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CATALYTIC REFORMING-SHIFT PROCESSORS FOR HYDROGEN GENERATION AND CONTINUOUS FUEL CELL OPERATION

机译:氢气产生和连续燃料电池操作的催化重整转换器

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Improved multi-operational reforming and gas-shift processing and conversion systems for methane, natural gas, and coal gas to hydrogen and carbon oxide mixtures are utilized with product gases used to power hydrogen based fuel cells and to alternatively synthesize chemicals or fuels such as methanol. The systems involve effective reaction and separation processors as single, integrated or consecutive units to perform hydrocarbon conversion and recycling with product separation and downstream hydrogen utilization in fuel cells. Their design is based on reaction, separation and accompanied process engineering principles involving appropriate catalysis and specifications for feedstock and product gas composition. Experiments and modeling are underway to describe in detail the process function and operation of the developed systems. Inherent process parameters are varied within the models to describe variation effects on reactant conversion, yield, hydrogen throughput. Such parameters are among others the temperature, pressure, feed composition and inlet flowrate in the reactor and the hydrogen purity, feed rate and power output from the fuel cell. These new reaction-fuel cell power systems contribute into environmental and greenhouse pollution prevention by eliminating air pollutants including nitric oxides and carbon dioxide.
机译:甲烷,天然气和煤气转化为氢气和二氧化碳混合物的改进的多操作重整和燃气变换处理和转化系统,与用于为基于氢的燃料电池提供动力以及可替代地合成化学物质或燃料(例如甲醇)的产品气一起使用。该系统涉及作为单个,集成或连续单元的有效反应和分离处理器,以进行烃转化和再循环,并进行燃料电池中的产物分离和下游氢利用。他们的设计基于反应,分离和伴随的过程工程原理,涉及适当的催化作用以及原料和产物气体组成的规格。实验和建模正在进行中,以详细描述已开发系统的过程功能和操作。模型中固有的工艺参数是变化的,以描述对反应物转化率,产率,氢气通过量的变化影响。这些参数尤其是温度,压力,进料组成和反应器中的入口流速以及氢纯度,进料速率和从燃料电池输出的功率。这些新的反应燃料电池动力系统通过消除包括一氧化氮和二氧化碳在内的空气污染物,为防止环境和温室污染做出了贡献。

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