Process for Producing Ultrafine Powders Based on Polyamides, Ultrafine Polyamide Powders and Their Use
    1.
    发明申请
    Process for Producing Ultrafine Powders Based on Polyamides, Ultrafine Polyamide Powders and Their Use 有权
    基于聚酰胺,超细聚酰胺粉末生产超细粉的方法及其应用

    公开(公告)号:US20080249237A1

    公开(公告)日:2008-10-09

    申请号:US12089998

    申请日:2006-10-12

    摘要: Process for preparing ultrafine powders based on polyamides by contacting polyamides having a relative solution viscosity ηrel in the range from 1.5 to 2.0, measured in 0.5% m-cresol solution at 25° C., with an alcoholic medium in the presence of inorganic particles under the action of pressure and/or temperature to generate an at least partial solution, and then precipitating the polyamide from the at least partial solution, characterized in that a suspension of the inorganic particles suspended in the alcoholic medium is used. The resulting ultrafine polyamide powders have a specific BET surface area in the range of 5-100 m2/g; a fineness d50 of less than 70 μm; an apparent density AD in the range from 250 to 1000 g/l; and a particle content of 0.1 to 80% by weight of inorganic particles based on the total weight of the polyamide powder. They are equally suitable for coatings and for mouldings and components with improved mechanical properties.

    摘要翻译: 通过使具有相对溶液粘度和相对粘度的聚酰胺在25℃下在0.5%间甲酚溶液中测量的1.5至2.0的范围内与醇混合来制备基于聚酰胺的超细粉末的方法 介质在无机颗粒存在下在压力和/或温度的作用下产生至少部分溶液,然后从至少部分溶液中沉淀聚酰胺,其特征在于悬浮在醇介质中的无机颗粒的悬浮液 用来。 得到的超细聚酰胺粉末的比BET比表面积为5-100m 2 / g; 细度d <50%小于70μm; 在250〜1000g / l范围内的表观密度AD; 和基于聚酰胺粉末的总重量的无机颗粒的0.1〜80重量%的颗粒含量。 它们同样适用于具有改善的机械性能的涂料和模制品和组分。

    PROCESS FOR PRODUCING ULTRAFINE POWDERS BASED ON POLYAMIDES, ULTRAFINE POLYAMIDE POWDERS AND THEIR USE
    2.
    发明申请
    PROCESS FOR PRODUCING ULTRAFINE POWDERS BASED ON POLYAMIDES, ULTRAFINE POLYAMIDE POWDERS AND THEIR USE 审中-公开
    基于聚氨酯,超级聚酰胺粉及其使用生产超细粉的方法

    公开(公告)号:US20120264877A1

    公开(公告)日:2012-10-18

    申请号:US13494082

    申请日:2012-06-12

    摘要: Process for preparing ultrafine powders based on polyamides by contacting polyamides having a relative solution viscosity ηrel in the range from 1.5 to 2.0, measured in 0.5% m-cresol solution at 25° C., with an alcoholic medium in the presence of inorganic particles suspended therein under the action of pressure and/or temperature to generate an at least partial solution, and then precipitating the polyamide from the at least partial solution; the resulting ultrafine polyamide powders have a specific BET surface area of 5-100 m2/g; a fineness d50 of less than 70 μm; an apparent density AD from 250 to 1000 g/l; and a particle content of 0.1 to 80% by weight of inorganic particles based on the total weight of the polyamide powder; which powders are equally suitable for coatings and for mouldings and components with improved mechanical properties.

    摘要翻译: 通过使具有相对溶液粘度和相对浓度的相对比例在1.5至2.0的范围内的聚酰胺制备基于聚酰胺制备的超细粉末的方法,其在25℃的0.5%间甲酚溶液中,在无机物存在下用醇介质 在压力和/或温度的作用下悬浮在其中的颗粒以产生至少部分溶液,然后从所述至少部分溶液中沉淀聚酰胺; 所得超细聚酰胺粉末的BET比表面积为5-100m 2 / g; 细度d50小于70μm; 表观密度AD为250〜1000g / l; 和基于聚酰胺粉末的总重量的无机颗粒的0.1〜80重量%的颗粒含量; 这些粉末同样适用于涂料和具有改进的机械性能的模制品和组分。

    Process for producing ultrafine powders based on polyamides, ultrafine polyamide powders and their use
    3.
    发明授权
    Process for producing ultrafine powders based on polyamides, ultrafine polyamide powders and their use 有权
    用于生产基于聚酰胺,超细聚酰胺粉末的超细粉末及其用途的方法

    公开(公告)号:US08232333B2

    公开(公告)日:2012-07-31

    申请号:US12089998

    申请日:2006-10-12

    摘要: Process for preparing ultrafine powders based on polyamides by contacting polyamides having a relative solution viscosity ηrel in the range from 1.5 to 2.0, measured in 0.5% m-cresol solution at 25° C., with an alcoholic medium in the presence of inorganic particles under the action of pressure and/or temperature to generate an at least partial solution, and then precipitating the polyamide from the at least partial solution, characterized in that a suspension of the inorganic particles suspended in the alcoholic medium is used. The resulting ultrafine polyamide powders have a specific BET surface area in the range of 5-100 m2/g; a fineness d50 of less than 70 μm; an apparent density AD in the range from 250 to 1000 g/l; and a particle content of 0.1 to 80% by weight of inorganic particles based on the total weight of the polyamide powder. They are equally suitable for coatings and for moldings and components with improved mechanical properties.

