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    • 54. 发明公开
    • Verfahren und Vorrichtung zur Reinigung kontaminierter Materialien
    • EP0896838A2
    • 1999-02-17
    • EP98115268.9
    • 1998-08-13
    • Czetsch, Alexander
    • Czetsch, Alexander
    • B09C1/06
    • F26B5/042B09C1/06F26B5/04F26B11/16F26B25/006F26B2200/18
    • Die Erfindung betrifft ein Verfahren zur Reinigung kontaminierter Materialien von schüttfähiger und/oder pastöser Konsistenz, insbesondere schadstoffbelasteter Böden, oder zur Trocknung von pastösen Stoffen und Schlämmen, insbesondere Schlämmen aus Kammerpressen, bei dem die Materialien zunächst in zumindest eine Trockenkammer eingebracht und zur Verdampfung von Wasser erwärmt werden, und bei dem anschließend die in vorgebbarer Weise getrockneten Materialien in wenigstens eine separate Dekontaminationskammer überführt und zur Verdampfung von Verunreinigungen weiter erwärmt werden, wobei zumindest in der Dekontaminationskammer vor und/oder nach Beginn der Erwärmung der Materialien ein Unterdruck hergestellt wird und die sich in der Trockenkammer und/oder in der Dekontaminationskammer befindenden Materialien zumindest zeitweise auflockernd bewegt werden. Die Erfindung betrifft außerdem eine Vorrichtung zur Durchführung dieses Verfahrens.
    • 在一种净化大量固体如土壤或糊状材料的方法中,新颖性在于:(a)首先将材料置于干燥室(1)中,在其中加热它们以蒸发水; (b)将干燥的材料转移到第二室(2)中,在其中将其进一步加热并使杂质蒸发; (c)进一步到第二级加热过程(2),在室内降低压力; (d)干燥室(1,2)中的材料不时松动和转动; 和(e)室(1,2)将蒸发的水和其它杂质排放到它们各自的冷凝器(4a,b)。 还要求保护的是用于执行该过程的合适组件。
    • 56. 发明授权
    • Removal of organics and volatile metals from soils using thermal desorption
    • 通过热解吸有机物和挥发性金属的去除土壤
    • EP0540342B1
    • 1997-03-05
    • EP92309941.0
    • 1992-10-29
    • WESTINGHOUSE ELECTRIC CORPORATION
    • Lahoda, Edward JohnGrant, David Charles
    • B09B3/00A62D3/00C02F11/00
    • F26B25/006B09B3/0091B09C1/06
    • The removal of organics and volatile metals from soils using thermal desorption comprises moving contaminated materials, positioned on a belt conveyor (36), through a chamber (20) under oxygen conditions, temperature conditions, and residence time effective to substantially avoid incineration of the contaminants. The method further comprises heating the contaminated material for volatilizing the contaminants and for producing a processed material that is substantially decontaminated. To carry the volatilized contaminants from the chamber (20), a transport gas may be passed through the chamber (20) countercurrent to the movement of the contaminated material. A gas stream including the volatilized contaminants and the transport gas may be passed through a condenser (70) and through a scrubber (80) for producing a substantially cleaned gas and a contaminated liquid concentrate. The cleaned gas may be recycled back into the chamber (20) as the transport gas or passed through a gas cleaning system (86) prior to discharge into the atmosphere. The liquid concentrate is passed through a water treatment system (90) for producing substantially cleaned water. The water may be passed through an air cooler (92) and recycled back into the quencher (70) or may be passed through a carbon absorption column (94) and recycled as quench water for the processed material.
    • 58. 发明公开
    • Removal of organics and volatile metals from soils using thermal desorption
    • 通过热解吸从土壤中有机物和挥发性金属的去除。
    • EP0540342A2
    • 1993-05-05
    • EP92309941.0
    • 1992-10-29
    • WESTINGHOUSE ELECTRIC CORPORATION
    • Lahoda, Edward JohnGrant, David Charles
    • B09B3/00A62D3/00C02F11/00
    • F26B25/006B09B3/0091B09C1/06
    • The removal of organics and volatile metals from soils using thermal desorption comprises moving contaminated materials, positioned on a belt conveyor (36), through a chamber (20) under oxygen conditions, temperature conditions, and residence time effective to substantially avoid incineration of the contaminants. The method further comprises heating the contaminated material for volatilizing the contaminants and for producing a processed material that is substantially decontaminated. To carry the volatilized contaminants from the chamber (20), a transport gas may be passed through the chamber (20) countercurrent to the movement of the contaminated material. A gas stream including the volatilized contaminants and the transport gas may be passed through a condenser (70) and through a scrubber (80) for producing a substantially cleaned gas and a contaminated liquid concentrate. The cleaned gas may be recycled back into the chamber (20) as the transport gas or passed through a gas cleaning system (86) prior to discharge into the atmosphere. The liquid concentrate is passed through a water treatment system (90) for producing substantially cleaned water. The water may be passed through an air cooler (92) and recycled back into the quencher (70) or may be passed through a carbon absorption column (94) and recycled as quench water for the processed material.
    • 利用热解吸有机物和从土壤中挥发性金属的去除包括通过氧条件,温度条件,和停留时间下有效的腔室(20)移动的被污染的材料,设置在带式传送器(36)以基本上避免污染物的焚烧 , 加热受污染的材料挥发的污染物和用于产生处理的材料的方法,还包括并基本上净化。 携带从所述腔室(20)中的挥发性污染物,输送气体可以通过所述室(20)逆流传递到污染的材料的运动。 的气体流包括挥发性污染物和输送气体可以通过冷凝器(70),并通过用于产生基本上清洁的气体和被污染的液体浓缩物的洗涤器(80)传递。 清洁的气体可以再循环回到腔室(20)作为传输气体或通过气体清洁系统(86)排放到大气中之前通过。 所述液体浓缩物是通过水处理系统(90),用于产生基本清洁水通过。 水可以通过向空气冷却器(92)通过并再循环回到猝灭剂(70),或者可以通过碳吸收塔(94)传递和回收作为急冷水用于加工的材料。
    • 60. 发明公开
    • Control system for an industrial dryer
    • 工业干燥机控制系统
    • EP0413517A3
    • 1992-07-08
    • EP90308788.0
    • 1990-08-09
    • W.R. Grace & Co.-Conn.
    • Hansen, Dennis L.Zagar, Steve J.Norz, Gerald R.
    • F26B13/10F26B21/14F26B25/00
    • F26B25/006F26B13/10F26B21/14
    • A dryer (10) used to remove a flammable solvent or vapors from a traveling web of material (12) or the dryer. The dryer (10) consists of a chamber which is preferably a large metallic cylinder (14) through which the web of material (12) moves longitudinally. Seals (16,18) in the metallic cylinder at the points of entry and exit of the traveling web permit the control system to maintain the desired environment under controlled pressure within the metallic cylinder. The web of material travels successively through one or more zones within the metallic cylinder. At each zone, the web of material is exposed to a pressurized atmosphere which may be at increasingly higher temperatures. The solvent is recovered from the pressurized atmosphere by rapid cooling, membrane separation or absorption. Sensors within each zone measure the oxygen content of the pressurized atmosphere. If the oxygen content exceeds a given threshold, pressurized nitrogen or other inert gas is added. Through the use of a carbon bed (60) at the last zone, the pressurized atmosphere from that zone is rendered sufficiently free of solvent to be exhausted to the air or a nitrogen recovery unit, thereby maintaining the desired overall pressure within the metallic cylinder.