利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

6 条记录 (耗时 0.01 秒)

    Pocket air velocity gauge
    1.
    发明授权
    Pocket air velocity gauge 失效
    口袋风速表

    公开(公告)号：US4713972A

    公开(公告)日：1987-12-22

    申请号：US876225

    申请日：1986-06-19

    申请人： Hans-Dieter Stockburger

    发明人： Hans-Dieter Stockburger

    IPC分类号： G01P5/04 ,  G01F1/28

    CPC分类号： G01P5/04

    摘要： In a pocket air velocity gauge, in order to expand the controlled, flow-dependent pointer deflection and the measuring scale to an angular range of at least 270.degree., the air flows through an inlet opening (22) on the back of a housing into a ring channel (12) extending around a pointer shaft (6) and over about 360.degree. and leaves it through a lateral outlet opening (13). In so doing, the air moves an air vane (37) fastened to the pointer shaft (6) counter to a restoring spring force in proportion to the velocity of the air. The ring channel (12) is provided with a cross section widening in the flow direction, and the pointer shaft (6) has assigned to it a second restoring spring which becomes active only after a certain angle deflection of the pointer.

    摘要翻译： 在口袋式空气流量计中，为了将控制的，依赖于流量的指针偏转和测量标尺扩展至至少270°的角度范围，空气流过壳体背面的入口（22），进入 围绕指针轴（6）延伸并超过约360度的环形通道（12），并通过侧向出口（13）离开。 在这样做时，空气与固定在指针轴（6）上的空气叶片（37）相对于与空气的速度成比例的恢复弹簧力移动。 环形通道（12）具有在流动方向上变宽的横截面，并且指针轴（6）已经分配给第二恢复弹簧，该第二恢复弹簧仅在指针的一定角度偏转之后才起作用。

    Method of separation by fractional crystallization from a liquid mixture
    3.
    发明授权
    Method of separation by fractional crystallization from a liquid mixture 失效
    通过从液体混合物中分级结晶分离的方法

    公开(公告)号：US4493719A

    公开(公告)日：1985-01-15

    申请号：US479005

    申请日：1983-03-25

    申请人： Klaus Wintermantel ,  Dieter Stockburger ,  Hugo Fuchs

    发明人： Klaus Wintermantel ,  Dieter Stockburger ,  Hugo Fuchs

    IPC分类号： B01D9/04 ,  B01D9/00 ,  B01D9/02 ,  C07C37/84 ,  C07C39/14 ,  C07C51/43

    CPC分类号： B01D9/0013 ,  C07C37/84 ,  C07C51/43

    摘要： A method of separation by fractional crystallization from a liquid mixture in which the liquid mixture is repeatedly passed in turbulent flow through an indirectly cooled crystallization zone, which must be kept full. The liquid remaining after deposition of a layer of crystals on the wall of the crystallization zone is removed, whereupon the surface of the layer of crystals is washed and the crystals are melted by passing a melt of similar compositions to that of the layer of crystals through the crystallization zone. During crystallization the melt is maintained at the temperature of crystallization and crystallization is stopped when the frozen fraction is from 70 to 98%.

    摘要翻译： 通过分液结晶从液体混合物中分离的方法，其中液体混合物在湍流中重复通过间接冷却的结晶区，其必须保持充满。 去除在结晶区壁上沉积晶体层后剩余的液体，由此洗涤晶体层的表面，通过使具有类似组成的熔体与晶体层的熔体相融合，使晶体熔融 结晶区。 在结晶期间，熔体保持在结晶温度，当冷冻级分为70-98％时，结晶停止。

    Separation of a mixture of C.sub.4 -hydrocarbons by extractive distillation
    4.
    发明授权
    Separation of a mixture of C.sub.4 -hydrocarbons by extractive distillation 失效
    通过萃取蒸馏分离C {HD 4 {B-烃的混合物

    公开(公告)号：US4162198A

    公开(公告)日：1979-07-24

    申请号：US906469

    申请日：1978-05-17

    申请人： Dieter Stockburger ,  Klaus Volkamer ,  Detlef Bender ,  Klaus-Juergen Schneider ,  Harald Schwentker ,  Ulrich Wagner ,  Hans-Martin Weitz

    发明人： Dieter Stockburger ,  Klaus Volkamer ,  Detlef Bender ,  Klaus-Juergen Schneider ,  Harald Schwentker ,  Ulrich Wagner ,  Hans-Martin Weitz

    IPC分类号： B01D3/40 ,  C07C1/00 ,  C07C7/08 ,  C07C9/00 ,  C07C11/00 ,  C07C11/167 ,  C07C67/00 ,  B01D3/06

    CPC分类号： C07C7/08 ,  B01D3/40 ,  Y10S203/20

    摘要： A process for separating, by means of a selective solvent, a mixture of C.sub.4 -hydrocarbons which contains some hydrocarbons which are more soluble in the selective solvent and some which are less soluble therein, in which process the hydrocarbon mixture is separated, in an extractive distillation zone, into a top product which contains the less soluble hydrocarbons and an extract which contains the more soluble hydrocarbons and the selective solvent, the extract, taken off as the bottom product, is subjected to a flash evaporation and the resulting vapor component of the extract is recycled to the extractive distillation zone while the liquid phase remaining after the flash evaporation is fed to a solvent recovery zone, in which the liquid phase obtained from the flash evaporation is separated into a product containing the hydrocarbons and, as the bottom product, the selective solvent which has been freed from the hydrocarbons, the resulting selective solvent is recycled to the extractive distillation zone and the product which is obtained from the solvent recovery zone and contains the hydrocarbons is partially or completely recycled to the extractive distillation zone, after increasing the pressure in a compression zone, in which process the extract taken off the extractive distillation zone is brought, prior to the flash evaporation to a higher pressure than the pressure in the extractive distillation zone and thereafter the extract which is under this higher pressure is heated, in a heat exchange zone, by indirect heat exchange with the selective solvent obtained as the bottom product from the solvent recovery zone, and the heated extract is subsequently let down, in the flash evaporation, to a pressure which is at least equal to the pressure in the extractive distillation zone and is higher than the pressure in the solvent recovery zone.

    摘要翻译： 通过选择性溶剂分离出含有一些较易溶于选择性溶剂的烃和一些较不溶于其中的烃类的混合物的混合物的方法，在该方法中，烃混合物在萃取过程中分离 蒸馏区，成为含有较少溶解性烃的顶部产物和含有较多可溶性烃和选择性溶剂的提取物，作为底部产物取出的萃取物进行闪蒸，并将得到的蒸气成分 萃取液再循环到萃取蒸馏区，闪蒸蒸发后剩余的液相被送入溶剂回收区，其中将从闪蒸蒸发获得的液相分离成含有烃的产物，作为底部产物， 已经从烃中除去的选择性溶剂，所得到的选择性溶剂被再循环到萃取物中 蒸馏区和从溶剂回收区获得并且含有烃的产物在增加压缩区中的压力之后部分或完全再循环到萃取蒸馏区，在该过程中，提取物从萃取蒸馏区被带走 在闪蒸蒸发到比萃取蒸馏区中的压力高的压力之前，然后将在该较高压力下的提取物在热交换区域中与作为底部产物获得的选择性溶剂进行间接热交换 然后将被加热的提取物在闪蒸中降至至少等于萃取蒸馏区压力的压力，并高于溶剂回收区的压力。