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52 条记录 (耗时 0.036 秒)

    Process for highly substituted carboxyalkyl celluloses and mixed ethers thereof
    1.
    发明授权
    Process for highly substituted carboxyalkyl celluloses and mixed ethers thereof 失效
    高度取代的羧基烷基纤维素及其混合醚的方法

    公开(公告)号：US4507474A

    公开(公告)日：1985-03-26

    申请号：US573164

    申请日：1984-01-24

    申请人： Wilfried Raehse ,  Norbert Kuehne ,  Willi Wuest ,  Konrad Engelskirchen

    发明人： Wilfried Raehse ,  Norbert Kuehne ,  Willi Wuest ,  Konrad Engelskirchen

    IPC分类号： C08B11/12 ,  C08B11/193 ,  C08B11/00

    CPC分类号： C08B11/193 ,  C08B11/12

    摘要： A process for the production of carboxyalkyl celluloses having an average degree of substitution of at least 1.0. The process comprises up to 3 stages, but without any intermediate purification. The preferred suspension medium is isopropanol. In each stage of the process, the carboxyalkylating agent is used in quantities of less than 2.5 moles per mole of anhydroglucose unit and the alkylating agent in quantities of less than 5 moles per mole of anhydroglucose unit. The total water content of the system throughout the reaction as a whole must not exceed 450% by weight, based on the quantity by weight of cellulose used. Water contents of from 80 to 250% by weight are preferred.

    摘要翻译： 平均取代度至少为1.0的羧基烷基纤维素的制造方法。 该方法包括多达3个阶段，但没有任何中间纯化。 优选的悬​​浮介质是异丙醇。 在该方法的每个阶段中，每摩尔葡糖酐单元和烷基化剂的量小于2.5摩尔/摩尔脱水葡萄糖单元，所述羧烷基化剂的用量小于2.5摩尔。 基于所使用的纤维素的重量，整个反应中的系统的总含水量不得超过450重量％。 水含量为80-250重量％是优选的。

    Process and means for the purification of cellulose ethers
    4.
    发明授权
    Process and means for the purification of cellulose ethers 失效
    用于纤维素醚净化的方法和方法

    公开(公告)号：US4968789A

    公开(公告)日：1990-11-06

    申请号：US238664

    申请日：1988-08-31

    申请人： Willi Wuest ,  Wilfried Raehse ,  Guenther Just ,  Dieter Kuehling ,  Siegfried Emde ,  Erhard Kuehn

    发明人： Willi Wuest ,  Wilfried Raehse ,  Guenther Just ,  Dieter Kuehling ,  Siegfried Emde ,  Erhard Kuehn

    IPC分类号： C08B11/20

    CPC分类号： C08B11/20

    摘要： Process and means for purifying cellulose ethers without flocculation points or with relatively high flocculation points (up to 95.degree. C.) and thermoplastic, i.e. highly propoxylated, products made from cellulose in any form, the crude product is first suspended and the suspension liquid subsequently separated in a reverse filter centrifuge a single-stage or multistage wash can be carried out. The filter cake is discharged by reversal of the filter cloth of the centrifuge.

    摘要翻译： 用于纯化纤维素醚的方法和方法，无需絮凝点或相对较高的絮凝点（高达95℃）和热塑性物质即高度丙氧基化的任何形式的纤维素制成的产品，首先将粗产物悬浮，然后悬浮液 在反向过滤离心机中分离可以进行单级或多级洗涤。 滤饼通过反转离心机的滤布排出。

    Process for working up water-soluble cellulose derivatives having high flocculation points
    5.
    发明授权
    Process for working up water-soluble cellulose derivatives having high flocculation points 失效
    处理高絮凝点的水溶性纤维素衍生物的方法

    公开(公告)号：US5013832A

    公开(公告)日：1991-05-07

    申请号：US86439

    申请日：1987-08-17

    申请人： Wilfried Raehse ,  Willi Wuest ,  Guenther Just

    发明人： Wilfried Raehse ,  Willi Wuest ,  Guenther Just

    IPC分类号： C08B11/20

    CPC分类号： C08B11/20

    摘要： A process for working up water-soluble cellulose derivatives, more especially with flocculation points above 85.degree. C., after removal by condensation of readily volatile constituents of the crude product mixture resulting from an etherification reaction, by suspension of the crude product in hot water and subsequent separation of the suspension and washing liquids, wherein the separation of the suspension and washing liquids is carried out at elevated temperature and under pressure applied to the separator as a whole.

    摘要翻译： 通过将粗产物悬浮在热水中，处理水溶性纤维素衍生物的方法，更特别是絮凝点高于85℃，通过由醚化反应产生的粗产物混合物容易挥发成分的冷凝除去后， 以及随后分离悬浮液和洗涤液体，其中悬浮液和洗涤液体的分离在升高的温度和施加到分离器整体的压力下进行。

    Crossflow microfiltration process for the separation of biotechnologically produced materials
    7.
    发明授权
    Crossflow microfiltration process for the separation of biotechnologically produced materials 失效
    用于分离生物技术生产材料的交叉流微量过程

    公开(公告)号：US4751003A

    公开(公告)日：1988-06-14

    申请号：US858408

    申请日：1986-05-01

    申请人： Wilfried Raehse ,  Franz-Josef Carduck ,  Norbert Kuehne

    发明人： Wilfried Raehse ,  Franz-Josef Carduck ,  Norbert Kuehne

    IPC分类号： B01D37/00 ,  C12M1/12 ,  C12N1/02 ,  C12N9/50 ,  C12N9/52 ,  C12P1/00 ,  B01D13/00 ,  C12N9/48

    CPC分类号： C12P1/00 ,  B01D61/147 ,  B01D63/06 ,  C12M29/02 ,  C12M33/14 ,  C12M47/10 ,  C12N9/50 ,  B01D2315/10 ,  Y10S435/814

