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    • 71. 发明授权
    • Hot bed desalination process
    • 热床脱盐过程
    • US4218290A
    • 1980-08-19
    • US907953
    • 1978-05-22
    • John R. PhillipsRichard N. Jacobson
    • John R. PhillipsRichard N. Jacobson
    • C02F1/10C02B1/04
    • C02F1/10Y10S203/11
    • Aqueous saline solutions are converted in part to potable water by passing a compressed aqueous saline solution through one or more beds of contained pellets of higher temperature to heat the aqueous solution to a flash vaporization temperature, then passing the solution to one or more flash vaporization zones. Vaporized potable water from each vaporization zone is separately passed to contained bed of pellets where water is condensed and pellets heated. Simultaneously, a bed of pelletized solids is heated to supplant the highest temperature bed in the system used for heating. By selective switching of beds, the system is kept in continuous operation with a heated bed of pellets replacing the highest temperature bed previously used to heat the aqueous saline solution. The bed used for water condensation is transferred to the heating cycle for subsequent introduction to the system.
    • 通过使压缩的盐水溶液通过一个或多个含较高温度的颗粒的床将盐水溶液部分转化为饮用水,以将水溶液加热至闪蒸温度,然后将溶液通入一个或多个闪蒸区域 。 来自每个蒸发区的蒸发的饮用水分别通过含水的冷凝水和沉淀颗粒的颗粒。 同时,将加热的颗粒状固体床取代用于加热的系统中的最高温度床。 通过床的选择性切换,将系统保持在连续操作中,加热的颗粒团替代先前用于加热盐水溶液的最高温度的床。 用于水冷凝的床被转移到加热循环中,以便随后引入系统。
    • 72. 发明授权
    • Method for the transfer of heat
    • 换热方法
    • US4213830A
    • 1980-07-22
    • US835584
    • 1977-09-22
    • Franz Koppl
    • Franz Koppl
    • F22B1/00B01D1/26B01D3/06C02F1/04F28D19/00C02B1/04
    • B01D3/065B01D1/26C02F1/048Y10S203/08Y10S203/17
    • A method is provided for the transfer of heat from a source of thermal energy to at least one thermal user or heat consuming apparatus wherein waste water, such as from an industrial process, is used as the heat transfer medium and wherein a portion of the waste water flow is evaporated in an indirect heat exchanger under pressure to yield a mixture of steam and heated liquid waste water. The steam is supplied to an indirect heat exchanger for supplying heat to the heat consuming apparatus and the heated waste water is subsequently vaporized in a plurality of stages by reducing the pressure on the waste water in each stage and by using the steam formed by the vaporization in each stage to supply part of the heat of vaporization for the waste water in the subsequent stage. When the heat requirement of the heat consuming apparatus is reduced, the heat exchanger supplying heat to the heat consuming apparatus may be valved out of the system or the steam flow thereto may be reduced. With an increased waste water yield from the particular process, a portion of the pressurized steam formed therefrom in the high pressure evaporator which flows to the heat exchanger for the heat consuming apparatus may be diverted to another part of the system.
