Process for preparation of coated peroxygen compounds
    1.
    发明授权
    Process for preparation of coated peroxygen compounds 有权
    涂层过氧化合物的制备方法

    公开(公告)号:US06239095B1

    公开(公告)日:2001-05-29

    申请号:US09348008

    申请日:1999-07-06

    IPC分类号: C11D300

    摘要: A process for the preparation of coated peroxygen compounds, in particular sodium percarbonate, by fluidized bed coating. By using a fluidized bed reactor with a radial inflow base, the passage openings of which allow the fluidized bed gas to emerge in the region of the opening at an angle of less than 35°, measured with respect to the horizontal, in the form of directed part streams, and in which are arranged spray nozzles, the pulse of which points in the same direction as the pulse of the fluidizing gas, it is possible to obtain products with an increased active oxygen stability. A circular reactor, the inflow base of which has lamellae overlapping like turbine blades and nozzles aligned in the direction of rotation of the fluidized bed is preferred.

    摘要翻译: 一种通过流化床涂层制备涂层过氧化合物,特别是过碳酸钠的方法。 通过使用具有径向流入基底的流化床反应器,其通道开口允许流化床气体以相对于水平方向测量的小于35°的角度以开口的区域出现,其形式为 定向部件流,其中布置有喷嘴,其脉冲指向与流化气体的脉冲相同的方向,可以获得具有增加的活性氧稳定性的产物。 圆形反应器,其流入基座具有如涡轮叶片重叠的薄片和沿流化床的旋转方向排列的喷嘴。

    Method for Production of Granular Sodium Percarbonate
    6.
    发明申请
    Method for Production of Granular Sodium Percarbonate 审中-公开
    颗粒过碳酸钠的生产方法

    公开(公告)号:US20100171230A1

    公开(公告)日:2010-07-08

    申请号:US12442865

    申请日:2007-07-17

    IPC分类号: B29B9/10

    CPC分类号: C01B15/103 B01J2/16

    摘要: The process for producing granular sodium percarbonate by fluidized bed buildup granulation comprises the spraying of an aqueous solution of hydrogen peroxide and of an aqueous solution of sodium carbonate with at least one multisubstance nozzle with external mixing into a fluidized bed comprising sodium percarbonate particles and simultaneously evaporating water, and is characterized in that the solution of sodium carbonate additionally comprises sodium carbonate and/or sodium percarbonate in suspended form and is passed through a dispersing apparatus for dispersion of solids before being fed to the multisubstance nozzle.The process allows the blockage of the multisubstance nozzle to be avoided and sodium percarbonate dust to be recycled from the offgas stream of the fluidized bed into the granulation.

    摘要翻译: 通过流化床堆积制粒生产颗粒状过碳酸钠的方法包括将过氧化氢水溶液和碳酸钠水溶液与至少一个多质量喷嘴进行外部混合喷入包含过碳酸钠颗粒的流化床中并同时蒸发 水,其特征在于,碳酸钠溶液另外包含悬浮形式的碳酸钠和/或过碳酸钠,并且在进料到多功能喷嘴之前通过用于分散固体的分散装置。 该过程允许避免多功能喷嘴的堵塞,并且将过碳酸钠粉尘从流化床的废气流再循环到造粒中。

    Process for the production of epoxide resins
    7.
    发明授权
    Process for the production of epoxide resins 失效
    环氧树脂生产工艺

    公开(公告)号:US4306054A

    公开(公告)日:1981-12-15

    申请号:US91654

    申请日:1979-11-05

    IPC分类号: C08G59/00 C08G59/06 C08G59/24

    摘要: The invention relates to the continuous production of epoxide resins of low, medium and high molecular weight, and also to their purification and to that of the waste water. No raw materials are required in addition to epichlorohydrin, 2,2-bis-(4-hydroxyphenyl)-propane, alkali hydroxide and water. The raw materials are fed at a shear rate of 7.5-50.times.10.sup.4 sec.sup.-1 (at a peripheral speed of the rotor of 15 to 50 m/sec and a distance of the rotor elements from the stator elements of 0.01 to 0.02 cm) continuously into a reactor and mixed in such a way that by the concentration of high kinetic energy in a very limited space the interfaces of the phases of the heterogeneous reaction mixture are increased to an extreme extent and the reagents are caused to react with one another within 5 sec. at the latest.The reaction proceeds very evenly in the reactor. By conversion of the kinetic energy and reaction heat of the chemical reaction the necessary reaction temperature is maintained for the reaction system within the reactor. The resins obtained and also their waste water are extracted in a pulsation unit in a counterflow, by means of water or organic solvents. This process enables epoxide resins of superior quality to be economically produced. The contamination of the waste water can be thus reduced to a minimum.

    摘要翻译: 本发明涉及连续生产低,中,高分子量的环氧树脂,以及它们的净化和废水的环氧树脂。 除表氯醇,2,2-双 - (4-羟基苯基) - 丙烷,碱金属氢氧化物和水外,不需要任何原料。 原料以7.5-50×104秒-1的转速(转子的圆周速度为15〜50m /秒,转子元件与定子元件的距离为0.01〜0.02cm)连续进入 反应器并以这样的方式混合,即通过在非常有限的空间中浓缩高动能,将非均相反应混合物的相的界面增加到极端程度,并使试剂在5秒内彼此反应 。 最新的 该反应在反应器中非常均匀地进行。 通过转化化学反应的动能和反应热,维持反应器内的反应体系所需的反应温度。 所获得的树脂及其废水通过水或有机溶剂在逆流中以脉动单元提取。 该方法能够经济地生产出优质的环氧树脂。 废水的污染因此可以降至最低。