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    • 1. 发明申请
    • CATALYTIC-HYDROTHERMAL DISPOSAL PROCESS OF CHEMICAL MILITARY MATERIALS
    • 用于催化水处置武器的化学物质
    • WO1996034662A1
    • 1996-11-07
    • PCT/EP1995001710
    • 1995-05-05
    • UHDE GMBHHEDERER, HartmutTHIAGARAJAN, NatarajanANDERSEN, Kjeld
    • UHDE GMBH
    • A62D03/00
    • A62D3/20A62D3/35A62D2101/02A62D2101/22A62D2101/24A62D2101/26
    • The chemical military materials include both the group of chemical agents used in chemical weapons and the group of fuels used in military aircraft. Chemical military materials must be disposed of at the end of their storage life. A continuous process is disclosed for that purpose. The chemical military materials are first suspended and/or dissolved in water and an alkaline catalyst is added to the aqueous mixture. A reaction mixture is thus obtained. The reaction mixture is brought to the reaction pressure by liquid feeding means, for example a high pressure pump. The reaction pressure lies between 100 bars and 1000 bars. The reaction mixture is heated up to a reaction temperature lower than the critical temperature of pure water. The usual reaction temperature is 350 DEG C. The reaction mixture heated up to the reaction temperature then flows over a catalyst bed that contains a catalytic zirconium dioxide. The catalysed reactions produce a hot mixture of converted materials that is substantially free of chemical military materials. The hot mixture of converted materials is cooled down and expanded in a separator, producing a gaseous phase with CO2, CH4 and H2, an oily phase and an aqueous phase with dissolved salts that may all be dumped.
    • 武器的化学物质包括该组的可作为化学武器的化学战剂,以及在军用飞机使用的组的燃料。 武器的化学物质必须在其保质期后丢弃。 这是在一个连续的过程中完成的。 在此,化学武器材料首先悬浮在水和/或溶解的和水的混合物中加入碱性催化活性添加剂。 使得进料混合物生产的。 然后,与这样的液体资金进料混合物。 带来作为高压泵向反应压力。 反应压力为100巴和1000巴之间。 将进料混合物被加热到低于纯水的临界温度的反应温度。 典型的反应温度为350℃。加热到反应温度进料混合物通过催化剂床有催化作用的二氧化锆,其中所述热产生Konvertgemisch在催化的反应,这是无化学物质臂基本上通过。 热Konvertgemisch被冷却并在分离器放松。 被填埋在此,气相与CO 2,CH 4和H 2,油相和水相含有溶解的盐出现。
    • 4. 发明申请
    • POWER-GENERATION METHOD USING COMBINED GAS AND STEAM TURBINES
    • 发电过程中由组合的气体/汽轮机过程来
    • WO1997010416A1
    • 1997-03-20
    • PCT/EP1995003649
    • 1995-09-16
    • UHDE GMBHLIU, CiRADTKE, KarstenKELLER, Heinz-Jochen
    • UHDE GMBH
    • F01K23/06
    • F01K23/068Y02E20/16Y02E20/18
    • The invention concerns a method of power generation using a so-called COGAS (combined gas and steam) turbine installation, the aim being to improve the method with regard to the initial costs and energy consumption so that power can be generated as cheaply as possible. This is achieved by virtue of the fact that air (5) taken from the surrounding atmosphere is split into an essentially oxigen-containing stream (7) and an essentially nitrogen-containing stream (6) and the two streams fed further at approximately atmospheric pressure. The essentially nitrogen-containing stream (6) is mixed with an air stream (10) to form a mixed nitrogen/air stream (11) and the mixed-gas stream thus produced is brought to combustion-chamber pressure in the compressor (107) of the gas turbine (105), the combustion of the combustion gases in the combustion chamber (164) of the gas turbine being carried out with the greater part of this compressed mixed-gas stream.
    • 与使用所谓的组合式过程的发电方法,即 组合的燃气和蒸汽涡轮过程是要实现在能耗和投资成本方面的过程控制的改进和尽可能经济设计为可能的。 (5)从环境中抽这是由空气来实现,并且在(7)和基本上含氮部分流(6)中分离和部分流在环境压力下约持续大致含氧部分流的空气分离(200),该 基本上含氮部分流(6)具有用于bilding混合空气(11)的空气流(10)混合,在所述燃气涡轮机(105)的压缩机(107)所得到的混合气被带到燃烧室压力和所述燃烧气体的燃烧在 进行与该压缩混合气的最大部分的燃气涡轮机组的燃烧室(164)。