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    Apparatuses and Methods for Controlling Heat for Rapid Thermal Processing of Carbonaceous Material
    2.
    发明申请
    Apparatuses and Methods for Controlling Heat for Rapid Thermal Processing of Carbonaceous Material 审中-公开
    用于控制碳质材料快速热处理的热量的装置和方法

    公开(公告)号：US20140363343A1

    公开(公告)日：2014-12-11

    申请号：US14346517

    申请日：2012-09-14

    Applicant: Sathit Kulprathipanja ,  Paolo Palmas

    Inventor： Sathit Kulprathipanja ,  Paolo Palmas

    IPC: C10B53/02

    CPC classification number: C10B53/02 ,  B01J8/0055 ,  B01J8/1836 ,  B01J8/26 ,  B01J8/32 ,  B01J2208/00176 ,  B01J2208/00194 ,  B01J2208/00292 ,  B01J2208/00513 ,  C10B49/22 ,  C10C5/00 ,  F23C10/04 ,  F23C2206/103 ,  F23G2201/304 ,  F23G2203/502 ,  F23G2209/26 ,  F28D7/1615 ,  F28F1/14 ,  Y02E50/14

    Abstract: Embodiments of apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material are provided herein. The apparatus comprises a reheater for containing a fluidized bubbling bed comprising an oxygen-containing gas, inorganic heat carrier particles, and char and for burning the char into ash to form heated inorganic particles. An inorganic particle cooler is in fluid communication with the reheater to receive a first portion of the heated inorganic particles. The inorganic particle cooler is configured to receive a cooling medium for indirect heat exchange with the first portion of the heated inorganic particles to form first partially-cooled heated inorganic particles that are fluidly communicated to the reheater and combined with a second portion of the heated inorganic particles to form second partially-cooled heated inorganic particles. A reactor is in fluid communication with the reheater to receive the second partially-cooled heated inorganic particles.

    Abstract translation: 本文提供了用于控制用于碳质材料的快速热处理的热量的装置和方法的实施例。 该装置包括一个再热器，用于容纳包含含氧气体，无机热载体颗粒和炭的流化鼓泡床，并用于将炭烧成灰分以形成加热的无机颗粒。 无机颗粒冷却器与再热器流体连通以接收第一部分加热的无机颗粒。 无机颗粒冷却器构造成接收用于与加热的无机颗粒的第一部分进行间接热交换的冷却介质，以形成第一部分冷却的加热的无机颗粒，其流体连通到再热器并与第二部分加热的无机颗粒 颗粒形成第二部分冷却的加热无机颗粒。 反应器与再热器流体连通以接收第二部分冷却的加热的无机颗粒。

    Oxygen-producing oxycombustion boiler
    4.
    发明授权
    Oxygen-producing oxycombustion boiler 有权
    生产氧气的氧化锅炉

    公开(公告)号：US08171893B2

    公开(公告)日：2012-05-08

    申请号：US10590357

    申请日：2005-02-22

    Applicant: Jean-Xavier Morin ,  Corinne Beal ,  Silvestre Suraniti

    Inventor： Jean-Xavier Morin ,  Corinne Beal ,  Silvestre Suraniti

    IPC: F23C10/18

    CPC classification number: F23C10/04 ,  F23C10/18 ,  F23L7/007 ,  Y02E20/322 ,  Y02E20/344

    Abstract: The boiler of the invention has a circulating fluidized bed, uses solid fuels and the oxygen obtained by high temperature oxygen production membranes, and is characterized in that the membranes are placed in the bed. These membranes are, for example, of the OTM (Oxygen Transport Membranes) type. Since the membranes operate at over 700° C., their positioning in the outer bed is ideally selected because the temperature of the solids circulating in the outer bed is between 750 and 900° C. This is particularly remarkable because the operating temperature windows of the circulating fluidized bed coincide with the optimal temperature window of use of the membranes.

