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公开(公告)号：US6039008A
公开(公告)日：2000-03-21
申请号：US241158
申请日：1999-02-01
申请人： David K. Anderson , John H. Chiu , Steven F. McNary , Nicole M. Phyfe , David G. Turek , Donald G. Mylchreest
发明人： David K. Anderson , John H. Chiu , Steven F. McNary , Nicole M. Phyfe , David G. Turek , Donald G. Mylchreest
CPC分类号： F22B31/0084
摘要： There is provided a circulating fluidized bed steam generator (CFB) having an improved structural support system and an improved combined hot solids-gas separator for separating gas and solids from a combined gas-solids stream. The combined hot solids-gas separator is in the form of a cyclone assembly having a plurality of wall portions forming a separation chamber and an inlet for passage of a combined gas-solids stream into the separation chamber. The lowermost extent of the inlet forms a threshold over which the combined gas-solids stream flows in entering the separation chamber. The separation chamber is operable to separate the combined gas-solids stream into a predominantly gas exit stream and a predominantly solids exit stream in a manner by which separated out solids to be discharged from the separation chamber via the predominantly solids exit stream are collected within the separation chamber at a location lower than the inlet. The cyclone assembly further includes a separated solids discharge for the discharge therethrough of the predominantly solids exit stream having the collected separated out solids therein and a gas outlet duct for outward flow of the predominantly gas exit stream out of the separation chamber.
摘要翻译： 提供了具有改进的结构支撑系统的循环流化床蒸汽发生器（CFB）和用于从组合的气体 - 固体物流中分离气体和固体的改进的组合热固体 - 气体分离器。 组合的热固体 - 气体分离器是旋风组件的形式，其具有形成分离室的多个壁部分和用于将组合的气体 - 固体物流通入分离室的入口。 入口的最低范围形成阈值，组合的气体 - 固体物流在其上进入分离室。 分离室可操作以将组合的气体 - 固体物流分离成主要为气体的出口物流和主要为固体的出口物流，通过该方式，通过主要为固体的出口物流从分离室排出的分离的固体被收集在 分离室位于低于入口的位置。 旋风组件还包括分离的固体排出物，用于排出其中具有收集的分离出的固体的主要为固体的出口流，以及气体出口管道，用于将主要为气体的出口流向外流出分离室。
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公开(公告)号：US20100294180A1
公开(公告)日：2010-11-25
申请号：US12468290
申请日：2009-05-19
申请人： John H. Chiu , George D. Mylchreest
发明人： John H. Chiu , George D. Mylchreest
CPC分类号： F23L7/007 , F23C10/10 , F23C2206/103 , Y02E20/344
摘要： In a method for operating a steam generator, a transport reactor is provided. Only a substantially pure oxygen feed stream is introduced into the transport reactor in an amount sufficient to maintain the transport reactor at or above a specific system load. The specific load is the system load when only the substantially pure oxygen feed stream is provided to the transport reactor at a minimum flow velocity for operating the transport reactor. A fuel is combusted in the presence of the substantially pure oxygen feed stream to produce a flue gas, which contains solid material. The solid material is separated from the flue gas and passed to a heat exchanger. The heat exchange may be one of a moving bed heat exchanger or a fluidized bed heat exchanger. The solid material is directed to the transport reactor to contribute to the combustion process.
摘要翻译： 在蒸汽发生器的操作方法中，提供输送反应器。 仅将基本上纯的氧气进料流以足以将输送反应器维持在或高于特定系统负荷的量引入输送反应器。 当仅以基本上纯的氧气进料流以最小流速提供给输送反应器以操作输送反应器时，具体负荷是系统负荷。 燃料在基本上纯的氧气进料流的存在下燃烧以产生含有固体材料的烟道气。 将固体材料与烟道气分离并通入热交换器。 热交换器可以是移动床式热交换器或流化床热交换器之一。 固体材料被引导到输送反应器以有助于燃烧过程。
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公开(公告)号：US09638418B2
公开(公告)日：2017-05-02
申请号：US12468290
申请日：2009-05-19
申请人： John H. Chiu , George D. Mylchreest
发明人： John H. Chiu , George D. Mylchreest
CPC分类号： F23L7/007 , F23C10/10 , F23C2206/103 , Y02E20/344
摘要： In a method for operating a steam generator, a transport reactor is provided. Only a substantially pure oxygen feed stream is introduced into the transport reactor in an amount sufficient to maintain the transport reactor at or above a specific system load. The specific load is the system load when only the substantially pure oxygen feed stream is provided to the transport reactor at a minimum flow velocity for operating the transport reactor. A fuel is combusted in the presence of the substantially pure oxygen feed stream to produce a flue gas, which contains solid material. The solid material is separated from the flue gas and passed to a heat exchanger. The heat exchange may be one of a moving bed heat exchanger or a fluidized bed heat exchanger. The solid material is directed to the transport reactor to contribute to the combustion process.
