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    Process and equipment for the thermal annihilation of the protein contained in a material of animal or vegetable origin
    52.
    发明申请
    Process and equipment for the thermal annihilation of the protein contained in a material of animal or vegetable origin 审中-公开
    用于动物或植物来源材料中所含蛋白质热湮灭的方法和设备

    公开(公告)号：US20020193652A1

    公开(公告)日：2002-12-19

    申请号：US10116448

    申请日：2002-04-04

    Inventor： Adolfo Fernandez Mesa

    IPC: A62D003/00

    CPC classification number: F23G7/10 ,  A61L2/0011 ,  A61L2/0023 ,  A61L11/00 ,  B09B3/00 ,  B09B3/0083 ,  B09B2220/04 ,  F23G1/00 ,  F23G5/033 ,  F23G5/04 ,  F23G5/085 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23G2201/101 ,  F23G2203/40 ,  Y02W30/20

    Abstract: The present invention discloses a process and equipment for the complete thermal annihilation of proteins contained in material of animal or vegetable origin, in solid or semisolid state, that comprises the steps of: (a) previously milling the material of animal or vegetable origin to assure that the drying step reaches to be completed in the whole material, without remaining areas or pieces with high humidity that can not reach high temperatures by being shielded from the heat; (b) drying the whole material to be able to increase the combustion temperature of the solids from 800null C. to 1350null C.; (c) thermally annihilating the material, by means of a combustion in a refractory oven, either shredded or powdered and in suspension, to achieve the high required temperature to be reached and kept within the whole material; that there is an homogeneous oxygen concentration and that it can be sure that the time of treatment allows for getting the thermal annihilation; and (d) recovering the heat of combustion of the material, which should be carried out only after the total oxidation of the material, never during its combustion, for not allowing to decrease the temperature before the treatment of thermal annihilation has been completed.

    Abstract translation: 本发明公开了一种用于将动物或植物来源的固体或半固体状态的蛋白质完全热湮灭的方法和设备，其包括以下步骤：（a）预先研磨动物或植物来源的材料以确保 干燥步骤在整个材料中完成，没有剩余的高湿度的区域或片段不能通过屏蔽而达不到高温; （b）干燥整个材料以使固体的燃烧温度从800℃提高到1350℃; （c）通过在耐火炉中的燃烧，将粉末或粉末状和悬浮状态的材料热湮灭，以达到达到并保持在整个材料内的高要求的温度; 具有均匀的氧气浓度，并且可以确保处理时间允许获得热湮灭; 和（d）回收材料的燃烧热量，其仅在材料的全部氧化之后才能在其燃烧期间才能进行，以便在热湮灭处理之前不允许降低温度。

    WASTE SLUDGE INCINERATOR USING PYROLYSIS AND GASIFICATION, AND RELATIVE PROCESS
    56.
    发明申请
    WASTE SLUDGE INCINERATOR USING PYROLYSIS AND GASIFICATION, AND RELATIVE PROCESS 审中-公开
    使用溶解和气化的废弃物焚烧炉及相关工艺

    公开(公告)号：WO2015049659A1

    公开(公告)日：2015-04-09

    申请号：PCT/IB2014/065021

    申请日：2014-10-02

    Applicant: ENI S.P.A.

    Inventor： MASSETTI, Felicia ,  PISTELLI, Maria Ilaria ,  PINTI, Medardo

    IPC: C02F11/10 ,  C10J3/00 ,  F23G5/00 ,  F23G5/027 ,  F23G5/04 ,  F23G5/20 ,  F23G5/46

    CPC classification number: F23G7/001 ,  C02F11/06 ,  C02F11/10 ,  C10J3/005 ,  C10J3/60 ,  C10J2200/158 ,  C10J2300/1246 ,  F23G5/006 ,  F23G5/027 ,  F23G5/0273 ,  F23G5/04 ,  F23G5/20 ,  F23G5/44 ,  F23G5/46 ,  F23G2201/101 ,  F23G2201/302 ,  F23G2201/303 ,  F23G2201/40 ,  F23G2203/211 ,  F23G2206/10 ,  F23G2209/12 ,  F23G2900/50001 ,  F23G2900/50201 ,  F23G2900/50204 ,  F23G2900/52001 ,  F23G2900/52002 ,  F23G2900/54402 ,  Y02W10/40

