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Catalytic reactor for endothermic reaction processes, particularly for light hydrocarbon steam reforming

机译:用于吸热反应过程的催化反应器,特别是用于轻烃蒸汽重整的催化反应器

摘要

The catalytic reactor, particularly for steam reforming reactions, is a succession of reaction chambers suitable to carry out the series reactions forecasted in the hydrogen production process by means of the light hydrocarbons steam reforming (like: natural gas, LPG, etc.). Particularly, the reaction chambers of the reactor allows the exploitation of more than the 75% of the whole volume, making it available to be filled with suitable catalysts to perform the following reactions: hydrocarbons de-sulphurisation, pre-reforming, reforming, high shift temperature, low shift temperature and possible methanation.;The catalytic reactor results as constituted from: a first inner chamber filled with the hydrocarbons de-sulphurisation catalyst; a second chamber external to the first chamber and connected with her, filled with the pre-reforming catalyst; a third chamber inner and integrated to the second chamber and connected with her, filled with the reforming catalyst; a fourth chamber external to the third and connected with her, in succession filled with: the high temperature shift catalyst, the low temperature shift catalyst and, if necessary, the methanation catalyst. The fourth chamber have two ring shaped cavities: first one on top connected to the third chamber that is connected with the reactant water to control the temperature of the gases coming from the third chamber, as well; the second one at the bottom for the collection and the exit of the reaction products. The inlet of the reactants is in the first chamber. The third chamber besides operate in connection with one or more burners, each-one equipped with a couple of nozzles. The wrap of the catalytic reactor, fifth chamber, has the opening for the combustion exhausts gases exit.
机译:催化反应器,特别是用于蒸汽重整反应的反应器,是一系列反应室,适合于通过轻烃蒸汽重整(如天然气,LPG等)进行制氢过程中预测的串联反应。特别地,反应器的反应腔室可利用超过总体积的75%,使其可填充有合适的催化剂以进行以下反应:烃脱硫,预重整,重整,高转化率催化反应器的结果由以下组成:第一内腔中充满了烃类脱硫催化剂;在第一腔室外部并与之连接的第二腔室,其填充有预重整催化剂;第三腔,内部与第二腔成一体并与第二腔连通,并充满重整催化剂。第四腔室在第三腔室的外部并与其相连,该第四腔室依次填充有:高温变换催化剂,低温变换催化剂和(如果需要)甲烷化催化剂。第四腔室具有两个环形腔室:第一个在顶部连接到第三腔室,第三腔室与反应水连接以控制来自第三腔室的气体的温度。第二个位于底部,用于收集和排出反应产物。反应物的入口在第一腔室中。此外,第三腔室与一个或多个燃烧器相连,每个燃烧器配有一对喷嘴。催化反应器的外壳,第五腔室,具有用于燃烧废气排出的开口。

著录项

  • 公开/公告号EP1779925B1

    专利类型

  • 公开/公告日2009-06-24

    原文格式PDF

  • 申请/专利权人 HYDRO GEN AMODIO S A S;

    申请/专利号EP20060425730

  • 发明设计人 AMODIO FILIPPO;

    申请日2006-10-23

  • 分类号B01J8/04;

  • 国家 EP

  • 入库时间 2022-08-21 19:17:53

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