Distiller for liquids, liquids distillation method and equipment for treating sewage, which equipment includes said distiller
    1.
    发明申请
    Distiller for liquids, liquids distillation method and equipment for treating sewage, which equipment includes said distiller 审中-公开
    液体蒸馏器,液体蒸馏方法和处理污水的设备,该设备包括所述蒸馏器

    公开(公告)号:US20050051418A1

    公开(公告)日:2005-03-10

    申请号:US10480501

    申请日:2002-05-30

    申请人: Ramiro Lama

    发明人: Ramiro Lama

    摘要: The distiller includes an exchanger (6) of tubes (7) which fill with the liquid to be treated, means (14) of heating, means (23) for compressing the steam from evaporation of the liquid, means (24) for feeding the compressed steam around the tubes (7) and means (27, 28) for inducing turbulence into the liquid, preferably by making the compressed steam bubble inside it. The method includes heating the liquid and supplying it to the tubes of the exchanger, compressing the resulting steam and bringing it into contact with the exterior of the tubes. The equipment uses a distiller such as that described. The invention permits treatment of sewage and other liquids by distillation, with minimum energy consumption and in a small space.

    摘要翻译: 蒸馏器包括一个装有待处理液体的管道(7)的交换器(6),加热装置(14),用于压缩来自蒸发液体的蒸汽的装置(23),用于将 围绕管(7)的压缩蒸汽和用于将湍流引入液体的装置(27,28),优选地通过在其内部形成压缩的蒸气泡。 该方法包括加热液体并将其提供给交换器的管,压缩所得蒸汽并使其与管的外部接触。 设备使用如所述的蒸馏器。 本发明允许通过蒸馏处理污水和其它液体,具有最小的能量消耗和小的空间。

    Water distillation and aeration apparatus
    2.
    发明授权
    Water distillation and aeration apparatus 失效
    水蒸馏和曝气装置

    公开(公告)号:US5332476A

    公开(公告)日:1994-07-26

    申请号:US978302

    申请日:1992-11-17

    申请人: Naisin Lee

    发明人: Naisin Lee

    摘要: An apparatus and method for fluid distillation in general, and in particular, of water, adapted for consumer or home use, but capable of being made and operated so that it is suitable for separating solvents and solutes and other industrial use. The apparatus includes a housing having divider structure to form one or more compartments for receiving water to be distilled. The divider structure also presents a fluid passage for receiving water vapor which is formed when the upper portion of the water in the housing is boiled by a heater. An aerator is provided in the housing below the heater and in a location within the water compartment. The aerator operates to direct air under a slight pressure into the water so that air bubbles can be generated in the water. The air bubbles will rise and break the surface of the water as the upper part of the water is being boiled by the heater. This causes a vapor pressure to be generated in the space above the water level and water vapor is then caused to move through the fluid passage downwardly to a lower chamber in which the water vapor is collected as a condensate. As the water vapor moves downwardly in the fluid passage, it moves in heat exchange relationship to the water in the compartment of the housing. Several embodiments of the housing of the present invention are disclosed herein.

    摘要翻译: 一般用于流体蒸馏的装置和方法,特别是用于消费者或家庭使用的水,但能够制造和操作的装置和方法,使其适用于分离溶剂和溶质以及其它工业用途。 该装置包括具有分隔结构的壳体,以形成用于接收待蒸馏水的一个或多个室。 分隔结构还具有用于接收水蒸气的流体通道,该水蒸汽在壳体中的水的上部被加热器煮沸时形成。 在加热器下方的壳体中以及在水舱内的位置中设置一个充气器。 曝气器用于将微气压的空气引导到水中,使得在水中产生气泡。 当水的上部被加热器煮沸时,气泡会上升并破坏水面。 这导致在水位上方的空间中产生蒸汽压力,然后使水蒸汽通过流体通道向下移动到下部室,在该下部室中收集水蒸汽作为冷凝物。 当水蒸汽在流体通道中向下移动时,其与壳体的隔室中的水以热交换关系移动。 本文公开了本发明的外壳的几个实施例。

    Evaporation of liquids with dispersant added
    3.
    发明授权
    Evaporation of liquids with dispersant added 失效
    用分散剂蒸发液体

    公开(公告)号:US5156706A

    公开(公告)日:1992-10-20

    申请号:US187817

    申请日:1988-04-29

    申请人: Hugo H. Sephton

    发明人: Hugo H. Sephton

    IPC分类号: B01D1/00 B01D1/10

    摘要: A vertical tube evaporation process for the concentration of saline water and other liquids, including the addition of an anionic mono-molecular dispersant thereto which interacts with materials precipitated during concentration and inhibits the formation of scale or fouling depositions on evaporator surfaces, and wherein the additive is incorporated into the precipitated materials and improves their removal during the descaling or defouling of evaporator surfaces by rendering such precipitates redispersable in fresh water or in a non-saturated liquid used for descaling or defouling of evaporator surfaces.

