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公开(公告)号:US09339767B2
公开(公告)日:2016-05-17
申请号:US13818250
申请日:2011-09-01
CPC分类号: B01D63/00 , B01D61/366 , B01D61/368 , B01D63/066 , B01D65/00 , B01D2313/08 , B01D2313/086 , B01D2313/20
摘要: A membrane container 6 has a casing 10 including a fluid inlet 14 and a fluid outlet 16 and a membrane container body 9 including a plurality of flow paths 11 which is arranged along the flow direction of the treated fluid and in parallel to one another. Each of the plurality of flow paths 11 includes a most upstream portion 11A which is connected to the fluid inlet 14, and a most downstream portion 11C which is connected to the fluid outlet 16. Return portions 15 and 17 configured to reverse the flow direction of the treated fluid are provided between the most upstream portion 11A and the most downstream portion 11C. After passing through the fluid inlet 14, the treated fluid flows from the most upstream portion 11A down to the most downstream portion 11C via the return portions 15 and the upper return portion 17.
摘要翻译: 膜容器6具有包括流体入口14和流体出口16的壳体10和包括沿着处理流体的流动方向彼此平行布置的多个流路11的膜容器主体9。 多个流路11中的每一个包括连接到流体入口14的最上游部分11A和连接到流体出口16的最下游部分11C。构造成使流体流动方向相反的返回部分15和17 经处理的流体设置在最上游部分11A和最下游部分11C之间。 经过流体入口14后,处理过的流体经由返回部分15和上返回部分17从最上游部分11A向下流到最下游部分11C。
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公开(公告)号:US20130186818A1
公开(公告)日:2013-07-25
申请号:US13818250
申请日:2011-09-01
IPC分类号: B01D63/00
CPC分类号: B01D63/00 , B01D61/366 , B01D61/368 , B01D63/066 , B01D65/00 , B01D2313/08 , B01D2313/086 , B01D2313/20
摘要: A membrane container 6 has a casing 10 including a fluid inlet 14 and a fluid outlet 16 and a membrane container body 9 including a plurality of flow paths 11 which is arranged along the flow direction of the treated fluid and in parallel to one another. Each of the plurality of flow paths 11 includes a most upstream portion 11A which is connected to the fluid inlet 14, and a most downstream portion 11C which is connected to the fluid outlet 16. Return portions 15 and 17 configured to reverse the flow direction of the treated fluid are provided between the most upstream portion 11A and the most downstream portion 11C. After passing through the fluid inlet 14, the treated fluid flows from the most upstream portion 11A down to the most downstream portion 11C via the return portions 15 and the upper return portion 17.
摘要翻译: 膜容器6具有包括流体入口14和流体出口16的壳体10和包括沿着处理流体的流动方向彼此平行布置的多个流路11的膜容器主体9。 多个流路11中的每一个包括连接到流体入口14的最上游部分11A和连接到流体出口16的最下游部分11C。构造成使流体流动方向相反的返回部分15和17 经处理的流体设置在最上游部分11A和最下游部分11C之间。 经过流体入口14后,处理过的流体经由返回部分15和上返回部分17从最上游部分11A向下流到最下游部分11C。
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公开(公告)号:US20100288682A1
公开(公告)日:2010-11-18
申请号:US12465079
申请日:2009-05-13
申请人: Hiroyuki Osora , Yoshio Seiki , Atsuhiro Yukumoto , Yukio Tanaka , Shinji Ogino , Haruaki Hirayama
发明人: Hiroyuki Osora , Yoshio Seiki , Atsuhiro Yukumoto , Yukio Tanaka , Shinji Ogino , Haruaki Hirayama
CPC分类号: B01D61/362 , B01D65/08 , B01D2317/04 , B01D2321/20
摘要: A dehydrating system is designed to maintain the availability of a plant having the dehydrating system using a water separation membrane by allowing a water separation membrane unit to be replaced while the plant is in operation. The dehydrating system comprises at least two water separation membrane units in use arranged parallel to the direction of flow of a fluid to be processed, is configured so that at least one spare water separation membrane unit can be installed parallel to the direction of flow of the fluid to be processed with respect to the at least two water separation membrane units, having monitoring devices for the product fluid to be taken out, and maintains the properties of the product fluid by operating the spare water separation membrane unit depending on the properties of the product fluid monitored by the monitoring devices.
