Granulated fatty alcohol sulfate products
    84.
    发明授权
    Granulated fatty alcohol sulfate products 失效
    颗粒状脂肪醇硫酸盐产品

    公开(公告)号:US5539139A

    公开(公告)日:1996-07-23

    申请号:US377659

    申请日:1995-01-24

    摘要: A granulated fatty alcohol sulphate is characterized by a bulk density greater than 600 g/lit when no consolidation stress is imparted, it has a particle size-distribution such that at least 15% of the particles are larger than 1000 .mu.m, and less than 10% of the particles are smaller than 250 .mu.m, and has a bulk density which is dependent on the consolidation stress in the range 200 kg/cm.sup.2 to at least 750 kg/cm.sup.2.

    摘要翻译: 颗粒状脂肪醇硫酸盐的特征在于当不施加固结应力时,堆积密度大于600g / l,其具有使得至少15%的颗粒大于1000μm的粒度分布,并且小于 10%的颗粒小于250μm,并且具有取决于200kg / cm 2至至少750kg / cm 2范围内的固结应力的堆积密度。

    Process for producing granular detergent composition
    85.
    发明授权
    Process for producing granular detergent composition 失效
    生产颗粒洗涤剂组合物的方法

    公开(公告)号:US4478735A

    公开(公告)日:1984-10-23

    申请号:US376963

    申请日:1982-05-11

    摘要: A process for producing a granular detergent composition containing a surface active agent, a zeolite, an alkali metal silicate, and other detergent builder is described. This granular detergent composition is produced by either (1)(a) preparing an aqueous slurry containing, as a dispersing medium, the surface active agent;(b) bubbling a gas into the aqueous slurry to form a slurry containing bubbles having an average bubble diameter of 40 through 100 microns and having a specific gravity of 0.7 through 0.9;(c) mixing the resultant aqueous slurry with the zeolite, the alkali metal silicate, and the other builders to form a detergent slurry; and(d) spray drying the detergent slurry to form the granular detergent composition or (2)(a) preparing a detergent slurry containing the surface active agent, the zeolite, the alkali metal silicate, and/or other detergent builders;(b) passing the detergent slurry through a centrifugal pump, while a gas is bubbled into the detergent slurry, whereby the detergent slurry containing bubbles having an average diameter of 40 through 100 microns and having a specific gravity of 0.7 through 0.9 is formed; and(c) spray drying the detergent slurry to form the granular detergent composition.

    摘要翻译: 描述了一种制备含有表面活性剂,沸石,碱金属硅酸盐和其它洗涤剂助洗剂的颗粒洗涤剂组合物的方法。 这种颗粒状洗涤剂组合物通过(1)(a)制备含有作为分散介质的表面活性剂的含水浆料来制备; (b)将气体鼓泡到含水浆料中以形成含有气泡直径为40-100微米,比重为0.7至0.9的气泡的浆料; (c)将所得含水浆料与沸石,碱金属硅酸盐和其它助洗剂混合以形成洗涤剂浆液; 和(d)喷雾干燥洗涤剂浆料以形成颗粒状洗涤剂组合物或(2)(a)制备含有表面活性剂,沸石,碱金属硅酸盐和/或其它洗涤剂助洗剂的洗涤剂浆料; (b)使清洁剂浆液通过离心泵,同时使气体鼓泡到洗涤剂浆液中,由此形成含有平均直径为40-100微米,比重为0.7至0.9的气泡的洗涤剂浆液; 和(c)喷雾干燥洗涤剂浆料以形成粒状洗涤剂组合物。

    Spray dried detergents containing sodium-potassium double silicate
    86.
    发明授权
    Spray dried detergents containing sodium-potassium double silicate 失效
    含有钠二氧化硅的喷雾干燥剂

    公开(公告)号:US3709837A

    公开(公告)日:1973-01-09

    申请号:US3709837D

    申请日:1970-12-30

    发明人: WELDES H

    IPC分类号: C11D3/08 C11D11/02 C11D7/14

    CPC分类号: C11D11/02 C11D3/08 Y10S159/14

    摘要: A method has been found for increasing the silicate content in spray dried detergents without decreasing the spray dryer throughput. The method involves the preparation of detergent slurries with high solids content by adding alkali metal silicates to the slurries in the form of sodium-potassium double silicate glass. Thus, the amount of water that must be removed in the drying tower is reduced and/or the silicate content can be increased when compared with slurries prepared with sodium silicate solutions.

    摘要翻译: 已经发现用于增加喷雾干燥洗涤剂中的硅酸盐含量而不降低喷雾干燥器生产量的方法。 该方法涉及通过向钠 - 钾双硅酸盐玻璃形式的浆料中加入碱金属硅酸盐来制备具有高固体含量的洗涤剂浆料。 因此,与用硅酸钠溶液制备的浆料相比,干燥塔中必须除去的水量减少和/或硅酸盐含量增加。

    Multilevel spray-drying method
    87.
    发明授权
    Multilevel spray-drying method 失效
    多级喷雾干燥方法

    公开(公告)号:US3629951A

    公开(公告)日:1971-12-28

    申请号:US6001170

    申请日:1970-07-31

    申请人: PROCTER & GAMBLE

    CPC分类号: C11D11/02 B01D1/18 Y10S159/14

    摘要: A method is provided for spray-drying large volumes of a synthetic detergent slurry which comprises spraying the slurry into the spray-drying chamber in at least two different levels of uniformly spaced atomizing nozzles. The lowest level of nozzles is critically positioned at a point in the spray chamber below a 190* F. isotherm and above a boiling point isotherm. From 30 to 80 percent of the slurry is atomized at this lowest level. The balance of the same slurry is sprayed through the remaining levels. Apparatus is provided for practicing this process.