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166 条记录 (耗时 0.019 秒)

    Continuous process for making a non-Newtonian paste or cream like material
    102.
    发明授权
    Continuous process for making a non-Newtonian paste or cream like material 失效
    制作非牛顿酱或奶油样材料的连续工艺

    公开(公告)号：US5320832A

    公开(公告)日：1994-06-14

    申请号：US44422

    申请日：1993-04-09

    申请人： Rolando M. Catiis ,  Robin S. Cabanas ,  Joseph Binshtock

    发明人： Rolando M. Catiis ,  Robin S. Cabanas ,  Joseph Binshtock

    IPC分类号： A61K8/02 ,  A61K20060101 ,  A61K8/00 ,  A61K8/19 ,  A61K8/21 ,  A61K8/24 ,  A61K8/25 ,  A61K8/26 ,  A61K8/46 ,  A61K8/73 ,  A61K9/00 ,  A61K9/06 ,  A61K9/10 ,  A61Q11/00 ,  B01J20060101 ,  B01J13/00 ,  B01J14/00 ,  A61K7/16 ,  A61K7/18

    CPC分类号： A61Q11/00 ,  A61K8/02 ,  A61K8/24 ,  A61K8/73 ,  Y10S514/937 ,  Y10S514/944 ,  Y10S514/969 ,  Y10S516/924

    摘要： A continuous process for preparing a paste or cream like material which comprises the steps of means for forming under non vacuum conditions at a temperature of 90.degree. F. to 120.degree. F. a first low viscosity homogenous slurry of at least one non aqueous solvent and a gelling or bodying agent; means for forming a second low viscosity homogenous slurry under non vacuum conditions at a temperature of 90.degree. F. to 130.degree. F., means for forming a low viscosity mixture of said first low viscosity slurry and said second low viscosity slurry by a high shear mixing under non vacuum conditions at a temperature of 90.degree. F. to 130.degree. F. for 0.1 to 5 seconds; means for transforming under non vacuum and non mixing conditions at a temperature of 65.degree. F. to 120.degree. F. said low viscosity mixture into a non Newtonian mixture; and means for deaerating said non Newtonian mixture under vacuum conditions for a period of less than 3 seconds to form said paste or cream like material.

    摘要翻译： 一种用于制备糊状或膏状材料的连续方法，其包括以下步骤：在非真空条件下在90°F至120°F的温度下形成第一低粘度均匀浆液至少一种非水溶剂和 胶凝剂或凝胶剂; 用于在非真空条件下在90°F至130°F下形成第二种低粘度均匀浆料的装置，用于通过高剪切形成所述第一低粘度浆料和所述第二低粘度浆料的低粘度混合物的装置 在非真空条件下在90°F至130°F的温度下混合0.1至5秒; 用于在非真空和非混合条件下在65°F至120°F的温度下转化的装置。所述低粘度混合物变成非牛顿混合物; 以及用于在真空条件下使所述非牛顿混合物脱气少于3秒的时间的装置，以形成所述糊状或霜状材料。

    Bulk material reactor
    103.
    发明授权
    Bulk material reactor 失效
    散装物料堆

    公开(公告)号：US5305535A

    公开(公告)日：1994-04-26

    申请号：US688520

    申请日：1991-06-11

    申请人： Juergen Ritter

    发明人： Juergen Ritter

    IPC分类号： B01D46/34 ,  B01D53/08 ,  B01J20060101 ,  B01J8/12 ,  B01J8/16 ,  F26B17/12 ,  F26B25/00 ,  F26B9/00

    CPC分类号： F26B17/12 ,  B01D46/34 ,  B01D53/08 ,  B01J8/12 ,  B01J8/16 ,  F26B25/002 ,  B01D2259/40081 ,  B01D53/0446

    摘要： In a bulk material reactor comprising a reactor housing in which is arranged a travelling bed of 6,6' formed of bulk material 7,7', and a feed device 14-16-17 located on the top side, and a removal device 10 located on the underside of travelling bed 6,6,' as well as a gas inlet opening 2, and a gas outlet opening 3 located on various sides of travelling bed 6,6', the narrowing of gas-flow pathways through transfer device 10 is avoided and uniform flow-through pathways of equal length are provided for the gas flowing through the reactor whereby furthermore, travelling bed 6,6' is bounded along its lower side through staggered transfer plates 10 arranged in a cascade formation between which plates bulk material 7,7' collects to form an angle of repose 11 by means of which the trickling away of bulk material 7,7' is prevented while the system is stopped, whereby such transfer plates 10 can be moved backward and forward in such a way that motion in the transfer plates 10 permits bulk material 7,7' to fall therefrom, and whereby travelling bed 6,6' is designed on its top side with a surface 9 whose slope corresponds to that of staggered sloping transfer plates 10.

