知搜-全球专利检索

  1. 登录
  2. 注册

搜索结果

55 条记录 (耗时 0.025 秒)

    System for controlling circulatory amount of particles in circulating fluidized bed furnace
    3.
    发明授权
    System for controlling circulatory amount of particles in circulating fluidized bed furnace 有权
    循环流化床炉中颗粒循环量控制系统

    公开(公告)号：US08292977B2

    公开(公告)日：2012-10-23

    申请号：US12526598

    申请日：2007-03-02

    申请人： Toshiyuki Suda ,  Yoshiaki Matsuzawa ,  Toshiro Fujimori

    发明人： Toshiyuki Suda ,  Yoshiaki Matsuzawa ,  Toshiro Fujimori

    IPC分类号： B01J19/00 ,  B01J8/18

    CPC分类号： F27B15/18 ,  C10J3/482 ,  C10J3/56 ,  C10J3/62 ,  C10J3/723 ,  C10J2300/093 ,  C10J2300/0973 ,  C10J2300/1606 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10J2300/1853 ,  F23C10/10 ,  F23C10/32 ,  F23C2206/102

    摘要： The invention has its object to arbitrarily adjust an amount of particles to be circulated without changing a flow rate of a gasification agent to thereby enhance gasification efficiency in a fluidized bed gasification furnace.The fluidized bed gasification furnace 107 comprises first and second chambers 113 and 114 in communication with each other in a fluidized bed 105. The hot particles 102 separated in the separator 104 and raw material M are introduced into the first chamber 113. The particles 102 introduced from the first chamber 113 through interior in the fluidized bed 105 to the second chamber 114 are supplied in an overflow manner to the fluidized bed combustion furnace 100. A first pressure controller 121 is provided to control the resultant gas induction means 116 such that the pressure in the first chamber 113 is kept to preset pressure 120; and a second pressure controller 124 is provided to control the exhaust gas induction means 118 such that difference between pressure in the first and second chambers 113 and 114 is equal to the preset differential pressure 123, so that the fluidized bed 105 in the first chamber 113 is controlled in height to control an amount of particles 102 to be circulated.

    摘要翻译： 本发明的目的是任意调节待循环的颗粒的量，而不改变气化剂的流速，从而提高流化床气化炉的气化效率。 流化床气化炉107包括在流化床105中彼此连通的第一和第二室113和114.将在分离器104中分离的热颗粒102和原料M引入第一室113中。引入颗粒102 从第一室113通过流化床105内部到第二室114以溢流方式供给到流化床燃烧炉100.提供第一压力控制器121以控制所得到的气体诱导装置116，使得压力 在第一室113中保持预设压力120; 并且提供第二压力控制器124以控制排气感应装置118，使得第一和第二室113和114中的压力差等于预设压差123，使得第一室113中的流化床105 被控制在高度以控制要循环的颗粒102的量。

    LOOP SEAL FOR RECYCLING SOLIDS FROM A CYCLONE AND FLUIDIZED BED REACTOR AND METHOD USING THE SAME
    5.
    发明申请
    LOOP SEAL FOR RECYCLING SOLIDS FROM A CYCLONE AND FLUIDIZED BED REACTOR AND METHOD USING THE SAME 有权
    从循环和流化床反应器中回收固体的循环密封及其使用方法

    公开(公告)号：US20120138861A1

    公开(公告)日：2012-06-07

    申请号：US13376291

    申请日：2010-06-05

    申请人： Guohai Liu

    发明人： Guohai Liu

    IPC分类号： B01J8/02 ,  F15C1/16 ,  C01B3/34

    CPC分类号： F23C10/10 ,  F23C10/32 ,  Y10T137/2087

    摘要： A loop seal for a fluidized bed reactor comprising a vertical downcomer segment connected to a dipleg for receiving solids particles from the dipleg, a horizontal segment downstream of the downcomer, a riser segment downstream of the horizontal segment, and a downwardly inclined segment downstream of the riser, whereby the solids are entrained to the fluidized bed reactor. An eductor is added to the angled leg to induce the underflow gas from the cyclone; one of the preferred motive fluids to the eductor is the fines from fuel preparation and the carrying gas for the fines. Also provided are a fluidized bed reactor comprising the loop seal, and a method for producing syngas from coal and steam using the same.