摘要翻译: 脱水系统被设计成通过在工厂运行时允许更换水分离膜单元来保持具有使用水分离膜的脱水系统的设备的可用性。 脱水系统包括至少两个平行于待处理流体的流动方向布置的水分离膜单元,其被配置成使得至少一个备用水分离膜单元可平行于流动方向 相对于至少两个水分离膜单元进行处理的流体,具有用于待取出的产品流体的监测装置,并且通过根据其特性来操作备用水分离膜单元来维持产品流体的性质 产品流体由监控设备监控。
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公开(公告)号:US20140027367A1
公开(公告)日:2014-01-30
申请号:US13818024
申请日:2011-09-01
IPC分类号: B01D61/58
CPC分类号: B01D61/58 , B01D61/362 , B01D2311/25 , B01D2313/083 , B01D2315/04 , B01D2317/02 , B01D2317/022 , B01D2317/04 , C07C29/76 , C07C31/08
摘要: Provided is a dehydrator 1 configured to separate water from treated fluid, which includes a first tank 2 for storing the treated fluid before water is separated therefrom, a second tank 3 into which the treated fluid whose water has been separated therefrom flows, a separation membrane configured to separate water from the treated fluid, and a plurality of membrane container units 101 through 110 provided between the first tank 2 and the second tank 3 and in parallel to one another along a direction of flow of the treated fluid. The treated fluid is configured to reciprocate between the first tank 2 and the second tank 3 and is configured to pass through the plurality of membrane container units for a plurality of times.
摘要翻译: 提供了一种脱水器1,其被配置为从处理过的流体中分离出水,其包括用于在水分离之前储存处理过的流体的第一罐2,其中已经分离水的处理流体流入的第二罐3, 被配置为从处理过的流体中分离出水,以及设置在第一罐2和第二罐3之间并沿着处理流体的流动方向彼此平行的多个膜容器单元101至110。 经处理的流体被配置为在第一罐2和第二罐3之间往复运动,并且被配置为穿过多个膜容器单元多次。
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公开(公告)号:US08142662B2
公开(公告)日:2012-03-27
申请号:US12465079
申请日:2009-05-13
申请人: Hiroyuki Osora , Yoshio Seiki , Atsuhiro Yukumoto , Yukio Tanaka , Shinji Ogino , Haruaki Hirayama
发明人: Hiroyuki Osora , Yoshio Seiki , Atsuhiro Yukumoto , Yukio Tanaka , Shinji Ogino , Haruaki Hirayama
CPC分类号: B01D61/362 , B01D65/08 , B01D2317/04 , B01D2321/20
摘要: A dehydrating system is designed to maintain the availability of a plant having the dehydrating system using a water separation membrane by allowing a water separation membrane unit to be replaced while the plant is in operation. The dehydrating system comprises at least two water separation membrane units in use arranged parallel to the direction of flow of a fluid to be processed, is configured so that at least one spare water separation membrane unit can be installed parallel to the direction of flow of the fluid to be processed with respect to the at least two water separation membrane units, having monitoring devices for the product fluid to be taken out, and maintains the properties of the product fluid by operating the spare water separation membrane unit depending on the properties of the product fluid monitored by the monitoring devices.
摘要翻译: 脱水系统被设计成通过在工厂运行时允许更换水分离膜单元来保持具有使用水分离膜的脱水系统的设备的可用性。 脱水系统包括至少两个平行于待处理流体的流动方向布置的水分离膜单元,其被配置成使得至少一个备用水分离膜单元可平行于流动方向 相对于至少两个水分离膜单元进行处理的流体,具有用于待取出的产品流体的监测装置,并且通过根据其特性来操作备用水分离膜单元来维持产品流体的性质 产品流体由监控设备监控。
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公开(公告)号:US20110011725A1
公开(公告)日:2011-01-20
申请号:US12677168
申请日:2008-12-24
申请人: Yukio Tanaka , Hiroyuki Osora , Yoshio Seiki , Atsuhiro Yukumoto , Haruaki Hirayama , Shinji Ogino
发明人: Yukio Tanaka , Hiroyuki Osora , Yoshio Seiki , Atsuhiro Yukumoto , Haruaki Hirayama , Shinji Ogino
IPC分类号: B01D3/36
CPC分类号: B01D63/066 , B01D61/362 , B01D63/06 , B01D2311/04 , B01D2311/08 , B01D2311/103 , B01D2311/25 , B01D2317/022 , C10G33/06
摘要: Provided are a dehydrating system and a dehydrating method which achieve improvement in a membrane performance. The dehydrating system includes a first preheater 3a; multiple dehydrating apparatuses 1a, 1b and 1c which are connected in series downstream of the preheater and which are configured to remove water from an organic aqueous solution; and returning means 6 for returning a part of the organic aqueous solution having passed through one or more of the dehydrating apparatuses to the dehydrating apparatuses or the dehydrating apparatus upstream of the dehydrating apparatuses.
