Fuel dilution for reducing NOx production
    151.
    发明申请
    Fuel dilution for reducing NOx production 审中-公开
    用于减少NOx生产的燃料稀释

    公开(公告)号:US20070048679A1

    公开(公告)日:2007-03-01

    申请号:US11546787

    申请日:2006-10-12

    Abstract: A combustion device and combustion method for mixing a fuel and a fluid to form a diluted fuel mixture and passing the diluted fuel mixture through a nozzle. The nozzle comprises a nozzle body having an inlet face, an outlet face, and an inlet flow axis passing through the inlet face and the outlet face, and one or more slots extending through the nozzle body from the inlet face to the outlet face, each slot having a slot axis.

    Abstract translation: 一种用于混合燃料和流体以形成稀释燃料混合物并使稀释的燃料混合物通过喷嘴的燃烧装置和燃烧方法。 喷嘴包括具有入口面,出口面和通过入口面和出口面的入口流轴的喷嘴体,以及从入口面延伸到出口面的一个或多个狭槽,每个槽从入口面延伸到出口面 槽具有槽轴。

    Combined fluidized bed and pulverized coal combustion method
    152.
    发明授权
    Combined fluidized bed and pulverized coal combustion method 失效
    联合流化床和粉煤燃烧法

    公开(公告)号:US07004089B2

    公开(公告)日:2006-02-28

    申请号:US10476684

    申请日:2001-05-11

    CPC classification number: F23C6/047 F23C10/002 F23C2201/101 F23C2201/301

    Abstract: The invention relates to a combined fluidized bed and pulverized coal combustion method and system. In the method, fluidizing air (4) is injected into a fluidized bed (2) situated in the bottom portion of the combustion chamber (3). Into the combustion chamber, to above the fluidized bed (2), is fed a mixture of pulverized coal and a carrier gas from a second set of fuel feed means (6) at a mass flow rate which is higher or at least substantially equal to the upper ignition limit of the mixture, and the mixture of the pulverized coal and the carrier gas at least by the fluidizing air (4), and at least a fraction of the fuel fed via the second set of fuel feed means (6) is combusted above the fluidized bed (2).

    Abstract translation: 本发明涉及一种组合流化床和粉煤燃烧方法及系统。 在该方法中,将流化空气(4)注入位于燃烧室(3)底部的流化床(2)中。 在燃烧室内到达流化床(2)的上方,以来自第二组燃料供给装置(6)的粉煤和载气的混合物以更高或至少基本上等于 至少通过流化空气(4),混合物的上限点火极限和粉煤与载体气体的混合物,以及经由第二组燃料供给装置(6)供给的燃料的至少一部分是 在流化床(2)上方燃烧。

    Method for the combined reduction of nitrogen oxide and sulfur dioxide concentrations in the furnace region of boilers
    154.
    发明授权
    Method for the combined reduction of nitrogen oxide and sulfur dioxide concentrations in the furnace region of boilers 失效
    锅炉炉区氮氧化物和二氧化硫浓度综合降低的方法

    公开(公告)号:US06722295B2

    公开(公告)日:2004-04-20

    申请号:US09964853

    申请日:2001-09-28

    Applicant: Bert Zauderer

    Inventor: Bert Zauderer

    Abstract: A method for the combined reduction of sulfur dioxide, SO2, and nitrogen oxides, NOx, in the gas stream of a furnace from the combustion of fossil fuels is disclosed. In a narrow gas temperature zone in a furnace, NOx is converted to nitrogen by reaction with a reducing agent such as urea or ammonia with negligible residual ammonia and other reaction pollutants. In about this same temperature zone, SO2 will react with calcium oxide particles, derived from the calcination of lime, Ca(OH)2, or limestone, CaCO3, to form CaSO4 particles. A wide size distribution of aqueous droplets, containing dispersed lime or very fine limestone particles and dissolved urea or ammonia, is injected at the outer edge of the furnace gas zone at which the SO2 and NOx reduction reaction are effective. The key element in this invention is that the aqueous droplet size distribution is optimized for the specific furnace dimension while the concentration of the reactants, urea or ammonia and lime or very fine limestone, is optimized for optimum reaction rates. Special injectors produce the different size droplets that vaporize throughout said gas zone, thereby distributing said lime or limestone particles and urea or ammonia gas molecules exclusively throughout the combustion gas zone being treated. Also disclosed is a system to produce said aqueous mixture and effectively accomplish this injection. This method can be combined with other NOx and SO2 reduction processes to sharply reduce overall NOx and SO2 emissions from the combustion gas effluent.

