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1. 发明申请

US20100288678A1 HOT SOLIDS PROCESS HAVING AN OUTPUT SUITABLE FOR THE INPUT TO A PETROCHEMICAL PROCESS 审中-公开
标题翻译：具有适用于输入石油化学工艺的输出的热固体工艺
公开(公告)号：US20100288678A1
公开(公告)日：2010-11-18
申请号：US12749238
申请日：2010-03-29
申请人： Herbert E. ANDRUS, JR. , John H. CHIU , Gregory N. LILJEDAHL , Paul R. THIBEAULT , Carl R. BOZZUTO , Corinne BEAL , Michal T. BIALKOWSKI , Andreas BRAUTSCH , Laurent MAGHDISSIAN , Michel VANDYCKE
发明人： Herbert E. ANDRUS, JR. , John H. CHIU , Gregory N. LILJEDAHL , Paul R. THIBEAULT , Carl R. BOZZUTO , Corinne BEAL , Michal T. BIALKOWSKI , Andreas BRAUTSCH , Laurent MAGHDISSIAN , Michel VANDYCKE
IPC分类号： C10G1/00
CPC分类号： C10G1/00 , C10G29/02 , C10G2300/202 , C10G2300/807 , C10J3/00 , C10J3/12 , C10J3/725 , C10J2300/0993 , C10J2300/0996 , C10J2300/1807
摘要： A hot solids process wherein a predetermined output, which is designed to be suitable for use as an input to a petrochemical process, is capable of being generated through the use of the hot solids process. The mode of operation of such a hot solids process is designed to be such that preferably a portion of the otherwise normally unusable product output, which is produced from a petrochemical process, is designed to be utilized as an input to the hot solids process for purposes of generating from the hot solids process the predetermined output that is suitable for use as an input to a petrochemical process.
摘要翻译：热固体过程，其中设计为适合用作石油化学工艺的输入的预定输出能够通过使用热固体过程产生。这种热固体过程的操作模式被设计成使得优选地，由石油化学工艺生产的一部分通常不可用的产品输出被设计为用作热固体过程的输入，以用于目的从热固体处理产生适合用作石油化学工艺的输入的预定输出。

2. 发明授权

US09638418B2 Oxygen fired steam generator 有权
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
IPC分类号： F23L7/00 , F23C10/10
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.

3. 发明授权

US09163830B2 Sealpot and method for controlling a solids flow rate therethrough 有权
标题翻译：密封罐和用于控制通过其中的固体流速的方法
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
IPC分类号： F23C10/10 , F22B31/00 , B01J8/00 , F23C10/32
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。

4. 发明授权

US08110012B2 System for hot solids combustion and gasification 有权
标题翻译：热固体燃烧和气化系统
公开(公告)号：US08110012B2
公开(公告)日：2012-02-07
申请号：US12533780
申请日：2009-07-31
申请人： John H. Chiu , Herbert E. Andrus , Gregory N. Liljedahl , Paul R. Thibeault
发明人： John H. Chiu , Herbert E. Andrus , Gregory N. Liljedahl , Paul R. Thibeault
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。

5. 发明申请

US20100290975A1 HOT SOLIDS PROCESS SELECTIVELY OPERABLE FOR COMBUSTION PURPOSES AND GASIFICATION PURPOSES 审中-公开
标题翻译：热固性过程可选择用于燃烧用途和气化目的
公开(公告)号：US20100290975A1
公开(公告)日：2010-11-18
申请号：US12749166
申请日：2010-03-29
申请人： Herbert E. ANDRUS, JR. , John H. CHIU , Gregory N. LILJEDAHL , Paul R. THIBEAULT , Carl R. BOZZUTO , Corinne BEAL , Michal T. BIALKOWSKI , Andreas BRAUTSCH , Laurent MAGHDISSIAN , Michel VANDYCKE
发明人： Herbert E. ANDRUS, JR. , John H. CHIU , Gregory N. LILJEDAHL , Paul R. THIBEAULT , Carl R. BOZZUTO , Corinne BEAL , Michal T. BIALKOWSKI , Andreas BRAUTSCH , Laurent MAGHDISSIAN , Michel VANDYCKE
IPC分类号： C10J3/46 , C01B31/20 , C01B31/18 , C01B3/02
CPC分类号： C01B3/344 , C10J3/00 , C10J3/12 , C10J3/46 , C10J3/54 , C10J3/725 , C10J2300/0993 , C10J2300/0996 , C10J2300/1807 , F23C10/002 , F23C10/005 , F23C10/02 , F23J7/00
摘要： A hot solids process operable selectively for combustion purposes and gasification purposes wherein a pre-identified product is selected from a group of products to be generated through the use of the hot solids process. Based on the nature of the pre-identified product, which is to be generated through the use of the hot solids process, a specific fuel from which the pre-identified product is capable of being derived is selected from a group of fuels. Then, from a group of reactors there is selected a first reactor, which is operable for generating in the first reactor the pre-identified product as an output from the first reactor. Thereafter, from a group of reactors, there is selected a second reactor, which is operable for effecting in the second reactor the conversion of air and of a predetermined carrier selected from a group of carriers to produce a predefined output from the second reactor.
摘要翻译：用于燃烧目的和气化目的的选择性操作的热固体过程，其中预先鉴定的产物选自通过使用热固体过程产生的一组产物。基于通过使用热固体过程产生的预先识别的产品的性质，从一组燃料中选择预先鉴定的产物能够衍生的特定燃料。然后，从一组反应器中选择第一反应器，其可操作以在第一反应器中产生预先鉴定的产物作为来自第一反应器的输出。此后，从一组反应器中选择第二反应器，其可操作以在第二反应器中实现空气和选自一组载体的预定载体的转化，从而产生来自第二反应器的预定输出。

