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    • 3. 发明申请
    • DEHYDRATOR
    • US20100206789A1
    • 2010-08-19
    • US12678673
    • 2009-01-13
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiHaruaki HirayamaYukio TanakaHideo KashiwagiKatsufumi Inoue
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiHaruaki HirayamaYukio TanakaHideo KashiwagiKatsufumi Inoue
    • B01D61/36
    • B01D61/362B01D61/58B01D2313/24B01D2317/022C07C29/76C07C31/08
    • Provided is a dehydrator that requires no excessively large apparatus structure and achieves cost-saving while maintaining suction efficiency at a desired level by use of suction means. A dehydrator 100 for separating water from a target liquid 13 includes at least two water separation membrane units 1a and 1b which are provided in series in a flow direction of the target liquid 13. The water separation membrane unit 1a on an upstream side out of the water separation membrane units 1a and 1b is connected to suction means 7 for sucking a gas phase containing water through one condenser 4, and the one condenser 4 condenses water in the gas phase and thereby separates the water. The gas phase sucked by the suction means 7 from the one condenser 4 is transferred to at least one downstream condenser 8 provided downstream of the one condenser 4, and the downstream condenser 8 condenses water in the gas phase and thereby separates the water. The water separation membrane unit 1b on a downstream side of the water separation membrane unit 1a is connected to a steam ejector 3, and the condenser 4 for condensing water in a gas phase passed through the steam ejector 3 condenses water and thereby separates the water.
    • 提供一种脱水机,其不需要过大的装置结构,并且通过使用抽吸装置将抽吸效率保持在期望的水平,从而节省成本。 用于从目标液体13分离水的脱水器100包括沿目标液体13的流动方向串联设置的至少两个水分离膜单元1a和1b。在上游侧的水分离膜单元1a 水分离膜单元1a和1b连接到抽吸装置7,用于通过一个冷凝器4吸入含有水的气相,并且一个冷凝器4冷凝气相中的水,从而分离水。 由抽吸装置7从一个冷凝器4吸入的气相被转移到设置在一个冷凝器4下游的至少一个下游冷凝器8,下游冷凝器8冷凝气体中的水分,从而分离出水分。 水分离膜单元1a的下游侧的水分离膜单元1b与蒸汽喷射器3连接,用于冷凝通过蒸汽喷射器3的气相中的水的冷凝器4冷凝水分,从而分离水。
    • 5. 发明授权
    • Dehydrator
    • 脱水器
    • US08496806B2
    • 2013-07-30
    • US12678673
    • 2009-01-13
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiHaruaki HirayamaYukio TanakaHideo KashiwagiKatsufumi Inoue
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiHaruaki HirayamaYukio TanakaHideo KashiwagiKatsufumi Inoue
    • B01D19/00B01D61/10B01D61/12B01D1/26
    • B01D61/362B01D61/58B01D2313/24B01D2317/022C07C29/76C07C31/08
    • Provided is a dehydrator that requires no excessively large apparatus structure and achieves cost-saving while maintaining suction efficiency at a desired level by use of suction means. A dehydrator 100 for separating water from a target liquid 13 includes at least two water separation membrane units 1a and 1b which are provided in series in a flow direction of the target liquid 13. The water separation membrane unit 1a on an upstream side out of the water separation membrane units 1a and 1b is connected to suction means 7 for sucking a gas phase containing water through one condenser 4, and the one condenser 4 condenses water in the gas phase and thereby separates the water. The gas phase sucked by the suction means 7 from the one condenser 4 is transferred to at least one downstream condenser 8 provided downstream of the one condenser 4, and the downstream condenser 8 condenses water in the gas phase and thereby separates the water. The water separation membrane unit 1b on a downstream side of the water separation membrane unit 1a is connected to a steam ejector 3, and the condenser 4 for condensing water in a gas phase passed through the steam ejector 3 condenses water and thereby separates the water.
