-
公开(公告)号:US20110062062A1
公开(公告)日:2011-03-17
申请号:US12861302
申请日:2010-08-23
CPC分类号: B01D61/06 , B01D61/022 , B01D2311/14 , C02F1/001 , C02F1/441 , C02F2103/08 , C02F2209/005 , C02F2209/03 , C02F2303/10 , Y02A20/131 , Y02W10/30
摘要: According to one embodiment, a power recovery apparatus used in a desalination apparatus including a reverse osmosis membrane which extracts fresh water from seawater and ejects concentrated water includes a pressure conversion section and a seawater supply section to collect energy of the concentrated water. The pressure conversion section includes a movable part dividing inside of the conversion section into first and second spaces, moves the movable part by causing the first space to receive the concentrated water, and pushes out seawater filled in the second space by the movable part to output the seawater. The pressure conversion section further includes a drive mechanism which drives the movable part so as to output the seawater from the second space. The seawater supply section merges the seawater from the pressure conversion section with the seawater supplied to the reverse osmosis membrane.
摘要翻译: 根据一个实施例,在包括从海水中抽出淡水并喷出浓缩水的反渗透膜的脱盐装置中使用的动力回收装置包括压力转换部和海水供给部,以收集浓缩水的能量。 压力转换部包括将转换部分分割为第一和第二空间的可动部分,通过使第一空间接收浓缩水来移动可动部分,并且通过可移动部分推出填充在第二空间中的海水以输出 海水。 压力转换部还包括驱动机构,该驱动机构驱动可动部,以从第二空间输出海水。 海水供给部将来自压力转换部的海水与供给到反渗透膜的海水合并。
-
公开(公告)号:US20110062063A1
公开(公告)日:2011-03-17
申请号:US12862300
申请日:2010-08-24
CPC分类号: C02F1/441 , B01D61/06 , B01D2311/14 , C02F2103/08 , Y02A20/131
摘要: According to one embodiment, a power recovery apparatus used in a desalination apparatus including a reverse osmosis membrane which extracts fresh water from seawater and ejects concentrated water includes a pressure conversion section and a seawater supply section to collect energy of the concentrated water. The pressure conversion section includes a movable part dividing inside of the conversion section into first and second spaces, moves the movable part by causing the first space to receive the concentrated water, and pushes out seawater filled in the second space by the movable part to output the seawater. The seawater supply section merges the seawater from the pressure conversion section with the seawater supplied to the reverse osmosis membrane.
摘要翻译: 根据一个实施例,在包括从海水中抽出淡水并喷出浓缩水的反渗透膜的脱盐装置中使用的动力回收装置包括压力转换部和海水供给部,以收集浓缩水的能量。 压力转换部包括将转换部分分割为第一和第二空间的可动部分,通过使第一空间接收浓缩水来移动可动部分,并且通过可移动部分推出填充在第二空间中的海水以输出 海水。 海水供给部将来自压力转换部的海水与供给到反渗透膜的海水合并。
-
公开(公告)号:US20110073203A1
公开(公告)日:2011-03-31
申请号:US12868492
申请日:2010-08-25
IPC分类号: F16L37/34
CPC分类号: B01D61/20 , C02F2103/08 , C02F2201/002 , Y10T137/87949
摘要: A five-port switch valve includes a cylinder having five chambers defined by four partitions, and two actuators. The valve body of one actuator alternately opens and closes a hole formed in the partition and a hole formed in the partition. The valve body of the other actuator alternately opens and closes a hole formed in the partition and a hole formed in the partition. By virtue of this structure, brine fed into the central chamber through a port is alternately fed into two pressure converters through ports.
