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    • 32. 发明授权
    • Process and apparatus for cyclonic combustion
    • 用于气旋燃烧的工艺和设备
    • US5462430A
    • 1995-10-31
    • US011670
    • 1993-01-29
    • Mark J. Khinkis
    • Mark J. Khinkis
    • F23C3/00F23C6/04F23M5/08F23M3/14F23C9/06
    • F23C6/045F23C3/006F23M5/08F23C2201/102
    • A process and apparatus for cyclonic combustion with ultra-low pollutant emissions and high efficiency wherein a fuel and primary combustion air mixture is tangentially injected into a reducing primary combustion zone of a cyclonic combustor. The primary combustion air is injected into the reducing primary combustion zone in an amount equal to between about 30% and about 90% of a stoichiometric requirement for complete combustion of the fuel. Secondary combustion air is tangentially injected into an oxidizing secondary combustion zone of the cyclonic combustor, in an amount equal to between about 10% and about 90% of the stoichiometric requirement for complete combustion of the fuel. Primary combustion products from the reducing primary combustion zone are mixed with the tangentially injected secondary air for completing combustion within the oxidizing secondary combustion zone. Combustion chamber walls which define the reducing primary combustion zone and the oxidizing secondary combustion zone are water-cooled.
    • 一种用于具有超低污染物排放和高效率的气旋燃烧的方法和装置,其中将燃料和初级燃烧空气混合物切向注入到气旋燃烧器的还原性初级燃烧区中。 一次燃烧空气以等于燃料完全燃烧的化学计量要求的约30%至约90%的量被注入到还原一次燃烧区中。 二次燃烧空气以等于燃料完全燃烧的化学计量要求的约10%至约90%的量切向注入到气旋燃烧器的氧化二次燃烧区域中。 来自还原性初级燃烧区的初级燃烧产物与切向注入的二次空气混合,以在氧化二次燃烧区内完成燃烧。 限定还原一次燃烧区和氧化二次燃烧区的燃烧室壁是水冷的。
    • 35. 发明授权
    • Fossil fuel-fired boilerless steamer
    • 化石燃油无锅炉
    • US06467402B1
    • 2002-10-22
    • US09834230
    • 2001-04-12
    • Mark J. KhinkisJames T. ColeDonald E. FritzscheM. Frank G. Johnson
    • Mark J. KhinkisJames T. ColeDonald E. FritzscheM. Frank G. Johnson
    • A47J3712
    • A47J36/30
    • A fossil fuel-fired apparatus for steaming food having at least one housing wall forming a housing, a steam chamber disposed within the housing and forming an annular space between the steam chamber and the housing wall, and at least one fossil fuel burner disposed beneath the bottom portion of the steam chamber and oriented to produce steam from water in a bottom portion of the steam chamber. Disposed within the annular space are guides for directing the hot products of combustion generated by the burners along the exterior wall surface of the steam chamber, thereby maintaining the temperature of the steam chamber walls above the temperature of the saturated steam and preventing condensation of the steam in the steam chamber.
    • 一种用于蒸煮食物的矿物燃料燃烧设备,其具有形成壳体的至少一个壳体壁,设置在壳体内的蒸汽室,并且在蒸汽室和壳体壁之间形成环形空间,以及至少一个化石燃料燃烧器, 蒸汽室的底部并且被定向以在蒸汽室的底部中的水产生蒸汽。 设置在环形空间内的引导件用于沿着蒸汽室的外壁表面引导由燃烧器产生的燃烧热产物,从而将蒸汽室壁的温度保持在饱和蒸汽的温度以上并防止蒸汽冷凝 在蒸汽室。
    • 36. 发明授权
    • Combustion process
    • 燃烧过程
    • US5163374A
    • 1992-11-17
    • US750197
    • 1991-08-27
    • Amirali G. RehmatMark J. Khinkis
    • Amirali G. RehmatMark J. Khinkis
    • F23C6/04F23C10/08F23C10/26
    • F23C10/26F23C10/08F23C6/04
    • A process for combustion of hydrocarbonaceous materials containing high levels of sulfur, fuel-bound nitrogen and low levels of ash which inhibits the emissions of oxides of nitrogen and sulfur, reduces solid waste disposal, and produces useable by-products. In the first step of the process, the hydrocarbonaceous material is burned in a fluidized bed into which a calcium based sorbent is introduced, producing a mixture of gaseous products of combustion and particulate matter, ash and calcium containing solids. In a second step of the process, the mixture of gaseous products of combustion and particulate matter is completely burned in a cyclonic combustion reactor. In a third step of the process, the ash and calcium-containing solids generated in the fluidized bed are withdrawn from the fluidized bed, cooled and contacted with steam in a regenerator producing calcium hydroxide, ash and unspent sorbent which are recycled to the fluidized bed.