    摘要翻译： PCT No.PCT / EP90 / 01354 Sec。 371日期1991年6月11日 102（e）1991年6月11日PCT PCT 1990年8月20日PCT公布。 出版物WO91 / 02586 日期为1991年3月7日。在包括反应器壳体的散装材料反应器中，其中布置有由散装材料7,7'形成的6,6'的移动床，以及位于顶部的进料装置14-16-17 位于行进床6,6的下侧的移除装置10以及气体入口2和位于移动床6,6'的各侧的气体出口3，气体的变窄 通过转移装置10的流动路径被避免，并且为流过反应器的气体提供了相等长度的均匀流通通道，此外，行进床6,6'沿着其下侧限定了交错的传递板10 板之间形成层叠材料7,7'收集以形成休止角11，通过该角度，在系统停止时防止散装材料7,7'的滴落，由此可将这种转印板10向后移动 并以这样的方式前进，使得转印板10中的运动 允许散装材料7,7'从其中落下，并且由此在其顶侧设计了行进床6,6'，其表面9的斜面对应于交错的倾斜传递板10的斜面。

    Hazardous waste reactor system
    109.
    发明授权
    Hazardous waste reactor system 失效
    有害废物反应堆系统

    公开(公告)号：US4874587A

    公开(公告)日：1989-10-17

    申请号：US89573

    申请日：1987-08-26

    申请人： Terry R. Galloway

    发明人： Terry R. Galloway

    IPC分类号： B01D53/44 ,  A62D3/00 ,  B01D53/34 ,  B01D53/72 ,  B01D53/74 ,  B01J20060101 ,  B01J19/24 ,  C01B3/32 ,  C02F20060101 ,  C07B20060101 ,  C10B53/00 ,  F23G20060101 ,  F23G5/027 ,  F23G5/10 ,  F23G7/06

    CPC分类号： C10B53/00 ,  B01D53/72 ,  B01J19/243 ,  C01B3/32 ,  B01J2208/00061 ,  B01J2208/00415 ,  B01J2208/00495 ,  B01J2208/00513 ,  B01J2208/0061 ,  B01J2208/02 ,  Y10S588/90

    摘要： A method and reactor system are described for decomposing organic compounds. A gaseous mixture of organic compounds and water, equal to or in excess of stoichiometry, is passed into a first reaction zone having a temperature range between about 200.degree. C. and 1400.degree. C. The first reaction zone has a labyrinthine path which presents organically adsorbent surfaces to the gaseous mixture to provide a residence time in the first reaction zone sufficient to react substantially all of the gaseous organic compounds and the water at high rate. The effluent from the first reaction zone, still with water equal to or in excess of stoichiometry, is then passed to a second reaction zone having a temperature range between about 750.degree. C. and 1820.degree. C. to decompose the organic compounds remaining in the effluent. The first reaction zone is an annulus which is coaxial with and surrounds the second reaction zone. The labyrinthine path is formed by particulate ceramic material.

    摘要翻译： 描述了用于分解有机化合物的方法和反应器系统。 将等于或超过化学计量的有机化合物和水的气体混合物进入温度范围在约200℃至1400℃的第一反应区。第一反应区具有有机物呈现的迷宫路径 吸附剂表面到气态混合物，以提供在第一反应区中的停留时间，足以基本上以高速率反应所有气态有机化合物和水。 来自第一反应区的流出物仍然具有等于或超过化学计量的水然后被传递到温度范围在约750℃和1820℃之间的第二反应区，以将残留在 流出物。 第一反应区是与第二反应区同轴并且围绕第二反应区的环。 迷宫路径由颗粒陶瓷材料形成。