摘要翻译: 提供一种实现膜性能提高的脱水系统和脱水方法。 脱水系统包括第一预热器3a; 多个脱水装置1a,1b和1c,其串联连接在预热器的下游,并被构造成从有机水溶液中除去水; 以及将通过一个或多个脱水装置的一部分有机水溶液返回到脱水装置上游的脱水装置或脱水装置的返回装置6。
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公开(公告)号:US20100206789A1
公开(公告)日:2010-08-19
申请号:US12678673
申请日:2009-01-13
申请人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Yukio Tanaka , Hideo Kashiwagi , Katsufumi Inoue
发明人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Yukio Tanaka , Hideo Kashiwagi , Katsufumi Inoue
IPC分类号: B01D61/36
CPC分类号: B01D61/362 , B01D61/58 , B01D2313/24 , B01D2317/022 , C07C29/76 , C07C31/08
摘要: 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.
摘要翻译: 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。
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公开(公告)号:US08496806B2
公开(公告)日:2013-07-30
申请号:US12678673
申请日:2009-01-13
申请人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Yukio Tanaka , Hideo Kashiwagi , Katsufumi Inoue
发明人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Yukio Tanaka , Hideo Kashiwagi , Katsufumi Inoue
CPC分类号: B01D61/362 , B01D61/58 , B01D2313/24 , B01D2317/022 , C07C29/76 , C07C31/08
摘要: 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.
摘要翻译: 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。
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公开(公告)号:US08721890B2
公开(公告)日:2014-05-13
申请号:US12665854
申请日:2008-12-24
申请人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Kazuto Kobayashi , Yukio Tanaka
发明人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Kazuto Kobayashi , Yukio Tanaka
CPC分类号: B01D61/362 , B01D67/0048 , B01D71/027 , B01D71/028 , B01D71/38 , B01D71/56 , B01D71/64 , B01D2313/38 , B01D2317/022 , B01D2317/027 , B01D2323/12 , C07C29/76 , C07C31/08
摘要: A dehydrating system using multiple water separation membranes aims to prevent damage to the water separation membrane units and also to take appropriate measures against decrease in water permeation rate of the water separation membranes. Provided is a dehydrating system (100) for removing water from a target fluid, including at least two water separation membrane units (1, 2, 3) connected in series in a flow direction of the target fluid; two or more heat exchangers (11, 21, 31) respectively provided in front of the water separation membrane units (1, 2, 3), each of the heat exchangers (11, 21, 31) raising a temperature of the target fluid to a temperature which is lower than a boiling point of the target fluid but close to the boiling point.
摘要翻译: 使用多个水分离膜的脱水系统旨在防止水分离膜单元的损坏,并且还采取适当措施降低水分离膜的渗水速率。 提供一种用于从目标流体中除去水的脱水系统(100),其包括沿着目标流体的流动方向串联连接的至少两个水分离膜单元(1,2,3) 分别设置在水分离膜单元(1,2,3)前面的两个或多个热交换器(11,21,31),每个热交换器(11,21,31)将目标流体的温度升高到 其温度低于目标流体的沸点但接近沸点。
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公开(公告)号:US20100320148A1
公开(公告)日:2010-12-23
申请号:US12665854
申请日:2008-12-24
申请人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Kazuto Kobayashi , Yukio Tanaka
发明人: Atsuhiro Yukumoto , Hiroyuki Osora , Yoshio Seiki , Haruaki Hirayama , Kazuto Kobayashi , Yukio Tanaka
CPC分类号: B01D61/362 , B01D67/0048 , B01D71/027 , B01D71/028 , B01D71/38 , B01D71/56 , B01D71/64 , B01D2313/38 , B01D2317/022 , B01D2317/027 , B01D2323/12 , C07C29/76 , C07C31/08
摘要: A dehydrating system using multiple water separation membranes aims to prevent damage to the water separation membrane units and also to take appropriate measures against decrease in water permeation rate of the water separation membranes. Provided is a dehydrating system (100) for removing water from a target fluid, including at least two water separation membrane units (1, 2, 3) connected in series in a flow direction of the target fluid; two or more heat exchangers (11, 21, 31) respectively provided in front of the water separation membrane units (1, 2, 3), each of the heat exchangers (11, 21, 31) raising a temperature of the target fluid to a temperature which is lower than a boiling point of the target fluid but close to the boiling point.
摘要翻译: 使用多个水分离膜的脱水系统旨在防止水分离膜单元的损坏,并且还采取适当措施降低水分离膜的渗水速率。 提供一种用于从目标流体中除去水的脱水系统(100),其包括沿着目标流体的流动方向串联连接的至少两个水分离膜单元(1,2,3) 分别设置在水分离膜单元(1,2,3)前面的两个或多个热交换器(11,21,31),每个热交换器(11,21,31)将目标流体的温度升高到 其温度低于目标流体的沸点但接近沸点。
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