Material für elektrophotographische Reproduktion
    3.
    发明公开
    Material für elektrophotographische Reproduktion 无效
    再生产材料。

    公开(公告)号:EP0031481A1

    公开(公告)日:1981-07-08

    申请号:EP80107575.5

    申请日:1980-12-04

    发明人: Lind, Erwin, Dr.

    IPC分类号: G03G5/06 G03G5/09

    摘要: Elektrophotographisches Aufzeichnungsmaterial aus einem elektrisch leitenden, insbesondere zur Herstellung von Druckformen oder gedruckten Schaltungen geeigneten Schichtträger und einer photoleitfähigen Schicht aus organischem Photoleiter, Bindemittel, Sensibilisierungsfarbstoffen und üblichen Zusätzen, wobei der Photoleiter eine Verbindung der allgemeinen Formel
    darstellt, in welcher

    R Wasserstoff, Alkyl, Alkoxyl mit 1-4 C-Atomen, Halogen oder Dialkylamino mit 1-4 C-Atomen,
    R 2 Dialkylamino mit 1-4 C-Atomen und
    X Stickstoff oder -CR 3 mit
    R 3 gegebenenfalls durch Halogen-, Alkylamino- oder Dialkylamino-Gruppen oder Alkyl mit 1-4 C-Atomen substituiertes Phenyl

    bedeuten, das Bindemittel aus der Gruppe der alkalilöslichen Bindemittel ausgewählt ist und der Sensibilisierungsfarbstoff einen zwischen 400 und 550 nm absorbierenden Cyaninfarbstoff und einen zwischen 450 und 600 nm absorbierenden Aminoxanthenfarbstoff umfaßt.

    摘要翻译: 1.一种电子照相记录材料,由导电层载体,特别是适用于制造印刷形式或印刷电路的载体以及包含有机光电导体,碱溶性粘合剂,敏化染料, 其包含在400和550nm之间的花青染料和常规添加剂,其中光电导体代表通式的化合物,见图:EP0031481,P5,F1,其中R1表示氢,烷基,具有1至4个C原子的烷氧基, 卤素或具有1至4个C原子的二烷基氨基,R 2表示具有1至4个C原子的二烷基氨基,X表示氮或-CR 3,其中R 3为任选被卤素,烷基氨基或二烷基氨基或具有1至4个C原子的烷基的苯基 其特征在于,所述敏化染料还包含在450和600nm之间吸收的氨基呫吨染料。

    SYSTEM FOR THE PRODUCTION OF CARBON BLACK
    5.
    发明授权
    SYSTEM FOR THE PRODUCTION OF CARBON BLACK 失效
    植物拉斯生产

    公开(公告)号:EP0635044B1

    公开(公告)日:1996-02-07

    申请号:EP93909087.4

    申请日:1993-04-05

    IPC分类号: C09C1/48 C01B3/24

    CPC分类号: C09C1/487 C01B3/24 C09C1/485

    摘要: In a system for the production of carbon black and hydrogen by the decomposition of hydrocarbon gas, there is in connection with the thermal decomposition reactor (1) provided a reactor (2) with adjustable temperature zones in order to influence and control the properties of the carbon black as well as to modify the surface and structure of the carbon black. The reactor has means for supplying gases and materials in the various temperature zones. Downstream of the reactor (2) there is provided a cooler (3) for the reactions products, in which feed gas and plasma gas can be preheated (19) and which is followed by separation means which may preferably consist of a cyclone (4, 5) for separating coarse particles from the carbon component. The cyclone (4, 5) is connected to a filter device (7) wherein carbon black of the desired particle size and structure is filtered out to a silo (8) and further processing. The system is equipped with a pipe for transfer of hydrogen partly to the chemical process industry, as an energy carrier, as well as back to the reactor (2) via a return pipe.

    SYSTEM FOR THE PRODUCTION OF CARBON BLACK
    6.
    发明公开
    SYSTEM FOR THE PRODUCTION OF CARBON BLACK 失效
    植物拉斯生产。

    公开(公告)号:EP0635044A1

    公开(公告)日:1995-01-25

    申请号:EP93909087.0

    申请日:1993-04-05

    IPC分类号: C01B3 C09C1

    CPC分类号: C09C1/487 C01B3/24 C09C1/485

    摘要: In a system for the production of carbon black and hydrogen by the decomposition of hydrocarbon gas, there is in connection with the thermal decomposition reactor (1) provided a reactor (2) with adjustable temperature zones in order to influence and control the properties of the carbon black as well as to modify the surface and structure of the carbon black. The reactor has means for supplying gases and materials in the various temperature zones. Downstream of the reactor (2) there is provided a cooler (3) for the reactions products, in which feed gas and plasma gas can be preheated (19) and which is followed by separation means which may preferably consist of a cyclone (4, 5) for separating coarse particles from the carbon component. The cyclone (4, 5) is connected to a filter device (7) wherein carbon black of the desired particle size and structure is filtered out to a silo (8) and further processing. The system is equipped with a pipe for transfer of hydrogen partly to the chemical process industry, as an energy carrier, as well as back to the reactor (2) via a return pipe.