    Abstract: The present invention relates to reaction equipment for the treatment of organic and/or inorganic waste of refineries or petrochemical plants comprising: • - a drying and pyrolysis device (4) which rotates around its longitudinal, tilted rotation axis (A), • - a gasification device (6) which rotates around its longitudinal, horizontal rotation axis (B), • - a combustion device (14) comprising a burner (13) having a longitudinal horizontal axis (C), • - at least one settling chamber (15) for the collection of intermediate solid residues and the accumulation of intermediate gaseous reaction products, • - at least one outlet duct of the gaseous end-products (16), at least one outlet duct of the solid end-products (7), and at least one inlet duct of the feedstock (2) • - said combustion device (14), drying and pyrolysis device (4), gasification device (6) are physically separated and positioned on three different levels, • - the longitudinal rotation axis (A) of the drying and pyrolysis device (4) is tilted with respect to both the longitudinal rotation axis (B) of the gasification device (6) and also with respect to the longitudinal axis (C) of the combustion device (14), • - the longitudinal rotation axis (B) of the gasification device (6) is parallel to the longitudinal axis (C) of the combustion device (14), • - the combustion device (14) is in fluid communication with the drying and pyrolysis device (4), • - the drying and pyrolysis device (4) comprises, in its interior, a first indirect heat exchange device (3) in which the combustion fumes coming from the combustion device (14) flow, • - at least one settling chamber (15) in fluid communication with said drying and pyrolysis device (4) and with said gasification device (6) and with said combustion device (14), • - conveying means (5) are positioned in the settling chamber (15) and put the drying and pyrolysis device (4) in fluid communication with the gasification device, • - it comprises a second heat exchange device (12) in fluid communication with the first indirect heat exchange device (3) and the combustion device (14), • - it comprises means for the suction of the intermediate gaseous reaction products, said means being positioned in the settling chamber (15).

    Abstract translation: 本发明涉及用于处理炼油厂或石油化工厂的有机和/或无机废物的反应设备，包括： - 围绕其纵向倾斜旋转轴线（A）旋转的干燥和热解装置（4）， - - 一种燃烧装置（14），包括具有纵向水平轴线（C）的燃烧器（13）， - 至少一个沉降室（15） ），用于收集中间固体残余物和中间气体反应产物的积聚， - 至少一个气体终产物（16）的出口管道，至少一个固体终产物（7）的出口管道，和 原料（2）的至少一个入口管道•所述燃烧装置（14），干燥和热解装置（4），气化装置（6）被物理地分离并定位在三个不同的水平上， - 纵向旋转轴线 A）干燥a d热解装置（4）相对于气化装置（6）的纵向旋转轴线（B）倾斜并且相对于燃烧装置（14）的纵向轴线（C）倾斜， - 纵向旋转 气化装置（6）的轴线（B）平行于燃烧装置（14）的纵向轴线（C）; - 燃烧装置（14）与干燥和热解装置（4）流体连通， - 干燥和热解装置（4）在其内部包括第一间接热交换装置（3），其中来自燃烧装置（14）的燃烧烟雾流动; - 至少一个沉降室（15） 与所述干燥和热解装置（4）和所述气化装置（6）和所述燃烧装置（14）流体连通，•输送装置（5）定位在沉降室（15）中，并将干燥和 与气化装置流体连通的热解装置（4）， - 它包括 与所述第一间接热交换装置（3）和所述燃烧装置（14）流体连通的第二热交换装置（12）， - 其包括用于吸入中间气体反应产物的装置，所述装置位于 沉降室（15）。

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