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Methods for converting hydrocarbon fuel into hydrogen rich gas and for operating a fuel cell, and apparatus for producing electricity from hydrocarbon fuel

机译:用于将碳氢化合物燃料转化为富氢气体并操作燃料电池的方法以及用于从碳氢化合物燃料发电的设备

摘要

"METHODS FOR HYDROGEN RICH GAS HYDROCAR FUEL CONVERSION AND FOR OPERATING A FUEL CELL, AND ELECTRICITY PRODUCTION APPARATUS FROM THE HYDROCAR FUEL." An illustrative method for converting hydrocarbon fuel to hydrogen rich gas includes the steps of: reacting the hydrocarbon fuel with steam in the presence of reforming catalyst and a carbon dioxide fixing material to produce a first hydrogen gas; and removing carbon monoxide from the first hydrogen gas to produce the hydrogen rich gas, wherein the removal step utilizes a selected selective methanation or oxidation process. In one illustrative embodiment the carbon dioxide fixing material is selected from calcium oxide, calcium hydroxide, strontium oxide, strontium hydroxide, alanite, andralite, anquerite, anortite, aragonite, calcite, dolomite, clinozoisite, huntite, hydrotalcite. , lausonite, meionite, stroncianite, vaterita, jutnorita, mimnrecordita, benstonita, olecminsquita, nierereita, natrofairchildita, farichildita, zemcorita, butschlita, shirtita, remondita, petersenita, calyconite, cane, carciite nature and any combination thereof. The reforming catalyst in a preferred and illustrative embodiment is selected from nickel, platinum, rhodium, palladium, ruthenium, or similar supported reforming catalyst or combinations thereof. In such cases the reforming catalyst is preferably supported on a high surface area support thereby promoting the reforming reaction and more preferably is selected from alumina, titania, zirconia, or compounds of the like nature or combinations thereof. It is preferred that in an illustrative embodiment the temperature of the reaction step is from about 400Â ° C to about 800Â ° C.
机译:“用于富氢汽油燃料转化和操作燃料电池的方法,以及由该氢燃料产生的电力的装置。”将烃类燃料转化为富氢气体的说明性方法包括以下步骤:在重整催化剂和二氧化碳固定材料的存在下,使烃类燃料与蒸汽反应以产生第一氢气;从第一氢气中除去一氧化碳以产生富氢气体,其中所述除去步骤利用选择的选择性甲烷化或氧化过程。在一个说明性实施方案中,二氧化碳固定材料选自氧化钙,氢氧化钙,氧化锶,氢氧化锶,方铁石,红柱石,方铁矿,钙铁矿,文石,方解石,白云石,硅铁石、,石,水滑石。 ,月桂石,陨石,锶锶矿,vaterita,jutnorita,mimnrecordita,benstonita,olecminsquita,nierereita,natrofairchildita,farichildita,zemcorita,butschlita,shirtita,remondita,petersenita,钙铝榴石,甘蔗,蔗糖,钙镁石性质以及在优选和说明性实施方案中,重整催化剂选自镍,铂,铑,钯,钌或类似的负载型重整催化剂或它们的组合。在这种情况下,重整催化剂优选负载在高表面积载体上,从而促进重整反应,更优选选自氧化铝,二氧化钛,氧化锆或类似性质的化合物或其组合。优选地,在示例性实施方式中,反应步骤的温度为约400℃至约800℃。

著录项

  • 公开/公告号BR0208933A

    专利类型

  • 公开/公告日2005-05-10

    原文格式PDF

  • 申请/专利权人 TEXACO DEVELOPMENT CORPORATION;

    申请/专利号BR20020208933

  • 发明设计人 JAMES F. STEVENS;

    申请日2002-04-18

  • 分类号C01B3/38;C01B3/56;C01B3/58;H01M8/06;C01B3/32;

  • 国家 BR

  • 入库时间 2022-08-21 22:18:45

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