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CL2017001631A1 - Processes and systems of membrane operated osmotically for the recovery of extracted solute. - Google Patents

Processes and systems of membrane operated osmotically for the recovery of extracted solute.

Info

Publication number
CL2017001631A1
CL2017001631A1 CL2017001631A CL2017001631A CL2017001631A1 CL 2017001631 A1 CL2017001631 A1 CL 2017001631A1 CL 2017001631 A CL2017001631 A CL 2017001631A CL 2017001631 A CL2017001631 A CL 2017001631A CL 2017001631 A1 CL2017001631 A1 CL 2017001631A1
Authority
CL
Chile
Prior art keywords
recovery
processes
membrane
solute
systems
Prior art date
Application number
CL2017001631A
Other languages
Spanish (es)
Inventor
Robert Mcginnis
Original Assignee
Oasys Water Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from PCT/US2010/054512 external-priority patent/WO2011059751A2/en
Application filed by Oasys Water Inc filed Critical Oasys Water Inc
Publication of CL2017001631A1 publication Critical patent/CL2017001631A1/en

Links

Classifications

    • 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
    • B01D61/10—Accessories; Auxiliary operations
    • 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
    • B01D61/06—Energy recovery
    • 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
    • B01D61/364—Membrane distillation
    • B01D61/3641—Membrane distillation comprising multiple membrane distillation steps
    • 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
    • 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
    • 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
    • B01D2311/25—Recirculation, recycling or bypass, e.g. recirculation of concentrate into the feed
    • 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
    • B01D2311/26—Further operations combined with membrane separation processes
    • B01D2311/2626—Absorption or adsorption
    • 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
    • B01D2311/26—Further operations combined with membrane separation processes
    • B01D2311/2669—Distillation
    • 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
    • B01D2311/26—Further operations combined with membrane separation processes
    • B01D2311/2674—Condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/36—Energy sources
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/30—Wastewater or sewage treatment systems using renewable energies
    • Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/30—Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy

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

<p>LA INVENCIÓN DESCRIBE PROCESOS Y SISTEMAS DE MEMBRANA ACCIONADA OSMÓTICAMENTE PARA LA RECUPERACIÓN DE SOLUTOS EXTRAÍDOS EN LOS PROCESOS DE MEMBRANA ACCIONADA OSMÓTICAMENTE. PROCESOS DE MEMBRANA ACCIONADA OSMÓTICAMENTE INVOLUCRAN LA EXTRACCIÓN DE UN SOLVENTE DE UNA PRIMERA SOLUCIÓN PARA CONCENTRAR SOLUTO AL USAR UNA SEGUNDA SOLUCIÓN CONCENTRADA PARA EXTRAER EL SOLVENTE DE LA PRIMERA SOLUCIÓN A TRAVÉS DE UNA MEMBRANA SEMI-PERMEABLE. LA RECUPERACIÓN DE SOLUTO EXTRAÍDO TAMBIÉN PUEDE INCLUIR EL USO DE RECUPERACIÓN DE SOLUTO MULTI-ETAPAS USANDO COLUMNAS DE DESTILACIÓN Y/O MEMBRANAS, DONDE LA RECUPERACIÓN SE PUEDE ASISTIR POR UNA BOMBA DE CALOR.</p><p> THE INVENTION DESCRIBES PROCESSES AND SYSTEMS OF OSMONTICALLY OPERATED MEMBRANE FOR THE RECOVERY OF SOLVES REMOVED IN THE PROCESSES OF MEMBRANE ACTIVATED MEMBRANE. OSMOTALLY OPERATED MEMBRANE PROCESSES INVOLVED THE REMOVAL OF A SOLVENT FROM A FIRST SOLUTION TO CONCENTRATE SOLUTE BY USING A SECOND SOLUTION CONCENTRATED TO REMOVE THE SOLVENT FROM THE FIRST SOLUTION THROUGH A SEMI-PERMEABLE MEMBRANE. RECOVERY OF REMOVED SOLUTE CAN ALSO INCLUDE THE USE OF RECOVERY OF MULTI-STAGES SOLUTE USING DISTILLATION COLUMNS AND / OR MEMBRANES, WHERE RECOVERY CAN BE ASSISTED BY A HEAT PUMP. </p>

CL2017001631A 2010-09-22 2017-06-20 Processes and systems of membrane operated osmotically for the recovery of extracted solute. CL2017001631A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US38529610P 2010-09-22 2010-09-22
PCT/US2010/054512 WO2011059751A2 (en) 2009-10-28 2010-10-28 Forward osmosis separation processes

Publications (1)

Publication Number Publication Date
CL2017001631A1 true CL2017001631A1 (en) 2018-04-13

Family

ID=45874354

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2017001631A CL2017001631A1 (en) 2010-09-22 2017-06-20 Processes and systems of membrane operated osmotically for the recovery of extracted solute.

