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Production of carbon, a component of hydrocarbon fuels and raw materials for chemical industry from RAW RUBBER-industrial and domestic waste

机译:用RAW RUBBER-工业和家庭废物生产碳,碳氢化合物的一种成分和化学工业的原料

摘要

1. Production of carbon, hydrocarbon fuel components and raw materials for the chemical industry from the raw material - rubber-containing industrial and household waste, comprising a grinding of raw materials, the separation of rubber crumb from other ingredients, feeding the reactor with RK PIC RK thermolysis in a vertical flow of solvent - hydrocarbon mixture, alkylaromatics comprising, at a temperature and pressure close to critical 320-350 ° C and 40-60 MPa circulating through the moving and fluidized bed RK TU, characterized in that the thermolysis It is carried out in a reactor at a weight ratio of organic solvent to the waste is less than 1.0, wherein the circulation of the organic solvent is selected so that all products obtained in the thermolysis of rubber, completely carried out of the reactor in the stream with a solvent, thus the solvent used simultaneously awaiting agent and the coolant, and reaktsii.2 scavenger from the reactor products. Manufacture according to claim 1, characterized in that the TU separated from gaseous reaction products in cyclones detached at a pressure of 0.3-0.8 MPa lower due to restricting unit disposed on the conduit between the reactor and cyclone, which regulate the pressure in the reactor at 4.0 ± 0.1 MPa.3. Manufacture according to claim 1, characterized in that, to reduce the temperature of the circulating coolant in direct contact with the RK and exclude compaction and coking of heavy hydrocarbons in thermolysis products, the circulating coolant is heated twice in the furnace and part of the heat is transferred directly to PIC RK and part - through the coil surface and through the wall
机译:1.从原材料(含橡胶的工业废料和生活垃圾)中生产化学工业用碳,碳氢燃料成分和原材料,包括研磨原材料,将橡胶屑与其他成分分离,向反应器供入RK PIC RK在溶剂-烃混合物的垂直流中热解的烷基芳烃,在接近临界320-350°C和40-60 MPa的温度和压力下通过移动和流化床RK TU循环,其特征在于热解在反应器中以有机溶剂与废物的重量比小于1.0进行反应,其中选择有机溶剂的循环,以使在橡胶热解中获得的所有产物在物流中完全从反应器中带出用溶剂,因此同时使用的溶剂是等待剂和冷却剂,以及从反应器产物中回收的Reaktsii.2清除剂。 2.根据权利要求1所述的制造方法,其特征在于,由于在反应器和旋风分离器之间的导管上设置有限制单元,所述旋风分离器在气旋分离器中从气态反应产物中分离出来的TU降低了0.3-0.8MPa的压力,所述限制单元调节了4.0±0.1兆帕3。 2.根据权利要求1所述的制造方法,其特征在于,为了降低与RK直接接触的循环冷却剂的温度并排除热解产物中重烃的压实和结焦,循环冷却剂在炉中加热两次,部分热量被加热。直接传递到PIC RK和零件-通过线圈表面和墙壁

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