    摘要翻译： 一种用于流化床反应器的环形密封件，包括连接到用于接收来自纬度的固体颗粒的垂直降管段，在降液管下游的水平段，在水平段下游的提升管段和 提升管，由此将固体夹带到流化床反应器中。 将喷射器添加到成角度的腿部以诱导来自旋风分离器的下溢气体; 喷射器中优选的动力流体之一是来自燃料制备和罚款的携带气体的细粉。 还提供了包括环密封件的流化床反应器，以及使用该密封件从煤和蒸汽产生合成气的方法。

    PYROLYSIS METHOD IN CONNECTION WITH A BOILER AND A PYROLYSIS APPARATUS
    6.
    发明申请
    PYROLYSIS METHOD IN CONNECTION WITH A BOILER AND A PYROLYSIS APPARATUS 有权
    与锅炉和热解器相关的热解方法

    公开(公告)号：US20090242377A1

    公开(公告)日：2009-10-01

    申请号：US12414119

    申请日：2009-03-30

    申请人： Timo Honkola ,  Pasi Salonen ,  Jani Lehto

    发明人： Timo Honkola ,  Pasi Salonen ,  Jani Lehto

    IPC分类号： C10B49/00

    CPC分类号： C10B49/22 ,  F22B31/0007 ,  F23C10/06 ,  F23C10/10 ,  F23C10/32 ,  F23C2900/10005 ,  Y02E50/14 ,  Y02P20/129

    摘要： A pyrolysis apparatus comprises a furnace (1) operating by fluidized bed combustion, a pyrolyzer (4) and flow paths, which connect the furnace (1) and the pyrolyzer (4) for arranging the circulation (C) of carrier material of the fluidized bed combustion between the furnace and the pyrolyzer The apparatus also comprises a supply inlet (14) for supplying fuel to be pyrolyzed to the pyrolyzer (4), fluidizing gas supply means (5) arranged in the pyrolyzer for fluidizing the mixture of carrier material and fuel, and an outlet (6) for taking condensible gaseous substances separated from the fuel to be pyrolyzed out of the pyrolyzer (4), and a condenser for condensing the condensible gaseous substances. The carrier material circulation is arranged at the furnace (1) by a cocurrent principle along the flow path of hot flue gases, which comprises a separator (3) located higher than the pyrolyzer (4), which separator is arranged to separate carrier material from flue gases, while the circulation also comprises a connecting conduit (11) between the separator (3) and the pyrolyzer (4) for moving the carrier material by gravity to the pyrolyzer (4), and a return path (12) between the pyrolyzer (4) and the furnace (1) for returning the carrier material to the furnace (1). The outlet (6) is arranged in the chamber formed by the pyrolyzer (4) in its upper part in a space above the fluidized mixture of carrier material and fuel in order to remove the condensible gaseous substances from the pyrolyzer.

    摘要翻译： 热解装置包括通过流化床燃烧操作的炉（1），热解器（4）和流路，其连接炉（1）和热解器（4），用于布置流化床的载体材料的循环（C） 炉和热解器之间的床燃烧该装置还包括用于将待热解的燃料供应到热解器（4）的供应入口（14），布置在热解器中的流化气体供应装置（5），用于使载体材料和 燃料和用于从与热解器（4）热解的燃料分离的可冷凝气态物质的出口（6）和用于冷凝可冷凝气态物质的冷凝器。 载体材料循环通过沿着热烟道气流动的并流原理排列在炉子（1）处，其包括位于高于热解器（4）的分离器（3），该分离器被布置成将载体材料与 烟道气，而循环还包括在分离器（3）和热解器（4）之间的连接导管（11），用于通过重力将载体材料移动到热解器（4），以及在热解器之间的返回路径（12） （4）和用于将载体材料返回到炉（1）的炉（1）。 出口（6）布置在由热解器（4）形成的室中，其上部位于载体材料和燃料的流化混合物上方的空间中，以从热解器中除去可冷凝的气态物质。