    • 提供了一种用于将热量从热能源传递到至少一个热用户或热消耗装置的方法,其中诸如来自工业过程的废水被用作传热介质,并且其中一部分废物 在间接热交换器中在压力下蒸发水流,得到蒸汽和加热的废液的混合物。 蒸汽被供给到用于向热消耗装置供热的间接热交换器,并且随后通过减少每个阶段中的废水的压力并且通过使用由蒸发形成的蒸汽在多个阶段中将被加热的废水蒸发 在每个阶段为后续阶段的废水提供部分蒸发热。 当热消耗装置的热量需求降低时,向热耗装置供热的热交换器可以被排出系统外,或者可以减少蒸汽流。 随着特定方法的废水产量增加,在高压蒸发器中形成的加压蒸汽的一部分流向用于热消耗装置的热交换器可以被转移到系统的另一部分。
    • 73. 发明授权
    • Geothermal mineral extraction system
    • 地热矿物提取系统
    • US4211613A
    • 1980-07-08
    • US855358
    • 1977-11-28
    • Milton Meckler
    • Milton Meckler
    • C02F1/14E21B43/28E21B43/40F24J3/08C02B1/04
    • C02F1/14E21B43/281E21B43/40F24J3/085Y02E10/14Y02W10/37Y10S159/902Y10S203/01Y10S203/11Y10S203/16
    • Minerals are recovered from warm geothermal brines by installing a brine eductor device such as a venturi at the end of a thermally insulated drill casing. The geothermal brine is recovered by flowing a warm, low saline carrier solution at high flow rate through the device to pick up a selected flow of brine. On entering the device the geothermal brine is diluted in an amount sufficient to preclude precipitation and scaling as the mixture flows to the surface. The flow velocity is adequate to entrain any non-dissolved solids without settlement. Thermal losses to the surrounding strata are minimized by the thermal insulation surrounding the casing. The mineral values are recovered from the mixture by flashing, evaporation, and filtration. Clarified solution, filter liquor and make-up water as necessary are combined to form the low salinity carrier solution which is heated in heat exchangers before recycling to the eductor device. The heat exchange fluid may be heated by solar concentrators assisted by fossil fuel, geothermal and/or solar buffer stages.
    • 通过在绝热钻套的末端安装诸如文丘里管的盐水喷射器装置,从温暖的地热盐水中回收矿物质。 通过将高温低温盐水载体溶液以高流速流过该装置以拾取选定的盐水流来回收地热盐水。 在进入设备时,地热盐水的稀释量足以防止混合物流入表面时出现沉淀和结垢。 流速足以夹带任何不溶解的固体而不沉降。 通过围绕套管的隔热将周围地层的热损失最小化。 通过闪蒸,蒸发和过滤从混合物中回收矿物质值。 将澄清溶液,滤液和补充水组合起来形成低盐度载体溶液,该溶液在热交换器中被加热到再循环到喷射装置之前。 热交换流体可以由化石燃料,地热和/或太阳能缓冲段辅助的太阳能集中器加热。
    • 74. 发明授权
    • Apparatus for desalinating water
    • US4211609A
    • 1980-07-08
    • US869000
    • 1978-01-12
    • Richard E. Diggs
    • Richard E. Diggs
    • B01D3/00B01D3/10C02F1/14C02B1/04F24J3/02
    • C02F1/14B01D3/00B01D3/10Y02W10/37Y10S159/903Y10S203/01
    • An apparatus and method for removing contaminants from water having solid contaminants dissolved therein. Contaminated water flows across a grid and into a storage tank. The grid utilizes solar energy to heat that water to a predetermined temperature. A heat transfer structure which is dome-shaped and receives water from the storage tank and a preheater means utilizing solar energy heats the water to a further predetermined temperature. An evaporator means receives the heated water and exposes it to a vacuum condition so that the temperature of the water is above the saturation temperature. The water is thus vaporized, and solid contaminants dissolved therein are separated therefrom. The solids are deposited on a plurality of moving belts and are then moved into a solids removal system. The solids removal system comprises a plurality of trap door pairs upon which the solids are deposited and which are sequentially opened so that the vacuum conditions existing in the evaporator are not disturbed. Vapor transferring means removes the water vapor from the evaporator and transfers it to the heat transfer structure wherein it is condensed to form distillate which is free of solid contaminants. Distillate removal means then removes the distillate from the heat transfer structure to collection or usage means.