    • 含有高含量硫,燃料结合氮和低水平灰分的含烃材料的燃烧过程,其抑制氮和硫的氧化物的排放,减少固体废物处理,并产生可用的副产物。 在该方法的第一步中,烃类物质在流化床中燃烧,其中引入钙基吸附剂,产生燃烧气体产物和颗粒物质,灰分和含钙固体的混合物。 在该方法的第二步骤中,燃烧和颗粒物质的气态产物的混合物在旋风燃烧反应器中完全燃烧。 在该方法的第三步骤中,在流化床中产生的灰分和含钙固体从流化床中排出,冷却并在再生器中与蒸汽接触,产生氢氧化钙,灰分和未使用的吸附剂,再循环到流化床 。
    • 37. 发明授权
    • Ultra-low pollutant emission combustion method and apparatus
    • 超低污染物排放燃烧方法和装置
    • US5158445A
    • 1992-10-27
    • US682425
    • 1991-04-08
    • Mark J. Khinkis
    • Mark J. Khinkis
    • F23C3/00F23C6/04F23C7/02F23R3/34
    • F23C6/047F23C3/006F23C7/02F23R3/346F23C2201/102
    • A method and apparatus for ultra-low pollutant emission combustion of fossil fuel is disclosed in which a first portion of fuel to be combusted is introduced into a primary combustion chamber together with primary combustion air, producing either a reducing or oxidizing combustion zone and a portion of water having a heat capacity equivalent to the heat capacity of a portion of primary combustion air. The first portion of fuel is combusted in the primary combustion chamber and the combustion products derived therefrom pass through an orifice into a secondary combustion chamber. Also introduced into the secondary combustion chamber is a second portion of fuel and secondary combustion air in an amount sufficient to complete combustion of the total amount of fuel in the apparatus. In addition, water is introduced into the secondary combustion chamber in an amount having a heat capacity equivalent to an amount of secondary combustion air. The products of combustion from the secondary combustion chamber are passed through an orifice into a dilution chamber into which dilution air is introduced, producing ultra-low pollutant emissions vitiated air. The vitiated air is subsequently discharged from the dilution chamber.