    Abstract translation: 公开了一种从化石燃料燃烧中将炉子气流中的二氧化硫,二氧化硫和氮氧化物,NOx组合减少的方法。 在炉内的窄气体温度区域,通过与还原剂如尿素或氨反应,将NOx转化为氮气,残余氨和其它反应污染物可忽略不计。 在这个相同的温度区内,SO2会与氧化钙颗粒发生反应,这些氧化钙颗粒来源于煅烧石灰,Ca(OH)2或石灰石CaCO3,形成CaSO 4颗粒。 在SO2和NOx还原反应有效的炉气区的外边缘处注入含有分散的石灰或非常细的石灰石颗粒和溶解的尿素或氨的水滴的大尺寸分布。 本发明的关键要素是针对特定的炉子尺寸优化了水滴尺寸分布,同时针对最佳反应速率优化了反应物,尿素或氨和石灰或非常细的石灰石的浓度。 特殊注射器产生在所有气体区域内蒸发的不同大小的液滴,从而将所述石灰或石灰石颗粒和尿素或氨气分子专门分布在被处理的整个燃烧气体区域。 还公开了一种制备所述含水混合物并有效地实现该注入的系统。 这种方法可以与其他NOx和SO2还原过程相结合,从而大大降低来自燃烧气体流出物的总体NOx和SO2排放。

    Formation of a stable wax slurry from a Fischer-Tropsch reactor effluent
    156.
    发明授权
    Formation of a stable wax slurry from a Fischer-Tropsch reactor effluent 失效
    从费 - 托反应器流出物形成稳定的蜡浆料

    公开(公告)号:US06313361B1

    公开(公告)日:2001-11-06

    申请号:US09135625

    申请日:1998-08-18

    Abstract: A process is provided for treating a liquid effluent from a gas to liquid conversion reactor. A synthesis gas is initially converted to a liquid hydrocarbon phase in the gas to liquid conversion reactor. The liquid hydrocarbon phase includes a heavier liquid paraffinic wax compound and a lighter liquid paraffinic compound. The liquid hydrocarbon phase is discharged from the gas to liquid conversion reactor in a reactor effluent and an abrasive solid particle medium is entrained in the reactor effluent to form a fluidizable mixture. The reactor effluent is conveyed past a heat transfer surface which is cooler than the reactor effluent. The fluidizable mixture is contacted with the heat transfer surface and the liquid hydrocarbon phase is cooled to a temperature below the melting point of the heavier liquid paraffinic wax compound. Consequently, the heavier liquid paraffinic wax compound is converted to a plurality of unconsolidated solid wax particles. A slurry is formed from the plurality of unconsolidated solid wax particles and the remaining lighter liquid paraffinic compound.

    Abstract translation: 提供了一种处理从气体到液体转化反应器的液体流出物的方法。 合成气体最初在气体/液体转化反应器中转化为液态烃相。 液体烃相包括较重的液体石蜡蜡化合物和较轻的液体石蜡化合物。 液体烃相在反应器流出物中从气体到液体转化反应器排出,并将磨料固体颗粒介质夹带在反应器流出物中以形成可流化的混合物。 反应器流出物被输送通过比反应器流出物更冷的传热表面。 可流化的混合物与传热表面接触,液态烃相被冷却至低于较重液体石蜡蜡化合物的熔点的温度。 因此,较重的液体石蜡蜡化合物转化为多种未固结的固体蜡颗粒。 从多个未固结的固体蜡颗粒和剩余的较轻的液体石蜡化合物形成浆料。

    Method and apparatus for NOx reduction in flue gases
    157.
    发明授权
    Method and apparatus for NOx reduction in flue gases 有权
    烟气中NOx还原的方法和装置

    公开(公告)号:US06258336B1

    公开(公告)日:2001-07-10

    申请号:US09276910

    申请日:1999-03-26

    Abstract: In a furnace having a primary combustion zone for combustion of a fuel and oxidant, an in-furnace method for reducing nitrogen oxides in combustion products generated in the primary combustion zone in which at least one fluid fuel selected from the group consisting of natural gas, hydrogen, CxHy compounds, CxHyOz compounds and mixtures thereof in an amount in a range of about 2.0% to about 25% of a total heat input to the furnace and at least one nitrogenous compound selected from the group consisting of ammonia, amines, urea, cyanuric acid and mixtures thereof are injected into the furnace downstream of the primary combustion zone, forming an overall fuel-lean NOx-reduction zone.

