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    • 3. 发明申请
    • SYSTEM FOR HOT SOLIDS COMBUSTION AND GASIFICATION
    • 用于热固体燃烧和气化的系统
    • WO2010014938A2
    • 2010-02-04
    • PCT/US2009052467
    • 2009-07-31
    • ALSTOM TECHNOLOGY LTDCHIU JOHN HANDRUS JR HERBERT ELILJEDAHL GREGORY NTHIBEAULT PAUL R
    • CHIU JOHN HANDRUS JR HERBERT ELILJEDAHL GREGORY NTHIBEAULT PAUL R
    • C10J3/54C10J3/721C10J3/725C10J2300/0996C10J2300/1807Y02E20/16Y02E20/18Y02P20/129
    • 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.
    • 在用于热固体燃烧和气化的改造系统中,化学回路系统包括吸热还原器反应器12,其具有至少一个用于将碳质燃料和CaCO3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并包括空气入口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从所述CaS /气体出口32和34被引入到所述第一CaS入口和第二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从其中引入CaSO 4到第一和第二CaSO 4入口62,66。化学循环系统是 与现有的发电系统的至少一部分流体连通。
    • 4. 发明申请
    • REDUCING CARBON DIOXIDE (CO2) EMISSIONS FROM THE BURNING OF A FOSSIL FUEL
    • 减少二氧化碳(CO2)排放物燃烧燃料
    • WO2009105419A2
    • 2009-08-27
    • PCT/US2009034265
    • 2009-02-17
    • ALSTOM TECHNOLOGY LTDJUKKOLA GLEN D
    • JUKKOLA GLEN DANDRUS JR HERBERT EMCCARTNEY MICHAEL S
    • F23J15/02B01D53/34B01D53/62
    • F23J15/027B01D53/62B01D2251/404B01D2257/504F23J15/02F23J2215/50F23J2217/40Y02A50/2342Y02C10/04Y02C10/08Y02E20/326
    • A system (10) for reducing carbon dioxide emissions from gasses generated in burning fossil fuel, includes a vessel (20), separator (38) and reheater (50). The upper portion (12) of the vessel (20) receives downward flowing, first type solid particles capable of absorbing heat from upward flowing gasses (22) and second type solid particles capable of capturing carbon dioxide from the gasses. The separator (38) separates the second type solid particles (26) with the captured carbon dioxide from the gasses discharged from the first vessel discharge, and directs the separated second type solid particles (26) with the captured carbon dioxide to a separator discharge. The reheater (28) directs the first type solid particles and the second type solid particles (24) with the captured carbon dioxide in a downwardly flow to a first reheater discharge, such that heat from the first type solid particles causes the captured carbon dioxide to be released from the second type solid particles (26).
    • 用于减少在燃烧化石燃料中产生的气体二氧化碳排放的系统(10)包括容器(20),分离器(38)和再热器(50)。 容器(20)的上部(12)容纳向下流动的能够从向上流动的气体(22)吸收热量的第一类型固体颗粒和能够从气体中捕获二氧化碳的第二类型固体颗粒。 分离器(38)将第二类型固体颗粒(26)与从第一容器排放物排出的气体中捕获的二氧化碳分离,并将分离的第二类型固体颗粒(26)与捕获的二氧化碳引导至分离器排出物。 再热器(28)将第一类固体颗粒和第二类固体颗粒(24)以捕获的二氧化碳向下流动引导到第一再热器排放物,使得来自第一类型固体颗粒的热量将捕获的二氧化碳 从第二类固体颗粒(26)中释放出来。