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    • 8. 发明授权
    • Method for drying and producing microporous particles and a drying device
    • 干燥和生产微孔颗粒的方法和干燥装置
    • US06438867B1
    • 2002-08-27
    • US09623873
    • 2000-09-11
    • Friedhelm TeichHeiner SchellingHerbert KösterHorst KratzerWolfgang ReichertMartin GallBernd Ziegler
    • Friedhelm TeichHeiner SchellingHerbert KösterHorst KratzerWolfgang ReichertMartin GallBernd Ziegler
    • F26B300
    • F26B7/00
    • In a process for drying microporous, fluid-containing particles, the heat required for increasing the temperature is supplied by convection by reducing the interfacial tension of the fluid, preferably to 0 to 1/10, in particular to 0 to 1/20, of the interfacial tension of the fluid at room temperature, by appropriately increasing the temperature at from close to the critical pressure to supercritical pressure of the fluid. Furthermore, microporous, three-dimensionally networked particles are prepared by a process in which the drying process is used. In addition, an apparatus is used for carrying out the drying process, the apparatus comprising a pressure container having an inner container and pressure-withstanding outer container and suitable measuring and control apparatuses and pump apparatuses and heat exchangers, the inner container being provided for holding the particles to be dried and a gap being provided between the inner container and the outer container.
    • 在微孔,含流体颗粒的干燥过程中,通过降低流体的界面张力,优选为0至1/10,特别是0至1/20,通过对流来提供增加温度所需的热量 流体在室温下的界面张力,通过将接近临界压力的温度适当地提高到流体的超临界压力。 此外,通过使用干燥方法的方法制备微孔,三维网状颗粒。 此外,使用装置进行干燥处理,该装置包括具有内部容器和耐压外部容器的压力容器以及合适的测量和控制装置以及泵装置和热交换器,所述内部容器设置用于保持 待干燥的颗粒和在内部容器和外部容器之间设置的间隙。
    • 9. 发明授权
    • Method for producing phosgene
    • 生产光气的方法
    • US08993803B2
    • 2015-03-31
    • US13255665
    • 2010-03-10
    • Gerhard OlbertKai ThieleByoung-Yeon KimHeiner Schelling
    • Gerhard OlbertKai ThieleByoung-Yeon KimHeiner Schelling
    • C07C51/58C01B31/28
    • C01B31/28C01B32/80
    • A process for preparing phosgene by reaction of a feed stream (1) obtained by combining and mixing a chlorine feed stream (2) and a carbon monoxide feed stream (3), with the carbon monoxide being introduced in a stoichiometric excess over chlorine, in catalyst tubes filled with beds of activated carbon in a reactor R having a bundle of catalyst tubes,to give a product gas mixture (4)which is separated into a liquid, phosgene-comprising product stream (5) and an offgas stream (6) comprising carbon monoxide which is discharged via a pressure-regulating valve, where the reaction of the feed stream (1) in the reactor R and the separation of the product gas mixture (4) are carried out under a pressure in the range from 2.0 to 6.0 bar gauge pressure, whereinthe excess of carbon monoxide in the feed stream (1) to the reactor R is regulated by continuously measuring the flow and the concentration of carbon monoxide in the offgas stream (6), calculating the actual value of the excess of carbon monoxide in the feed stream (1) to the reactor R from these measurements in combination with the continuously measured values for the flow of the carbon monoxide feed stream (3) and the flow of and the chlorine concentration in the chlorine feed stream (2) and matching this to the intended value of the excess of carbon monoxide in the feed stream (1) to the reactor R by adapting the flow of the carbon monoxide feed stream (3), is proposed.
    • 通过将通过混合和混合氯进料流(2)和一氧化碳进料流(3)获得的进料流(1)与以氯化学计量过量的一氧化碳反应制备光气的方法, 在具有一束催化剂管的反应器R中填充有活性炭床的催化剂管,得到产物气体混合物(4),其被分离成液体,含光气的产物流(5)和废气流(6) 包括通过压力调节阀排出的一氧化碳,其中反应器R中的进料流(1)与产物气体混合物(4)的分离反应在2.0〜 6.0巴表压,其中通过连续测量废气流(6)中的一氧化碳的流量和浓度来调节进料流(1)中通过反应器R的过量一氧化碳,计算过量的实际值 的碳水化合物 将来自这些测量的进料流(1)中的一氧化碳与来自一氧化碳进料流(3)的流量和氯进料流(2)中的流量和氯浓度的连续测量值结合的反应器R ),并通过适应一氧化碳进料流(3)的流量将其与进料流(1)中过量的一氧化碳的预期值相匹配。