    摘要翻译: 用于浓缩盐水和其他液体的垂直管蒸发方法,包括向其中加入阴离子单分子分散剂,其与浓缩期间沉淀的物质相互作用并且抑制蒸发器表面上的垢或结垢沉积,并且其中添加剂 通过使这种沉淀物可再分散在淡水中或在用于除垢或除垢蒸发器表面的非饱和液体中,在蒸发器表面除垢或除垢之前将其并入沉淀的材料中并改善其去除。

    Stripping column installation for separating materials with high boiling
point difference
    4.
    发明授权
    Stripping column installation for separating materials with high boiling point difference 失效
    用于分离材料的剥离柱安装具有高沸点差

    公开(公告)号:US5057190A

    公开(公告)日:1991-10-15

    申请号:US473877

    申请日:1990-02-02

    CPC分类号: B01D1/10 B01D3/322 Y10S203/20

    摘要: A stripping column installation especially for separating starting materials with a high boiling point difference comprises a stripping column having a withdrawal plate and a column sump, and a circulating boiler connected with the stripping column and having a pipe bundle through which a sump product from the stripping column flows. The circulating boiler has an upper plate and a separating wall which separates a space above the upper plate into two chambers. One of the chambers has a connection for receiving the sump product from the stripping column, while the other of the chambers has a connection for discharging the sump product after heating in the boiler. The circulating boiler is located relative to the stripping column so that a height difference is produced between a liquid level on the withdrawal plate of the stripping column and the upper plate of the circulating boiler, the height difference having a value selected so that a total pressure of a liquid column at each point of a first portion of a pipe path in the circulating boiler lies above the vapor pressure of the sump product to be heated.

    摘要翻译: 特别用于分离具有高沸点差的起始材料的汽提塔装置包括具有取出板和塔槽的汽提塔,以及与汽提塔连接并具有管束的循环锅炉,通过该管束从汽提塔 列流。 循环锅炉具有上板和分隔壁,将上板上方的空间分成两个室。 其中一个室具有用于从汽提塔接收集水器产品的连接,而另一个室具有用于在锅炉中加热之后排出集水器产品的连接。 循环锅炉相对于汽提塔定位,使得在汽提塔的取出板上的液面与循环锅炉的上板之间产生高度差,该高度差具有选择的值,使得总压力 在循环锅炉中的管道的第一部分的每个点处的液柱的位置高于待加热的贮槽产品的蒸汽压力。

    Vaporization of liquids
    6.
    发明授权
    Vaporization of liquids 失效
    液体蒸发

    公开(公告)号:US4765398A

    公开(公告)日:1988-08-23

    申请号:US46316

    申请日:1987-05-06

    申请人: Utah Tsao

    发明人: Utah Tsao

    IPC分类号: B01D1/10 F22B1/00

    CPC分类号: B01D1/10 Y10S165/183

    摘要: Two immiscible liquids are vaporized in heat exchanger tubes in a manner such that each tube receives both liquids and neither liquid is completely vaporized in the tubes.

    摘要翻译: 两种不混溶的液体在热交换器管中蒸发,使得每个管接收两种液体,并且两种液体在管中都没有完全蒸发。

    Falling strand devolatilization apparatus
    8.
    发明授权
    Falling strand devolatilization apparatus 失效
    脱链脱挥发器

    公开(公告)号:US3966538A

    公开(公告)日:1976-06-29

    申请号:US532339

    申请日:1974-12-13

    申请人: Carl G. Hagberg

    发明人: Carl G. Hagberg

    摘要: The invention relates to an improved falling strand devolatilization apparatus. Said apparatus includes in combination a flash chamber for devolatilizing an input material fed as heated falling strands from the tubes of a shell and tube heat exchanger mounted in gastight relationship to said flash chamber. Said heat exchanger tubes are fed by a first pump through a headerbonnet with volatiles being removed from said flash chamber by a second pump adapted to evacuate said chamber.

    摘要翻译: 本发明涉及一种改进的降链脱挥发分装置。 所述装置组合包括闪蒸室,用于使从作为加热的落下的股线供给的输入材料脱孔化,所述输入材料从与所述闪蒸室气密关系的壳管式热交换器的管安装。 所述热交换器管由第一泵通过主流通道,其中挥发物通过适于抽空所述室的第二泵从所述闪蒸室除去。

    Process and apparatus for separating liquids
    10.
    发明授权
    Process and apparatus for separating liquids 失效
    分离液体的方法和装置

    公开(公告)号:US3686077A

    公开(公告)日:1972-08-22

    申请号:US3686077D

    申请日:1970-04-01

    申请人: STAMICARBON

    发明人: KONING HENDRIK DE

    摘要: A PROCESS FOR THE SEPARATION OF LOWER BOILING POINT LIQUIDS FROM THOSE OF A HIGH BOILING POINT, AND APPARATUS THEREFOR IS DISCLOSED. THE LIQUID MIXTURE IS SUPPLIED TO THE BASE OF THE EXTRACTOR AND PASSED UPWARDS UNDER CONTROLLED TEMPERATURE AND REDUCED PRESSURE IN THE VAPOR STATE THROUGH SEVERAL TUBES, WHOSE LENGTH IS FROM 15 TO 35 TIMES THEIR DIAMETER; THE VAPOR LEAVES THE TUBES AT A

    VELOCITY APPROACHING THE VELOCITY OF SOUND IN THE VAPOR, AND IS SUBSEQUENTLY CONDENSED. THE LOWER BOILING LIQUID THUS RECOVERED IS OF HIGH PURITY, OFTEN REPRESENTING UP TO 90% OF THE TOTAL LOWER BOILING FRACTION OF THE MIXTURE ENTERING THE EVAPORATOR.