利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

52 条记录 (耗时 0.015 秒)

    VERFAHREN UND VORRICHTUNG ZUR AUFBEREITUNG VON FLÜSSIGKEITEN
    2.
    发明公开
    VERFAHREN UND VORRICHTUNG ZUR AUFBEREITUNG VON FLÜSSIGKEITEN 有权
    方法和设备的处理流体

    公开(公告)号：EP1363855A1

    公开(公告)日：2003-11-26

    申请号：EP02719791.2

    申请日：2002-02-09

    申请人： Neubert, Susanne

    发明人： NEUBERT, Joachim ,  STAAB, Karl-Ferdinand

    IPC分类号： C02F1/04 ,  B01D3/34 ,  B01D3/06 ,  B01D3/42 ,  B01D1/28

    CPC分类号： C02F1/048 ,  B01D1/28 ,  B01D3/06 ,  B01D3/346 ,  Y10S159/27 ,  Y10S159/28 ,  Y10S203/08

    摘要： The invention relates to a method and a device for treating liquids as treatment fluids such as sea and/or brine water, which comprise a base liquid containing dissolved or undissolved impurities, essentially liquids and/or gaseous or salt forms. The liquid which is to be treated is introduced into at least one pre-heating/separating device (5, 8, 9, 14, 15, 16; 10, 11, 12, 17, 19; 5', 8', 9', 12', 13', 14', 5', 10', 11', 15', 16', 17) for pre-heating and pre-cleaning in such a manner that the liquid to be treated is pre-heated by a pre-heating heat exchanger (8, 11; 8', 10') to a temperature below boiling point of the base liquid. The impurities having a boiling point which is lower than the base liquid are evaporated, thermally expelled and disposed in a separator (9, 14, 15, 16; 12, 17, 18, 19; 9', 12', 13', 14', 11', 15', 16', 17'). Subsequently, a carrier gas is fed to the treatment liquid and the mixture obtained therefrom is evaporated to form a damp carrier gas-vapour mixture whereby the base liquid is evaporated and the liquid impurities whose boiling point is higher than the base liquid remain as a residue and /or all the salts contained in the base liquid remain in the form of brine. Subsequently, the damp carrier gas-vapour mixture is fed into a concentrate separator (30; 28') wherein the liquid residue and the brine are separated in the form of a concentrate. The carrier gas-vapour residue is fed into the condensate separator (38; 36'), wherein the condensate and the carrier gas are separated.

    APPARATUS FOR DESALINATING SALT WATER BY MEMBRANE DISTILLATION
    7.
    发明公开
    APPARATUS FOR DESALINATING SALT WATER BY MEMBRANE DISTILLATION 失效
    膜蒸馏脱盐装置

    公开(公告)号：EP0229150A1

    公开(公告)日：1987-07-22

    申请号：EP86904428.0

    申请日：1986-06-16

    申请人： SVENSKA UTVECKLINGS AB

    发明人： KJELLANDER, Nils ,  RODESJÖ, Bo

    IPC分类号： C02F ,  B01D61 ,  C02F1

    CPC分类号： B01D61/364 ,  Y10S159/27 ,  Y10S159/28 ,  Y10S203/04 ,  Y10S203/09 ,  Y10S203/18 ,  Y10S203/19

    摘要： Dans un appareil de dessalement d'eau de mer, une unité de distillation comprend une membrane hydrophobe poreuse perméable à la vapeur mais imperméable à l'eau et une surface de condensation disposée à une certaine distance de la membrane. L'agencement de distillation comprend également une première unité de chauffage et de transport de l'eau à distiller d'un côté de la membrane, et une deuxième unité de transport d'un liquide plus froid que l'eau, situé du côté de la surface de condensation éloigné de la membrane. L'eau distillée est collectée et aspirée entre la membrane et la surface de condensation. La première unité comprend des tuyaux en boucle fermée (11, 12, 13) connectés en série avec le côté chaud (10) de l'unité de distillation (1); la deuxième unité comprend des tuyaux en boucle fermée (14, 15, 16) connectés en série avec le côté froid (11) de l'unité de distillation (1). Un robinet de purge (17) aspire l'eau des tuyaux en boucle (11, 12, 13) de la première unité; une vanne de remplissage (20) et une conduite (23) aspirent l'eau des tuyaux en boucle (14, 15, 16) de la deuxième unité. Les tuyaux en boucle fermée de la première et de la deuxième unités sont reliés entre eux par une conduite de connexion (25). Un échangeur de chaleur (50) est connecté aux tuyaux en boucle (11, 12, 13) de la première unité pour fournir de l'énergie à l'eau présente dans les tuyaux en boucle de la première unité.