摘要翻译: 五口切换阀包括具有由四个隔板限定的五个腔室的气缸和两个致动器。 一个致动器的阀体交替地打开和关闭形成在隔板中的孔和形成在隔板中的孔。 另一执行器的阀体交替地打开和关闭形成在隔板中的孔和形成在隔板中的孔。 由于这种结构,通过端口进入中心室的盐水通过端口交替地供给到两个压力转换器中。
-
公开(公告)号:US09145310B2
公开(公告)日:2015-09-29
申请号:US13104756
申请日:2011-05-10
申请人: Ryo Namba , Katsuya Yokokawa , Hideaki Yamagata , Koichi Matsui , Futoshi Kurokawa , Takeshi Matsushiro
发明人: Ryo Namba , Katsuya Yokokawa , Hideaki Yamagata , Koichi Matsui , Futoshi Kurokawa , Takeshi Matsushiro
IPC分类号: B01D35/00 , B01D21/24 , G01N31/00 , C02F1/44 , G01N31/22 , B01D61/06 , B01D69/12 , B01D61/02 , C02F103/08
CPC分类号: C02F1/441 , B01D61/02 , B01D61/06 , B01D69/12 , B01D2311/04 , B01D2311/08 , C02F2103/08 , C02F2209/005 , C02F2209/03 , C02F2209/40 , C02F2303/10 , G01N31/221 , Y02A20/131 , Y02W10/30 , B01D2311/14 , B01D2311/16
摘要: According to one embodiment, a seawater desalination apparatus includes a pressure sensor configured to measure a pressure of seawater which is supplied to a reverse osmosis membrane that is configured to separate seawater into fresh water and condensed seawater and to discharge the fresh water and the condensed seawater, a sensor configured to measure a flow amount of the fresh water which is discharged from the reverse osmosis membrane, a sensor configured to measure a flow amount of the condensed seawater discharged from the reverse osmosis membrane or a flow amount of the seawater discharged from a booster pump, a sensor configured to measure a flow amount of the seawater which is supplied to a power recovery device, and a controller configured to execute control based on values measured by the sensors.
摘要翻译: 根据一个实施例,海水淡化装置包括:压力传感器,被配置为测量供应到反渗透膜的海水压力,所述反渗透膜被构造成将海水分离成淡水和冷凝的海水并排出淡水和冷凝的海水 被配置为测量从反渗透膜排出的淡水的流量的传感器,构造成测量从反渗透膜排出的浓缩海水的流量的传感器或从反渗透膜排出的海水的流量 增压泵,被配置为测量供应到动力回收装置的海水的流量的传感器,以及被配置为基于由所述传感器测量的值执行控制的控制器。
-
公开(公告)号:US08834712B2
公开(公告)日:2014-09-16
申请号:US13013241
申请日:2011-01-25
申请人: Kyosuke Katayama , Takeshi Matsushiro , Futoshi Kurokawa , Takanori Fukagawa , Kazuhiko Kimijima , Koichi Matsui
发明人: Kyosuke Katayama , Takeshi Matsushiro , Futoshi Kurokawa , Takanori Fukagawa , Kazuhiko Kimijima , Koichi Matsui
CPC分类号: C02F1/008 , C02F1/441 , C02F1/444 , C02F2103/08 , C02F2209/03 , C02F2209/40 , Y02A20/131
摘要: According to one embodiment, a seawater desalination system includes a membrane filtering pump, a first to third flowmeter, a filtering membrane, a high-pressure pump, a pressure gauge, a reverse osmosis membrane, a discharge valve and a control module. The membrane filtering pump outputs seawater according to a first control signal. The first flowmeter measures flow rate Q1. The high-pressure pump outputs filtered water from the filtering membrane according to a second control signal. The first pressure gauge measures pressure P1. The reverse osmosis membrane desalinates the filtered water into fresh water. The second flowmeter measures flow rate Q2. The third flowmeter measures flow rate Q3. The discharge valve discharges a high-concentration salt water according to a third control signal. The control module performs first, second, and third flow rate control with reference to the flow rate Q1, Q2 and Q3 and the pressure P1.