    Abstract translation: 本发明的锅炉具有循环流化床，使用固体燃料和由高温氧气生产膜获得的氧气，其特征在于将膜放置在床中。 这些膜例如是OTM（氧气输送膜）型。 由于膜的工作温度超过700°C，所以它们在外层床上的定位是理想的选择，因为在外层床中循环的固体的温度为750-900℃。这是特别显着的，因为 循环流化床与使用膜的最佳温度窗口重合。

    Fluidized Bed Heat Exchanger for a Circulating Fluidized Bed Boiler and a Circulating Fluidized Bed Boiler with a Fluidized Bed Heat Exchanger
    5.
    发明申请
    Fluidized Bed Heat Exchanger for a Circulating Fluidized Bed Boiler and a Circulating Fluidized Bed Boiler with a Fluidized Bed Heat Exchanger 有权
    用于循环流化床锅炉的流化床热交换器和具有流化床热交换器的循环流化床锅炉

    公开(公告)号：US20090293818A1

    公开(公告)日：2009-12-03

    申请号：US12299982

    申请日：2007-05-09

    Applicant: Kari Kauppinen

    Inventor： Kari Kauppinen

    IPC: F22B27/14 ,  F23J3/00 ,  F23C10/04 ,  F22B31/08

    CPC classification number: F23C10/04 ,  F22B31/0092 ,  F23C10/32 ,  F23C2206/103

    Abstract: A heat exchanger and a circulating fluidized bed boiler with a heat exchanger including a first fluidized bed heat exchange chamber and a second fluidized bed heat exchange chamber, arranged in connection with a furnace of the circulating fluidized bed boiler, a first inlet channel for introducing hot solids from a particle separator of the external circulation of the circulating fluidized bed boiler into the first heat exchange chamber, a second inlet channel for introducing solids to the second heat exchange chamber, a first discharge for removing a first portion of the cooled solids from the first heat exchange chamber to the second inlet channel and a second discharge for removing cooled solids from the second heat exchange chamber to the furnace, the heat exchange chamber including an inlet for introducing hot solids directly from the internal circulation of the furnace to the second heat exchange chamber. The heat exchanger also preferably includes a third discharge for removing a second portion of the cooled solids from the first heat exchange chamber directly to the furnace.

    Abstract translation: 一种具有热交换器的热交换器和循环流化床锅炉，其包括与循环流化床锅炉的炉相连接设置的第一流化床热交换室和第二流化床热交换室，用于引入热的第一入口通道 固体从循环流化床锅炉的外部循环的颗粒分离器进入第一热交换室，用于将固体引入第二热交换室的第二入口通道，用于从第一热交换室中除去第一部分冷却的固体的第一排出物 第一热交换室到第二入口通道，以及第二排出物，用于从第二热交换室向炉中除去冷却的固体，热交换室包括用于将热固体直接从炉的内部循环引入第二热量的入口 交换室。 热交换器还优选地包括用于将第二部分冷却的固体从第一热交换室直接排到炉子的第三排出物。

    Method and Device For the Thermochemical Conversion of a Fuel
    6.
    发明申请
    Method and Device For the Thermochemical Conversion of a Fuel 审中-公开
    燃料的热化学转化方法和装置

    公开(公告)号：US20080149011A1

    公开(公告)日：2008-06-26

    申请号：US11883835

    申请日：2006-01-28

    Applicant: Peter Quicker ,  Gerold Dimaczek ,  Frank Fojtik

    Inventor： Peter Quicker ,  Gerold Dimaczek ,  Frank Fojtik

    IPC: F23C10/00 ,  F23C10/22 ,  F23C10/24 ,  F27B15/00

    CPC classification number: F23C10/12 ,  F23C10/04 ,  F23C10/20 ,  F23C10/24

    Abstract: The invention relates to a method for the thermochemical conversion of a fuel, comprising the following steps: a) provision of a fluidised-bed reactor with a central first combustion zone (1) and a second combustion zone (7) that is separated from the first by flow conduction means (2, 15), the first combustion zone (1) being provided with a supply opening (16) for supplying fuel and a unit (3), which lies opposite the supply opening (16) on the floor (B) of the fluidised bed reactor, for deviating a stream of fuel into the second combustion zone (7); b) feeding of fuel through the supply opening (16), so that a stream of fuel forms that is directed towards the floor (B); c) deviation of the stream of fuel on the floor (B) into the second combustion zone (7), so that the stream of fuel is guided in an essentially opposite direction; and d) additional deviation of the stream of fuel in the vicinity of the supply opening (16), causing the stream of fuel to be returned to the first combustion zone.

