MX2020010256A - Aparato de membranas que tiene un rendimiento de la osmosis forzada mejorado y metodo para separar una solucion que lo utiliza. - Google Patents
Aparato de membranas que tiene un rendimiento de la osmosis forzada mejorado y metodo para separar una solucion que lo utiliza.Info
- Publication number
- MX2020010256A MX2020010256A MX2020010256A MX2020010256A MX2020010256A MX 2020010256 A MX2020010256 A MX 2020010256A MX 2020010256 A MX2020010256 A MX 2020010256A MX 2020010256 A MX2020010256 A MX 2020010256A MX 2020010256 A MX2020010256 A MX 2020010256A
- Authority
- MX
- Mexico
- Prior art keywords
- forward osmosis
- region
- permeate
- same
- membrane apparatus
- Prior art date
Links
- 239000012528 membrane Substances 0.000 title abstract 6
- 238000009292 forward osmosis Methods 0.000 title abstract 4
- 238000000034 method Methods 0.000 title 1
- 239000012466 permeate Substances 0.000 abstract 6
- 239000011259 mixed solution Substances 0.000 abstract 2
- 238000005373 pervaporation Methods 0.000 abstract 2
- 230000006698 induction Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
-
- 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
- B01D61/002—Forward osmosis or direct osmosis
- B01D61/005—Osmotic agents; Draw solutions
-
- 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
- B01D61/58—Multistep processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
- B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
-
- 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
- B01D61/002—Forward osmosis or direct osmosis
- B01D61/0022—Apparatus therefor
-
- 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
-
- 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
- B01D61/36—Pervaporation; Membrane distillation; Liquid permeation
- B01D61/362—Pervaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/04—Hollow fibre modules comprising multiple hollow fibre assemblies
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- 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
- C02F1/445—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by forward osmosis
-
- 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
- C02F1/448—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by pervaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/06—Specific process operations in the permeate stream
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/10—Temperature control
- B01D2311/103—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/14—Pressure control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/24—Quality control
- B01D2311/246—Concentration control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/24—Specific pressurizing or depressurizing means
- B01D2313/243—Pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/32—Intermediate chambers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2319/00—Membrane assemblies within one housing
- B01D2319/02—Elements in series
- B01D2319/025—Permeate series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2319/00—Membrane assemblies within one housing
- B01D2319/04—Elements in parallel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2319/00—Membrane assemblies within one housing
- B01D2319/06—Use of membranes of different materials or properties within one module
-
- 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
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (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
