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    • 87. 发明公开
    • VORRICHTUNG UND VERFAHREN ZUR REINIGUNG UND GEWINNUNG VON ENERGIEHALTIGEN GASEN
    • EP3024912A1
    • 2016-06-01
    • EP14765845.4
    • 2014-07-18
    • Leyendecker, Kurt
    • Leyendecker, Kurt
    • C10K1/02C10J3/30
    • The invention relates to a device and a method for purifying and obtaining gases that contain energy, wherein a filter container (2) equipped with an energy carrier as a filter material (energy-carrier filter material) (13) is used, which filter container comprises, in the upper region thereof, a material lock (4) for supplying the filter container (2) as well as a gas outlet stub (9) and, on a bottom thereof, a material outlet opening (17), such that a gravity-induced material flow from the material lock (4) to the material output opening (17) is made possible, wherein the filter container is operatively connected to a gasification and/or combustion apparatus via the material outlet opening (17).
    • 本发明涉及一种用于净化和获得含有能量的气体的装置和方法,其中使用装备有作为过滤材料的能量载体(能量载体过滤材料)(13)的过滤容器(2),该过滤容器 在其上部区域包括用于供应过滤器容器(2)的材料锁(4)以及气体出口短管(9),并且在其底部包括材料出口(17),使得 重力感应材料从材料锁(4)流到材料输出口(17)成为可能,其中过滤容器经由材料出口(17)可操作地连接到气化和/或燃烧装置。
    • 89. 发明公开
    • BIOMASS SYNGAS PURIFICATION PROCESS UNDER POSITIVE PRESSURE FOR PRODUCING OIL AND SYSTEM CONFIGURATION THEREOF
    • 清洗过程中生物质合成气下压力油的生产和系统配置THEREFOR
    • EP2799526A4
    • 2015-09-23
    • EP12863066
    • 2012-10-26
    • WUHAN KAIDI ENG TECH RES INST
    • ZHANG YANFENGNIE HONGTAOXIA MINGGUILIU WENYANZHANG LIANG
    • C10K1/00C01B3/02C10K1/02C10K1/04C10K1/06C10K1/10
    • C01B3/02C10G2300/1011C10J3/06C10J2300/0916C10J2300/1238C10K1/02C10K1/028C10K1/046C10K1/06Y02P20/123Y02P20/124Y02P20/129Y02P20/145Y02P30/20
    • Provided is a biomass syngas purification process under positive pressure for producing oil and the system thereof. In the process, an oxidation air blower is employed to blast a high-temperature pyrolysis gasifier; a high-temperature syngas extracted from the gasifier enters a water-cooled chilling tower via a water-cooled flue, and the gas is partly chilled to solidify slag by spraying water; the waste heat is recovered by a waste heat boiler of a water-tube type and a waste heat boiler of a heat-tube type in two stages with double pressure; the by-products, middle pressure steam and low pressure steam, are ejected externally; after the heavy tar is condensed and recovered by the waste heat boiler of the heat-tube type, the resulting syngas enters a Venturi scrubber without padding, scrubbing dust extraction, a wet electrostatic precipitator for deep dust extraction, and is purified by removing tar fog; then the acceptable syngas is transported to a wet gas-holder for storage or supplied for use down-stream. The purification aims of cooling of the syngas in stages, gradient recycling of waste heat, stepwise dust extraction and tar removal are achieved and the technical problems of a complex system, long flow, high energy consumption, low efficiency, and poor stability and economy are resolved by optimizing the process and controlling the appropriate process parameters.
    • 提供的是在正压力下生产油和系统及其生物质的合成气的纯化过程。 在这个过程中,在氧化空气鼓风机采用爆炸高温热解气化器; 从气化器中提取的高温的合成气进入通过水冷烟道水冷冷却塔,气体是部分地通过冷却水喷洒到固化的炉渣; 的废热通过水 - 管型和在两个阶段双压力的热管式的废热锅炉的废热锅炉回收; 的副产物,中压蒸汽和低压蒸汽,被外部排出; 重焦油被冷凝并通过热管型的废热锅炉回收后,将所得的合成气进入没有填充一个文丘里洗涤器,洗涤除尘,为深除尘湿式静电除尘器,而通过去除焦油雾纯化 ; 然后将合成气可接受被输送到湿气柜用于储存或用于提供下游。 纯化的目的在阶段的合成气的冷却的,废热,逐步吸尘和焦油去除,并且获得了一个复杂的系统的技术问题,长的流动,能耗高,效率低,且稳定性差,经济的梯度回收是 通过优化工艺和控制合适的工艺参数得到解决。