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    • 1. 发明授权
    • Method of regenerating particulate adsorption agents
    • 再生颗粒吸附剂的方法
    • US4058374A
    • 1977-11-15
    • US694521
    • 1976-06-10
    • Harald JuntgenJurgen KleinGunther Gappa
    • Harald JuntgenJurgen KleinGunther Gappa
    • B01J8/36B01J20/34C01B31/08C02F1/28B01D53/08B01D53/12
    • C01B31/088B01J20/08B01J20/20B01J20/3416B01J20/3433B01J20/3458B01J8/36C02F1/28B01J2220/56
    • An apparatus for performing the method of the invention for the thermal regeneration of contaminated particulate adsorption agents in a fluidized state includes a regeneration chamber which has separate first and second zones for the thermal treatment of the adsorption agents in a fluidized state. A first inlet is provided for admitting contaminated adsorption agents into the first zone and a separate second inlet is provided for admitting contaminated adsorption agents into the second zone. A first outlet is provided for removing regenerated adsorption agents from the first zone whereas a separate second outlet is provided for removing regenerated adsorption agents from the second zone. Means for fluidizing and thermally treating the contaminated adsorption agents so as to regenerate the same includes a combustion chamber arranged to supply hot fluidizing gases to both of the treatment zones. A gas outlet in the regeneration chamber serves to exhaust the fluidizing gases from both of the treatment zones.
    • 用于进行流化状态的污染颗粒吸附剂的热再生的本发明方法的装置包括具有分离的第一和第二区的再生室,用于在流化状态下热处理吸附剂。 提供第一入口用于将污染的吸附剂引入第一区域,并且提供单独的第二入口用于将污染的吸附剂引入第二区域。 提供第一出口用于从第一区域除去再生的吸附剂,而提供单独的第二出口用于从第二区域除去再生的吸附剂。 用于流化和热处理污染的吸附剂以再生污染的吸附剂的装置包括布置成向两个处理区域供应热流化气体的燃烧室。 再生室中的气体出口用于从两个处理区域排出流化气体。
    • 3. 发明授权
    • Method and apparatus for regenerating absorption particles
    • 用于再生吸收颗粒的方法和装置
    • US4017422A
    • 1977-04-12
    • US657406
    • 1976-02-12
    • Gunther GappaHarald JuntgenJurgen Klein
    • Gunther GappaHarald JuntgenJurgen Klein
    • B01J8/36B01J20/34C01B31/08B01D53/34B01D15/06
    • B01J8/36B01J20/20B01J20/3416B01J20/3458B01J20/3483C01B31/088B01J2220/56
    • A housing has a foraminous floor adapted to support a bed of adsorption particles. A plurality of baffles spaced above this floor subdivide the bed into a plurality of compartments. Impurity-carrying particles are fed to the compartment at one end of the elongated chamber and the particles overflow a weir at the compartment at the other end of the chamber. A hot gas is passed up through the bed in all of the chambers to deadsorb the particles and the baffles are spaced so that in the direction of flow each baffle projects more deeply into the bed to flow the flow toward the outlet end. A gas above the furthest upstream compartment is collected and condensed to recover useful constituents, and the gas from the other compartments is burned. It is possible to provide an upstream and a downstream compartment at an upper level and below them several downstream compartments, with the gas from the downstream compartments flowing up through the two upper compartments. The chamber has a length equal to at least twice its width and preferably equal to approximately the same multiple of its width as number of compartments it is divided into.