    Abstract translation: 本发明涉及一种用于燃料热化学转化的方法，包括以下步骤：a）提供具有中心第一燃烧区（1）和第二燃烧区（7）的流化床反应器 首先通过流动传导装置（2,15），第一燃烧区（1）设置有用于供应燃料的供应开口（16）和与地板上的供应开口（16）相对的单元（3） B），用于将燃料流偏离到第二燃烧区（7）中; b）通过供应开口（16）进给燃料，使得形成指向地板（B）的燃料流; c）将地板（B）上的燃料流偏离到第二燃烧区（7）中，使得燃料流沿基本上相反的方向被引导; 和d）在供应开口（16）附近的燃料流的附加偏差，导致燃料流返回到第一燃烧区。

    Oxygen-producing oxycombustion boiler
    7.
    发明申请
    Oxygen-producing oxycombustion boiler 有权
    生产氧气的氧化锅炉

    公开(公告)号：US20070175411A1

    公开(公告)日：2007-08-02

    申请号：US10590357

    申请日：2005-02-22

    Applicant: Jean-Xavier Morin ,  Corinne Beal ,  Silvestre Suraniti

    Inventor： Jean-Xavier Morin ,  Corinne Beal ,  Silvestre Suraniti

    IPC: F23C10/00

    CPC classification number: F23C10/04 ,  F23C10/18 ,  F23L7/007 ,  Y02E20/322 ,  Y02E20/344

    Abstract: The boiler of the invention has a circulating fluidized bed, uses solid fuels and the oxygen obtained by high temperature oxygen production membranes, and is characterized in that the membranes are placed in the bed. These membranes are, for example, of the OTM (Oxygen Transport Membranes) type. Since the membranes operate at over 700° C., their positioning in the outer bed is ideally selected because the temperature of the solids circulating in the outer bed is between 750 and 900° C. This is particularly remarkable because the operating temperature windows of the circulating fluidized bed coincide with the optimal temperature window of use of the membranes.

    Abstract translation: 本发明的锅炉具有循环流化床，使用固体燃料和由高温氧气生产膜获得的氧气，其特征在于将膜放置在床中。 这些膜例如是OTM（氧气输送膜）型。 由于膜的工作温度超过700°C，所以它们在外层床上的定位是理想的选择，因为在外层床中循环的固体的温度为750-900℃。这是特别显着的，因为 循环流化床与使用膜的最佳温度窗口重合。

    Fluidized Bed Apparatus and its Components
    10.
    发明申请
    Fluidized Bed Apparatus and its Components 审中-公开
    流化床设备及其部件

    公开(公告)号：US20160356488A1

    公开(公告)日：2016-12-08

    申请号：US15038641

    申请日：2014-08-15

    Applicant: DOOSAN LENTJES GMBH

    Inventor： Damian Goral ,  Klaus-Dieter Pohl ,  Oguzhan Narin

    IPC: F23C10/04 ,  F22B31/00 ,  F28D7/00 ,  F28F9/02 ,  F28D13/00 ,  F28D7/08

    CPC classification number: F23C10/04 ,  F01K5/02 ,  F22B31/0092 ,  F23C10/00 ,  F23C2206/103 ,  F28D7/0041 ,  F28D7/082 ,  F28D13/00 ,  F28F9/026 ,  F28F9/0268 ,  F28F9/22 ,  F28F2009/226

    Abstract: A fluidized bed heat exchanger with a chamber (24) comprises a solid particles inlet port (22), a solid particles outlet port (30), arranged at a distance to the inlet port (22), means (46) for introducing a fluidizing gas from a bottom area into the chamber (24). The heat exchanger has furthermore several heat exchange tubes (28) being arranged at a distance to each other. The heat exchange tubes (28) are each arranged in a meandering fashion and a wall-like pattern and extend substantially parallel to the main flow direction of the solid particles on their way to and through the outlet port (30).

    Abstract translation: 具有室（24）的流化床热交换器包括固体颗粒入口（22），与入口端（22）一定距离设置的固体颗粒出口（30），用于引入流化床 气体从底部区域进入腔室（24）。 热交换器还有几个热交换管（28）彼此间隔一定距离设置。 热交换管（28）各自以曲折的方式和壁状图案布置，并且在它们通过和通过出口（30）的途中基本上平行于固体颗粒的主流动方向延伸。

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