Reactor for gasifying solid fuels
    21.
    发明授权
    Reactor for gasifying solid fuels 失效
    用于气化固体燃料的反应堆

    公开(公告)号:US4426809A

    公开(公告)日:1984-01-24

    申请号:US349875

    申请日:1982-02-18

    Abstract: Solid fuels are gasified in a fixed bed with gasifying agents passed through the fixed bed from below. The gasification residues are withdrawn as solid ash or as liquid slag under the fixed bed. The reactor is charged with solid fuels through a lock chamber and with tar through a supply conduit. The tar is delivered to the fuel in numerous individual streams, which are distributed over the cross-section of the fixed bed.In the gasifying reactor, an inclined distributor surface is disposed over the fixed bed and has numerous passage openings for the tar and the solid fuels. The outlet end of the tar supply conduit is directed to the upper portion of the distributor surface. A tar tub having outlet openings is associated with the distributor surface and serves to receive the tar. The distributor surface is rotatable on a vertical axis.

    Abstract translation: 固体燃料在固定床中气化,气化剂从下方通过固定床。 气化残渣作为固体灰分或作为固定床下的液态渣排出。 反应器通过锁定室装入固体燃料,焦油通过供应导管。 焦油被分配在固定床的横截面上的许多单独的流中被输送到燃料中。 在气化反应器中,倾斜的分配器表面设置在固定床上并且具有许多用于焦油和固体燃料的通道开口。 焦油供应管道的出口端被引导到分配器表面的上部。 具有出口开口的焦油桶与分配器表面相关联并用于接收焦油。 分配器表面可在垂直轴线上旋转。

    Method for gasifying finely-divided coal in a fixed bed gasifier
    24.
    发明授权
    Method for gasifying finely-divided coal in a fixed bed gasifier 失效
    在固定床气化炉中气化微细煤的方法

    公开(公告)号:US4290780A

    公开(公告)日:1981-09-22

    申请号:US095764

    申请日:1979-11-16

    Applicant: Philip J. Dudt

    Inventor: Philip J. Dudt

    Abstract: A process for gasifying finely-divided coal in a fixed bed gasifier, the process comprising: charging finely-divided coal to a stirred semi-fluidized carbonizer reaction zone where the coal is contacted with oxygen and agglomerated into coal derived particulate solids of a size suitable as a feedstock to a fixed bed gasifer and thereafter passed to a fixed bed gasifer.

    Abstract translation: 一种用于在固定床气化器中气化精细分解的煤的方法,该方法包括:将细碎煤装入搅拌的半流化碳化器反应区,其中煤与氧接触并聚集成煤衍生的大小合适的颗粒固体 作为固定床气体的原料,然后通过固定床气体。

    Coal gasifying burner with rotating grill
    25.
    发明授权
    Coal gasifying burner with rotating grill 失效
    带旋转格栅的煤气化燃烧器

    公开(公告)号:US4274341A

    公开(公告)日:1981-06-23

    申请号:US65877

    申请日:1979-08-13

    Abstract: A coal gasifying burner characterized by a rotating grill which is composed of grill disks arranged on two pipes with a narrow gap between the grills and which rotates very slowly inwards when viewed from the top sloped side walls made of metal sheet having a sloper compatible with coal flow, a cylindrical jacket placed around the periphery of the nozzle which delivers combustion air to the burner, gasification of a quantity of coal located on the sloping side walls around a narrow area where coal combustion takes place, and combustion of the generated coal gas outside of the burner by secondary air which cools the system and gets heated itself by the coal cooking process.

    Abstract translation: 一种煤气化燃烧器,其特征在于旋转格栅,其由格栅盘组成,格栅盘布置在格栅之间,格栅之间具有窄间隙,并且当从具有与煤相兼容的冲洗板的金属板制成的顶部倾斜侧壁观察时非常缓慢向内旋转 流动,围绕喷嘴周边放置燃烧空气的圆筒形套管,将燃烧空气传送到燃烧器的气体,位于发生煤燃烧的狭窄区域周围的倾斜侧壁上的煤的气化,以及产生的煤气外部的燃烧 的燃烧器通过二次空气冷却系统并通过煤烹饪过程自身加热。

    Apparatus and method for the gasification of solid carbonaceous material
    27.
    发明授权
    Apparatus and method for the gasification of solid carbonaceous material 失效
    用于固体碳质材料气化的装置和方法

    公开(公告)号:US4095960A

    公开(公告)日:1978-06-20

    申请号:US739846

    申请日:1976-11-09

    Abstract: A process and apparatus are provided for converting particulate carbonaceous fuel, such as high-sulfur bituminous coal, into a combustible gas, the process comprising forming an ignited fluidized bed of said particulate carbonaceous fuel in a closed-bottom shaft furnace, the shaft furnace having a roof enclosure, directing a jet stream of oxygen downward into the bottom zone of said ignited fluidized bed of particulate fuel by means of an oxygen lance passing axially through said roof enclosure in sealing engagement therewith, the velocity of said oxygen stream into said bottom zone being sufficient to form a dynamic highly turbulent suspension of said particulate fuel and its particulate reaction products deflecting substantially radially outwardly and upwardly and then inwardly and downwardly in a toroidally circulating manner in the bottom zone of said fluidized bed, continuously removing effluent gases formed by the reaction of said oxygen with said fluidized bed, and maintaining said fluidized bed by continually feeding makeup fuel to said shaft furnace.When the jet-fluidized bed is operated continuously below ash-fusion temperatures, said bed will accumulate and maintain a high percentage of particulate ash which is continuously withdrawn from the furnace.When the jet-fluidized bed is operated above ash-fusion temperatures and fluxes and sulfur fixation agents are fed with the coal, a molten bath is formed on the bottom of the furnace, said bath serving to collect ash, sulfides, iron, and other coal impurities in molten products which flow out of the furnace through tap holes.

    Abstract translation: 提供了一种方法和装置,用于将诸如高硫烟煤的颗粒碳质燃料转化为可燃气体,该方法包括在封闭底部竖炉中形成所述颗粒状碳质燃料的点燃流化床,所述竖炉具有 屋顶外壳,通过轴向穿过所述屋顶外壳与其密封接合的氧气喷枪将氧气的喷射流向下引导到所述点燃的颗粒燃料的流化床的底部区域中,所述氧气流进入所述底部区域的速度 足以形成所述颗粒燃料及其颗粒状反应产物的动态高度湍流悬浮液,其在所述流化床的底部区域中以环形循环方式基本上径向向外且向上然后向内和向下偏转,连续地除去由所述流化床形成的流出气体 所述氧与所述流化床的反应,并维持s 通过不断地向所述竖炉供给补充燃料来帮助流化床。

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