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    HIGH-TEMPERATURE FURNACE AND METHOD FOR CONVERTING ORGANIC MATERIALS TO SYNTHESIS GAS
    74.
    发明申请
    HIGH-TEMPERATURE FURNACE AND METHOD FOR CONVERTING ORGANIC MATERIALS TO SYNTHESIS GAS 审中-公开
    将有机材料转化为合成气体的高温炉和方法

    公开(公告)号：US20120217442A1

    公开(公告)日：2012-08-30

    申请号：US13501597

    申请日：2009-10-15

    Applicant: Peter Jeney

    Inventor： Peter Jeney

    IPC: C01B3/02 ,  B01J19/00

    CPC classification number: F27B7/10 ,  C10J3/005 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/0976 ,  C10J2300/1276 ,  F23G5/0276 ,  F23G5/20 ,  F23G7/10 ,  F23G2201/304 ,  F27B7/2016 ,  F27B7/34 ,  F27D11/02 ,  Y02P20/145

    Abstract: High-temperature apparatus (10) for converting an starting material (M) to a synthesis gas (G) and comprising a feeding device (30) and a rotationally symmetrical furnace pipe (20) having a rotation axis (R). The feeding device (30) conducts the starting material (M) into an inner chamber (I) of the furnace pipe (20), and conveying elements (22) are arranged in the inner chamber (I) of the furnace pipe (20) in order to convey the starting material (M) in the direction of an exit side (A) of the furnace pipe (20). The apparatus (10) comprises an elongate resistance heating (23), which protrudes into the interior (I) of the furnace pipe (20) and which comprises at least one hot zone (H1) and a less hot zone (H2), wherein the hot zone (H1) follows the less hot zone (H2) as viewed from the entry zone (E), and wherein the resistance heating (23) is configured such that a temperature that is above 1200° C., is achievable in the inner chamber (I) of the furnace pipe (20).

    Abstract translation: 用于将原料（M）转化为合成气（G）并包括具有旋转轴线（R）的进料装置（30）和旋转对称的炉管（20）的高温装置（10）。 供给装置30将原料（M）导入炉管（20）的内室（I），输送元件（22）配置在炉管（20）的内室（I） 以便在炉管（20）的出口侧（A）的方向上输送原料（M）。 该设备（10）包括伸入炉管（20）的内部（I）并且包括至少一个热区（H1）和较少热区（H2）的细长电阻加热器（23），其中 从入口区（E）观察，热区（H1）跟随较少的热区（H2），并且其中电阻加热（23）构造成使得可以在高于1200℃的温度 炉管（20）的内室（I）。

    FLUIDIZED-BED GASIFICATION METHOD AND FACILITY THEREFOR
    78.
    发明申请
    FLUIDIZED-BED GASIFICATION METHOD AND FACILITY THEREFOR 有权
    流化床气化方法及其设备

    公开(公告)号：US20110120007A1

    公开(公告)日：2011-05-26

    申请号：US12999163

    申请日：2009-06-12

    Applicant: Yoshiaki Matsuzawa ,  Toshiyuki Suda ,  Kenichiro Kondo

    Inventor： Yoshiaki Matsuzawa ,  Toshiyuki Suda ,  Kenichiro Kondo

    IPC: C10J3/48 ,  C10J3/46

    CPC classification number: C10J3/463 ,  C10J3/482 ,  C10J3/56 ,  C10J2300/093 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10J2300/1853 ,  F23C10/005 ,  F23C10/10 ,  F23G5/0276 ,  F23G5/30 ,  F23G7/001 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503

    Abstract: Provided are a fluidized-bed combustion furnace 1, a separator 8 for separation into bed material 11 and an exhaust gas, a fluidized-bed gasification furnace 40 into which the bed material 11 is introduced through a downcomer 46 and into which raw material is introduced, a circulation passage for circulating char and the bed material 11 to the combustion furnace 1, a dispersion section 43 extending along a width of a bed-material-introduction-side wall 41 of the gasification furnace 40 to receive the bed material 11 from the downcomer, fluidizing-gas introduction means 47 for blowing fluidizing gas into the dispersion section 43 to fluidize the bed material 11 in the section 43, and a supply section 48 for supplying the bed material 11 in the dispersion section 43 to the fluidized-bed gasification furnace 40 substantially evenly throughout the width on the bed-material-introduction side.

    Abstract translation: 提供了流化床燃烧炉1，用于分离成床材料11的分离器8和废气，流化床气化炉40，通过降液管46将床料11引入其中并将原料引入其中 用于将炭和床料11循环到燃烧炉1的循环通道，沿着气化炉40的床料引入侧壁41的宽度延伸的分散部43，以从床 降液管，用于将流化气体吹入分散部分43以使部分43中的床料11流化的流化气体引入装置47和用于将分散部分43中的床材料11供给到流化床气化 炉床40在床材引入侧的整个宽度上基本上均匀。

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