会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 22. 发明授权
    • Method for reducing nitrogen oxides in flue gas
    • 减少烟气中氮氧化物的方法
    • US4950473A
    • 1990-08-21
    • US263470
    • 1988-10-27
    • Claus FlockenhausManfred GalowKlaus MerkelHans-Eugen BuhlerHartmut Kainer
    • Claus FlockenhausManfred GalowKlaus MerkelHans-Eugen BuhlerHartmut Kainer
    • B01D53/56F23J15/00
    • B01D53/56F23J15/003F23J2215/10
    • Apparatus and method for reducing nitrogen oxides in flue gas within a flue gas duct includes a number of distributor tubes for the injection of a reducing agent into the flue gas within the duct. Each distributor tube includes a control valve to be able to set an appropriate injection of the reducing agent to respond to different concentrations of the nitrogen oxides within the flue gas over the cross section of the flue gas duct. Each distributor tube comprises at least two parallel distributor tube segments which extend from opposite sides of the flue gas duct to the center of the flue gas duct. The two parallel distribution tube segments include a plurality of openings along the lengths thereof to supply the reducing agent generally evenly throughout their aligned portions of the cross section. The control valve is employed to adjust the reducing agent to provide the proper quantity thereof which corresponds to the particular concentration of nitrogen oxides within the flue gas at each corresponding portion of the entire cross section.
    • 用于还原烟气管道内的烟气中的氮氧化物的装置和方法包括用于将还原剂注入管道内的烟道气中的多个分配管。 每个分配器管包括一个控制阀,以便能够设定合适的还原剂的注入,以响应烟道气中的氮氧化物在烟道气管道的横截面上的不同浓度。 每个分配器管包括至少两个平行的分配器管段,其从烟道气管道的相对侧延伸到烟气管道的中心。 两个平行的分配管段包括沿其长度的多个开口,以在整个横截面的整个对齐部分中大致均匀地供给还原剂。 使用控制阀来调节还原剂以提供适当的量,这对应于在整个横截面的每个对应部分处的烟道气中氮氧化物的特定浓度。
    • 24. 发明授权
    • Method of and apparatus for catalytic conversion of gases
    • 催化转化气体的方法和装置
    • US4407974A
    • 1983-10-04
    • US371265
    • 1982-04-23
    • Claus FlockenhausErich HacklerWerner Lommerzheim
    • Claus FlockenhausErich HacklerWerner Lommerzheim
    • B01J8/18C07C1/00C07C1/04C07C9/04C07C67/00C10K3/04
    • C07C1/042B01J8/1836C07C1/048Y02P20/131
    • A method of catalytic conversion of feed gases, particularly of a low-sulphur gas mixture rich in carbon monoxide and hydrogen, into a product gas mixture containing methane and/or higher hydrocarbons under high pressure includes the step of removing heat of reaction from the catalytic conversion from a reaction zone by feeding both water and steam to form a cooling medium through a pipe coil in the reaction zone. This forms superheated steam in the pipe coil and the superheated steam is then converted into another form of energy, for example in a turbo-generator. Preferably the reaction zone is a fluidized bed. For carrying out this method a reactor is used, which is preferably a fluidized bed reactor and in this reactor the piping system forming the superheater is disposed in the lower part of the reaction zone. The superheater is connected to a feedwater line and to a steam inlet line and a steam turbine is connected to a steam output line leading from the superheater.
