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    • 21. 发明授权
    • Two stage fluid bed regenerator
    • 两级流化床再生器
    • US4391586A
    • 1983-07-05
    • US320308
    • 1981-11-12
    • George N. Brown
    • George N. Brown
    • C01B31/08F27B15/00F23B5/02
    • C01B31/087C01B31/088
    • Improved method and apparatus are disclosed for regenerating wet spent carbon containing volatile impurities wherein the wet spent carbon is dried in a drying zone utilizing incinerated reactivation zone gaseous effluent. The improvement of the invention provides that the portion of reactivation zone gaseous effluent used to dry the wet spent carbon in the drying zone is continuously recycled to the reactivation zone for incineration to remove any volatile impurities which may have been removed from the wet spent carbon during drying. The balance of the reactivation zone gaseous effluent may be discharged into the atmosphere without further incineration.
    • 公开了改进的方法和装置用于再生含有挥发性杂质的湿废碳,其中湿废碳在干燥区中使用焚烧的再活化区气体流出物进行干燥。 本发明的改进规定,用于干燥干燥区中的湿废碳的再活化区气态流出物的一部分被连续地再循环到再活化区以进行焚化以除去可能从湿废碳中除去的任何挥发性杂质 烘干。 再活化区气态流出物的平衡可以排放到大气中而不进一步焚烧。
    • 23. 发明授权
    • Two stage fluid bed regeneration of spent carbon
    • 二级流化床再生废碳
    • US4248706A
    • 1981-02-03
    • US947059
    • 1978-09-29
    • Albert J. Repik
    • Albert J. Repik
    • C01B31/08B01J20/34B01D53/08C01B31/10C02F1/28
    • C01B31/087
    • Method and apparatus are disclosed for regenerating wet spent carbon containing volatile impurities wherein the wet spent carbon is dried in a drying zone utilizing incinerated reactivation zone gaseous effluent. The reactivation zone gaseous effluent is derived by reactivating dried spent carbon in a reactivation zone at pyrolysis conditions to remove volatile components from the adsorbent. Removal is effected utilizing combustion gases. The reactivation zone gaseous effluent is comprised of the combustion gases, the vaporized volatile impurities, and, where steam is employed in the reactivation zone to remove fixed carbon, substantial quantities of carbon monoxide and hydrogen. By interposing the incineration zone between the drying and reactivation zone, efficiency of the overall process is maximized. The combustible components of the combustion gases, the volatile impurities and the carbon monoxide and hydrogen, produced by removal of fixed carbon with steam, are burned in such a manner that the heat of combustion is used for drying the incoming wet spent carbon and for maintaining pyrolysis conditions required for reactivation. The effluent gases may be discharged directly into the atmosphere without further incineration.
    • 公开了用于再生含有挥发性杂质的湿废碳的方法和装置,其中使用焚烧的再活化区气态流出物在干燥区中干燥湿废碳。 再活化区气态流出物是通过在热解条件下在再活化区中再次干燥的废碳以从吸附剂中除去挥发性组分得到的。 使用燃烧气体进行去除。 再活化区气体流出物由燃烧气体,蒸发的挥发性杂质组成,并且在再活化区中使用蒸汽以除去固定碳,大量一氧化碳和氢气的情况下。 通过将焚烧区置于干燥和再生区之间,整个过程的效率最大化。 通过用蒸汽去除固定碳产生的燃烧气体的可燃组分,挥发性杂质和一氧化碳和氢气被燃烧,使得燃烧热用于干燥进入的湿废碳并维持 重新激活所需的热解条件。 废气可以直接排放到大气中而不进一步焚烧。
    • 24. 发明授权
    • Process for regenerating contaminated activated carbon
    • 再生污染活性炭的方法
    • US4217191A
    • 1980-08-12
    • US882083
    • 1978-03-01
    • Denis DoniatJean-Michel CorajoudJacques MosettiAugusto Porta
    • Denis DoniatJean-Michel CorajoudJacques MosettiAugusto Porta
