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    • 2. 发明授权
    • Apparatus and method for crystallization
    • 用于结晶的装置和方法
    • US06334878B1
    • 2002-01-01
    • US09384578
    • 1999-08-27
    • Ichiro MiyaharaTatsuo KitamuraMasato YokoyamaTakashi Koko
    • Ichiro MiyaharaTatsuo KitamuraMasato YokoyamaTakashi Koko
    • C30B708
    • B01D9/0004B01D9/0036
    • An apparatus for crystallization, which contains a crystallization vessel, a seed supplying device, a feed solution supplying device and a tube baffle disposed within the crystallization vessel. The tube baffle is provided with a crystallization portion in an inner area and a lower area thereof, and the tube baffle and the crystallization vessel define a classification portion there between. The apparatus further contains an agitating fan for agitating the seed crystals and the feed solution, and a plurality of plate baffles disposed within the classification portion which define a buffer portion and a gravitational settling portion. The apparatus further contains a device for generating a rising velocity of a slurry containing fine crystals in the gravitational settling portion by discharging the slurry so that the rising velocity of the slurry is greater than a settling velocity of the fine crystals and an outlet for discharging the crystallized material.
    • 一种用于结晶的装置,其包含结晶容器,种子供应装置,进料溶液供应装置和设置在结晶容器内的管挡板。 管道挡板在其内部区域和下部区域中设置有结晶部分,并且管道挡板和结晶容器在其间限定分类部分。 该装置还包括用于搅拌晶种和进料溶液的搅拌风扇,以及设置在分级部分内的限定缓冲部分和重力沉降部分的多个板挡板。 该装置还包括一种用于通过排出浆料来产生包含重力沉降部分中的细晶体的浆料的上升速度的装置,使得浆料的上升速度大于细晶体的沉降速度, 结晶材料。
    • 6. 发明授权
    • Monocrystalline powder and monograin membrane production
    • 单晶粉和单晶膜生产
    • US06488770B1
    • 2002-12-03
    • US09719036
    • 2000-12-06
    • Dieter MeissnerEnn MellikovMare Altosaar
    • Dieter MeissnerEnn MellikovMare Altosaar
    • C30B708
    • C30B9/00C30B29/40C30B29/46C30B29/60
    • For production of monocrystalline powders there is formed a melt to which a fluxing agent is added. The melt contains the components of a semiconductor material, an example being the components of copper indium diselenide which are generally used in a stoichiometric composition. The melt is usually heated to temperatures of between 300° C. and 1000° C. Monocrystalline powder grains grow. The desired recrystallization takes place at temperatures above the melting points of the materials to be fused. Once the powder grains have the desired size, the growth is stopped by quenching. The appropriate instant of quenching as well as the appropriate temperature profile for obtaining desired powder sizes are determined by, for example, preliminary experiments. Thereafter the fluxing agent is eliminated. Monograin membranes are produced from the powders produced according to the process and are used in particular in solar cells. The process is simple and inexpensive. Powder grains of uniform size are obtained.
    • 为了生产单晶粉末,形成了熔体,添加助熔剂。 熔体包含半导体材料的组分,例如通常以化学计量组成使用的二硒化铜铟的组分。 熔体通常被加热至300℃至1000℃之间的温度。单晶粉末颗粒生长。 所需的再结晶在高于要熔融的材料的熔点的温度下进行。 一旦粉末颗粒具有所需的尺寸,则通过淬火来停止生长。 通过例如初步实验来确定适当的淬火时间以及用于获得所需粉末尺寸的适当温度曲线。 此后消除助熔剂。 单晶膜由根据该方法生产的粉末生产并且特别用于太阳能电池中。 该过程简单而便宜。 获得均匀尺寸的粉末颗粒。
    • 9. 发明授权
    • Dynamically controlled crystallization method and apparatus and crystals obtained thereby
    • 由此获得动态控制的结晶方法和装置和晶体
    • US06596081B1
    • 2003-07-22
    • US09622553
    • 2000-12-12
    • Leonard ArnowitzEmanuel Steinberg
    • Leonard ArnowitzEmanuel Steinberg
    • C30B708
    • B01D1/00B01D9/00C30B7/08C30B23/00Y10S117/901Y10T117/1004Y10T117/1008
    • A method and apparatus for dynamically controlling the crystallization of molecules including a crystallization chamber (14) or chambers for holding molecules in a precipitant solution, one or more precipitant solution reservoirs (16, 18), communication passages (17, 19) respectively coupling the crystallization chamber(s) with each of the precipitant solution reservoirs, and transfer mechanisms (20, 21, 22, 24, 26, 28) configured to respectively transfer precipitant solution between each of the precipitant solution reservoirs and the crystallization chamber(s). The transfer mechanisms are interlocked to maintain a constant volume of precipitant solution in the crystallization chamber(s). Precipitant solutions of different concentrations are transferred into and out of the crystallization chamber(s) to adjust the concentration of precipitant in the crystallization chamber(s) to achieve precise control of the crystallization process. The method and apparatus can be used effectively to grow crystals under reduced gravity conditions such as microgravity conditions of space, and under conditions of reduced or enhanced effective gravity as induced by a powerful magnetic field.
    • 一种用于动态地控制分子的结晶的方法和装置,包括结晶室(14)或用于在沉淀剂溶液中保持分子的室,一个或多个沉淀剂溶液储存器(16,18),连通通道(17,19) 每个沉淀溶液储存器的结晶室以及被配置成分别在每个沉淀剂溶液储存器和结晶室之间转移沉淀剂溶液的转移机构(20,21,22,24,26,28)。 转移机构互锁以在结晶室中保持恒定体积的沉淀剂溶液。 将不同浓度的沉淀溶液转移进出结晶室,以调节沉淀剂在结晶室中的浓度,以实现结晶过程的精确控制。 该方法和装置可以有效地用于在诸如微重力空间条件的减重重力条件下以及在由强​​磁场引起的有效重力降低或增强的条件下生长晶体。