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    • 2. 发明授权
    • Method for regeneration of moist powder adsorption agents
    • 湿粉吸附剂再生方法
    • US4535065A
    • 1985-08-13
    • US421111
    • 1982-09-20
    • Juergen KleinPeter Schulz
    • Juergen KleinPeter Schulz
    • B01J8/24B01J20/34C01B31/08C02F1/28C01B31/10C10J3/54
    • C01B31/088B01J20/20B01J20/3416B01J20/3458B01J20/3483C01B31/087C02F1/283B01J2220/56
    • In a method for regeneration of moist powder adsorption agent, the moist-charged adsorption agent is first fed into the lower area of a fluidized bed which is provided with an aeration and heat-carrying material; the agent then is fed upwardly through the heat-carrying material while being simultaneously dried, and then the agent is withdrawn together with the vortex gas from the fluidized bed. The agent is separated from the vortex gas in a successively switched separator, and is then fed to a further fluidized bed which is provided with a further aeration and heat-carrying material. The agent is fed in that further bed upwardly through the further heat-carrying material and is simultaneously regenerated. The agent is then discharged together with the further vortex gas from the further fluidized bed. The vortex gases which are withdrawn can be reused as mixing gases during the vortex gas generation. The adsorption agent can be mixed with a sludge, for example, from a sewage treatment plant, which, if necessary, is gasified together with the substances of the adsorption agents in the regeneration step.
    • 在湿粉末吸附剂的再生方法中,首先将加湿吸附剂进料到设有曝气和承载材料的流化床的下部区域中, 然后将试剂向上通过载热材料同时干燥,然后将试剂与来自流化床的涡流气体一起取出。 该试剂在连续切换的分离器中与涡流气体分离,然后进料到另外的流化床中,该床具有进一步的曝气和加热材料。 将该试剂在该另外的床中通过另外的载热材料向上进料,并同时再生。 然后将试剂与来自另外的流化床的另外的涡流一起排出。 在涡流生成过程中,被排出的涡流可以作为混合气体重新使用。 吸附剂可以与例如污水处理厂的污泥混合,如果需要,在再生步骤中将其与吸附剂的物质一起气化。
    • 9. 发明授权
    • Procedure for the recovery and/or cleaning of carbon formed as a result
of combustion processes
    • 由于燃烧过程而形成的碳的回收和/或清洁的程序
    • US5723717A
    • 1998-03-03
    • US382608
    • 1995-02-02
    • Gunter H. Kiss
    • Gunter H. Kiss
    • B01D53/00C01B31/08C10B53/00C10J3/84C10B47/00
    • C01B31/087B01D53/005C10B53/00C10J3/84
    • A procedure for the recovery and/or cleaning of carbon formed as a result of thermal processes. This carbon is present with supernatant C in equilibrium with CO.sub.2 and CO (Boudouard equilibrium) after being transformed into CO.sub.2 with oxygen in a synthesis gas at an elevated temperature. In so doing, the synthesis gas is brought to a temperature higher than 800.degree. and then, using H.sub.2 O, abruptly cooled to a temperature less than 100.degree. C., the carbon-water-dispersion is also used as an adsorption agent and the contaminants and residue are bound together in the waste gases, the carbon-water-dispersion is concentrated, the carbon sludge forming at the elevated temperature, preferably greater than 1200.degree. C., is dried. During the drying process the contaminants or contaminant components are vaporized from the carbon sludge and then condensed and the dried carbon is returned to the initial combustion process.
    • 由于热处理而形成的碳的回收和/或清洁的程序。 在高温下在合成气中用氧气转化为CO 2后,该碳存在与CO 2和CO(Boudouard平衡)平衡的上清液C. 这样做使合成气达到高于800°的温度,然后使用H 2 O突然冷却至低于100℃的温度,碳水分散体也用作吸附剂,污染物 并且残留物在废气中结合在一起,碳水分散体被浓缩,在升高的温度,优选大于1200℃下形成的碳污泥被干燥。 在干燥过程中,污染物或污染物成分从碳污泥蒸发,然后冷凝,并将干燥的碳返回到初始燃烧过程。