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Process and equipment for gasifying carbonaceous wastes, if appropriate with addition of toxic and highly toxic wastes, to give synthesis gas

机译:气化含碳废物的方法和设备,必要时还添加有毒和剧毒废物,以产生合成气

摘要

In a process for gasifying carbonaceous wastes, biomasses and also hazardous wastes, if appropriate with addition of toxic and highly toxic wastes, to give synthesis gas, the substances to be gasified are, together with a crude gas part stream recycled from an iron bath reactor, subjected to a pyrolysis at temperatures from about 400 to 1100 DEG C in a fluidised-bed reactor. Pyrolysis coke comminuted to about 0 to 3 mm and, if necessary, further heat generator is added to the pyrolysis gas containing the fine pyrolysis coke and the mixture is passed into an iron bath reactor, which is fed with oxygen as oxidising agent. Toxic or highly toxic substances can be charged to the fluidised-bed pyrolysis or, if they cannot be processed therein, can be added to the gas stream fed to the iron bath reactor. The equipment for carrying out the process consists of a combination of a fluidised-bed reactor 10 with an iron bath reactor 71. The melting vessel contains a plinth 75 in which the nozzles for introducing pyrolysis gas, oxygen and loaded solids are arranged at an angle relative to one another. IMAGE
机译:在气化含碳废物,生物质以及有害废物(如果需要的话)中添加有毒和高毒废物的气化过程,以生成合成气时,要气化的物质与从铁浴反应器中回收的原油分流一起在流化床反应器中于约400-1100℃下进行热解。将热解焦炭粉碎至约0至3毫米,如有必要,可将进一步的生热剂添加到含有细热解焦炭的热解气体中,并将​​混合物通入铁浴反应器中,并向其中供入氧气作为氧化剂。可以将有毒或剧毒物质加入流化床热解炉中,或者,如果不能在其中进行处理,则可以将其加入到送入铁浴反应器的气流中。进行该过程的设备包括流化床反应器10和铁浴反应器71的组合。熔融容器包含底座75,在底座75中以一定角度布置用于引入热解气体,氧气和负载固体的喷嘴。相对于彼此。 <图像>

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