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    • 43. 发明授权
    • Method and system for rich-lean catalytic combustion
    • 富催化燃烧的方法和系统
    • US07444820B2
    • 2008-11-04
    • US10969390
    • 2004-10-20
    • Meredith B. Colket, III
    • Meredith B. Colket, III
    • F02C7/22F02C7/26
    • F23L15/04F23C6/045F23C13/00F23R3/40Y02E20/348
    • A gas turbine engine using a rich-lean catalytic combustion system includes a rich catalytic burner and a lean catalytic burner. The rich catalytic burner includes a rich catalytic reactor and a heat exchanger. The rich catalytic reactor catalytically burns a fuel rich mixture to provide a heated fuel. The heat exchanger receives a stream of air that absorbs a portion of the heat from the catalytic burning of the fuel rich mixture to keep the reaction in the rich catalytic reactor at or below a threshold temperature. A resulting heated air from the heat exchanger and the heated fuel are mixed in a mixing zone to provide a heated fuel-air mixture. The lean catalytic burner receives and burns the heated fuel-air mixture.
    • 使用富贫催化燃烧系统的燃气涡轮发动机包括富催化燃烧器和贫催化燃烧器。 富催化燃烧器包括富催化反应器和热交换器。 富催化反应器催化燃烧富燃料混合物以提供加热燃料。 热交换器接受空气流,其吸收来自富燃料混合物的催化燃烧的一部分热量,以使富催化反应器中的反应保持在或低于阈值温度。 来自热交换器和加热燃料的所得加热空气在混合区中混合以提供加热的燃料 - 空气混合物。 贫催化燃烧器接收并燃烧加热的燃料 - 空气混合物。
    • 44. 发明授权
    • Deozonating device with integrated heat exchanger
    • 具有集成热交换器的脱气装置
    • US07416713B2
    • 2008-08-26
    • US11257496
    • 2005-10-24
    • Klaus NonnenmacherGuido Rohrbach
    • Klaus NonnenmacherGuido Rohrbach
    • B01D53/66B01J19/00
    • F23G7/063B01D53/66B01D2257/106B01D2258/0216F23G7/065F23L15/04F28D9/0031Y02E20/348
    • The invention is concerned with a device of destroying ozone in gases by employing a recuperative plate heat exchanger (1) and an integrated electrical heating element (19, 21). The recuperative plate heat exchanger (1) is equipped with at least two planes, a preheating plane (11) and a recooling plane (13), whereby the flow direction of the gas treated in the recooling plane (13) is reversed relative to the ozone-containing gas in the preheating plane (11). Preferably, the flow directions of the preheating plane (11) and the recooling plane (13) cross over. The electrical heating element (19, 21) is situated in a reaction chamber (3) and heats up the ozone-containing gas preheated in the heat-exchanger up to temperatures of 350° C. or more, and thus destroys the ozone within the gas almost to completion. The plate heat exchanger (1) works almost without pressure losses.
    • 本发明涉及通过采用换热板式热交换器(1)和集成电加热元件(19,21)来破坏气体中的臭氧的装置。 再生板式热交换器(1)配备有至少两个平面,即预热平面(11)和再冷却平面(13),由此在再冷却平面(13)中处理的气体的流动方向相对于 预热平面(11)中含臭氧的气体。 优选地,预热平面(11)和再冷却平面(13)的流动方向交叉。 电加热元件(19,21)位于反应室(3)中,将在热交换器中预热的含臭氧气体加热至350℃以上的温度,从而破坏在 气体几乎完成。 板式换热器(1)几乎没有压力损失。
    • 46. 发明授权
    • Method and plant for manufacturing cement clinker
    • 制造水泥熟料的方法和设备
    • US07390357B2
    • 2008-06-24
    • US10526155
    • 2003-07-11
    • Lars Skaarup JensenJens Peter Hansen
    • Lars Skaarup JensenJens Peter Hansen
    • C04B2/10
    • C04B7/365F23L15/04F27B7/20F27B7/2025Y02E20/348
    • Described is a method for manufacturing cement clinker by which method cement raw meal is preheated and burned in a plant comprising a cyclone preheater (1) and a kiln (5). The method is peculiar in that that at least a portion of the raw meal is extracted from the cyclone preheater (1), that this raw meal is introduced into a separate unit (21) in which it is given a retention time under oxidating conditions provided by means of a gas stream for forming SO2 and for expelling organic carbon, that the formed SO2 and the expelled organic carbon are subsequently discharged from the separate unit (21) entrained in the gas stream for further treatment in a subsequent process stage, and that the raw meal is reintroduced into the cyclone preheater (1). Hereby is obtained an effective reduction of the VOC, CO as well as the SO2 emission without necessitating utilization of additional energy for heating. By giving the extracted and partially preheated raw meal a retention time under oxidating conditions separate from the cyclone preheater it is obtained that sulphide will oxidate into SO2 and that organic carbon is expelled from the raw meal, so that the thus formed SO2 and the thus expelled organic carbon can be entrained in a separate, relatively small gas stream and subjected to subsequent treatment in the optimum manner.
