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    NOZZLE FOR FEEDING THERMOREACTIVE PLASTIC
    3.
    发明专利
    NOZZLE FOR FEEDING THERMOREACTIVE PLASTIC 未知

    公开(公告)号：BG62796B1

    公开(公告)日：2000-08-31

    申请号：BG10239098

    申请日：1998-04-16

    Applicant: APLICATOR SYSTEM AB

    Inventor： SAND KJELL

    IPC: B05B7/08 ,  C01J3/48

    Abstract: The nozzle is used for the processing of plastics. Its usage reduces the injection losses. The nozzle consists of a steel cylinder (10) with a flange (11). In the lower part of cylinder (10) concentric cavity (12) is machined, and at its other end there are two plane surfaces (13) inclined to its longitudinal axis towards each other at an angle of from 70 to 140 deg.C. In each surface (13) an orientated groove (14) is bored. The grooves form an angle of 70-140 deg.C in between, the peak of which is outside the nozzle. 4 claims, 3 figures

    LA DISSOCIATION MOLECULAIRE DU CO2 PAR PLASMA APPLIQUEE A LA PRODUCTION D'ENERGIE DE CARBURANT ET AU TRAITEMENT DES DECHETS URBAINS.
    4.
    发明专利
    LA DISSOCIATION MOLECULAIRE DU CO2 PAR PLASMA APPLIQUEE A LA PRODUCTION D'ENERGIE DE CARBURANT ET AU TRAITEMENT DES DECHETS URBAINS. 未知

    公开(公告)号：BE1014956A6

    公开(公告)日：2004-07-06

    申请号：BE200100720

    申请日：2001-11-07

    Applicant: ABSIL FELICIEN

    IPC: C10J3/18 ,  C10J3/84 ,  C01J3/48

    Abstract: Le procédé consiste en la pyrolyse des déchets ménagers par la chaleur de la dissociation moléculaire d'un gaz ou d'un mélange de gaz à une température supérieure à 3000°C obtenue grâce à l'énergie électrique sous forme de plasma, de chauffage inductif ou par pertes dans le dielectrique que constitue le gaz. Une injection de graphite dans le plasma, modifiera l'équilibre atomique et provoquere dès 2000°C, une réaction exothermique considérable. Les températures très élevées seront maintenues dans des limites acceptables par les installations Turbine-Vapeur et Turbine-Gaz-Vapeur par des injections de CO2 et H2 à des endroits bien précis. A un endroit précis du cycle, on pourra extraire H2du gaz de synthèse. Toutes les injections de CO2 et H2O seront telles que les gaz d'échappement de la Turbine-Gaz seront composés de CO2 et H2O dans le rapport: CO2=11/9 H2Oà la température de l'ordre de 770K°. On ajoutera, à un gaz d'échappement, la quantité adéquate de gaz naturel afin d'obtenir à 500K°,

    Gasification apparatus for a finely divided combustible material
    5.
    发明授权
    Gasification apparatus for a finely divided combustible material 失效
    用于细分的可燃材料的气化装置

    公开(公告)号：US5445658A

    公开(公告)日：1995-08-29

    申请号：US201365

    申请日：1994-02-24

    Applicant: Rainer Durrfeld ,  Johannes Kowoll ,  Eberhard Kuske ,  Hans Niermann ,  Gerhard Wilmer ,  Joachim Wolff

    Inventor： Rainer Durrfeld ,  Johannes Kowoll ,  Eberhard Kuske ,  Hans Niermann ,  Gerhard Wilmer ,  Joachim Wolff

    IPC: C10J3/46 ,  C10J3/48 ,  C10J3/78 ,  C10J3/86 ,  C01J3/48 ,  C01J3/52 ,  C01J3/84 ,  C01J3/86

    CPC classification number: C10J3/485 ,  C10J3/78 ,  C10J3/84 ,  C10J3/86 ,  C10J2300/1246 ,  F28F2265/26 ,  Y02P20/129

    Abstract: The gasification apparatus for gasification of finely divided combustible material under pressure includes a gasification reactor which produces a crude gas, a quenching pipe and a convection-heated boiler with a boiler housing, all mounted inside a pressurized vessel. A gas flow guiding device is provided above the quenching pipe for conducting a mixed gas flow containing the crude gas and a quenching gas from the quenching pipe into the convection-heated boiler which surrounds the quenching pipe concentrically. A gas outlet device is provided for the gas flow from the convection-heated boiler and from the pressurized vessel. The gasification reactor is supported at its bottom end in the pressurized vessel at anchoring points. The convection-heated surface elements of the convection-heated boiler are supported by the quenching pipe and the boiler housing but in a stress-free manner. A quenching gas inlet device is provided and includes a circumferential gap between an inlet section of the quenching pipe and an adjacent outlet section of the gasification reactor through which a quenching gas is conducted to form, together with the crude gas, the mixed gas flow.

    Abstract translation: 用于在压力下气化细分的可燃材料的气化装置包括产生粗气的气化反应器，淬火管和具有锅炉壳体的对流加热锅炉，全部安装在加压容器内。 气体导流装置设置在淬火管上方，用于将含有粗气体和淬火气体的混合气体流从淬火管进入对向加热的锅炉，该对流加热锅炉同时围绕淬火管。 气体出口装置用于来自对流加热锅炉和加压容器的气流。 气化反应器在其底端处在锚定点处的加压容器中。 对流加热锅炉的对流加热表面元件由淬火管和锅炉壳体支撑，但是以无应力的方式。 提供了一种淬火气体入口装置，其包括在淬火管的入口部分和气化反应器的相邻出口部分之间的周向间隙，通过该周向间隙与淬火气体一起形成与粗气体一起形成混合气体流。

    PARTIAL OXIDATION FEED SYSTEM AND METHOD
    6.
    发明申请
    PARTIAL OXIDATION FEED SYSTEM AND METHOD 审中-公开

    公开(公告)号：WO2013159270A9

    公开(公告)日：2013-10-31

    申请号：PCT/CN2012/074505

    申请日：2012-04-23

    Applicant: GENERAL ELECTRIC COMPANY ,  STEELE, Raymond Douglas ,  LEININGER, Thomas ,  LI, Shiguang

    Inventor： STEELE, Raymond Douglas ,  LEININGER, Thomas ,  LI, Shiguang

    IPC: C01J3/48 ,  C01J3/46 ,  C10J1/06

    Abstract: A partial oxidation feed system (10) and a method are provided. The system (10) includes a slag additive slurry feed system (31) configured to combine a slurrying agent (24), a mineral slag additive (22), and a liquid slurrying medium (25) to generate a stabilized mineral slurry (26). The slurrying agent (24) is configured to increase a viscosity of the stabilized mineral slurry (26). The system (10) also includes a partial oxidation system (12) configured to receive the stabilized mineral slurry (26), a feedstock (16), and oxygen (14) into a gasifier reaction chamber (27). The partial oxidation system (12) is configured to partially oxidize the feedstock (16) to produce a gaseous product (18) and a solid product (20).

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