    MOVING BED HEAT EXCHANGER FOR CIRCULATING FLUIDIZED BED BOILER
    7.
    发明申请
    MOVING BED HEAT EXCHANGER FOR CIRCULATING FLUIDIZED BED BOILER 有权
    循环流化床锅炉移动床热交换器

    公开(公告)号：US20090151902A1

    公开(公告)日：2009-06-18

    申请号：US11954855

    申请日：2007-12-12

    申请人： Robert V. Jacobs ,  Glen D. Jukkola ,  George D. Mylchreest ,  Bard C. Teigen ,  Richard E. Waryasz ,  John E. Ferguson ,  Laurie Ferguson

    发明人： Robert V. Jacobs ,  Glen D. Jukkola ,  George D. Mylchreest ,  Bard C. Teigen ,  Richard E. Waryasz ,  John E. Ferguson ,  Laurie Ferguson

    IPC分类号： F28D13/00 ,  F22B1/18

    CPC分类号： F23C10/10 ,  F23C10/005 ,  F23C10/32 ,  F23C2206/103 ,  F28D7/00 ,  F28D13/00 ,  F28D2021/0045

    摘要： A moving bed heat exchanger (155) includes a vessel having an upper portion (200), a lower portion (210) with a floor (272) including a discharge opening therein, and an intermediate portion (205). The vessel directs a gravity flow of hot ash particles (140) received thereby from the upper portion (200) through the intermediate portion (205) to the floor (272) of the lower portion (210) of the vessel, where the hot ash particles (140) are collected. Tubes in the intermediate portion (205) of the vessel direct a flow of working fluid in a direction substantially orthogonal to the direction of the gravity flow of the hot ash particles (140) through the intermediate portion (205) of the vessel such that heat from the hot ash particles (140) is transferred to the working fluid thereby cooling the hot ash particles (140).

    摘要翻译： 移动床热交换器（155）包括具有上部（200）的容器，具有包括其中的排放口的底部（272）的下部（210）和中间部分（205）。 容器将从上部（200）接收的热灰分颗粒（140）的重力流通过中间部分（205）引导到容器的下部（210）的地板（272），其中热灰 收集颗粒（140）。 容器的中间部分（205）中的管道沿与容器的中间部分（205）的热灰尘颗粒（140）的重力流动方向基本正交的方向引导工作流体流，使得热量 从热灰分颗粒（140）转移到工作流体，从而冷却热灰分（140）。

    Method and Device For Measuring Circulation Quantity of Bed Material in Circulating Fluidized Bed Combustor
    8.
    发明申请
    Method and Device For Measuring Circulation Quantity of Bed Material in Circulating Fluidized Bed Combustor 有权
    循环流化床燃烧器中床料循环量的方法和装置

    公开(公告)号：US20080153048A1

    公开(公告)日：2008-06-26

    申请号：US11813250

    申请日：2005-12-27

    申请人： Takahiro Murakami ,  Koubun Kyo ,  Toshiyuki Suda

    发明人： Takahiro Murakami ,  Koubun Kyo ,  Toshiyuki Suda

    IPC分类号： F27B15/20

    CPC分类号： G01F1/007 ,  F23C10/10 ,  F23C10/32

    摘要： In order to quantitatively evaluate actual circulation quantity of bed material extremely simply and to enhance accuracy of comparison of results of thermal balance examined through simulation or the like with actual operation results, time is measured which is required for bed material in a downcomer 5 to reach an upper predetermined height H1 from a lower reference height H0 during stopped feeding of fluidizing air to an external heat exchanger 7; a flow rate of the bed material as circulation quantity is determined from the time and an accumulated amount of the bed material based on an inner diameter D of the downcomer 5.

    摘要翻译： 为了非常简单地定量评价床材的实际循环量，通过模拟等与实际运行结果相比提高热平衡结果的比较精度，可以测量降液管5中床材所需的时间 在将流化空气停止供给到外部热交换器7期间，从较低的基准高度H 0> 0的上部预定高度H 1> 1; 基于降液管5的内径D，从床材料的时间和累积量确定床材料的流量作为循环量。