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公开(公告)号：US09163830B2
公开(公告)日：2015-10-20
申请号：US12749284
申请日：2010-03-29
申请人： John H. Chiu , Bard C. Teigen
发明人： John H. Chiu , Bard C. Teigen
CPC分类号： F23C10/08 , B01J8/0025 , B01J2208/00752 , B01J2208/00769 , F22B31/0084 , F23C10/02 , F23C10/10 , F23C10/32
摘要： A sealpot for a combustion power plant includes a downcomer standpipe which receives solids of the combustion power plant, a bed including a first end and a second opposite end, the first end connected to the downcomer standpipe, a discharge standpipe disposed at the second opposite end of the bed, and an orifice plate disposed between the bed and the discharge standpipe separating the discharge standpipe from the bed. The orifice plate includes apertures disposed at a height above the bed which allow transport of fluidized solids and gas through the orifice plate.
摘要翻译： 用于燃烧发电厂的密封罐包括接收燃烧动力装置的固体的降液管立管，包括第一端和第二相对端的床，第一端连接到降液管立管，设置在第二相对端的排放立管 以及设置在床和排放立管之间的孔板，其将排放立管与床分离。 孔板包括设置在床上方的高度的孔，其允许流化固体和气体通过孔板的输送。
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公开(公告)号：US08110012B2
公开(公告)日：2012-02-07
申请号：US12533780
申请日：2009-07-31
IPC分类号： B01J7/00
CPC分类号： C10J3/54 , C10J3/721 , C10J3/725 , C10J2300/0996 , C10J2300/1807 , Y02E20/16 , Y02E20/18 , Y02P20/129
摘要： In a retrofit system for hot solids combustion and gasification, a chemical looping system includes an endothermic reducer reactor 12 having at least one materials inlet 22 for introducing carbonaceous fuel and CaCO3 therein and a CaS/gas outlet 26. A first CaS inlet 40 and a first CaSO4 inlet 64 are also defined by the reducer reactor 12. An oxidizer reactor 14 is provided and includes an air inlet 68, a CaSO4/gas outlet 46, a second CaS inlet 44, and a second CaSO4 inlet 66. A first separator 30 is in fluid communication with the CaS/gas outlet 26 and includes a product gas and a CaS/gas outlet 32 and 34 from which CaS is introduced into said first and second CaS inlets. A second separator 50 is in fluid communication with the CaSO4/gas outlet 46 and has an outlet 52 for discharging gas therefrom, and a CaSO4 outlet from which CaSO4 is introduced into the first and second CaSO4 inlets 62, 66. The chemical looping system is in fluid communication with at least a portion of an existing power generation system.
摘要翻译： 在用于热固体燃烧和气化的改进系统中，化学循环系统包括吸热还原反应器12，其具有至少一个用于将碳质燃料和CaCO 3引入其中的材料入口22和CaS /气体出口26.第一CaS入口40和 第一CaSO 4入口64也由还原反应器12限定。提供氧化反应器14，包括空气入口68，CaSO 4 /气体出口46，第二CaS入口44和第二CaSO 4入口66.第一分离器30 与CaS /气体出口26流体连通，并且包括产物气体和CaS /气体出口32和34，CaS从其引入到所述第一和第二CaS入口中。 第二分离器50与CaSO 4 /气体出口46流体连通，并且具有用于从其中排出气体的出口52和CaSO 4出口，CaSO 4从其引入第一和第二CaSO 4入口62,66。化学循环系统是 与现有发电系统的至少一部分流体连通。
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公开(公告)号：US20100242815A1
公开(公告)日：2010-09-30
申请号：US12749284
申请日：2010-03-29
申请人： John H. Chiu , Bard C. Teigen
发明人： John H. Chiu , Bard C. Teigen
CPC分类号： F23C10/08 , B01J8/0025 , B01J2208/00752 , B01J2208/00769 , F22B31/0084 , F23C10/02 , F23C10/10 , F23C10/32
摘要： A sealpot for a combustion power plant includes a downcomer standpipe which receives solids of the combustion power plant, a bed including a first end and a second opposite end, the first end connected to the downcomer standpipe, a discharge standpipe disposed at the second opposite end of the bed, and an orifice plate disposed between the bed and the discharge standpipe separating the discharge standpipe from the bed. The orifice plate includes apertures disposed at a height above the bed which allow transport of fluidized solids and gas through the orifice plate.
