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WO2003031342A1 - Procede et appareil d'epuration des eaux superficielles - Google Patents

Procede et appareil d'epuration des eaux superficielles Download PDF

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Publication number
WO2003031342A1
WO2003031342A1 PCT/NL2002/000637 NL0200637W WO03031342A1 WO 2003031342 A1 WO2003031342 A1 WO 2003031342A1 NL 0200637 W NL0200637 W NL 0200637W WO 03031342 A1 WO03031342 A1 WO 03031342A1
Authority
WO
WIPO (PCT)
Prior art keywords
membrane
feed
pipe
chemicals
permeate
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.)
Ceased
Application number
PCT/NL2002/000637
Other languages
English (en)
Inventor
Leo Peter Wessels
Ronaldus Cornelius Maria Jong
Bastiaan Martijn Rietman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Waterleiding Overijssel Nv Mij
Original Assignee
Waterleiding Overijssel Nv Mij
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
Application filed by Waterleiding Overijssel Nv Mij filed Critical Waterleiding Overijssel Nv Mij
Publication of WO2003031342A1 publication Critical patent/WO2003031342A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
    • 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
    • B01D61/027—Nanofiltration
    • 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
    • B01D61/08—Apparatus therefor
    • 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
    • B01D63/10—Spiral-wound membrane modules
    • 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
    • C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/16—Use of chemical agents
    • B01D2321/162—Use of acids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/16—Use of chemical agents
    • B01D2321/164—Use of bases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/16—Use of chemical agents
    • B01D2321/168—Use of other chemical agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/18—Use of gases
    • B01D2321/185—Aeration

Definitions

  • Spiral-wound membranes are known to be very susceptible to fouling due to particles, but also due to the growth of biomass, in which case one speaks of biofouling.
  • the deposited particles cause clogging in the feed spacers, while certain nutrients in the feed water may lead to the growth of biomass.
  • This biomass grows between the spacer and can cling to everything.
  • One thing and another results in the biomass being very difficult to remove by, for example, flushing.
  • Chemicals that according to the invention may be considered are: anti-sealants, base, acid, disinfecting chemicals, biocides, bactericides or oxygen-eliminating components such as, for example, bisulphite or hydrazine. After the addition of the chemicals -the flow along the membrane is stopped and the membrane is exposed to the chemicals for 1 to 10 minutes, after which the chemicals are flushed out of the membrane. It is observed that between step 2. and step 1. an extra flush of feed water may take place, while the feed flows through the membrane from top to bottom.
  • gas in the form of preferably compressed air, optionally in combination with chemicals (15), is supplied to the feed in order to aid the release of fouling components while in addition, subject to the use of suitable chemicals, bacteria, biomass and the like can be killed.
  • the O-rings (6) are used as seals between the membrane module (3) and the pressure pipe (2) in order to make it possible to reverse the direction of flow (seal for both flow directions) .
  • the vertical disposition of the pressure pipe (2) aids proper venting.
  • various pipes in the apparatus according to the invention are provided with regulating valves and shut-off valves (no reference numbers), for regulating or shutting off, respectively, the feed, perme- ate, concentrate and filtrate streams as well as the wash- water stream.
  • step 1 the flow direction through the feed spacer during production (step 1) is counter to the flow direction during flushing (step 2) .
  • the present method and apparatus are to be used in particular for the purification of liquids.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nanotechnology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

L'invention concerne un procédé d'épuration d'eaux superficielles ou d'effluents provenant de l'épuration des eaux d'égouts. Selon l'invention, les substances flottantes, les particules solides, les bactéries, les virus et les substances dissoutes telles que le sel, les substances organiques dissoutes, les pesticides etc., sont éliminés simultanément. Pour ce faire, on fait intervenir au moins un tuyau sous pression (2) monté verticalement et doté d'une membrane (3) de nanofiltration ou d'hyperfiltration en spirale. Le flux de refoulement vers la membrane est parallèle. Le procédé de l'invention comprend les opérations suivantes :1) production de perméat et décharge simultanée et continue de concentré, et, (2) flux dans la membrane sans production simultanée de perméat. L'invention concerne également un dispositif de réalisation de ce procédé.
PCT/NL2002/000637 2001-10-08 2002-10-04 Procede et appareil d'epuration des eaux superficielles Ceased WO2003031342A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL1019130 2001-10-08
NL1019130A NL1019130C2 (nl) 2001-10-08 2001-10-08 Werkwijze en inrichting voor het zuiveren van oppervlaktewater.

Publications (1)

Publication Number Publication Date
WO2003031342A1 true WO2003031342A1 (fr) 2003-04-17

Family

ID=19774143

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NL2002/000637 Ceased WO2003031342A1 (fr) 2001-10-08 2002-10-04 Procede et appareil d'epuration des eaux superficielles

Country Status (2)

Country Link
NL (1) NL1019130C2 (fr)
WO (1) WO2003031342A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006069405A1 (fr) * 2004-12-22 2006-06-29 Dressel Pte Ltd. Separation de particules solides du liquide dans lequel elles sont dispersees
NL1030142C2 (nl) * 2005-10-07 2007-04-11 Kiwa Water Res B V Inrichting voor het zuiveren van water en werkwijze voor het gebruik ervan.
WO2015164505A1 (fr) * 2014-04-22 2015-10-29 Dairy Process Systems, Inc. Système permettant de réduire les pertes de produit, la dilution de produit, la dilution chimique et la consommation d'eau dans un système de séparation par membrane à flux transversal

