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    • 4. 发明申请
    • APPARATUS AND METHOD FOR CARRYING OUT CHEMICAL AND PHYSICAL MATERIALS TRANSFORMATIONS
    • 用于进行化学和物理材料转换的装置和方法
    • US20110015281A1
    • 2011-01-20
    • US12920498
    • 2009-03-05
    • Wolfgang LortzKarlheinz FilzWerner WillUwe Diener
    • Wolfgang LortzKarlheinz FilzWerner WillUwe Diener
    • B01F17/00B01J19/00B01J13/00B02C9/00
    • B01J19/26B01F5/0256B01J19/0053B01J19/02B01J2208/00539B01J2208/0069B01J2219/00247
    • Reactor for carrying out chemical and physical materials transformations, which comprises a reaction space enclosed by a reactor housing, where the reactor housing has at least two lateral fluid inlets having adjustably mounted nozzles which include an angle of about 20-160 degrees and through which fluid jets which impinge on one another at a common collision point within the reaction space are passed and the reactor has a fluid outlet at the bottom of the reaction space, which is characterized in that—an exchangeable bottom plate•which has a hole as fluid outlet and•on which moveably supported spheres are located so as to block the original path of the individual fluid jets in the unaligned state rests on the bottom of the reaction space and—a half shell standing upright on the bottom of the reaction space is located between each moveably supported sphere and the wall of the reactor space and—bottom plate, half shell and moveably supported spheres comprise one or more hard materials.
    • 用于进行化学和物理材料转化的反应器,其包括由反应器壳体包围的反应空间,其中反应器壳体具有至少两个侧向流体入口,其具有可调节地安装的喷嘴,其包括约20-160度的角度,并且流体 通过在反应空间内的共同碰撞点处彼此撞击的喷嘴,并且反应器在反应空间的底部具有流体出口,其特征在于 - 具有作为流体出口的孔的可更换的底板 和在其上可移动地支撑的球体被定位成阻挡在未对准状态下的各个流体射流的原始路径位于反应空间的底部,并且直立在反应空间底部的半壳体位于 每个可移动地支撑的球体和反应器空间和底板的壁,半壳体和可移动支撑的球体包括一个或多个硬质 材料
    • 7. 发明授权
    • Process for the production of metal oxide and metalloid oxide dispersions
    • 用于生产金属氧化物和类金属氧化物分散体的方法
    • US08529651B2
    • 2013-09-10
    • US12894539
    • 2010-09-30
    • Wolfgang LortzChristoph Batz-SohnGabriele PerletWerner WillGerrit Schneider
    • Wolfgang LortzChristoph Batz-SohnGabriele PerletWerner WillGerrit Schneider
    • B24D3/02C09C1/68C09K3/14C01B33/12
    • C09G1/02C01B13/145C01B33/1417C01F7/026C01P2002/50C01P2006/12C01P2006/22C03C1/006C09K3/1463
    • Process for the production of an aqueous dispersion of pyrogenically produced metal oxide and metalloid oxide powders with a BET surface area of between 5 and 600 m2/g, with a metal oxide or metalloid oxide content in the dispersion of between 5 and 25 wt. %, comprising the following steps: water, which is optionally adjusted to pH values of between 2 and 4 by adding acids, is circulated from a receiving vessel via a rotor/stator machine, and metal oxide or metalloid oxide powder is introduced, using a feed device, into the shear zone between the slots in the rotor teeth and the stator slots, continuously or discontinuously and with the rotor/stator machine running, in a quantity such that a predispersion with a solids content of between 20 and 40 wt. % results, and, after all the metal oxide powder or metalloid oxide powder has been added, the feed device closes and shearing continues in such a way that the shear rate is in the range of between 10000 and 40000 s−1, and then, by dilution, the predispersion is adjusted to the desired solids content of the dispersion while maintaining the dispersing conditions.
    • 制备热解法生产的金属氧化物和类金属氧化物粉末的水性分散体的方法,其BET表面积为5至600m 2 / g,分散体中的金属氧化物或准金属氧化物含量为5至25重量%。 %,包括以下步骤:通过添加酸任选地将pH调节至2至4的水通过转子/定子机从接收容器循环,并引入金属氧化物或准金属氧化物粉末,使用 进料装置连续或不连续地进入转子齿中的狭槽和定子槽之间的剪切区域中,并且转子/定子机器运行,其量使得固体含量为20至40重量%的预分散体。 %的结果,并且在添加了所有的金属氧化物粉末或准金属氧化物粉末之后,进料装置关闭并且剪切继续进行,使得剪切速率在10000和40000s -1之间,然后, 通过稀释,将预分散体调节至分散体的所需固体含量,同时保持分散条件。
    • 9. 发明申请
    • PROCESS FOR THE PRODUCTION OF METAL OXIDE AND METALLOID OXIDE DISPERSIONS
    • 生产金属氧化物和金属氧化物分散体的方法
    • US20110155951A1
    • 2011-06-30
    • US12894539
    • 2010-09-30
    • Wolfgang LORTZChristoph Batz-SohnGabriele PerletWerner WillGerrit Schneider
    • Wolfgang LORTZChristoph Batz-SohnGabriele PerletWerner WillGerrit Schneider
    • C09K3/00
    • C09G1/02C01B13/145C01B33/1417C01F7/026C01P2002/50C01P2006/12C01P2006/22C03C1/006C09K3/1463
    • Process for the production of an aqueous dispersion of pyrogenically produced metal oxide and metalloid oxide powders with a BET surface area of between 5 and 600 m2/g, with a metal oxide or metalloid oxide content in the dispersion of between 5 and 25 wt. %, comprising the following steps:water, which is optionally adjusted to pH values of between 2 and 4 by adding acids, is circulated from a receiving vessel via a rotor/stator machine, andmetal oxide or metalloid oxide powder is introduced, using a feed device, into the shear zone between the slots in the rotor teeth and the stator slots, continuously or discontinuously and with the rotor/stator machine running, in a quantity such that a predispersion with a solids content of between 20 and 40 wt. % results, and, after all the metal oxide powder or metalloid oxide powder has been added,the feed device closes and shearing continues in such a way that the shear rate is in the range of between 10000 and 40000 s−1, andthen, by dilution, the predispersion is adjusted to the desired solids content of the dispersion while maintaining the dispersing conditions.
    • 制备热解法生产的金属氧化物和类金属氧化物粉末的水性分散体的方法,其BET表面积为5至600m 2 / g,分散体中的金属氧化物或准金属氧化物含量为5至25重量%。 %,包括以下步骤:通过添加酸任选地将pH调节至2至4的水通过转子/定子机从接收容器循环,并引入金属氧化物或准金属氧化物粉末,使用 进料装置连续或不连续地进入转子齿中的狭槽和定子槽之间的剪切区域中,并且转子/定子机器运行,其量使得固体含量为20至40重量%的预分散体。 %的结果,并且在添加了所有的金属氧化物粉末或准金属氧化物粉末之后,进料装置关闭并且剪切继续进行,使得剪切速率在10000和40000s -1之间,然后, 通过稀释,将预分散体调节至分散体的所需固体含量,同时保持分散条件。