摘要翻译： 用于燃烧发电厂的密封罐包括接收燃烧动力装置的固体的降液管立管，包括第一端和第二相对端的床，第一端连接到降液管立管，设置在第二相对端的排放立管 以及设置在床和排放立管之间的孔板，其将排放立管与床分离。 孔板包括设置在床上方的高度的孔，其允许流化固体和气体通过孔板的输送。
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公开(公告)号：US20100050654A1
公开(公告)日：2010-03-04
申请号：US12533780
申请日：2009-07-31
CPC分类号： C10J3/54 , C10J3/721 , C10J3/725 , C10J2300/0996 , C10J2300/1807 , Y02E20/16 , Y02E20/18 , Y02P20/129
摘要： In a retrofit system for hot solids combustion and gasification, a chemical looping system includes an endothermic reducer reactor 12 having at least one materials inlet 22 for introducing carbonaceous fuel and CaCO3 therein and a CaS/gas outlet 26. A first CaS inlet 40 and a first CaSO4 inlet 64 are also defined by the reducer reactor 12. An oxidizer reactor 14 is provided and includes an air inlet 68, a CaSO4/gas outlet 46, a second CaS inlet 44, and a second CaSO4 inlet 66. A first separator 30 is in fluid communication with the CaS/gas outlet 26 and includes a product gas and a CaS/gas outlet 32 and 34 from which CaS is introduced into said first and second CaS inlets. A second separator 50 is in fluid communication with the CaSO4/gas outlet 46 and has an outlet 52 for discharging gas therefrom, and a CaSO4 outlet from which CaSO4 is introduced into the first and second CaSO4 inlets 62, 66. The chemical looping system is in fluid communication with at least a portion of an existing power generation system.
摘要翻译： 在用于热固体燃烧和气化的改进系统中，化学循环系统包括吸热还原反应器12，其具有至少一个用于将碳质燃料和CaCO 3引入其中的材料入口22和CaS /气体出口26.第一CaS入口40和 第一CaSO 4入口64也由还原反应器12限定。提供氧化反应器14，包括空气入口68，CaSO 4 /气体出口46，第二CaS入口44和第二CaSO 4入口66.第一分离器30 与CaS /气体出口26流体连通，并且包括产物气体和CaS /气体出口32和34，CaS从其引入到所述第一和第二CaS入口中。 第二分离器50与CaSO 4 /气体出口46流体连通，并且具有用于从其中排出气体的出口52和CaSO 4出口，CaSO 4从其引入第一和第二CaSO 4入口62,66。化学循环系统是 与现有发电系统的至少一部分流体连通。
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8.发明授权Internal circulation fluidized bed (ICFB) combustion system and method of operation thereof 失效内循环流化床（ICFB）燃烧系统及其运行方法
公开(公告)号：US5401130A
公开(公告)日：1995-03-28
申请号：US173539
申请日：1993-12-23
申请人： John H. Chiu , Michael J. Hargrove , Glen D. Jukkola , Mark A. Douglas , Stuart A. Morrison , Steve Y. Wong
发明人： John H. Chiu , Michael J. Hargrove , Glen D. Jukkola , Mark A. Douglas , Stuart A. Morrison , Steve Y. Wong
CPC分类号： F23G5/30 , F23C10/14 , F23G7/10 , F23G2203/502 , F23G2205/121 , F23G2205/14 , F23G2205/18 , F23G2209/12 , F23G2209/22 , F23G2209/261
摘要： A fluidized bed combustion system (10) particularly suited for use to effect the incineration, i.e., combustion, therewith of wood waste/sludge mixtures that have high moisture and ash content which makes them difficult to burn. The fluidized bed combustion system (10) includes a fluidized bed combustor (12) embodying a fluidized bed (24) composed of bed solids. Air is injected into the fluidized bed (24) through an air distributor (28) to establish a first controlled fluidizing velocity zone and a second controlled fluidizing velocity zone therewithin. Material (42b) is introduced into the fluidized bed combustor (12) above the second controlled fluidizing velocity zone. Bed solids are projected from the first controlled fluidizing velocity zone to the second controlled fluidizing velocity zone whereupon the bed solids rain down upon the material (42b) and effect a covering thereof. The material (42b) is then dried and thereafter combusted. Inerts/tramp materials/clinkers as well as large diameter solids entrained with the material (42b) are segregated therefrom and then are removed (14,200) from the fluidized bed combustor (12).
摘要翻译： 流化床燃烧系统（10）特别适于用于实现焚烧，即燃烧具有高水分和灰分的木材废物/污泥混合物，这使得它们难以燃烧。 流化床燃烧系统（10）包括实现由床固体组成的流化床（24）的流化床燃烧器（12）。 空气通过空气分配器（28）注入到流化床（24）中，以在其中建立第一受控流化速度区和第二受控流化速度区。 材料（42b）被引入第二受控流化速度区之上的流化床燃烧器（12）。 床固体从第一受控流化速度区域投射到第二受控流化速度区域，随后床固体在材料（42b）上下降并影响其覆盖物。 然后将材料（42b）干燥并随后燃烧。 惰性物质/杂质材料/熟料以及与材料（42b）夹带的大直径固体与其分离，然后从流化床燃烧器（12）中除去（14,200）。
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