6. 发明申请

US20100242815A1 SEALPOT AND METHOD FOR CONTROLLING A SOLIDS FLOW RATE THERETHROUGH 有权
标题翻译：用于控制固体流速的密封件和方法
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
IPC分类号： F23C10/10 , F23J15/00
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。

7. 发明申请

US20100050654A1 SYSTEM FOR HOT SOLIDS COMBUSTION AND GASIFICATION 有权
标题翻译：热固体燃烧和气化系统
公开(公告)号：US20100050654A1
公开(公告)日：2010-03-04
申请号：US12533780
申请日：2009-07-31
申请人： John H. Chiu , Herbert E. Andrus , Gregory N. Liljedahl , Paul R. Thibeault
发明人： John H. Chiu , Herbert E. Andrus , Gregory N. Liljedahl , Paul R. Thibeault
IPC分类号： F02C3/28 , B01J10/00 , B01J8/00 , C10J3/00 , F02C6/00 , F01K11/02 , F01K23/14
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。

8. 发明授权

US5401130A Internal circulation fluidized bed (ICFB) combustion system and method of operation thereof 失效
标题翻译：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
IPC分类号： F23C10/24 , F22B1/02 , F23C10/14 , F23G5/30 , F23G7/10 , F23G5/00
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）。

9. 发明申请

US20100294180A1 OXYGEN FIRED STEAM GENERATOR 有权
标题翻译：氧气发电机
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
IPC分类号： F23J15/00 , F23L7/00 , F23L15/00 , F22B1/02
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。

10. 发明申请

US20100284894A1 HOT SOLIDS PROCESS SELECTIVELY OPERABLE BASED ON ITS PRIMARY PURPOSE 有权
标题翻译：基于其主要目的选择可行的固体过程
公开(公告)号：US20100284894A1
公开(公告)日：2010-11-11
申请号：US12749221
申请日：2010-03-29
申请人： Herbert E. ANDRUS, JR. , John. H. CHIU , Gregory N. LILJEDAHL , Paul R. THIBEAULT , Carl R. BOZZUTO , Corinne BEAL , Michal T. BIALKOWSKI , Andreas BRAUTSCH , Laurent MAGHDISSIAN , Michel VANDYCKE
发明人： Herbert E. ANDRUS, JR. , John. H. CHIU , Gregory N. LILJEDAHL , Paul R. THIBEAULT , Carl R. BOZZUTO , Corinne BEAL , Michal T. BIALKOWSKI , Andreas BRAUTSCH , Laurent MAGHDISSIAN , Michel VANDYCKE
IPC分类号： C01B31/20 , C10J3/46 , C01B3/24 , C01B3/36
CPC分类号： C10J3/00 , C10J3/725 , C10J2300/093 , C10J2300/0976 , C10J2300/0996 , C10J2300/1807 , F23C2900/99008 , Y02E20/346
摘要： A hot solids process selectively operable for purposes of generating at least one predetermined output based on what the specific nature of the primary purpose of the hot solids process is for which the at least one predetermined output that is selected from a multiplicity of predetermined outputs, such as H2 and CO2, is being produced, and wherein such primary purpose of the hot solids process is designed to be pre-selected from a group of primary purposes of the hot solids process that includes at least two of the generation of H2 for electric power purposes, the generation of SynGas for electric power production as well as for other industrial uses, the production of steam for electric power generation as well as for other uses, the production of process heat, the production of CO2 for agricultural purposes, and the generation of a feedstock such as H2 for use for the production of liquid hydrocarbons.
摘要翻译：热固体过程选择性地可操作用于基于热固体过程的主要目的的特定性质产生至少一个预定输出，对于该固体过程，选择多个预定输出的至少一个预定输出，例如作为H 2和CO 2，并且其中热固体过程的这种主要目的被设计为从热固体过程的一组主要目的中预先选择的，所述热固体过程包括产生用于电力的H2中的至少两个目的，生产用于电力生产和其他工业用途的SynGas，生产用于发电和其他用途的蒸汽，生产过程热量，用于农业生产的二氧化碳，以及生成的诸如H 2的原料用于生产液体烃。

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