    • C01B31/08C02F1/28C02F1/467C25F1/00
    • C01B31/087C02F1/283C02F1/4672C02F2303/16
    • Process for regenerating activated carbon particles contaminated by oxidizable impurities. An electrolysis cell is divided by a liquid-permeable membrane to define an anodic chamber and a cathode chamber therein both filled in operation with an electrolyte. Recycling conduits communicate with the anode chamber and a recirculating pump to establish a fluid circuit therewith. A suspension of particles of activated carbon contaminated by oxidizable impurities suspended in an aqueous solution of an electrolyte is loaded into the fluid circuit and circulated therethrough. A voltage applied to the electrodes of the electrolysis cell develops an electrolysis reaction in the aqueous solution of the electrolyte and atomic oxygen is liberated at the surface of the anode electrode. As particles of the activated carbon flow through the anode cell they contact the anode electrode and atomic oxygen is liberated at their surfaces which oxidizes impurities adsorbed by the particles. After the carbon particles have been circulated for a sufficient time to oxidize all of the impurities thereon, the regenerated particles of activated carbon and the aqueous solution of the electrolyte are discharged from the recirculating circuit.
    • 再生被可氧化杂质污染的活性炭颗粒的方法。 电解槽被液体渗透膜分隔,以确定阳极室和阴极室,其中两者均填充有电解液。 回收管道与阳极室和循环泵连通以与其建立流体回路。 被悬浮在电解质水溶液中的可氧化杂质污染的活性炭颗粒的悬浮液被加载到流体回路中并循环通过。 施加到电解池的电极的电压在电解质的水溶液中产生电解反应,并且在阳极电极的表面释放原子氧。 当活性炭的颗粒流过阳极电池时,它们接触阳极电极,原子氧在其表面释放,氧化颗粒吸附的杂质。 在碳粒子已经循环足够的时间以氧化其上的所有杂质之后,再生的活性炭颗粒和电解质水溶液从再循环回路排出。
    • 28. 发明授权
    • Wet combustion process
    • 湿法燃烧过程
    • US4017421A
    • 1977-04-12
    • US641335
    • 1975-12-16
    • Donald F. Othmer
    • Donald F. Othmer
    • B01D3/06C01B31/08C02F1/02C02F1/26C02F11/08C07C53/08B01D15/06B01D1/14
    • B01D3/065C01B31/087C02F1/02C02F1/025C02F1/265C02F11/08C07C53/08Y10S159/905Y10S210/918Y10S423/09
    • Aqueous solutions and suspensions of solid particles, even those containing less than one percent of organic materials, may be combusted with air, oxygen, or their mixtures in a process which provides for preheating in countercurrent batches of the raw original liquid by either open (direct contact) or closed (heat transfer surface) condensation of steam generated by multiple flash evaporations which cool earlier batches of hot liquid after the wet combustion. Excess heat may often be withdrawn from the process for power generation or other use as high pressure steam, with or without combustion gases and other non-condensibles. No pumps are necessary, liquid batches are pressurized by steam generated in the flash evaporations for which only one pressure vessel is required instead of the many in the continuous processes.Waste liquids as sewage sludges and black liquors from wood pulping may have their organic constituents, as measured by BOD or COD, so reduced that the final, spent liquid may be discharged directly to a receiving body of water.
    • 含有少于1%有机物质的固体颗粒的水溶液和悬浮液可以在空气,氧气或其混合物中燃烧,该方法通过开放(直接)将原始原液逆流批量预热 接触)或闭合(传热表面)通过多次闪蒸发生的蒸汽的冷凝,其在湿式燃烧之后冷却较早批次的热液体。 过热可能经常从用于发电或其他用途的过程中撤出,作为具有或不具有燃烧气体和其它不可冷凝物的高压蒸汽。 不需要泵,液体批料通过在仅需要一个压力容器而不是连续过程中的许多的闪蒸蒸发中产生的蒸汽加压。