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SHIFT CATALYST, METHOD FOR REFINING GAS IN COAL GASIFICATION PLANT, AND GAS REFINING EQUIPMENT

机译:浮选催化剂,煤制气厂煤气精制方法及煤气精制设备

摘要

PROBLEM TO BE SOLVED: To provide a method for refining a gas in a coal gasification plant capable of suppressing energy loss associated with CO2 recovery in a coal gasification plant and capable of maintaining the soundness of a CO shift catalyst.;SOLUTION: In a gas refining method provided with: a cleaning step 60 where, to a generated gas generated by gasifying a carbon-containing solid fuel and at least containing CO and H2S, a water-soluble substance contained in the generated gas is removed; a CO shift step 70 in which the CO contained in the generated gas after the cleaning step is reacted with water vapor using a shift catalyst so as to be converted into CO2 and H2; and a CO2/H2S recovery step 80 in which the CO2 and H2S contained in the gas after the CO shift step are removed, the CO shift step is composed of two or more multistage shift reactors 20a, 20b, 20c, the shift reactors 20a, 20b on the upstream side are filled with a high temperature shift catalyst 12a, and the shift reactor 20c on the downstream side is filled with a low temperature shift catalyst 12b.;COPYRIGHT: (C)2014,JPO&INPIT
机译:解决的问题:提供一种在煤气化装置中精制气体的方法,该方法能够抑制与煤气化装置中的CO 2 回收相关的能量损失,并且能够保持CO变换的安全性。解决方案:在一种气体精制方法中,该气体精制方法包括:清洁步骤60,其中对通过气化至少含CO和H 2 S的含碳固体燃料而产生的生成气体中,除去产生的气体中所含的水溶性物质; CO变换步骤70,其中,利用变换催化剂使清洗工序后的生成气体中所含的CO与水蒸气反应,从而变换为CO 2 和H 2 ;以及CO 2 / H 2 S回收步骤80,其中包含的CO 2 和H 2 S除去CO变换工序后的气体,CO变换工序由两个以上的多级变换反应器20a,20b,20c构成,在上游侧的变换反应器20a,20b中填充有高温变换催化剂12a,下游的变换反应器20c装有低温变换催化剂12b 。;版权所有:(C)2014,日本特许厅&INPIT

著录项

  • 公开/公告号JP2014104428A

    专利类型

  • 公开/公告日2014-06-09

    原文格式PDF

  • 申请/专利权人 HITACHI LTD;

    申请/专利号JP20120259423

  • 发明设计人 SASAKI TAKASHI;AKIYAMA TOMOKO;

    申请日2012-11-28

  • 分类号B01J23/88;C10K3/04;

  • 国家 JP

  • 入库时间 2022-08-21 16:18:03

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