摘要:
A process for producing a purified synthesis gas stream from a feed synthesis gas stream comprising besides the main constituents carbon monoxide and hydrogen also hydrogen sulphide, HCN and/or COS, the process comprising the steps of: (a) contacting one part of the feed synthesis gas stream with a water gas shift catalyst in a shift reactor in the presence of water/steam to react at least part of the carbon water/steam monoxide with water, to obtain a shifted synthesis gas stream enriched in hydrogen and in carbon dioxide; (b) contacting another part of the feed gas stream with a hydrolysis catalyst in the presence of water to remove HCN and/or COS to obtain a hydrolysed synthesis gas stream depleted in HCN and/or COS; (c) removing H 2 S from the shifted synthesis gas stream and from the hydrolysed synthesis gas stream by contacting these gas streams in a H 2 S-removal zone with an aqueous alkaline washing liquid to obtain a H 2 S-depleted synthesis gas stream and a sulphide-comprising aqueous stream; (d) contacting the sulphide-comprising aqueous stream with sulphide-oxidizing bacteria in the presence of oxygen in a bioreactor to obtain a sulphur slurry and a regenerated aqueous alkaline washing liquid; (e) removing carbon dioxide from the H 2 S-depleted synthesis gas stream, to obtain the purified synthesis gas stream.
摘要:
Catalyst for use in the high temperature shift reaction comprising in its active form a mixture of zinc alumina spinel and zinc oxide in combination with an alkali metal selected from the group consisting of Na, K, Rb, Cs and mixtures thereof.
摘要:
A method for supplying hydrogen to a fuel cell comprising (a) a medium-reducing step, which comprises reforming (1) a liquid fuel to generate a reformed gas containing hydrogen and carbon monoxide, and supplying the reformed gas to a hydrogen-purifying unit (2A,2B) containing a carbon monoxide-oxidizing catalyst and a hydrogen-generating medium, to reduce the hydrogen-generating medium (2a) and oxidize the carbon monoxide; and (b) a medium-oxidizing step, which comprises supplying steam to a hydrogen-purifying unit containing a carbon monoxide-oxidizing catalyst (1a) and a hydrogen-generating medium, to generate hydrogen while oxidizing the hydrogen-generating medium, the medium-reducing step and the medium-oxidizing step being conducted alternately.
摘要:
Operating conditions for generating hydrogen by the water-gas shift reaction have been found which reduce the aging of Pt - Re bimetallic water-gas shift catalysts. The process parameters provide a stable operation in residential fuel processors and in hydrogen generators for on-site hydrogen generation.
摘要:
A process and a reactor vessel for production of hydrogen via the water gas shift reaction at CO/CO 2 ratios above 1.9, and steam to gas rations below 0.5, are disclosed, The process includes first reacting a feed gas mixture of carbon monoxide and steam in the presence of a precious metal catalyst on a structural support, yielding a resultant gas, and then reacting the resultant gas in the presence of a non-precious metal catalyst on a support medium. The reactor vessel includes a chamber having an inlet duct and an outlet. A structural support having the precious metal catalyst is positioned upstream of the non-precious metal catalyst positioned within the chamber. The structural support may be positioned within the inlet duct or within the chamber. The support medium may be a granular medium or a structural support.
摘要翻译:的方法,和低于0.5的反应器容器,用于通过在CO / CO 2比1.9以上的水煤气变换反应生产氢气,蒸汽到气体口粮,被光盘游离缺失,该方法包括首先使一氧化碳和水蒸汽的原料气体混合物 在贵金属催化剂对一个结构支撑的存在,产生一个合成的气体,然后将所得的在非贵金属催化剂的支撑介质上的存在下反应的气体。 反应器容器包括:具有入口管道和出口上的腔室。 具有贵金属催化剂使用的结构支撑被定位在腔室内位于所述非贵金属催化剂的上游。 结构支架可以在入口管道内或在腔室内被定位。 该支撑介质可以是粒状介质或结构载体。
摘要:
An apparatus for producing hydrogen gas wherein the apparatus includes a reactor. In one embodiment, the reactor includes at least two conversion-removal portions. Each conversion-removal portion comprises a catalyst section (24) configured to convert CO in the stream to CO 2 and a membrane section (26) located downstream of and in flow communication with the catalyst section (24). The membrane section (26) is configured to selectively remove the CO 2 from the stream and to be in flow communication with a sweep gas (38, 40).
摘要:
The present invention is a method and apparatus (vessel) for providing a heat transfer rate from a reaction chamber through a wall to a heat transfer chamber substantially matching a local heat transfer rate of a catalytic thermal chemical reaction. The key to the invention is a thermal distance defined on a cross-sectional plane through the vessel inclusive of a heat transfer chamber, reaction chamber and a wall between the chambers. The cross-sectional plane is perpendicular to a bulk flow direction of the reactant stream, and the thermal distance is a distance between a coolest position and a hottest position on the cross-sectional plane. The thermal distance is of a length wherein the heat transfer rate from the reaction chamber to the heat transfer chamber substantially matches the local heat transfer rate.
摘要:
The present invention relates to a method and apparatus for thermal chemical reactions. The method and apparatus can provide an enhanced reaction rates for thermal chemical reactions. A microchannel apparatus comprising: a header; at least two flow microchannels, at least two orifices; wherein an orifice connects said header with each flow microchannel; and wherein the ratio of the cross-sectional area of each of said at least two orifices to the cross-sectional area of the flow microchannels connected to said orifices is between 0.0005 and 0.1.