    • 提供一种脱水机,其不需要过大的装置结构,并且通过使用抽吸装置将抽吸效率保持在期望的水平,从而节省成本。 用于从目标液体13分离水的脱水器100包括沿目标液体13的流动方向串联设置的至少两个水分离膜单元1a和1b。在上游侧的水分离膜单元1a 水分离膜单元1a和1b连接到抽吸装置7,用于通过一个冷凝器4吸入含有水的气相,并且一个冷凝器4冷凝气相中的水,从而分离水。 由抽吸装置7从一个冷凝器4吸入的气相被转移到设置在一个冷凝器4下游的至少一个下游冷凝器8,下游冷凝器8冷凝气体中的水分,从而分离出水分。 水分离膜单元1a的下游侧的水分离膜单元1b与蒸汽喷射器3连接,用于冷凝通过蒸汽喷射器3的气相中的水的冷凝器4冷凝水分,从而分离水。
    • 8. 发明授权
    • Method for transporting fluid
    • 运输流体的方法
    • US08496731B2
    • 2013-07-30
    • US12523620
    • 2008-03-14
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiShuichi KashimaHaruaki HirayamaHiroko OguchiNoboru OguchiSachiko Oguchi
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiAkira OguchiShuichi KashimaHaruaki Hirayama
    • B01D61/36B01D53/22
    • B01D61/362B01D71/021B01D71/027B01D71/028B01D2311/04B01D2325/02B63B25/08B63J99/00C10G31/09Y10T137/0391B01D2311/103
    • There is provided a method for transporting a fluid, in which even if the fluid is transported for a long period of time, dehydration after transportation is not needed, and the transported fluid can be used immediately after transportation. Specifically, there is provided a method for transporting a fluid, comprising steps of: dehydrating some of the transportation fluid during transportation by using a dehydration system comprising a separation membrane through which water permeates, and returning the dehydrated fluid to the transportation fluid so as to keep water content in the transportation fluid in a fixed range. In one embodiment, the transportation fluid is a liquid, and the dehydration system comprises a heater for heating the liquid to a temperature in a range in which the liquid does not boil, and a membrane separation apparatus for dehydrating the heated liquid, wherein the membrane separation apparatus is a PV method apparatus comprising a primary side chamber extending in an up and down direction to introduce the liquid from a lower portion thereof and discharge it from an upper portion thereof, a separation membrane in contact with the primary side chamber to allow water in the liquid to permeate through as a gas, and a secondary side chamber being located on the opposite side to the primary side chamber with the separation membrane held therebetween and being under a pressure lower than that in the primary side chamber.
    • 提供了一种输送流体的方法,其中即使流体长时间运输,也不需要运输后的脱水,运输后可以立即使用输送的流体。 具体地说,提供了一种输送流体的方法,其特征在于,包括以下步骤:通过使用包含分离膜的脱水系统在运输过程中使一些输送流体脱水,并将脱水流体返回到输送流体,以便 保持运输流体中的水分含量在一定范围内。 在一个实施方案中,输送流体是液体,脱水系统包括用于将液体加热到液体不沸腾的范围内的温度的加热器,以及用于使加热液体脱水的膜分离装置,其中, 分离装置是一种PV方法装置,它包括一个在上下方向上延伸的一次侧室,以从其下部引入液体并从其上部排出液体,分离膜与初级侧室接触以允许水 在液体中作为气体渗透,并且次级侧室位于与初级侧室相反的一侧,分离膜保持在其间并且处于比初级侧室低的压力下。
    • 9. 发明申请
    • METHOD FOR TRANSPORTING FLUID
    • 运输流体的方法
    • US20100258197A1
    • 2010-10-14
    • US12523620
    • 2008-03-14
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiAkira OguchiShuichi KashimaHaruaki Hirayama
    • Atsuhiro YukumotoHiroyuki OsoraYoshio SeikiAkira OguchiShuichi KashimaHaruaki Hirayama
    • F15D1/00
    • B01D61/362B01D71/021B01D71/027B01D71/028B01D2311/04B01D2325/02B63B25/08B63J99/00C10G31/09Y10T137/0391B01D2311/103
    • There is provided a method for transporting a fluid, in which even if the fluid is transported for a long period of time, dehydration after transportation is not needed, and the transported fluid can be used immediately after transportation. Specifically, there is provided a method for transporting a fluid, comprising steps of: dehydrating some of the transportation fluid during transportation by using a dehydration system comprising a separation membrane through which water permeates, and returning the dehydrated fluid to the transportation fluid so as to keep water content in the transportation fluid in a fixed range. In one embodiment, the transportation fluid is a liquid, and the dehydration system comprises a heater for heating the liquid to a temperature in a range in which the liquid does not boil, and a membrane separation apparatus for dehydrating the heated liquid, wherein the membrane separation apparatus is a PV method apparatus comprising a primary side chamber extending in an up and down direction to introduce the liquid from a lower portion thereof and discharge it from an upper portion thereof, a separation membrane in contact with the primary side chamber to allow water in the liquid to permeate through as a gas, and a secondary side chamber being located on the opposite side to the primary side chamber with the separation membrane held therebetween and being under a pressure lower than that in the primary side chamber.
    • 提供了一种输送流体的方法,其中即使流体长时间运输,也不需要运输后的脱水,运输后可以立即使用输送的流体。 具体地说,提供了一种输送流体的方法,其特征在于,包括以下步骤:使用包含分离膜的脱水系统在运输过程中使一些输送流体脱水,并将脱水流体返回到输送流体,以便 保持运输流体中的水分含量在一定范围内。 在一个实施方案中,输送流体是液体,脱水系统包括用于将液体加热到液体不沸腾的范围内的温度的加热器,以及用于使加热液体脱水的膜分离装置,其中, 分离装置是一种PV方法装置,它包括一个在上下方向上延伸的一次侧室,以从其下部引入液体并从其上部排出液体,分离膜与初级侧室接触以允许水 在液体中作为气体渗透,并且次级侧室位于与初级侧室相反的一侧,分离膜保持在其间并且处于比初级侧室低的压力下。