公开(公告)号：US4987115A

公开(公告)日：1991-01-22

申请号：US248808

申请日：1988-09-23

Applicant: Herwig Michel-Kim

Inventor： Herwig Michel-Kim

IPC: C01B31/08 ,  C01B31/10 ,  C10J3/02 ,  C10J3/54

CPC classification number: C10J3/721 ,  C01B31/088 ,  C01B31/10 ,  C10J3/02 ,  C10J3/34 ,  C10J3/54 ,  C10J2200/158 ,  C10J2300/1609 ,  Y02P20/129

Abstract: A method and an apparatus for producing generator gas and activated carbon from solid fuels. A first gasification stage is supplied with fuel by an underfeed charging system and preheated air, the air and fuel being supplied in the same direction. In a second gasification stage and accompanied by the supply of secondary air, an intermediate gasification takes place. Finally, in a third gasification stage, the gas is reacted with glowing coke or charcoal, and the heat of the exiting gas is used for heating the air. The fuel centrally entering the first gasification stage is led from the inside to the outside and then upwards. Part of the entering fuel is precombusted in a precombustion chamber linked with the supply of the preheated air for reducing the oxygen content of the preheated air. In the intermediate gasification stage, the gas with the admixed air is passed through a Venturi nozzle or tube with a diffuser. The flue coal entrained from the first gasification stage is at least partly returned to the throat of the Venturi tube. The return is assisted both by vacuum in the Venturi tube and mechanically.

Abstract translation: 一种从固体燃料生产发电机气体和活性炭的方法和装置。 第一气化阶段由欠充电系统和预热空气供应燃料，空气和燃料沿相同方向供应。 在第二气化阶段并伴随着二次空气的供应，发生中间气化。 最后，在第三气化阶段，气体与发光的焦炭或木炭反应，排出气体的热量用于加热空气。 中心进入第一气化阶段的燃料从内部引导到外部然后向上。 进入燃料的一部分被预燃烧在与预热空气供应相连的预燃室中，以减少预热空气的氧含量。 在中间气化阶段，具有混合空气的气体通过文丘里管或喷管扩散管。 从第一气化阶段夹带的烟道煤至少部分地返回文丘里管的喉部。 返回由文丘里管中的真空和机械辅助。

公开(公告)号：US5089030A

公开(公告)日：1992-02-18

申请号：US588605

申请日：1990-09-26

Applicant: Herwig Michel-Kim

Inventor： Herwig Michel-Kim

IPC: C01B31/08 ,  C01B31/10 ,  C10J3/02 ,  C10J3/54

CPC classification number: C10J3/721 ,  C01B31/088 ,  C01B31/10 ,  C10J3/02 ,  C10J3/34 ,  C10J3/54 ,  C10J2200/158 ,  C10J2300/1609 ,  Y02P20/129

Abstract: A method and an apparatus for producing generator gas and activated carbon from solid fuels. A first gasification stage is supplied with fuel by an underfeed charging system and preheated air, the air and fuel being supplied in the same direction. In a second gasification stage and accompanied by the supply of secondary air, an intermediate gasification takes place. Finally, in a third gasification stage, the gas is reacted with glowing coke or charcoal, and the heat of the exiting gas is used for heating the air. The fuel centrally entering the first gasification stage is led from the inside to the outside and then upwards. Part of the entering fuel is precombusted in a precombustion chamber linked with the supply of the preheated air for reducing the oxygen content of the preheated air. In the intermediate gasification stage, the gas with the admixed air is passed through a Venturi nozzle or tube with a diffuser. The flue coal entrained from the first gasification stage is at least partly returned to the throat of the Venturi tube. The return is assisted both by vacuum in the Venturi tube and mechanically.

公开(公告)号：US5026403A

公开(公告)日：1991-06-25

申请号：US319264

申请日：1988-05-10

Applicant: Herwig Michel-Kim

Inventor： Herwig Michel-Kim

IPC: C10J3/72 ,  B01J7/00 ,  C10J3/00 ,  C10J3/02 ,  C10J3/20 ,  C10J3/30 ,  C10J3/34 ,  C10J3/46 ,  C10J3/64

CPC classification number: C10J3/721 ,  C10J3/02 ,  C10J3/20 ,  C10J3/34 ,  C10J3/66 ,  C10J2200/158 ,  C10J2300/0943 ,  C10J2300/095 ,  C10J2300/0956 ,  C10J2300/1621 ,  Y02P20/129

Abstract: A three stage process for producing producer gas from biomass or other carbonizable waste products using a double gasifier is described. A reactor for the three stage process comprising a primary, an intermediate and secondary gasifier is also described. The primary gasifier utilizes a vertically adjustable fill level sieve and a discharge mechanism for the combustion residues. The primary fuel and the preheated primary air are supplied to the primary gasifier via the reactor base. The secondary gasifier, a coke producer is connected to the primary gasifier downstream. The intermediate gasifier, a fluw flow gas converter, is supplied with secondary air. The low temperature carbonized gas from the primary gasifier, as well as the carbon particles leaving the primary gasifier are introduced into the secondary gasifier through a radially symmetrical ring nozzle to provide a long residence time under reducing conditions. The reactor is also optionally provided with one other gas, comprising at least in part the product, producer gas, introduced via a bypass arrangement.

Abstract translation: 描述了使用双重气化器从生物质或其他可碳化废物产生生产气体的三阶段方法。 还描述了包括初级，中间和次级气化器的三级方法的反应器。 主气化器利用垂直可调的填充水平筛和用于燃烧残余物的排放机构。 初级燃料和预热的一次空气通过反应器底座供应给初级气化器。 二次气化器，焦炭生产者连接到下游的主气化器。 中间气化器（Fluw flow gas converter）被提供二次空气。 来自初级气化器的低温碳化气体以及离开主气化器的碳颗粒通过径向对称的环形喷嘴引入二次气化器中，以在还原条件下提供长的停留时间。 反应器还可选地设置有另一种气体，至少部分地包括通过旁路装置引入的产物，发生器气体。

公开(公告)号：US4541845A

公开(公告)日：1985-09-17

申请号：US662527

申请日：1984-10-18

Applicant: Herwig Michel-Kim

Inventor： Herwig Michel-Kim

IPC: B01D17/025 ,  B01D17/038 ,  B01D43/00 ,  B01D45/12 ,  B01D45/16 ,  B01D53/24 ,  B01D59/18 ,  B01D59/20 ,  B01D57/00

CPC classification number: B01D45/16 ,  B01D53/24 ,  B01D59/18

Abstract: A process for the separation of solid and/or liquid particles from gases or solids from liquids, as well as for the separation of gases or liquids with different densities is proposed, in which a Venturi tube is used. The gas and/or liquid mixture is introduced inwards in radially symmetrical manner from the outside through the slot of an annular nozzle at a high flow velocity which, in the case of gases, extends up to the velocity of sound. The gas is subject to the action of a high centrifugal acceleration in the slot, which has a radius of curvature of approximately 1 to 100 mm.

Abstract translation: 提出了一种用于从气体或固体从液体中分离固体和/或液体颗粒以及用于分离具有不同密度的气体或液体的方法，其中使用文氏管。 气体和/或液体混合物以径向对称的方式从外部通过环形喷嘴的槽以高流速向内引入，在气体的情况下，气体和/或液体混合物延伸到声速。 气体受到槽中高离心加速度的作用，其具有大约1至100mm的曲率半径。