摘要翻译: 根据一个实施例,海水淡化系统包括膜过滤泵,第一至第三流量计,过滤膜,高压泵,压力计,反渗透膜,排放阀和控制模块。 膜过滤泵根据第一控制信号输出海水。 第一流量计测量流量Q1。 高压泵根据第二控制信号从过滤膜输出过滤的水。 第一压力表测量压力P1。 反渗透膜将过滤的水脱盐为淡水。 第二流量计测量流量Q2。 第三台流量计测量流量Q3。 排放阀根据第三控制信号排出高浓度盐水。 控制模块参照流量Q1,Q2和Q3以及压力P1执行第一,第二和第三流量控制。
-
公开(公告)号:US20120061300A1
公开(公告)日:2012-03-15
申请号:US13186177
申请日:2011-07-19
申请人: Takeshi Matsushiro , Katsuya Yokokawa , Futoshi Kurokawa , Ryo Namba , Koichi Matsui , Hideaki Yamagata , Yuka Hiraga , Seiichi Murayama , Hiroyuki Tokimoto
发明人: Takeshi Matsushiro , Katsuya Yokokawa , Futoshi Kurokawa , Ryo Namba , Koichi Matsui , Hideaki Yamagata , Yuka Hiraga , Seiichi Murayama , Hiroyuki Tokimoto
IPC分类号: B01D61/12
CPC分类号: C02F1/441 , B01D61/022 , B01D61/025 , B01D61/04 , B01D61/06 , B01D61/08 , B01D61/10 , B01D61/12 , B01D61/14 , B01D61/58 , B01D2311/14 , B01D2313/243 , C02F1/444 , C02F2103/06 , C02F2103/08 , C02F2209/03 , C02F2303/10 , Y02A20/131 , Y02W10/30
摘要: According to one embodiment, a membrane filtration system includes a raw water tank, a pretreatment membrane module, a raw water feed line, a high-pressure RO membrane module, a high-pressure line, a preceding power recovery unit which pressurize the pretreated water by transmitting the pressure of the concentrate to the pretreated water, a succeeding power recovery unit which pressurize the raw water by transmitting a remaining pressure of the concentrate to the raw water, a concentrate discharge line, a first pressure transmission line communicating to the power recovery unit by being branched from the high-pressure line, a second pressure transmission line communicating to the power recovery unit by being branched from the raw water feed line, and a valve provided in the drain line to regulate a discharge of the concentrate from the power recovery unit in accordance with a pressure loss in the pretreatment membrane module.
摘要翻译: 根据一个实施例,膜过滤系统包括原水槽,预处理膜组件,原水供给管线,高压RO膜组件,高压管线,对预处理水进行加压的前面的动力回收单元 通过将浓缩物的压力传递给预处理水,后续动力回收单元,其通过将浓缩物的剩余压力传递到原水来对原水加压,浓缩物排出管线,与动力回收通信的第一压力传输线 通过从高压管线分支的第二压力传输线,通过从原水供给管线分支而与动力回收单元连通的第二压力传输线,以及设置在排水管线中的阀,用于调节浓缩物从动力排出 回收单元根据预处理膜组件中的压力损失。
-
公开(公告)号:US20110220561A1
公开(公告)日:2011-09-15
申请号:US13013241
申请日:2011-01-25
申请人: Kyosuke Katayama , Takeshi Matsushiro , Futoshi Kurokawa , Takanori Fukagawa , Kazuhiko Kimijima , Koichi Matsui
发明人: Kyosuke Katayama , Takeshi Matsushiro , Futoshi Kurokawa , Takanori Fukagawa , Kazuhiko Kimijima , Koichi Matsui
CPC分类号: C02F1/008 , C02F1/441 , C02F1/444 , C02F2103/08 , C02F2209/03 , C02F2209/40 , Y02A20/131
摘要: According to one embodiment, a seawater desalination system includes a membrane filtering pump, a first to third flowmeter, a filtering membrane, a high-pressure pump, a pressure gauge, a reverse osmosis membrane, a discharge valve and a control module. The membrane filtering pump outputs seawater according to a first control signal. The first flowmeter measures flow rate Q1. The high-pressure pump outputs filtered water from the filtering membrane according to a second control signal. The first pressure gauge measures pressure P1. The reverse osmosis membrane desalinates the filtered water into fresh water. The second flowmeter measures flow rate Q2. The third flowmeter measures flow rate Q3. The discharge valve discharges a high-concentration salt water according to a third control signal. The control module performs first, second, and third flow rate control with reference to the flow rate Q1, Q2 and Q3 and the pressure P1.
