optimal conditions illustrate that the use of steam as a sweep gas can produce more hydrogen at higher recovery yield, or produce more hydrogen using less sweep gas or membrane area. (c) 2007 Elsevier Ltd. All rights reserved.
机译:使用氮气和蒸汽作为吹扫气,对多孔陶瓷膜反应器中的甲烷蒸汽重整进行了多目标优化。非支配排序遗传算法(NSGA)被用于解决优化问题。已经获得了帕累托最优解,用于同时最大化氢气产生速率和回收率,以及同时最大化氢气产生速率和最小化吹扫气体流速或膜面积。在最佳条件下将氮气和蒸汽用作吹扫气的膜反应器性能的比较表明,使用蒸汽作为吹扫气可以以更高的回收率产生更多的氢,或者使用更少的吹扫气或膜面积产生更多的氢。 (c)2007 Elsevier Ltd.保留所有权利。

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