ES2545805R1 - Separation Membrane for Seawater Desalination Pretreatment and Seawater Desalination Pretreatment Device - Google Patents
Separation Membrane for Seawater Desalination Pretreatment and Seawater Desalination Pretreatment Device Download PDFInfo
- Publication number
- ES2545805R1 ES2545805R1 ES201490015A ES201490015A ES2545805R1 ES 2545805 R1 ES2545805 R1 ES 2545805R1 ES 201490015 A ES201490015 A ES 201490015A ES 201490015 A ES201490015 A ES 201490015A ES 2545805 R1 ES2545805 R1 ES 2545805R1
- Authority
- ES
- Spain
- Prior art keywords
- seawater desalination
- amount
- separation membrane
- saccharide
- pretreatment
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/04—Feed pretreatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/30—Polyalkenyl halides
- B01D71/32—Polyalkenyl halides containing fluorine atoms
- B01D71/36—Polytetrafluoroethene
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/20—Specific permeability or cut-off range
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/20—Prevention of biofouling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Nanotechnology (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Se proporciona una membrana de separación para el pretratamiento de desalación de agua de mar capaz de suministrar una cantidad adecuada de agua natural a una membrana de OI de manera constante con un flujo que se mantiene elevado y sin aumentar la presión, al tiempo que se retiran PET con una tasa de retirada elevada. También se proporciona un dispositivo de pretratamiento de desalación de agua de mar y un método de desalación de agua de mar. La membrana de separación para el pretratamiento de desalación de agua de mar es una membrana de separación para el pretratamiento de desalación de agua de mar usada en el pretratamiento para la desalación de agua de mar con una membrana de ósmosis inversa, donde#un flujo estándar A es de 2 m/d o más, que se define como valor máximo de un flujo que puede cumplir P2<=1,5x1, donde P1 representa una presión diferencial media de intermembrana para los 30 minutos iniciales y P2 representa una presión diferencial media de intermembrana para los 30 minutos posteriores a un lapso de 120 minutos, cuando se lleva a cabo la filtración a un flujo fijo, y#una tasa B de retirada de sacáridos o tasa C de retirada de carbono granular expresadas por medio de las ecuaciones siguientes es de 0,3, y de manera deseable de 0,5 o más;#Tasa B de retirada de sacáridos = (1 - cantidad de sacárido en el agua filtrada/cantidad de sacárido en el agua natural)#Tasa C de retirada de carbono granular = (1 - COP en el agua filtrada / COP en el agua natural)#donde COP se refiere a una cantidad de carbono orgánico en forma de partículas (una diferencia entre una cantidad de carbono orgánico total y una cantidad de carbono orgánico disuelto).A separation membrane is provided for seawater desalination pretreatment capable of supplying an adequate amount of natural water to an RO membrane constantly with a flow that remains high and without increasing the pressure, while withdrawing PET with a high withdrawal rate. A seawater desalination pretreatment device and a seawater desalination method are also provided. The separation membrane for seawater desalination pretreatment is a separation membrane for seawater desalination pretreatment used in the pretreatment for seawater desalination with a reverse osmosis membrane, where # a standard flow A is 2 m / c or more, which is defined as the maximum value of a flow that can meet P2 <= 1.5x1, where P1 represents an average intermembrane differential pressure for the initial 30 minutes and P2 represents an average differential pressure of intermembrane for the 30 minutes after a period of 120 minutes, when filtration is carried out at a fixed flow, and # a saccharide removal rate B or granular carbon removal rate C expressed by the following equations is 0.3, and desirably 0.5 or more; # Saccharide removal rate B = (1 - amount of saccharide in filtered water / amount of saccharide in natural water) # Carbon removal rate C granular = (1 - COP in filtered water / COP in natural water) # where COP refers to an amount of particulate organic carbon (a difference between a total organic carbon amount and a dissolved organic carbon amount).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP2011/072851 WO2013051110A1 (en) | 2011-10-04 | 2011-10-04 | Separation membrane for saltwater desalination pretreatment and saltwater desalination pretreatment device |
Publications (2)
Publication Number | Publication Date |
---|---|
ES2545805A2 ES2545805A2 (en) | 2015-09-15 |
ES2545805R1 true ES2545805R1 (en) | 2015-10-08 |
Family
ID=48043302
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES201490015A Pending ES2545805R1 (en) | 2011-10-04 | 2011-10-04 | Separation Membrane for Seawater Desalination Pretreatment and Seawater Desalination Pretreatment Device |
Country Status (5)
Country | Link |
---|---|
KR (1) | KR20140085444A (en) |
CN (1) | CN103874661B (en) |
ES (1) | ES2545805R1 (en) |
SG (1) | SG11201400896YA (en) |
WO (1) | WO2013051110A1 (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101267875B (en) * | 2005-09-20 | 2013-02-06 | 水通道蛋白有限公司 | Biomimetic water membrane comprising aquaporins used in the production of salinity power |
JP2011031122A (en) * | 2009-07-29 | 2011-02-17 | Sumitomo Electric Ind Ltd | Multilayered porous hollow fiber, hollow fiber membrane module, and filtration apparatus |
EP2463241A4 (en) * | 2009-08-06 | 2015-03-25 | Sumitomo Electric Industries | Water treatment device and water treatment method |
JP4525857B1 (en) * | 2009-12-11 | 2010-08-18 | 住友電気工業株式会社 | Pretreatment apparatus and pretreatment method for water treatment system |
-
2011
- 2011-10-04 SG SG11201400896YA patent/SG11201400896YA/en unknown
- 2011-10-04 CN CN201180073959.2A patent/CN103874661B/en not_active Expired - Fee Related
- 2011-10-04 ES ES201490015A patent/ES2545805R1/en active Pending
- 2011-10-04 KR KR1020147009232A patent/KR20140085444A/en not_active Application Discontinuation
- 2011-10-04 WO PCT/JP2011/072851 patent/WO2013051110A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
CN103874661B (en) | 2015-11-25 |
WO2013051110A1 (en) | 2013-04-11 |
ES2545805A2 (en) | 2015-09-15 |
CN103874661A (en) | 2014-06-18 |
SG11201400896YA (en) | 2014-10-30 |
KR20140085444A (en) | 2014-07-07 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FC2A | Grant refused |
Effective date: 20160905 |