    • 公开了一种用于化石燃料的超低污染物排放燃烧的方法和装置,其中要燃烧的燃料的第一部分与一次燃烧空气一起被引入主燃烧室,产生还原或氧化燃烧区和部分 的水的热容量相当于一次燃烧空气的一部分的热容量。 燃料的第一部分在主燃烧室中燃烧,并且由此产生的燃烧产物通过孔进入二次燃烧室。 还引入二次燃烧室中的燃料和二次燃烧空气的第二部分的量足以完全燃烧装置中燃料的总量。 此外,以与二次燃烧空气量相当的热容量的量将水引入二次燃烧室。 来自二次燃烧室的燃烧产物通过孔口进入稀释空气进入稀释室,产生超低污染物排放的空气。 随后将稀释的空气从稀释室排出。
    • 38. 发明授权
    • Ultra-low pollutant emission combustion process and apparatus
    • 超低污染物排放燃烧过程及装置
    • US5013236A
    • 1991-05-07
    • US354837
    • 1989-05-22
    • Mark J. Khinkis
    • Mark J. Khinkis
    • F23C3/00F23C6/04F23C7/02F23R3/34
    • F23R3/346F23C3/006F23C6/047F23C7/02F23C2201/102
    • An apparatus and method for ultra-low pollutant emission combustion of fossil fuel wherein an elongated cyclonic primary combustion chamber has a cross-sectional area about 4 to about 30 percent that of an elongated cyclonic secondary combustion chamber and a volume about 1 to about 20 percent the combined primary and secondary combustion chamber volume. A first fuel portion of about 1 percent to about 20 percent of the total fuel and primary combustion air in an amount selected from about 40 to about 90 percent and about 140 percent to about 230 percent of the stoichiometric requirement for complete combustion of the first fuel portion is introduced into the primary combustion chamber. A second fuel portion of about 80 to about 99 percent of the total fuel is introduced into the secondary combustion chamber with secondary combustion air in an amount of about 150 percent to about 260 percent of the stoichiometric requirement for complete combustion of the fuel. In preferred embodiments cyclonic flow is maintained through the combustor.
    • 用于化石燃料的超低污染物排放燃烧的装置和方法,其中细长的旋风主燃烧室的横截面积为细长旋风二次燃烧室的横截面积约4至约30%,体积约为1至约20% 主燃烧室和二次燃烧室的组合。 总燃料和初级燃烧空气的约1%至约20%的第一燃料部分选自第一燃料完全燃烧的化学计量要求的约40至约90%和约140%至约230% 部分被引入主燃烧室。 总燃料的约80%至约99%的第二燃料部分被引入二次燃烧室中,二次燃烧空气的量为燃料完全燃烧的化学计量要求的约150%至约260%。 在优选实施例中,通过燃烧器保持旋风流。
    • 39. 发明授权
    • Oxygen enriched continuous combustion in a regenerative furance
    • 富氧连续燃烧在再生能源中
    • US4909727A
    • 1990-03-20
    • US159219
    • 1988-02-23
    • Mark J. Khinkis
    • Mark J. Khinkis
    • F23C6/04F23L7/00F23L15/02
    • F23L7/007C03B5/2353C03B5/237F23C6/042F23L15/02Y02E20/344Y02E20/348Y02P40/535Y02P40/55Y02P40/57
    • A process and apparatus for oxygen-rich combustion wherein a first portion of about 5 to about 40 percent of the total fuel to be cracked and combusted is introduced to a cracking chamber where it is combusted and cracked at a temperature below about 2200.degree. F. to produce a cracked products mixture. Oxygen-rich gas of greater than about 30 volume percent oxygen is introduced to the cracking chamber in about 5 to about 50 percent of the stoichiometric requirement for complete combustion of the first portion of fuel introduced to that chamber. Cracked products mixture, a second remaining portion of fresh fuel and oxidizer having sufficient oxygen for substantially complete combustion of the combustible portion of the cracked porducts mixture and the fresh fuel are introduced to a combustion chamber wherein the combustible portion of the cracked products mixture and the fresh fuel are combusted. The process and apparatus provide continuous operation of a fuel cracking chamber when used with regenerative furnaces, such as in the glass making industry.
    • 一种用于富氧燃烧的方法和装置,其中待裂化和燃烧的总燃料的约5%至约40%的第一部分被引入裂解室,在其中在低于约2200°F的温度下燃烧和裂化。 产生裂纹产物混合物。 大于约30体积%氧气的富氧气体以引入到该室的第一部分燃料的完全燃烧的化学计量要求的约5至约50%被引入裂解室。 裂化产物混合物,剩余部分的新鲜燃料和氧化剂具有足够的氧气,用于基本上完全燃烧裂化产物混合物和新鲜燃料的可燃部分,其中可燃部分的裂化产物混合物和 新鲜燃料燃烧。 当与再生炉一起使用时,例如在玻璃制造工业中,该方法和装置提供燃料裂解室的连续操作。