    • 描述了一种用于制造水泥熟料的方法,通过该方法将水泥生料在包括旋风预热器(1)和窑(5)的设备中预热和燃烧。 该方法是特殊的,因为至少一部分生料从旋风预热器(1)中提取,将该生料加入到分离的单元(21)中,其中在提供的氧化条件下给予其保留时间 通过用于形成SO 2和排出有机碳的气流,形成的SO 2和排出的有机碳随后从夹带在气流中的分离单元(21)排出,以便在后续处理阶段进一步处理,并且 将生料再次引入旋风预热器(1)。 从而获得了VOC,CO以及SO2排放的有效减少,而不需要利用额外的能量进行加热。 通过在与旋风预热器分离的氧化条件下提取和部分预热的生料保留时间,得到硫化物将氧化成SO 2,并且有机碳从生料中排出,从而形成的SO 2并因此被排出 有机碳可以夹带在单独的相对小的气流中,并以最佳方式进行后续处理。
    • 47. 发明授权
    • Combustion system with recirculation of flue gas
    • 燃烧系统与废气再循环
    • US07350471B2
    • 2008-04-01
    • US11069769
    • 2005-03-01
    • Alexander I. Kalina
    • Alexander I. Kalina
    • F23L7/00
    • F23C9/08F22B35/002F23C2202/30F23L15/04Y02E20/348
    • An improved combustion method and corresponding apparatus is disclosed, where the method includes oxidizing a fuel in a combustion chamber with an oxidizing stream including an air stream and a first recycled flue gas stream and mixing a produced hot flue gas stream with a second recycled flue gas stream to form reduced temperature flue gas stream which can be used directly in a power generator or to heat a reactor. The method and apparatus allow flow rates of the streams to be adjusted so that temperatures in the combustion chamber and in the heat transfer unit or units of the power generator or reactor can be kept below temperature that would thermally damage the combustion chamber, heat transfer unit or units or the reactors.
    • 公开了一种改进的燃烧方法和相应的装置,其中所述方法包括用包括空气流和第一再循环烟道气流的氧化流来氧化燃烧室中的燃料,并将生产的热烟道气流与第二再循环烟道气 流以形成可以直接用于发电机中或加热反应器的还原温度的烟道气流。 该方法和设备允许调节流的流速,使得燃烧室和发电机或反应器的传热单元或单元中的温度可以保持在低于将损坏燃烧室的温度,热传递单元 或单位或反应堆。
    • 48. 发明申请
    • Industrial burner and method for operating an industrial burner
    • 工业燃烧器和操作工业燃烧器的方法
    • US20070037107A1
    • 2007-02-15
    • US11501429
    • 2006-08-09
    • Horst von SchweinitzAndreas Munko
    • Horst von SchweinitzAndreas Munko
    • F23N5/00F23D14/46F23C7/00F23D14/00
    • F23C3/00F23C2900/03005F23L15/04F23N5/08F23N5/12Y02E20/348
    • The industrial burner comprising a mixing chamber, which is provided with at least one opening into a furnace room, through which opening at least a partially-mixed fuel flow from the mixing chamber dispenses into the furnace room during operation. A combustion air supplier, through which the mixing chamber is supplied with combustion air during operation, and a fuel supplier, with which fuel is introduced into the mixing chamber, are provided. The fuel supplier can switch between a first and a second operation state, wherein in the first operation state, fuel is introduced into the mixing chamber at a first angle, and in the second operation state, fuel is introduced into the mixing chamber at substantially the same axial position with respect to the opening as in the first operation state and at a second angle with respect to the axial direction of the mixing chamber.
    • 该工业燃烧器包括混合室,该混合室设置有至少一个进入炉室的开口,通过该混合室,来自混合室的至少一部分混合的燃料流在操作期间分配到炉室中。 提供了在操作期间向混合室供给燃烧空气的燃烧空气供应器以及将燃料引入混合室的燃料供给器。 燃料供应商可以在第一和第二操作状态之间切换,其中在第一操作状态下,燃料以第一角度被引入混合室,而在第二操作状态下,燃料基本上被引入混合室 与第一操作状态相对于开口具有相同的轴向位置,并且相对于混合室的轴向以第二角度。
    • 50. 发明申请
    • System for catalytic combustion
    • 催化燃烧系统
    • US20060150635A1
    • 2006-07-13
    • US10529515
    • 2003-09-26
    • Shi SuAndrew BeathClifford Mallett
    • Shi SuAndrew BeathClifford Mallett
    • F23R3/40
    • F02C3/04F02C3/22F02C7/08F02C7/224F05D2220/60F05D2220/76F23C13/02F23L15/04F23R3/40Y02E20/348
    • A system comprising a compressor (10) having an inlet stream (25) and an outlet stream (26), a pre-heater (12) having a process inlet stream (29) and a process outlet stream (31), a catalytic combustor (13) having an inlet stream (32) and an outlet stream (33) and containing an catalyst, and a turbine (14) having an inlet stream (34) and an outlet stream (35), wherein, the outlet stream (26) of the compressor(10) is connected to the process inlet stream (29) of the pre-heater (12), the process outlet stream (31) of the pre-heater (12) is connected to the inlet stream (32) of the catalytic combustor (13). The outlet stream (33) of the catalytic combustor (13) is connected to the inlet stream (34) of the turbine (14). During operation of the system, the inlet stream (25) of the compressor (10) has a substantially constant and low concentration of fuel.
    • 一种包括具有入口流(25)和出口流(26)的压缩机(10)的系统,具有工艺入口流(29)和工艺出口流(31)的预热器(12),催化燃烧器 (13)具有入口流(32)和出口流(33)并且包含催化剂,以及具有入口流(34)和出口流(35)的涡轮机(14),其中出口流 压缩机(10)的过程出口流(31)连接到预热器(12)的过程进口流(29),预热器(12)的过程出口流(31)连接到入口流(32) 的催化燃烧器(13)。 催化燃烧器(13)的出口流(33)连接到涡轮(14)的入口流(34)。 在系统操作期间,压缩机(10)的入口流(25)具有基本恒定且低浓度的燃料。