    摘要： The invention relates to a process for the separation of biotechnologically produced valuable materials form a cell suspension by crossflow microfiltration to obtain an high specific permeate flux while retention stays near 0% for long periods. To enable crossflow microfiltration to be carried out on an industrial scale in biotechnology in the separation of biotechnologically produced extracellular valuable materials from a cell suspension, particularly in the separation of alkaline protease for recovering enzyme, under economically acceptacle conditions, alkaline protease of relatively high molecular weight, more especially enzyme >20,000 daltons, is separated from a fermenter solution using polysulfone tubes having micropore diameters of from 0.3 to 0.5 .mu.m at a rate of flow of the fermenter solution of from 3 to 6 m/s parallel to the membrane surface and with a pressure difference between the concentrate side and the permeate side of 2 bar, the ratio of the mean pore diameter of the membrane to the size of the microorganisms remaining in the concentrate being between 0.15 and 0.85

    摘要翻译： 本发明涉及通过交叉流微量过滤分离生物技术生产的有价值物质形成细胞悬浮液以获得高比浓度渗透通量的方法，同时保持长时间保持在0％附近。 为了使生物技术中的生物技术生产的细胞外有价值物质从细胞悬浮液分离，特别是在经济接受条件下分离用于回收酶的碱性蛋白酶的交叉流微量过滤，相对高分子量的碱性蛋白酶 重量，更特别是> 20,000道尔顿，使用平均于膜表面的发酵罐溶液流速为3至6m / s的流速，使用具有0.3-0.5μm微孔直径的聚砜管从发酵罐溶液中分离 并且浓缩物侧和渗透侧之间的压力差为2巴时，膜的平均孔径与保留在浓缩物中的微生物的尺寸之比在0.15和0之间。

    Coated enzyme preparation for detergents and cleaning formulations
    8.
    发明授权
    Coated enzyme preparation for detergents and cleaning formulations 失效
    用于洗涤剂和清洁剂的涂层酶制剂

    公开(公告)号：US5719115A

    公开(公告)日：1998-02-17

    申请号：US578526

    申请日：1996-03-05

    申请人： Kathleen Paatz ,  Wilfried Raehse ,  Werner Pichler ,  Norbert Kuehne ,  Horst Upadek

    发明人： Kathleen Paatz ,  Wilfried Raehse ,  Werner Pichler ,  Norbert Kuehne ,  Horst Upadek

    IPC分类号： C11D3/386 ,  C11D17/00 ,  C12N9/98 ,  C12N11/04 ,  C11D1/68 ,  C11D3/40

    CPC分类号： C12N9/98 ,  C11D17/0039 ,  C11D3/38672 ,  C12N11/04

    摘要： Enzyme granules containing an enzyme, an inorganic or organic carrier material and a uniform outer pigment-containing coating layer on the granules, wherein the outer coating layer contains 30 to 50% by weight of fine-particle inorganic pigment, 45 to 60% by weight of an alcohol or alcohol mixture having a melting point of from 45.degree. C. to 65.degree. C., up to 15% by weight of an emulsifier for the alcohol or alcohol mixture, up to 5% by weight of a dispersant for the pigment and up to 3% by weight of water, based on the weight of the outer coating layer.

    摘要翻译： PCT No.PCT / EP94 / 02079 Sec。 371日期：1996年3月5日 102（e）1996年3月5日PCT PCT。1994年6月27日PCT公布。 公开号WO95 / 02031 日期1995年1月19日在颗粒上含有酶，无机或有机载体材料和均匀的外层颜料的涂层的酶颗粒，其中外涂层含有30〜50重量％的微粒无机颜料，45 至60重量％的熔点为45℃至65℃的醇或醇混合物，至多15重量％的用于醇或醇混合物的乳化剂，至多5重量％ 用于颜料的分散剂和至多3重量％的水，基于外涂层的重量。

    Dry neutralisation method II
    10.
    发明申请
    Dry neutralisation method II 审中-公开
    干中和法二

    公开(公告)号：US20050245425A1

    公开(公告)日：2005-11-03

    申请号：US11148825

    申请日：2005-06-09

    申请人： Bernhard Orlich ,  Gerhard Blasey ,  Hans-Friedrich Kruse ,  Wilfried Raehse

    发明人： Bernhard Orlich ,  Gerhard Blasey ,  Hans-Friedrich Kruse ,  Wilfried Raehse

    IPC分类号： C11D11/00 ,  C11D17/06 ,  C11D17/00

    CPC分类号： C11D17/065 ,  C11D11/0088 ,  C11D17/06

    摘要： A process for making detergent granules having a bulk density of 300 to 700 g/l. A solid carrier containing neutralizing agent is mixed in a rotating mixer with a liquid binding agent containing surfactant acid to forma partially granulated premixture. The premixture is fluidized, sprayed with additional binder, and granulated in a fluidized bed reactor to form the detergent granules.

    摘要翻译： 一种制备体积密度为300-700g / l的洗涤剂颗粒的方法。 将含有中和剂的固体载体在旋转混合器中与含有表面活性剂酸的液体粘合剂混合以形成部分颗粒状预混合物。 将预混合物流化，用另外的粘合剂喷雾，并在流化床反应器中造粒形成洗涤剂颗粒。