    • 壳体具有适于支撑吸附颗粒床的多孔地板。 在该地板之间间隔开的多个挡板将床分成多个隔间。 杂质携带颗粒在细长室的一端被供给到隔室,并且颗粒在室的另一端处的隔室溢出堰。 热气体在所有室中通过床,以阻止颗粒并且隔板间隔开,使得在流动方向上,每个挡板更深地突入床中以使流动朝向出口端流动。 收集并浓缩最上游隔室上方的气体以回收有用的成分,并且来自其他隔室的气体被燃烧。 可以在上一级和下游隔室设置上游和下游隔室,其中下游隔室中的气体向上流过两个上隔室。 腔室的长度至少等于其宽度的两倍,并且优选地等于其宽度与其被分成的间隔的数量的大致相同的倍数。
    • 7. 发明授权
    • Process for the purification of waste waters with activated carbon
    • 用活性炭净化废水的方法
    • US4007116A
    • 1977-02-08
    • US598385
    • 1975-07-23
    • Gunther GappaHarald JuntgenJurgen KleinJurgen Reichenberger
    • Gunther GappaHarald JuntgenJurgen KleinJurgen Reichenberger
    • B01D15/00C01B31/08C02F1/28
    • C02F1/283C01B31/087
    • A process for the purification of waste water containing dissolved organic carbon contaminants which comprisesA. passing the waste water upwardly through a column of activated carbon particles,B. determining the total organic carbon content of the water before it enters the column and simultaneously at a location that is between 30 and 70% of the total height of the carbon particles in the column,C. continuously withdrawing the spent carbon particles from the bottom of the column at such a rate as to maintain an essentially constant preselected difference between the total organic carbon content of the water as it enters the column and at the preselected location that is between 30 and 70% of the height of the carbon particles in the column,D. continuously introducing fresh activated carbon particles or reactivated carbon particles at the top of the column at such a rate as to compensate for those withdrawn at the bottom of the column, andE. removing the purified water at the top of the column.
    • 一种净化含有溶解的有机碳污染物的废水的方法,其中包括A.通过活性碳颗粒柱进入废水,B.确定水的总有机碳含量,在进入柱之前和同时进行 位置在柱子内的碳颗粒的总高度的30%至70%之间,C.连续地从柱的底部以这样的速率取出空气中的碳粒子,以维持总有机物之间的基本恒定的差异 水的碳含量,因为它进入柱和在预定位置之间的碳含量在30和70%之间的碳颗粒的高度,D.连续地引入新鲜的活性碳颗粒或反应的碳颗粒在顶部 在这样一个等级的柱子,以补偿在塔的底部,和E.删除净化的水在顶部 的柱子
    • 8. 发明授权
    • Method for production of acetylene
    • 生产乙炔的方法
    • US4378232A
    • 1983-03-29
    • US218281
    • 1980-12-18
    • Cornelius PeuckertHerbert BaumannDirk BittnerJurgen KleinHarald Juntgen
    • Cornelius PeuckertHerbert BaumannDirk BittnerJurgen KleinHarald Juntgen
    • C07C1/00C10J3/00
    • C07C1/00
    • A method for the production of acetylene from coal and hydrogen is provided by electric arc heating. The coal has a content of volatile components (i.waf) from about 25 to 44 percent and a content of organic oxygen (i.waf) of less than 9 percent and is ground to a diameter of less than 0.5 mm. The coal is then separated into two to four grain size fractions and one of the grain size fractions is loaded on a hydrogen containing gas. The gas carrying the coal is heated by way of an electric arc with an energy of from about 5 to 20 kJ/l (in normal state). The ratio of electric power employed to coal stream is from about 4,000 to 40,000 kJ/kg coal. The coal is heated for a time duration about inversely proportional to the third root of the specific outer surface of the coal gain fraction. The resulting product gas is quenched with cold liquid hydrocarbons, with hydrogen or water. Acetylene yields of up to about 0.41 kg acetylene per kg coal can be obtained.
    • 通过电弧加热提供从煤和氢生产乙炔的方法。 煤的挥发性组分(i.waf)含量为约25至44%,有机氧含量(i.waf)小于9%,并被研磨成小于0.5mm的直径。 然后将煤分离成两至四个粒度级分,并将一种晶粒尺寸级分装载在含氢气体上。 携带煤的气体通过约5至20kJ / l的能量的电弧加热(在正常状态下)。 煤矿用电量比例约为4000〜40,000千焦/千克煤。 煤被加热一段时间,与煤增益部分的特定外表面的第三根成反比。 所得产物气体用冷液体烃与氢气或水淬灭。 可以获得每公斤煤高达约0.41千克乙炔的乙炔产量。