    摘要翻译: 通过使具有相对溶液粘度和相对浓度的相对比例在1.5至2.0的范围内的聚酰胺制备基于聚酰胺制备的超细粉末的方法,其在25℃的0.5%间甲酚溶液中,在无机物存在下用醇介质 颗粒在压力和/或温度的作用下产生至少部分溶液,然后从至少部分溶液沉淀聚酰胺,其特征在于使用悬浮在醇介质中的无机颗粒的悬浮液。 所得的超细聚酰胺粉末的比BET比表面积在5-100m 2 / g的范围内; 细度d50小于70μm; 在250〜1000g / l范围内的表观密度AD; 和基于聚酰胺粉末的总重量的无机颗粒的0.1〜80重量%的颗粒含量。 它们同样适用于具有改善的机械性能的涂料和模制品和组分。

    Method and device for producing dispersions
    5.
    发明授权
    Method and device for producing dispersions 有权
    生产分散体的方法和装置

    公开(公告)号:US07538142B2

    公开(公告)日:2009-05-26

    申请号:US10584464

    申请日:2004-12-01

    IPC分类号: B01F5/02 B01F3/10 B01F5/10

    摘要: A method and device for producing a finely divided dispersion of solids having a mean particle size of 10 nm to 10 µm, in which at least two flows of a predispersion are sprayed by means of pumps, preferably high-pressure pumps, through one nozzle each into a grinding chamber enclosed by a reactor housing onto a collision point, wherein the grinding chamber is flooded with the predispersion and the finally divided dispersion is removed from the grinding chamber by the overpressure of the predispersion continuing to flow into the grinding chamber.

    摘要翻译: 一种用于生产平均粒径为10nm至10μm的细分散固体分散体的方法和装置,其中通过泵,优选高压泵将至少两个预分散液流喷射至每个 进入由反应器壳体围绕在碰撞点上的研磨室中,其中研磨室充满预分散体,并且最终分散的分散体通过预分散体的超压继续流入研磨室而从研磨室移除。

    Stabilized, aqueous silicon dioxide dispersion
    8.
    发明授权
    Stabilized, aqueous silicon dioxide dispersion 有权
    稳定的二氧化硅水分散体

    公开(公告)号:US07374787B2

    公开(公告)日:2008-05-20

    申请号:US10644755

    申请日:2003-08-21

    IPC分类号: A23L2/70 C12H1/00

    摘要: An aqueous dispersion, having a silicon dioxide powder having a silicon dioxide content of 10 to 60 wt.%, wherein the aqueous dispersion is stable in the pH range of 2 to 6, the aqueous dispersion additionally contains at least one compound, which is at least partially soluble in aqueous solution in the pH range 2 to 6 in the form of polyvalent cations, these being stable in a silicate-like environment as an anionic component of the particle surface of the silicon dioxide powder, the quantity of cation-providing compound in relation to the surface of the silicon dioxide is 0.001 to 0.1 mg cation-providing compound/m2 silicon dioxide surface, the cation-providing compound being calculated as the oxide, and the zeta potential of the aqueous dispersion has values of less than or equal to zero.

    摘要翻译: 一种水分散体,其二氧化硅粉末的二氧化硅含量为10至60重量%,其中水分散体在pH范围为2至6时是稳定的,水分散体还含有至少一种化合物,其在 在多价阳离子形式的pH范围2〜6的水溶液中最少部分溶解,这些在作为二氧化硅粉末的粒子表面的阴离子成分的硅酸盐样环境中稳定,提供阳离子的化合物的量 相对于二氧化硅的表面为0.001〜0.1mg的提供阳离子的化合物/ m 2二氧化硅表面,阳离子提供化合物以氧化物计算,并且水溶液的ζ电位 色散的值小于或等于零。

    Process for the production of metal oxide and metalloid oxide dispersions
    9.
    发明授权
    Process for the production of metal oxide and metalloid oxide dispersions 有权
    用于生产金属氧化物和类金属氧化物分散体的方法

    公开(公告)号:US08529651B2

    公开(公告)日:2013-09-10

    申请号:US12894539

    申请日:2010-09-30

    摘要: 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.

    摘要翻译: 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。