    摘要翻译： 在海水淡化装置中，蒸馏单元包括可渗透蒸气但不透水的多孔疏水膜和离膜设置一定距离的冷凝表面。 蒸馏装置还包括第一单元和第二单元，所述第一单元用于加热和输送待在膜的一侧上蒸馏的水，所述第二单元用于输送位于膜一侧的比水更冷的液体。 远离膜的冷凝表面。 蒸馏水被收集并吸入膜和冷凝表面之间。 第一单元包括与蒸馏单元（1）的热侧（10）串联连接的闭环管（11,12,13）; 第二单元包括与蒸馏单元（1）的冷侧（11）串联连接的闭环管（14,15,16）。 清洗阀（17）从第一单元的环管（11,12,13）吸取水; 填充阀（20）和管道（23）从第二单元的环管（14,15,16）吸入水。 第一和第二单元的闭环管通过连接线（25）相互连接。 热交换器（50）连接到第一单元的环管（11,12,13），用于向第一单元的环管中的水供应能量。

    WATER-SOLUBLE ORGANIC MATERIAL CONDENSATION APPARATUS
    9.
    发明公开
    WATER-SOLUBLE ORGANIC MATERIAL CONDENSATION APPARATUS 有权
    KONDENSATIONSVORRICHTUNGFÜRWASSERLÖSLICHEORGANISCHE STOFFE

    公开(公告)号：EP1452219A4

    公开(公告)日：2006-03-22

    申请号：EP01978832

    申请日：2001-10-19

    申请人： BUSSAN NANOTECH RES INST INC

    发明人： IKEDA SHIRO ,  NAKANE TAKASHI

    IPC分类号： B01D53/22 ,  B01D3/00 ,  B01D3/14 ,  B01D3/32 ,  B01D3/36 ,  B01D5/00 ,  B01D61/36 ,  B01D71/02 ,  C07C7/144

    CPC分类号： B01D61/362 ,  B01D3/14 ,  B01D3/143 ,  B01D3/146 ,  B01D3/322 ,  B01D53/228 ,  B01D71/028 ,  Y10S159/27 ,  Y10S159/28 ,  Y10S203/08

    摘要： A water-soluble organic material condensation apparatus equipped with a distillation column for distilling an aqueous solution of a water-soluble organic material, wherein a vapor generated at the top of the distillation column or a condensed liquid from the vapor is introduced to a device other than the distillation column which has the function to separate water from the water-soluble organic material to thereby condense the water-soluble organic material through separating water and then the condensed water-soluble organic material is recycled to the distillation column. The device other than the distillation column is desirably a separative film such as a zeolite film. The apparatus is improved in the operation of the upper portion of the condensation section of the distillation column and allows energy savings during distillation.

    摘要翻译： 一种水溶性有机材料冷凝装置，其配备有用于蒸馏水溶性有机材料的水溶液的蒸馏塔，其中在蒸馏塔顶部产生的蒸气或来自蒸汽的冷凝液体被引入到其它装置 比具有从水溶性有机材料分离水分的功能的蒸馏塔通过分离水浓缩水溶性有机材料，然后将冷凝的水溶性有机材料再循环到蒸馏塔中。 蒸馏塔以外的装置优选为沸石膜等分离膜。 该装置在蒸馏塔的冷凝段的上部的操作中得到改进，并且在蒸馏期间能够节省能量。

    VERFAHREN UND VORRICHTUNG ZUR AUFBEREITUNG VON FLÜSSIGKEITEN
    10.
    发明授权
    VERFAHREN UND VORRICHTUNG ZUR AUFBEREITUNG VON FLÜSSIGKEITEN 有权
    方法和设备的处理流体

    公开(公告)号：EP1363855B1

    公开(公告)日：2004-08-25

    申请号：EP02719791.2

    申请日：2002-02-09

    申请人： Neubert, Susanne

    发明人： NEUBERT, Joachim ,  STAAB, Karl-Ferdinand

    IPC分类号： C02F1/04 ,  B01D3/34 ,  B01D3/06 ,  B01D3/42 ,  B01D1/28

    CPC分类号： C02F1/048 ,  B01D1/28 ,  B01D3/06 ,  B01D3/346 ,  Y10S159/27 ,  Y10S159/28 ,  Y10S203/08

    摘要： The invention relates to a method and a device for treating liquids as treatment fluids such as sea and/or brine water, which comprise a base liquid containing dissolved or undissolved impurities, essentially liquids and/or gaseous or salt forms. The liquid which is to be treated is introduced into at least one pre-heating/separating device (5, 8, 9, 14, 15, 16; 10, 11, 12, 17, 19; 5', 8', 9', 12', 13', 14', 5', 10', 11', 15', 16', 17) for pre-heating and pre-cleaning in such a manner that the liquid to be treated is pre-heated by a pre-heating heat exchanger (8, 11; 8', 10') to a temperature below boiling point of the base liquid. The impurities having a boiling point which is lower than the base liquid are evaporated, thermally expelled and disposed in a separator (9, 14, 15, 16; 12, 17, 18, 19; 9', 12', 13', 14', 11', 15', 16', 17'). Subsequently, a carrier gas is fed to the treatment liquid and the mixture obtained therefrom is evaporated to form a damp carrier gas-vapour mixture whereby the base liquid is evaporated and the liquid impurities whose boiling point is higher than the base liquid remain as a residue and /or all the salts contained in the base liquid remain in the form of brine. Subsequently, the damp carrier gas-vapour mixture is fed into a concentrate separator (30; 28') wherein the liquid residue and the brine are separated in the form of a concentrate. The carrier gas-vapour residue is fed into the condensate separator (38; 36'), wherein the condensate and the carrier gas are separated.