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WO2006020780A3 - Bundled element filtration system and method - Google Patents

Bundled element filtration system and method Download PDF

Info

Publication number
WO2006020780A3
WO2006020780A3 PCT/US2005/028577 US2005028577W WO2006020780A3 WO 2006020780 A3 WO2006020780 A3 WO 2006020780A3 US 2005028577 W US2005028577 W US 2005028577W WO 2006020780 A3 WO2006020780 A3 WO 2006020780A3
Authority
WO
WIPO (PCT)
Prior art keywords
elements
filtration system
filtration
provides
membrane
Prior art date
Application number
PCT/US2005/028577
Other languages
French (fr)
Other versions
WO2006020780A2 (en
Inventor
Wesley Clifton Boerm
Joseph F Sarro
Original Assignee
Intelligent Solutions Inc
Wesley Clifton Boerm
Joseph F Sarro
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 Intelligent Solutions Inc, Wesley Clifton Boerm, Joseph F Sarro filed Critical Intelligent Solutions Inc
Publication of WO2006020780A2 publication Critical patent/WO2006020780A2/en
Publication of WO2006020780A3 publication Critical patent/WO2006020780A3/en

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
    • 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
    • B01D63/12—Spiral-wound membrane modules comprising multiple spiral-wound assemblies
    • 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
    • B01D65/08—Prevention of membrane fouling or of concentration polarisation
    • 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
    • B01D2321/04—Backflushing
    • 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
    • B01D2321/10—Use of feed
    • 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
    • B01D2321/20—By influencing the flow
    • B01D2321/2008—By influencing the flow statically
    • B01D2321/2025—Tangential inlet

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

An filtration system and method provides the ability to filter a wide range of extremely fine particulate matter in solution ranging in size from micron size particles to molecular elements. The apparatus (10) includes a pressure vessel housing (12) a cross-flow filtration assembly (26) including a plurality of spiral wound type membrane filtration elements (28) in a parallel arrangement. The position of the vessel’s feed inlet (22) combined with the geometry of the membrane elements (28) provides a continuous scouring of the face of the elements (28). The system significantly reduces fouling of the elements (28), minimized the pressure drop through the elements (28), and allows the elements (28) to operate at a high efficiency for longer durations between backwash cycles.
PCT/US2005/028577 2004-08-10 2005-08-10 Bundled element filtration system and method WO2006020780A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US60024004P 2004-08-10 2004-08-10
US60/600,240 2004-08-10

Publications (2)

Publication Number Publication Date
WO2006020780A2 WO2006020780A2 (en) 2006-02-23
WO2006020780A3 true WO2006020780A3 (en) 2006-06-22

Family

ID=35908150

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2005/028577 WO2006020780A2 (en) 2004-08-10 2005-08-10 Bundled element filtration system and method

Country Status (1)

Country Link
WO (1) WO2006020780A2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110227351A (en) * 2019-07-17 2019-09-13 南通市肿瘤医院 A kind of injecting type plate membranous cochlea dynamic filter and working method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3977967A (en) * 1973-05-10 1976-08-31 Union Carbide Corporation Ultrafiltration apparatus and process for the treatment of liquids
US4282098A (en) * 1980-05-19 1981-08-04 Filter Specialists, Inc. Filter top hinge
US5240612A (en) * 1991-02-13 1993-08-31 Techsep Filtration of liquid media under conditions of non-steady tangential flow
US5919376A (en) * 1997-06-10 1999-07-06 Cae Ransohoff Inc. Filtration apparatus and method
US6423230B2 (en) * 1999-05-17 2002-07-23 North Carolina A & T State University Method for improving the permeate flux of a cross-flow membrane filter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3977967A (en) * 1973-05-10 1976-08-31 Union Carbide Corporation Ultrafiltration apparatus and process for the treatment of liquids
US4282098A (en) * 1980-05-19 1981-08-04 Filter Specialists, Inc. Filter top hinge
US5240612A (en) * 1991-02-13 1993-08-31 Techsep Filtration of liquid media under conditions of non-steady tangential flow
US5919376A (en) * 1997-06-10 1999-07-06 Cae Ransohoff Inc. Filtration apparatus and method
US6423230B2 (en) * 1999-05-17 2002-07-23 North Carolina A & T State University Method for improving the permeate flux of a cross-flow membrane filter

Also Published As

Publication number Publication date
WO2006020780A2 (en) 2006-02-23

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