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    • 4. 发明申请
    • METHOD AND APPARATUS FOR TREATING SALT STREAMS
    • 用于处理盐水的方法和装置
    • WO99064112A1
    • 1999-12-16
    • PCT/SE1999/001006
    • 1999-06-09
    • A62D3/00A62D3/20A62D101/22A62D101/28A62D101/40B01J3/00C02F11/08
    • A62D3/20A62D2101/22A62D2101/28A62D2101/40A62D2203/10B01J3/008C02F11/086Y02P20/544
    • A method for avoiding the precipitation of salts from a salt containing water stream prior to the stream reaching a supercritical water reactor is presented. The salt containing water stream is preferably kept at temperatures below supercritical conditions as the stream is transferred to the reactor. After the salt stream reaches the reactor the temperature of the salt stream is preferably raised to the appropriate temperature by mixing the salt stream, within the reactor, with a second stream that has been heated above the supercritical temperature of water. Alternatively, a method for preventing the clogging of the conduits upstream from the reactor may involve the mixing of two subcritical waste streams. One stream may include salts, the other preferably includes oxidizable material. The heat produced by the reaction of the oxidizable materials within the reactor preferably allows the mixture to remain at supercritical conditions for a time sufficient to oxidize substantially all of the oxidizable material.
    • 提出了一种在流到超临界水反应器之前避免盐从含盐水流中沉淀的方法。 含盐水流优选保持在低于超临界条件的温度,因为流被转移到反应器中。 在盐流到达反应器之后,盐流的温度优选通过将反应器内的盐流与已经被加热到水的超临界温度以上的第二流混合而升高到合适的温度。 或者,用于防止在反应器上游的导管堵塞的方法可能涉及两个亚临界废物流的混合。 一个流可以包括盐,另一个优选包括可氧化的材料。 由反应器内的可氧化材料的反应产生的热量优选允许混合物在超临界条件下保持足以氧化基本上所有可氧化材料的时间。
    • 5. 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。