Un aparato de membranas incluye una carcasa, una membrana de osmosis forzada que divide un espacio interno de la carcasa en una región de entrada y una región de mezcla, y una membrana de pervaporación que divide el espacio interno de la carcasa en la región de mezcla y una región de descarga. La membrana de osmosis forzada separa un líquido de filtración inicial de un líquido de entrada, que se dispone en la región de entrada y proporciona el líquido de filtración inicial separado a la región de mezcla, el líquido de filtración inicial se mezcla con un agente osmótico de osmosis forzada en la región de mezcla para crear una solución mezclada, la membrana de pervaporación separa un líquido de filtración final de la solución mezclada y proporciona el líquido de filtración final separado a la región de descarga, el líquido de filtración final se vaporiza en la región de descarga para crear vapor y una cantidad del vapor se ajusta mediante al menos uno de una temperatura de la solución mezclada y un grado de vacío de la región de descarga.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020180084959A KR101971244B1 (ko) | 2018-07-20 | 2018-07-20 | 정삼투 성능이 개선된 멤브레인 장치 및 이를 이용하는 용액 분리 방법 |
PCT/KR2019/003180 WO2020017729A1 (ko) | 2018-07-20 | 2019-03-19 | 정삼투 성능이 개선된 멤브레인 장치 및 이를 이용하는 용액 분리 방법 |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2020010256A true MX2020010256A (es) | 2020-10-22 |
Family
ID=66283047
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2020010256A MX2020010256A (es) | 2018-07-20 | 2019-03-19 | Aparato de membranas que tiene un rendimiento de la osmosis forzada mejorado y metodo para separar una solucion que lo utiliza. |
Country Status (12)
Country | Link |
---|---|
US (1) | US11090609B2 (es) |
EP (1) | EP3804840A4 (es) |
JP (1) | JP6724124B2 (es) |
KR (1) | KR101971244B1 (es) |
CN (1) | CN110732245B (es) |
AU (1) | AU2019306733B2 (es) |
CA (1) | CA3095479A1 (es) |
MX (1) | MX2020010256A (es) |
MY (1) | MY194666A (es) |
SG (1) | SG11202009435WA (es) |
TW (1) | TWI714147B (es) |
WO (1) | WO2020017729A1 (es) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102078056B1 (ko) * | 2019-03-29 | 2020-02-17 | 한국화학연구원 | 식물 재배용 양액 공급 시스템 |
US11577973B2 (en) * | 2020-06-16 | 2023-02-14 | City University Of Hong Kong | Fluid treatment apparatus |
KR102463595B1 (ko) * | 2021-02-16 | 2022-11-03 | 부산대학교 산학협력단 | 액체건조제를 이용한 저에너지 담수화 시스템 및 이를 이용한 담수화 방법 |
WO2023176565A1 (ja) * | 2022-03-17 | 2023-09-21 | 日東電工株式会社 | 膜分離システム、及び膜分離装置の運転方法 |
WO2023192421A1 (en) | 2022-03-30 | 2023-10-05 | Donaldson Company, Inc. | System and method for reclaiming solvent |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2009155596A2 (en) * | 2008-06-20 | 2009-12-23 | Yale University | Forward osmosis separation processes |
WO2004020189A1 (en) | 2002-08-30 | 2004-03-11 | Alza Corporation | Embossable and writable multilaminate backing construction |
WO2005089913A1 (en) * | 2004-03-16 | 2005-09-29 | Sri International | Membrane purification system |
US8029671B2 (en) * | 2006-06-13 | 2011-10-04 | Board Of Regents Of The Nevada System Of Higher Education, On Behalf Of The University Of Nevada, Reno | Combined membrane-distillation-forward-osmosis systems and methods of use |
JP4805201B2 (ja) * | 2007-03-22 | 2011-11-02 | 月島環境エンジニアリング株式会社 | 膜分離を用いた目的物質の分離方法と装置 |
KR101020316B1 (ko) * | 2010-04-28 | 2011-03-08 | 에스티엑스중공업 주식회사 | 막증류 방식을 이용한 정삼투 담수화 장치 |
SG189035A1 (en) * | 2010-09-22 | 2013-05-31 | Oasys Water Inc | Osmotically driven membrane processes and systems and methods for draw solute recovery |