    Abstract translation: 在具有用于燃烧和氧化剂燃烧的初级燃烧区的炉子中,用于还原在主燃烧区产生的燃烧产物中的氮氧化物的炉内方法,其中至少一种选自天然气, 氢,C x H y化合物,C x H y O z化合物及其混合物,其量为输入炉内总热量的约2.0%至约25%,以及至少一种选自氨,胺,脲, 将氰尿酸及其混合物注入到主燃烧区下游的炉中,形成总体贫燃氮氧化物还原区。

    Low emission U-fired boiler combustion system
    158.
    发明授权
    Low emission U-fired boiler combustion system 失效
    低排放型燃煤锅炉燃烧系统

    公开(公告)号:US6058855A

    公开(公告)日:2000-05-09

    申请号:US119097

    申请日:1998-07-20

    Abstract: At least one main combustion chamber contains at least one pulverized coal burner. Each pulverized coal burner is operatively arranged for minimizing NO.sub.X production and for maintaining a predetermined operating temperature to liquefy ash within the combustion chamber. The combustion chamber includes a slag drain for removing slag from the combustion chamber. A slag screen is positioned in a generally U-shaped furnace flow pattern. The slag screen is positioned between the combustion chamber and a radiant furnace. The radiant furnace includes a reburning zone for in-furnace No.sub.X reduction. The reburning zone extends between a reburning fuel injection source and at least one overfire air injection port for injecting air.

    Abstract translation: 至少一个主燃烧室包含至少一个粉煤燃烧器。 每个粉煤燃烧器可操作地布置成用于使NO x产生最小化并保持预定的操作温度以使燃烧室内的液化灰。 燃烧室包括用于从燃烧室除去渣的炉渣排出口。 炉渣筛位于大致U形炉流程图中。 炉渣筛位于燃烧室和辐射炉之间。 辐射炉包括用于炉内NoX还原的再燃烧区域。 再燃烧区域在再燃燃料喷射源和至少一个用于喷射空气的过火空气喷射端口之间延伸。

    Combusting a hydrocarbon gas to produce a reformed gas
    160.
    发明授权
    Combusting a hydrocarbon gas to produce a reformed gas 失效
    燃烧碳氢化合物气体以产生重整气体

    公开(公告)号:US5861441A

    公开(公告)日:1999-01-19

    申请号:US800642

    申请日:1997-02-14

    Abstract: A system and process are provided for converting a hydrocarbon gas to a reformed gas containing hydrogen and carbon monoxide. In accordance with a first embodiment, the system includes a primary combustor, compressor and power turbine. The process is practiced by compressing a feed air in the primary compressor to produce a primary air. The primary air is fed with a primary hydrocarbon gas to the primary combustor, producing a reformed gas that drives the primary power turbine. The primary power turbine is linked to the primary compressor, compressing the feed air in an energy self-sufficient manner. In a second embodiment, the system of the first embodiment further includes a secondary combustor, compressor and power turbine. The process is practiced in the same manner as the first embodiment, producing the reformed gas and driving the primary power turbine and compressor. A portion of the primary air is also fed with a secondary hydrocarbon gas to the secondary combustor, producing an off-gas that drives the secondary power turbine and compressor to compress a gas in an energy self-sufficient manner. In a third embodiment, the system is substantially the same as the second embodiment, but reconfigures the compressors and power turbines and further includes an auxiliary secondary power turbine. The process is practiced in the same manner as the first embodiment, producing the reformed gas and driving the primary power turbine and compressor. The off-gas is produced in the same manner as the second embodiment to drive the secondary power turbine, but the secondary power turbine drives an auxiliary primary compressor, compressing the feed air ahead of the primary compressor in an energy self-sufficient manner. The off-gas further drives the auxiliary secondary power turbine to provide additional power for alternate power users.

    Abstract translation: 提供了一种用于将烃气体转化为含有氢气和一氧化碳的重整气体的系统和方法。 根据第一实施例,该系统包括主燃烧器,压缩机和动力涡轮机。 该过程通过压缩主压缩机中的进料空气以产生一次空气来实施。 一次空气向初级燃烧器供给初级烃气体,产生驱动主动力涡轮机的重整气体。 主动力涡轮机连接到主压缩机,以能量自足的方式压缩进料空气。 在第二实施例中,第一实施例的系统还包括二次燃烧器,压缩机和动力涡轮机。 以与第一实施例相同的方式实施该过程,产生重整气体并驱动主动力涡轮机和压缩机。 一次空气的一部分还向次级燃烧器供给次级烃气体,产生驱动次级动力涡轮机和压缩机以能量自足的方式压缩气体的废气。 在第三实施例中,该系统基本上与第二实施例相同,但是重新配置压缩机和动力涡轮机,并且还包括辅助辅助动力涡轮机。 以与第一实施例相同的方式实施该过程,产生重整气体并驱动主动力涡轮机和压缩机。 废气以与第二实施例相同的方式产生以驱动二次动力涡轮机,但是二次动力涡轮机驱动辅助主压缩机,以能量自足的方式压缩主压缩机前方的进料空气。 废气进一步驱动辅助辅助动力涡轮机,为备用电力用户提供额外的电力。

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