    • 75. 发明授权
    • Apparatus for desalinating water
    • US4199406A
    • 1980-04-22
    • US868998
    • 1978-01-12
    • Richard E. Diggs
    • Richard E. Diggs
    • B01D3/00B01D3/10C02F1/14C02B1/04F24J3/02
    • C02F1/14B01D3/00B01D3/10Y02W10/37Y10S203/01
    • An apparatus and method for removing contaminants from water having solid contaminants dissolved therein. Contaminated water flows across a grid and into a storage tank. The grid utilizes solar energy to heat that water to a predetermined temperature. A heat transfer structure which is dome-shaped and receives water from the storage tank and a preheater means utilizing solar energy heats the water to a further predetermined temperature. An evaporator means receives the heated water and exposes it to a vacuum condition so that the temperature of the water is above the saturation temperature. The water is thus vaporized, and solid contaminants dissolved therein are separated therefrom. The solids are deposited on a plurality of moving belts and are then moved into a solids removal system. The solids removal system comprises a plurality of trap door pairs upon which the solids are deposited and which are sequentially opened so that the vacuum conditions existing in the evaporator are not disturbed. Vapor transferring means removes the water vapor from the evaporator and transfers it to the heat transfer structure wherein it is condensed to form distillate which is free of solid contaminants. Distillate removal means then removes the distillate from the heat transfer structure to collection or usage means.
    • 77. 发明授权
    • Liquid purifying apparatus
    • 液体净化装置
    • US4194950A
    • 1980-03-25
    • US849931
    • 1977-11-09
    • Robert I. Zalles
    • Robert I. Zalles
    • C02F1/10C02F1/18C02B1/04
    • C02F1/18C02F1/10
    • Liquid purifying apparatus in which an infeed chamber, an evaporator chamber and a condenser chamber are arranged in that order along a flow path. A first inflatable bag is interposed across the flow path between the infeed chamber and the evaporator chamber, and a second inflatable bag is interposed across the flow path between the evaporator chamber and the condenser chamber. These bags are respectively located substantially entirely in the evaporator and condenser chambers, and the bags each comprise a flexible layer of highly absorbent fibrous material including a plurality of plies. The liquid to be purified is introduced into the infeed chamber, and it flows into the evaporator chamber to a level such that a portion of the first bag is immersed in the liquid. The liquid spreads by immersion and capillary action over substantially all of the fibers in the first bag to form thin liquid films along the individual fibers. Upon the introduction of air into the infeed chamber and through the first bag to the evaporator chamber, the bag inflates, and the air passes over the individual fibers to vaporize the liquid films. The vapor proceeds through the secong bag into the condenser chamber to inflate the second bag and form the condensate. Previously purified liquid is used to form thin films on the fibers of the second bag to provide an additional evaporation effect and thereby reduce the temperature within the condenser chamber. In some embodiments this cooling action is augmented by directing the residual vapor through a series of perforations in the wall of the condenser chamber in a manner such that a further evaporation effect takes place as the vapor is discharged.
    • 液体净化装置,其中进料室,蒸发器室和冷凝器室沿着流动路径按顺序排列。 第一可充气袋横跨进料室和蒸发器室之间的流动路径插入,并且第二可膨胀袋横跨蒸发器室和冷凝器室之间的流动路径插入。 这些袋分别基本上完全位于蒸发器和冷凝器室中,并且袋各自包括包含多个层的高吸收性纤维材料的柔性层。 将要净化的液体引入进料室,并将其流入蒸发器室中以使第一袋的一部分浸入液体中的水平。 液体通过浸泡和毛细管作用在第一袋中的基本上所有纤维上扩散,以形成沿着单个纤维的薄液膜。 当空气进入​​进料室并通过第一袋到蒸发器室时,袋膨胀,并且空气通过单独的纤维以蒸发液体膜。 蒸汽通过盛袋进入冷凝器室,以使第二袋膨胀并形成冷凝物。 先前纯化的液体用于在第二袋的纤维上形成薄膜,以提供额外的蒸发效果,从而降低冷凝器室内的温度。 在一些实施例中,这种冷却作用通过使残余蒸汽在冷凝器室的壁中引导一系列穿孔以使得随着蒸气排放而发生进一步的蒸发效应的方式来增强。