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    • 23. 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。
    • 30. 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。