摘要翻译: 根据一个实施例,海水淡化系统包括膜过滤泵,第一至第三流量计,过滤膜,高压泵,压力计,反渗透膜,排放阀和控制模块。 膜过滤泵根据第一控制信号输出海水。 第一流量计测量流量Q1。 高压泵根据第二控制信号从过滤膜输出过滤的水。 第一压力表测量压力P1。 反渗透膜将过滤的水脱盐为淡水。 第二流量计测量流量Q2。 第三台流量计测量流量Q3。 排放阀根据第三控制信号排出高浓度盐水。 控制模块参照流量Q1,Q2和Q3以及压力P1执行第一,第二和第三流量控制。
-
公开(公告)号:US20120067791A1
公开(公告)日:2012-03-22
申请号:US13185782
申请日:2011-07-19
申请人: Katsuya YOKOKAWA , Takeshi Matsushiro , Ryo Namba , Hideaki Yamagata , Koichi Matsui , Futoshi Kurokawa
发明人: Katsuya YOKOKAWA , Takeshi Matsushiro , Ryo Namba , Hideaki Yamagata , Koichi Matsui , Futoshi Kurokawa
IPC分类号: B01D61/10 , C02F1/44 , C02F103/08
CPC分类号: C02F1/441 , B01D61/022 , B01D61/025 , B01D2311/18 , C02F1/66 , C02F2101/108 , C02F2103/08 , C02F2209/005 , C02F2209/05 , C02F2209/06 , C02F2303/10 , Y02A20/131 , Y02W10/30
摘要: According to one embodiment, a apparatus includes a controller configured to obtain values measured by a first sensor and a second sensor, receive pH target values at the entrance of a first reverse osmosis membrane and at the entrance of a second reverse osmosis membrane, and use a transfer function from the acid injection to pH at the entrance of the first reverse osmosis membrane, a transfer function from the alkaline injection to pH at the entrance of the first reverse osmosis membrane, a transfer function from the acid injection to pH at the entrance of the second reverse osmosis membrane, and a transfer function from the alkaline injection to pH at the entrance of the second reverse osmosis membrane, to control an injection rate of the acid injected from a first injection device and an injection rate of the alkali injected from a second injection device.
摘要翻译: 根据一个实施例,一种装置包括:控制器,其被配置为获得由第一传感器和第二传感器测量的值,在第一反渗透膜的入口处和在第二反渗透膜的入口处接收pH目标值,并且使用 从第一反渗透膜入口处的酸注入到pH的转移函数,从碱性注入到第一反渗透膜入口处的pH的转移函数,从酸注入到入口处的pH的转移函数 的第二反渗透膜,以及从第二反渗透膜入口处的碱性注入到pH的转移功能,以控制从第一注射装置注入的酸的注射速率和从第 第二注射装置。
-
公开(公告)号:US08702978B2
公开(公告)日:2014-04-22
申请号:US13185782
申请日:2011-07-19
申请人: Katsuya Yokokawa , Takeshi Matsushiro , Ryo Namba , Hideaki Yamagata , Koichi Matsui , Futoshi Kurokawa
发明人: Katsuya Yokokawa , Takeshi Matsushiro , Ryo Namba , Hideaki Yamagata , Koichi Matsui , Futoshi Kurokawa
CPC分类号: C02F1/441 , B01D61/022 , B01D61/025 , B01D2311/18 , C02F1/66 , C02F2101/108 , C02F2103/08 , C02F2209/005 , C02F2209/05 , C02F2209/06 , C02F2303/10 , Y02A20/131 , Y02W10/30
摘要: According to one embodiment, a apparatus includes a controller configured to obtain values measured by a first sensor and a second sensor, receive pH target values at the entrance of a first reverse osmosis membrane and at the entrance of a second reverse osmosis membrane, and use a transfer function from the acid injection to pH at the entrance of the first reverse osmosis membrane, a transfer function from the alkaline injection to pH at the entrance of the first reverse osmosis membrane, a transfer function from the acid injection to pH at the entrance of the second reverse osmosis membrane, and a transfer function from the alkaline injection to pH at the entrance of the second reverse osmosis membrane, to control an injection rate of the acid injected from a first injection device and an injection rate of the alkali injected from a second injection device.