US8752714B2 (en) * | 2011-03-01 | 2014-06-17 | Dow Global Technologies Llc | Sulfonated poly (aryl ether) membrane including blend with phenyl amine compound |
EP2686081A4 (en) * | 2011-04-25 | 2014-12-10 | Trevi Systems Inc | RECOVERING RETROGRADE SOLUBILITY SOLUTION FOR DIRECT OSMOSIS WATER TREATMENT |
US9714183B1 (en) * | 2011-06-28 | 2017-07-25 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Water walls for life support |
KR101256037B1 (ko) | 2011-07-18 | 2013-04-23 | 덕성여자대학교 산학협력단 | 이중질량분석기를 이용한 소변중 Lyso-Gb3의 분석 방법 및 이를 이용한 파브리병 진단 방법 |
KR101184787B1 (ko) * | 2012-04-16 | 2012-09-20 | 김경성 | 히트펌프를 이용한 막여과 장치 |
CN103663821B (zh) * | 2012-09-04 | 2017-12-22 | 宁波莲华环保科技股份有限公司 | 一种海水淡化方法和系统 |
CN107261847A (zh) * | 2013-02-08 | 2017-10-20 | Oasys水有限公司 | 渗透分离系统和方法 |
WO2015013358A1 (en) * | 2013-07-24 | 2015-01-29 | Hydration Systems, Llc | Method to improve forward osmosis membrane performance |
CN103551036B (zh) * | 2013-11-21 | 2016-03-02 | 洪梅 | 一种陶瓷分子筛膜高效渗透蒸发装置及工艺 |
CN103922530B (zh) * | 2014-04-25 | 2015-04-22 | 哈尔滨工业大学 | 一种循环式正渗透与渗透汽化一体化的水处理方法 |
WO2016057764A1 (en) * | 2014-10-10 | 2016-04-14 | Oasys Water, Inc. | Osmotic separation systems and methods |
CN106659976A (zh) * | 2014-11-07 | 2017-05-10 | 株式会社东芝 | 水处理方法、水处理系统以及水处理装置 |
CN104326616B (zh) * | 2014-11-28 | 2016-07-20 | 山东省环科院环境工程有限公司 | 一种节能精细化工废水深度处理系统及其处理方法 |
EP3261752A1 (en) * | 2015-02-26 | 2018-01-03 | King Abdullah University Of Science And Technology | Osmotically and thermally isolated forward osmosis-membrane distillation (fo-md) integrated module for water treatment applications |
CN104803451B (zh) * | 2015-04-23 | 2016-07-27 | 童成双 | 正渗透和反渗透技术相结合的海水淡化处理方法及装置 |
KR101732811B1 (ko) | 2015-10-22 | 2017-05-24 | 성균관대학교산학협력단 | 고분자 유도물질을 사용한 에너지 저감형 정삼투막-여과막 결합 수처리와 해수담수화 시스템 및 방법 |
JP2018083189A (ja) * | 2016-05-24 | 2018-05-31 | 旭化成株式会社 | 膜蒸留装置 |
CN106186190A (zh) * | 2016-08-09 | 2016-12-07 | 叶剑 | 一种高效环保的海水淡化处理工艺 |
CN205974138U (zh) * | 2016-08-25 | 2017-02-22 | 黑龙江省环境科学研究院 | 一种一体化循环渗透水处理系统 |
CN106277537A (zh) * | 2016-11-02 | 2017-01-04 | 中国石油大学(华东) | 一种用于高盐溶液连续脱水处理的新型组合工艺 |
-
2018
- 2018-07-20 KR KR1020180084959A patent/KR101971244B1/ko active IP Right Grant
- 2018-12-13 JP JP2018233624A patent/JP6724124B2/ja active Active
- 2018-12-21 CN CN201811570208.1A patent/CN110732245B/zh active Active
-
2019
- 2019-03-19 EP EP19836966.2A patent/EP3804840A4/en not_active Withdrawn
- 2019-03-19 MY MYPI2020005198A patent/MY194666A/en unknown
- 2019-03-19 CA CA3095479A patent/CA3095479A1/en not_active Abandoned
- 2019-03-19 WO PCT/KR2019/003180 patent/WO2020017729A1/ko unknown
- 2019-03-19 MX MX2020010256A patent/MX2020010256A/es unknown
- 2019-03-19 AU AU2019306733A patent/AU2019306733B2/en active Active
- 2019-03-19 SG SG11202009435WA patent/SG11202009435WA/en unknown
- 2019-03-19 US US16/623,682 patent/US11090609B2/en active Active
- 2019-06-27 TW TW108122652A patent/TWI714147B/zh active
Also Published As
Publication number | Publication date |
---|---|
SG11202009435WA (en) | 2020-10-29 |
WO2020017729A1 (ko) | 2020-01-23 |
US20210046424A1 (en) | 2021-02-18 |
TWI714147B (zh) | 2020-12-21 |
TW202012035A (zh) | 2020-04-01 |
AU2019306733B2 (en) | 2021-07-15 |
US11090609B2 (en) | 2021-08-17 |
CA3095479A1 (en) | 2020-01-23 |
MY194666A (en) | 2022-12-12 |
JP6724124B2 (ja) | 2020-07-15 |
KR101971244B1 (ko) | 2019-04-22 |
EP3804840A1 (en) | 2021-04-14 |
CN110732245B (zh) | 2022-04-08 |
AU2019306733A1 (en) | 2021-01-07 |
CN110732245A (zh) | 2020-01-31 |
EP3804840A4 (en) | 2022-05-04 |
JP2020011227A (ja) | 2020-01-23 |
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