Country Status (13)

Country Link
EP (1) EP2618917A4 (en)
JP (1) JP5943924B2 (en)
KR (1) KR101924531B1 (en)
CN (2) CN103221118A (en)
AU (1) AU2011305488B2 (en)
BR (1) BR112013006569A2 (en)
CA (1) CA2811925A1 (en)
CL (1) CL2017001631A1 (en)
EA (1) EA024894B1 (en)
IL (1) IL225359A (en)
MX (1) MX368886B (en)
SG (1) SG189035A1 (en)
WO (1) WO2012040335A2 (en)

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BR112012020112B1 (en) 2010-02-10 2021-08-24 Queen's University At Kingston METHOD FOR MODULARING IONIC FORCE
JP6599082B2 (en) 2010-12-15 2019-10-30 クィーンズ ユニバーシティー アット キングストン Switchable water composition and method for adjusting osmotic pressure gradient across a semipermeable membrane
GB201220832D0 (en) * 2012-11-20 2013-01-02 Fujifilm Mfg Europe Bv Electricity generation
EP2928586A1 (en) * 2012-12-04 2015-10-14 McGinnis, Robert Signal responsive solutes
JP6333573B2 (en) * 2014-02-19 2018-05-30 株式会社ササクラ Fresh water generator and fresh water generation method
US20210275967A1 (en) * 2016-09-27 2021-09-09 Oasys Water LLC Osmotically driven membrane processes and systems and methods for draw solute recovery
KR101971244B1 (en) * 2018-07-20 2019-04-22 베니트엠 주식회사 Forward osmosis performance improved membrane apparatus and method of separating solution using the same
KR102753930B1 (en) * 2019-11-29 2025-01-14 한국전력공사 Hybrid power generation system using waste heat and controlling device and method thereof
CN111302518B (en) * 2020-03-20 2021-09-10 山东科技大学 Method for recycling culture wastewater containing antibiotics by combining temperature difference concentration difference dual-driven membrane distillation and high-performance adsorbent
GB202405928D0 (en) * 2024-04-26 2024-06-12 Waterwhelm Ltd Draw agent recovery

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US3470093A (en) * 1966-11-09 1969-09-30 Hydrocarbon Research Inc Osmotic purification of solutions
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JPH035432A (en) * 1989-06-02 1991-01-11 Tsusho Sangiyoushiyou Kiso Sangiyoukiyokuchiyou Method for dehydrating alcohol with n-butane
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CA2654508C (en) * 2006-06-08 2014-07-29 Yale University Multi stage column distillation (mscd) method for osmotic solute recovery
US20080083605A1 (en) * 2006-10-10 2008-04-10 The Texas A&M University System Desalination System
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Also Published As

Publication number Publication date
JP2013537850A (en) 2013-10-07
EA024894B1 (en) 2016-10-31
BR112013006569A2 (en) 2016-06-07
IL225359A (en) 2016-12-29
CN103221118A (en) 2013-07-24
SG189035A1 (en) 2013-05-31
JP5943924B2 (en) 2016-07-05
EP2618917A4 (en) 2014-08-27
WO2012040335A2 (en) 2012-03-29
KR20130101520A (en) 2013-09-13
CA2811925A1 (en) 2012-03-29
EP2618917A2 (en) 2013-07-31
MX2013003271A (en) 2013-09-02
WO2012040335A3 (en) 2012-07-05
CN106823802A (en) 2017-06-13
EA201390426A1 (en) 2014-01-30
AU2011305488A1 (en) 2013-04-11
AU2011305488B2 (en) 2015-09-10
KR101924531B1 (en) 2018-12-04
IL225359A0 (en) 2013-06-27
AU2011305488A2 (en) 2013-05-02
MX368886B (en) 2019-10-21

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