摘要翻译: 根据一个实施例,一种装置包括:控制器,其被配置为获得由第一传感器和第二传感器测量的值,在第一反渗透膜的入口处和在第二反渗透膜的入口处接收pH目标值,并且使用 从第一反渗透膜入口处的酸注入到pH的转移函数,从碱性注入到第一反渗透膜入口处的pH的转移函数,从酸注入到入口处的pH的转移函数 的第二反渗透膜,以及从第二反渗透膜入口处的碱性注入到pH的转移功能,以控制从第一注射装置注入的酸的注射速率和从第 第二注射装置。
-
公开(公告)号:US20110056878A1
公开(公告)日:2011-03-10
申请号:US12855519
申请日:2010-08-12
申请人: Takeshi Matsushiro , Nobuyuki Ashikaga , Takashi Menju , Futoshi Kurokawa , Yoshie Akai , Koichi Matsui , Hideaki Yamagata , Hideyuki Tsuji , Takanori Fukagawa , Takahiro Soma
发明人: Takeshi Matsushiro , Nobuyuki Ashikaga , Takashi Menju , Futoshi Kurokawa , Yoshie Akai , Koichi Matsui , Hideaki Yamagata , Hideyuki Tsuji , Takanori Fukagawa , Takahiro Soma
IPC分类号: C02F1/44
CPC分类号: C02F1/44 , B01D61/022 , B01D61/025 , B01D61/027 , B01D61/145 , B01D61/147 , B01D61/58 , B01D65/02 , B01D2311/04 , B01D2321/08 , C02F1/001 , C02F1/441 , C02F1/442 , C02F1/444 , C02F2301/08 , B01D2311/2649
摘要: According to one embodiment, a membrane filtration system includes a raw water tank, a first tank, a second tank, a nanofiltration membrane module comprises a nanofiltration membrane, and removes the solute from the raw water with a solute removal rate of 1% to 30%, a first pump for supplying the raw water from the raw water tank to the module to cause the raw water to permeate through the membrane and send the water that has permeated through the membrane as a primary water to the first tank, a RO module comprises a RO membrane that further removes the solute from the primary water, and a second pump for supplying the primary water from the first tank to the RO module to cause the primary water to permeate through the membrane and send the water that has permeated through the membrane as a secondary water to the second tank.
摘要翻译: 根据一个实施方案,膜过滤系统包括原水槽,第一罐,第二罐,纳滤膜组件包括纳滤膜,并且从原水中去除溶质,溶质去除率为1%至30 %,用于将原水从原水槽供给到模块的第一泵,用于使原水透过膜并将作为主要水渗透通过膜的水送到第一罐,RO模块 包括进一步从初级水中除去溶质的RO膜和用于将初级水从第一罐供应到RO模块的第二泵,以使初级水渗透通过膜并且将已渗透通过的水 膜作为第二个水的二次水。
-
-
-
-
-
-
-
-
-