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    • 51. 发明授权
    • Apparatus for treating waste materials
    • 废物处理设备
    • US4980029A
    • 1990-12-25
    • US300609
    • 1989-01-23
    • Alfred BolzGunther Boos
    • Alfred BolzGunther Boos
    • C10B47/18C10B53/00C10B57/02C10G1/02
    • C10G1/02C10B47/18C10B53/00C10B57/02Y02P20/129
    • Gaseous, liguid and solid fuels are recovered from carbonaceous organic waste material by treating charges of waste material in several successive stages including preheating, drying and conversion into solid and gaseous phases, all as a result of heating in a common vessel or in two or three successive vessels. The solid phases are thereupon cooled prior to admission into a bin, either in a separate vessel or in the vessel for conversion into solid and gaseous phases. The gaseous phases are treated to separate oil from reaction water, combustible gases and inert gases. The charges are heated from without and are sealed from the atmosphere during all four stages of treatment. Each charge is mixed during heating and the intensity of mixing action, the heating action and/or the pressure in the vessel can be varied during one or more stages.
    • 气体,液体和固体燃料通过在几个连续阶段处理废料的装料从碳质有机废物中回收,包括预热,干燥和转化为固相和气相,这些都是由于在普通容器中加热或在两个或三个 连续的船只。 在固相进入容器之前,在单独的容器中或在容器中冷却,以转化成固相和气相。 处理气相以将油与反应水,可燃气体和惰性气体分离。 在所有四个治疗阶段期间,电荷从没有加热并且与大气密封。 在加热期间混合每个电荷,并且在一个或多个阶段期间可以改变混合作用的强度,加热作用和/或容器中的压力。
    • 52. 发明授权
    • Vacuum pyrolysis of scrap tires
    • 废轮胎的真空热解
    • US4740270A
    • 1988-04-26
    • US876071
    • 1986-06-19
    • Christian Roy
    • Christian Roy
    • C10B1/04C10B53/07C10B57/02C10G1/10C10B53/00C10B57/00
    • C10B53/07C10B1/04C10B57/02C10G1/10Y02P20/143
    • A process for the treatment of used rubber tires by vacuum pyrolysis in a reactor to produce liquid and gaseous hydrocarbons and a solid carbonaceous material is disclosed. According to the invention, the pyrolysis of the tires is carried out at a temperature in the range of about 360.degree. C. to about 415.degree. C., under a sub-atmospheric pressure of less than about 35 mm Hg and such that gases and vapors produced in the reactor have a residence time of the order of a few seconds. The process according to the invention enables one to increase the yield of the liquid hydrocarbons and lower the yields of the gaseous hydrocarbons and solid carbonaceous material, and to thereby produce hydrocarbon oils in substantially maximum yield. These hydrocarbon oils have a high calorific value and are thus suitable for use as heating fuel.
    • 公开了一种在反应器中通过真空热解处理二手橡胶轮胎以制备液体和气态烃和固体含碳材料的方法。 根据本发明,轮胎的热解在约360℃至约415℃的温度范围内,在小于约35mm Hg的亚大气压下进行,并使得气体和 在反应器中产生的蒸气具有几秒的停留时间。 根据本发明的方法使得能够提高液体烃的产率并降低气态烃和固体碳质材料的产率,从而以最大的收率生产烃油。 这些烃油具有高热值,因此适合用作加热燃料。
    • 53. 发明授权
    • Method for carbonizing cold-compacted briquettes
    • 碳化冷压块的方法
    • US4683030A
    • 1987-07-28
    • US719879
    • 1985-04-04
    • Heinrich WeberKurt LorenzHorst Dungs
    • Heinrich WeberKurt LorenzHorst Dungs
    • C10B53/08C10L5/16C10L5/20C10B47/18C10B57/02
    • C10L5/16C10B53/08C10L5/20Y02P20/129
    • Briquettes made from bituminous or sub-bituminous coal or peat are produced by grinding the coal, mixing it with a binder and compacting the mixture. They are then carbonized in a continuous process in a shaft oven. The coal may be predried and the finished briquettes may be preheated, with a subsequent drying and hardening. The carbonization is effected in two stages in an indirectly heated shaft oven, with the evolved gas being taken off about at the mid-height of the oven shaft, processed, and used for heating in the second, high-temperature stage. The flue gases from this high-temperature stage are used for heating in the first stage and for preheating. The second or high-temperature stage is followed by a cooling stage where the gases evolved in the second stage, and mainly comprising hydrogen are used and circulated. The evolved gas in excess is continuously removed from the cooling circuit.
    • 由沥青或次烟煤或泥炭制成的团块通过研磨煤,与粘合剂混合并压实混合物来生产。 然后将它们在轴烘箱中以连续的方法碳化。 煤可以预干燥,并且可以预热完成的团块,随后进行干燥和硬化。 在间接加热的竖炉中分两步进行碳化,放出的气体在烘箱轴的中间高度处被取出,进行处理,并用于第二高温阶段的加热。 来自该高温阶段的烟气用于第一阶段的加热和预热。 第二或高温阶段之后是冷却阶段,其中在第二阶段中放出的气体和主要包含氢的气体被使用和循环。 过量的放出气体从冷却回路连续地移出。