    • 将含有一氧化碳和氢的低硫气体混合物的进料气体特别是在高压下含有甲烷和/或高级烃的产物气体混合物的催化转化方法包括从催化剂中除去反应热的步骤 通过进料水和蒸汽从反应区转化成通过反应区中的管线形成冷却介质。 这在管线圈中形成过热蒸汽,然后将过热蒸汽转化成另一形式的能量,例如在涡轮发电机中。 优选地,反应区是流化床。 为了实施该方法,使用反应器,其优选为流化床反应器,并且在该反应器中,形成过热器的管道系统设置在反应区的下部。 过热器连接到给水管线和蒸汽入口管线,蒸汽轮机连接到从过热器引出的蒸汽输出管线。
    • 29. 发明授权
    • Apparatus for fluid catalytic conversion of gases
    • 用于流体催化转化气体的装置
    • US4258006A
    • 1981-03-24
    • US59522
    • 1979-07-23
    • Claus FlockenhausErich HacklerWerner Lommerzheim
    • Claus FlockenhausErich HacklerWerner Lommerzheim
    • B01J8/18C07C1/00C07C1/04C07C9/04C07C67/00C10K3/04B01J8/24
    • C07C1/042B01J8/1836C07C1/048Y02P20/131
    • A method of catalytic conversion of feed gases, particularly of a low-sulphur gas mixture rich in carbon monoxide and hydrogen, into a product gas mixture containing methane and/or higher hydrocarbons under high pressure includes the step of removing heat of reaction from the catalytic conversion from a reaction zone by feeding both water and steam to form a cooling medium through a pipe coil in the reaction zone. This forms superheated steam in the pipe coil and the superheated steam is then converted into another form of energy, for example in a turbo-generator. Preferably the reaction zone is a fluidized bed. The apparatus for carrying out this method comprises a reactor, which is preferably a fluidized bed reactor and in this reactor the piping system forming the superheater is disposed in the lower part of the reaction zone. The superheater is connected to a feedwater line and to a steam inlet line and a steam turbine is connected to a steam output line leading from the superheater.
    • 将含有一氧化碳和氢的低硫气体混合物的进料气体特别是在高压下含有甲烷和/或高级烃的产物气体混合物的催化转化方法包括从催化剂中除去反应热的步骤 通过进料水和蒸汽从反应区转化成通过反应区中的管线形成冷却介质。 这在管线圈中形成过热蒸汽,然后将过热蒸汽转化成另一形式的能量,例如在涡轮发电机中。 优选地,反应区是流化床。 用于实施该方法的装置包括反应器,其优选为流化床反应器,并且在该反应器中,形成过热器的管道系统设置在反应区的下部。 过热器连接到给水管线和蒸汽入口管线,蒸汽轮机连接到从过热器引出的蒸汽输出管线。
    • 30. 发明授权
    • Process and installation for drying and heating coal
    • 干燥加热煤的加工和安装
    • US4178150A
    • 1979-12-11
    • US863795
    • 1977-12-23
    • Claus FlockenhausHorst FachGunter GabrielManfred GalowJoachim Meckel
    • Claus FlockenhausHorst FachGunter GabrielManfred GalowJoachim Meckel
    • C10B57/10C10B57/08C10F5/00C10L9/08F26B17/10F27B15/00
    • C10B57/08
    • Coal is passed in a two-stage process through a drying and heating zone. The coal coming from the drying zone is separated from the heat carrier gas which is then passed into the atmosphere after going through an electrodust separator. The dried coal is delivered into the heating zone. The hot gas for the heating zone is furnished by a combustion device. The exhaust gas from the heating zone is separated from the heated coal which is recovered while the exhaust gas is passed back into the drying zone. Part of the hot combustion gas coming from the combustion chamber is branched off and passed into the exhaust gas coming out of the drying zone either directly behind the drying zone or behind the separator for separating the dried coal from the exhaust gas. The temperature of the exhaust gas from the drying zone is thus prevented from sinking below the sulfuric acid dewpoint or water vapor dewpoint which might result in corrosive damage to the apparatus, particularly to the electrodust separator.
    • 煤通过干燥和加热区在两阶段过程中通过。 来自干燥区的煤与热载体分离,然后通过电极分离器后将其通入大气中。 干燥的煤被输送到加热区。 加热区的热气由燃烧装置提供。 来自加热区域的废气与废气再次返回到干燥区域中被回收的加热煤分离。 来自燃烧室的热燃烧气体的一部分被分支并且从干燥区域直接排出干燥区域的废气或分离器之后的废气中,从而将干燥的煤与废气分离。 因此,防止来自干燥区域的废气的温度低于硫酸露点或水蒸气露点,这可能导致对设备,特别是电极分离器的腐蚀性损坏。