首页> 外国专利> AN APPLICATION OF A BAG-TYPE DUST REMOVING METHOD IN PROCESSING CRUDE SYNTHETIC GAS PRODUCED BY FLUIDIZED-BED EQUIPMENT OF COAL GASIFICATION AND BAG-TYPE DUST REMOVING EQUIPMENT THEREOF

AN APPLICATION OF A BAG-TYPE DUST REMOVING METHOD IN PROCESSING CRUDE SYNTHETIC GAS PRODUCED BY FLUIDIZED-BED EQUIPMENT OF COAL GASIFICATION AND BAG-TYPE DUST REMOVING EQUIPMENT THEREOF

机译:袋式除尘方法在煤制气化流化床制粗合成气及其袋式除尘设备中的应用

摘要

A dust removal method using baghouse filter to process raw syngas from fluidized bed coal gasifier, wherein temperature in the baghouse (300) is maintained at 180°C~250°C, pressure difference between the gas inlet (130) of the baghouse (300) and the gas outlet (110) of the baghouse (300) is controlled at 1000-5000Pa, the raw syngas from the fluidized bed coal gasifier enters the gas inlet under the pressure of 0.2-3.0Mpa. The present method effectively solves the technical problems of condensation and baghouse block due to high steam and ash content in the raw syngas from the fluidized bed coal gasifier and the present method is also applicable to remove dusts from the raw syngas produced by the fluidized bed coal gasifier under the conditions of high water-gas ratio (the water-gas ratio is up to 37%), high dust content (15-100g/Nm3 dusts) and 0.2-3.0Mpa pressure. The present invention also discloses a baghouse dust collector and a dense phase pneumatic conveying apparatus for the method.
机译:一种利用布袋除尘器除尘器处理流化床煤气化炉粗合成气的除尘方法,其中布袋除尘器(300)内的温度保持在180℃〜250℃,布袋除尘器(300)的进气口(130)之间的压差较大袋式除尘器(300)的出气口(110)控制在1000-5000Pa,来自流化床煤气化炉的粗合成气在0.2-3.0Mpa的压力下进入进气口。本方法有效地解决了流化床煤气化炉粗合成气中蒸汽和灰分含量高引起的冷凝和布袋除尘的技术问题,也适用于去除流化床煤产生的粗合成气中的粉尘。在高水气比(水气比高达37%),高粉尘含量(15-100g / Nm3粉尘)和0.2-3.0Mpa压力的条件下进行气化炉。本发明还公开了一种集尘室和该方法的密相气力输送装置。

著录项

  • 公开/公告号IN2010DN09234A

    专利类型

  • 公开/公告日2012-03-09

    原文格式PDF

  • 申请/专利权人

    申请/专利号IN9234/DELNP/2010

  • 发明设计人 GU MINGHAI;SUN SONGLIANG;LUO GUANGLIANG;

    申请日2010-12-24

  • 分类号B01D46/02;

  • 国家 IN

  • 入库时间 2022-08-21 17:24:24

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