    Simultaneous production of clean dewatered and clean saturated streams of synthesis gas
    7.
    发明公开
    Simultaneous production of clean dewatered and clean saturated streams of synthesis gas 失效
    同时生产合成气的清洁脱水和清洁饱和流

    公开(公告)号:EP0133622A3

    公开(公告)日:1985-04-03

    申请号:EP83107790

    申请日:1983-08-08

    IPC分类号: C01B03/36 C09C01/48 C01B03/52

    CPC分类号: C01B3/52 C01B3/36 C09C1/487

    摘要: The hot raw effluent gas stream from a free-flow partial oxidation gas generator is split into two hot raw gas streams which are separately processed. One split gas stream is cleaned by quenching and scrubbing with water. Entrained particulate carbon is removed therefrom as a carbon-water dispersion from which it is extracted with a liquid organic extractant. The resulting liquid organic extractant-carbon-water dispersion is vaporized using the sensible heat from the other split gas stream. Particulate carbon is then removed from the other split gas stream by scrubbing with a liquid hydrocarbon fuel to separate out a liquid hydrocarbon fuel-carbon dispersion which may be supplied to the gas generator as a portion of the feed. The remaining gaseous mixture is cooled and separated into a clean dewatered product gas stream, water, and liquid organic extractant. The latter two materials are recycled,

    摘要翻译: 来自自由流动部分氧化气体发生器的热的原料流出物流被分成两个分别处理的热原料气流。 通过用水淬火和擦洗来清洁一个分流气流。 夹带的颗粒碳作为碳水分散体从其中除去,用液体有机萃取剂萃取。 所得到的液体有机萃取剂 - 碳水分散体使用来自另一个裂解气流的显热来蒸发。 然后通过用液体碳氢化合物燃料洗涤从其它分离气体流中除去颗粒状碳,以分离作为进料的一部分可供应到气体发生器的液体烃燃料 - 碳分散体。 将剩余的气体混合物冷却并分离成干净的脱水产物气流,水和液体有机萃取剂。 后两种材料被回收利用。

    Simultaneous production of clean dewatered and clean saturated streams of synthesis gas
    8.
    发明公开
    Simultaneous production of clean dewatered and clean saturated streams of synthesis gas 失效
    Gleichzeitige Erzeugung eines reinen,entwässertenund eines reinen,wassergesättigtenSynthesegasstromes。

    公开(公告)号:EP0133622A2

    公开(公告)日:1985-03-06

    申请号:EP83107790.4

    申请日:1983-08-08

    IPC分类号: C01B3/36 C09C1/48 C01B3/52

    CPC分类号: C01B3/52 C01B3/36 C09C1/487

    摘要: The hot raw effluent gas stream from a free-flow partial oxidation gas generator is split into two hot raw gas streams which are separately processed. One split gas stream is cleaned by quenching and scrubbing with water. Entrained particulate carbon is removed therefrom as a carbon-water dispersion from which it is extracted with a liquid organic extractant. The resulting liquid organic extractant-carbon-water dispersion is vaporized using the sensible heat from the other split gas stream. Particulate carbon is then removed from the other split gas stream by scrubbing with a liquid hydrocarbon fuel to separate out a liquid hydrocarbon fuel-carbon dispersion which may be supplied to the gas generator as a portion of the feed. The remaining gaseous mixture is cooled and separated into a clean dewatered product gas stream, water, and liquid organic extractant. The latter two materials are recycled,

    摘要翻译: 来自自由流动部分氧化气体发生器的热的原料流出物流被分成两个分别处理的热原料气流。 通过用水淬火和擦洗来清洁一个分流气流。 夹带的颗粒碳作为碳水分散体从其中除去,用液体有机萃取剂萃取。 所得到的液体有机萃取剂 - 碳水分散体使用来自另一个裂解气流的显热来蒸发。 然后通过用液体碳氢化合物燃料洗涤从其它分离气体流中除去颗粒状碳,以分离作为进料的一部分供应到气体发生器的液体烃燃料 - 碳分散体。 将剩余的气体混合物冷却并分离成干净的脱水产物气流,水和液体有机萃取剂。 后两种材料被回收利用。

    A METHOD FOR DECOMPOSITION OF HYDROCARBONS
    10.
    发明授权
    A METHOD FOR DECOMPOSITION OF HYDROCARBONS 失效
    方法进行分解烃类

    公开(公告)号:EP0616599B1

    公开(公告)日:1996-02-28

    申请号:EP92924939.9

    申请日:1992-12-11

    IPC分类号: C01B3/24 C09C1/48

    摘要: In a method for decomposition of hydrocarbons for the production of hydrogen and carbon black, the feed stock is passed through a plasma torch, which causes a pyrolytic decomposition of the feed stock. The feed stock is transported through the plasma torch (A) in a cooled lead-in tube (1) and undergoes a first heating in an area in the immediate vicinity of the plasma flame. In the area immediately below the plasma flame a mixing of the hydrocarbon material and the plasma gas occurs, the temperature being increased to decomposition temperature for the raw material. In this area free hydrogen and dehydrogenated carbon material are produced in the form of drops of liquid. The material thereby produced is passed on to one or more subsequent stages where the final and complete decomposition of the hydrocarbons to carbon black and hydrogen occurs. In this area further raw material may be added which causes quenching and reacts with the already produced carbon black. An increase is thereby caused in particle size, density and amount produced without further energy supply, whereafter the products produced are expelled and separated and hot gas may be transported in a return pipe to the torch, in order to further increase the energy yield.