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11076716B2 (en) 2015-12-04 2021-08-03 Koninklijke Philips N.V. Filter assembly for use in a fluid container of a domestic appliance
CN112705051B (zh) * 2021-01-21 2023-03-31 烟台金正环保科技有限公司 一种使用上法兰及压紧套的膜柱

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0307047A1 (fr) * 1987-09-09 1989-03-15 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Module à membrane pour l'hyperfiltration ou l'ultrafiltration de liquides contaminants
JPH05269466A (ja) * 1992-03-26 1993-10-19 Tokyo Metropolis 下水から再生水を得る装置
JPH09299947A (ja) * 1996-05-20 1997-11-25 Nitto Denko Corp 逆浸透膜スパイラルエレメントおよびそれを用いた処理システム
WO1997046305A2 (fr) * 1996-05-31 1997-12-11 Haney Harold E Systeme de traitement de l'eau ameliore
JPH11137978A (ja) * 1997-11-10 1999-05-25 Tohoku Electric Power Co Inc 膜分離装置の膜汚染物質除去方法
WO2000029099A1 (fr) * 1998-11-13 2000-05-25 Dhv Water B.V. Procede et appareil permettant d'eliminer les substances flottantes et les sels d'un liquide au moyen de la filtration sur membrane
JP2001259381A (ja) * 2000-03-23 2001-09-25 Kurita Water Ind Ltd 膜濾過装置

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0307047A1 (fr) * 1987-09-09 1989-03-15 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Module à membrane pour l'hyperfiltration ou l'ultrafiltration de liquides contaminants
JPH05269466A (ja) * 1992-03-26 1993-10-19 Tokyo Metropolis 下水から再生水を得る装置
JPH09299947A (ja) * 1996-05-20 1997-11-25 Nitto Denko Corp 逆浸透膜スパイラルエレメントおよびそれを用いた処理システム
WO1997046305A2 (fr) * 1996-05-31 1997-12-11 Haney Harold E Systeme de traitement de l'eau ameliore
JPH11137978A (ja) * 1997-11-10 1999-05-25 Tohoku Electric Power Co Inc 膜分離装置の膜汚染物質除去方法
WO2000029099A1 (fr) * 1998-11-13 2000-05-25 Dhv Water B.V. Procede et appareil permettant d'eliminer les substances flottantes et les sels d'un liquide au moyen de la filtration sur membrane
JP2001259381A (ja) * 2000-03-23 2001-09-25 Kurita Water Ind Ltd 膜濾過装置

Non-Patent Citations (9)

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Title
DATABASE WPI Derwent World Patents Index; AN 1993-364479, XP002203361 *
DATABASE WPI Derwent World Patents Index; AN 1998-057306, XP002203359 *
DATABASE WPI Derwent World Patents Index; AN 1999-374417, XP002203360 *
DATABASE WPI Derwent World Patents Index; AN 2002-078072, XP002203358 *
PATENT ABSTRACTS OF JAPAN vol. 018, no. 043 (C - 1156) 24 January 1994 (1994-01-24) *
PATENT ABSTRACTS OF JAPAN vol. 1998, no. 03 27 February 1998 (1998-02-27) *
PATENT ABSTRACTS OF JAPAN vol. 1999, no. 10 31 August 1999 (1999-08-31) *
PATENT ABSTRACTS OF JAPAN vol. 2000, no. 26 1 July 2002 (2002-07-01) *
VAN PAASSEN J A M ET AL: "Integrated multi-objective membrane systems for surface water treatment: pre-treatment of nanofiltration by riverbank filtration and conventional ground water treatment", DESALINATION, ELSEVIER SCIENTIFIC PUBLISHING CO, AMSTERDAM, NL, vol. 118, no. 1-3, 20 September 1998 (1998-09-20), pages 239 - 248, XP004139086, ISSN: 0011-9164 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006069405A1 (fr) * 2004-12-22 2006-06-29 Dressel Pte Ltd. Separation de particules solides du liquide dans lequel elles sont dispersees
EA013949B1 (ru) * 2004-12-22 2010-08-30 Дрессел Пте Лтд. Фильтровальный блок и способ организации его работы
NL1030142C2 (nl) * 2005-10-07 2007-04-11 Kiwa Water Res B V Inrichting voor het zuiveren van water en werkwijze voor het gebruik ervan.
WO2007043879A1 (fr) * 2005-10-07 2007-04-19 Kiwa Water Research B.V. Appareil de purification d'eau et procede pour son utilisation
WO2015164505A1 (fr) * 2014-04-22 2015-10-29 Dairy Process Systems, Inc. Système permettant de réduire les pertes de produit, la dilution de produit, la dilution chimique et la consommation d'eau dans un système de séparation par membrane à flux transversal
US9586162B2 (en) 2014-04-22 2017-03-07 Dairy Process Systems, Inc. System for reducing product losses, product dilution, chemical dilution and water consumption in a crossflow membrane separation system
AU2015249750B2 (en) * 2014-04-22 2017-06-15 Jeffrey JAY System for reducing product losses, product dilution, chemical dilution and water consumption in a crossflow membrane separation system

Also Published As

Publication number Publication date
NL1019130C2 (nl) 2003-04-09

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