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Process and apparatus for gasifying solid fuels in gas producers

机译:在气体发生器中气化固体燃料的方法和设备

摘要

462,933. Gas producers. KRUPP AKT.-GES., F. March 17, 1936, No. 7982. Convention date, March 23, 1935. [Class 55 (i)] In a gas producer in which the air supply, with or without steam, and the gas withdrawal are effected in the neighbourhood of the gasefication zone, the former is introduced through a central pipe 12 and the latter removed through outlets 3 in the periphery of the shaft, so as to produce a relatively shallow gasefication zone of truncated conical form with symmetrical flow of the gases therethrough. The direction of gasefication is reversible by interchanging the air supply and gas withdrawal. In a modification of the process, the gas supply and withdrawal are effected at the same level so as to produce a disc-shaped gasefication zone. In the alternative method of working, steam from a heat-exchanger 15, supplied with feedwater from an annular tank 16 in the upper part of the shaft and heated by the evolved gases from the pipe 12, is supplied to an external ring-shaped pipe 6 provided with spaced nozzles 7 terminating in front of nozzle-shaped vertical air inlets 5, the gases thoroughly mixing in an annular channel 4 within the wall of the producer before issuing into the fuel bed through horizontal spaced nozzles 3 arranged below the narrowest section of the shaft. The wall of the producer is thus cooled. If the latter is unnecessary such as with a wall composed of sillimanite, the channel 4 and inlets 5 may be dispensed with. Air may also be mixed with the steam in the heat-exchanger through a valved inlet 19. The single offtake pipe 12 may be replaced by a number of concentrically arranged pipes, these pipes being provided with perforated hoods 13 to prevent removal of fuel particles.. In the reversed method of working, the steam supply pipes 18, 6 are removed and replaced by draw-off pipes for the gaseous products connected to the vertical channels 5. In a modified form of the producer, the cooling channels 4, 5 in the shaft wall are replaced by an air- or water-cooled jacket, and the steam admission nozzles 7 terminate horizontally in front of the horizontal air inlets 3, the latter being also cooled by the jacket through which they pass. The upper part of the jacket is of spiral form to increase the cooling air velocity.
机译:462,933。天然气生产商。 F. KRUPP AKT.-GES。,1936年3月17日,第7982号。会议日期,1935年3月23日。[第55(i)类]在气体产生器中,在有空气供应的情况下,有或无蒸汽,以及气体抽出在气化区附近进行,前者通过中心管12引入,后者通过竖井外围的出口3除去,从而产生了一个相对较浅的截锥形的对称对称的气化区。气体从中流过。气化方向可通过交换空气供应和抽气来实现。在该方法的变型中,气体的供给和排出在相同的水平上进行,以产生盘形的气化区。在另一种工作方法中,来自热交换器15的蒸汽由竖井上部的环形水箱16提供给水,并被来自管道12的放出的气体加热,再供给外部环形管道。如图6所示,在喷嘴形的垂直进气口5的前面设有间隔开的喷嘴7,气体在生产者壁内的环形通道4中充分混合,然后通过布置在喷嘴最窄部分下方的水平间隔开的喷嘴3进入燃料床。轴。生产者的壁因此被冷却。如果后者是不必要的,例如具有由硅线石组成的壁,则可以省去通道4和入口5。空气也可以通过阀式入口19与热交换器中的蒸汽混合。单个排气管12可以用许多同心布置的管子代替,这些管子上有穿孔的罩13,以防止燃料颗粒的去除。在相反的工作方法中,蒸汽供应管18、6被移除并由排泄管代替,用于连接到垂直通道5的气态产物。竖井壁被空气冷却或水冷的外套所代替,并且蒸汽进入喷嘴7在水平的进气口3的前面水平终止,后者也被它们所通过的外套冷却。外套的上部为螺旋形,以增加冷却空气的速度。

著录项

  • 公开/公告号GB462933A

    专利类型

  • 公开/公告日1937-03-18

    原文格式PDF

  • 申请/专利权人 FRIED. KRUPP AKTIENGESELLSCHAFT;

    申请/专利号GB19360007982

  • 发明设计人

    申请日1936-03-17

  • 分类号C10J3/00;C10J3/80;

  • 国家 GB

  • 入库时间 2022-08-24 05:42:52

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