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。

公开(公告)号：US08695514B2

公开(公告)日：2014-04-15

申请号：US12465822

申请日：2009-05-14

申请人： Glen D. Jukkola ,  Gregory N. Liljedahl ,  Nsakala Ya Nsakala ,  Mark Palkes

发明人： Glen D. Jukkola ,  Gregory N. Liljedahl ,  Nsakala Ya Nsakala ,  Mark Palkes

IPC分类号： F23B70/00

CPC分类号： F23C9/00 ,  F22B1/1884 ,  F22B37/42 ,  F23C2202/00 ,  Y02E20/344

摘要： An air infiltration abatement system (300) for a power plant (10) includes a recirculated flue gas source (175), a recirculated flue gas supply line (310) connected to the recirculated flue gas source (175) and a power plant component. The power plant component has a leakage area in fluid communication with the recirculated flue gas supply line (310). The recirculated flue gas source (175) receives a combustion flue gas (75) from an oxygen fired boiler (20) of the power plant (10), and provides the combustion flue gas (75) to the recirculated flue gas supply line (310). The recirculated flue gas supply line (310) supplies the combustion flue gas (75) as a recirculated flue gas (330) to the oxygen fired boiler (20) via the leakage area of the power plant component.

摘要翻译： 用于发电厂（10）的空气渗透减排系统（300）包括再循环烟道气源（175），连接到再循环烟道气源（175）的再循环烟道气供应管线（310）和发电厂部件。 发电厂部件具有与再循环烟道气供应管线（310）流体连通的泄漏区域。 再循环烟道气源（175）接收来自发电厂（10）的氧燃锅炉（20）的燃烧烟道气（75），并将燃烧烟道气（75）提供给再循环烟道气供应管线 ）。 再循环的烟气供应管线（310）经由发电厂部件的泄漏区域将作为再循环烟道气（330）的燃烧烟道气（75）供应到氧燃锅炉（20）。

公开(公告)号：US06202574B1

公开(公告)日：2001-03-20

申请号：US09351059

申请日：1999-07-09

申请人： Gregory N. Liljedahl ,  Mark Palkes

发明人： Gregory N. Liljedahl ,  Mark Palkes

IPC分类号： F23J1500

CPC分类号： F25J3/0266 ,  F23C9/003 ,  F23D1/00 ,  F23J15/06 ,  F23J2900/15061 ,  F23K3/02 ,  F23K2201/103 ,  F23K2900/01041 ,  F23L7/007 ,  F23L2900/07001 ,  F25J3/04533 ,  F25J2210/70 ,  Y02C10/12 ,  Y02E20/322 ,  Y02E20/344 ,  Y02E20/363

摘要： A fossil fuel fired combustion apparatus and a method for operating the fossil fuel fired combustion apparatus are provided which offer the flexibility to use carbon dioxide (CO2) both as a desirable end product and as support to the combustion process. The method includes the step of introducing a substantially pure oxygen feed stream into the fossil fuel fired combustion apparatus and the step of combusting a fossil fuel in the presence of the substantially pure oxygen feed stream to produce a flue gas having carbon dioxide and water vapor as its two largest constituent elements by volume. The method also includes the step of passing the flue gas through an oxygen feed stream pre-heater at which heat from the flue gas is transferred to the oxygen feed stream. Furthermore, the method includes the step of separating the flue gas into an end product portion and a recycling portion. The method additionally includes cooling and compressing the end product portion of the flue gas so as to yield carbon dioxide in a liquid phase and directing the recycling portion of the flue gas to the fossil fuel fired combustion unit to contribute to the combustion process therein.

摘要翻译： 提供化石燃料燃烧燃烧装置和操作化石燃料燃烧燃烧装置的方法，其提供使用二氧化碳（CO 2）作为期望的最终产物和作为对燃烧过程的支持的灵活性。 该方法包括将基本上纯的氧气进料流引入化石燃料燃烧燃烧装置的步骤，以及在基本上纯的氧气进料流存在下燃烧化石燃料以产生具有二氧化碳和水蒸气的烟道气的步骤 它的两个最大的构成要素按体积。 该方法还包括使烟道气通过氧气进料流预热器的步骤，在该预热器中将来自烟道气的热量转移到氧气进料流。 此外，该方法包括将烟道气分离成最终产品部分和再循环部分的步骤。 该方法还包括冷却和压缩烟道气的最终产品部分，以产生液相中的二氧化碳，并将烟道气的再循环部分引导到化石燃料燃烧的燃烧单元以有助于其中的燃烧过程。