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GB1066480A - Process for preparing filters having a microporous layer attached thereto and product - Google Patents

Process for preparing filters having a microporous layer attached thereto and product

Info

Publication number
GB1066480A
GB1066480A GB48642/64A GB4864264A GB1066480A GB 1066480 A GB1066480 A GB 1066480A GB 48642/64 A GB48642/64 A GB 48642/64A GB 4864264 A GB4864264 A GB 4864264A GB 1066480 A GB1066480 A GB 1066480A
Authority
GB
United Kingdom
Prior art keywords
layer
sheet
liquid
dispersion
particulate material
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.)
Expired
Application number
GB48642/64A
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.)
Pall Corp
Original Assignee
Pall Corp
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 Pall Corp filed Critical Pall Corp
Publication of GB1066480A publication Critical patent/GB1066480A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/111Making filtering elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/13Supported filter elements
    • B01D29/15Supported filter elements arranged for inward flow filtration
    • B01D29/21Supported filter elements arranged for inward flow filtration with corrugated, folded or wound sheets

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Laminated Bodies (AREA)

Abstract

A process for the manufacture of a corrugated microporous filter element comprises treating a porous substrate sheet in selected areas intended as the bases of corrugation folds, to reduce porosity by at least 10% relative to other areas of the sheet, folding the sheet along these areas and intermediate areas to form corrugations having base folds to a radius of curvature of at least 0.025 inch, applying to the corrugated sheet a dispersion comprising a suspending liquid and a particulate material, and causing the dispersion to flow through the sheet, thus depositing particulate material either on the substrate or within its pores, or both, to form a microporous layer. The maximum pore diameter may be 25 microns. The substrate sheet is preferably paper, optionally in two or more layers, and optionally resin-impregnated. Other materials include: plastics; textiles; felts and the like; porous sintered powder sheets; two wire-mesh sheets sintered together. The "reduction of porosity" may be effected by compression during formation of the corrugations, or by coating or impregnating (e.g. with synthetic resins). In the latter case a backing layer, or strips, having finer pores, may be applied permanently or temporarily to the reverse of the substrate sheet. If the corrugated sheet is to be used flat, the layer-forming suspension is applied to it in that form, but if it is to be used in tubular form its ends are joined and sealed prior to the application. The sheet may be impregnated with a setting agent for the corrugations prior to forming them, if necessary. For maximum adhesion of the microporous layer, a prior anchoring layer is laid down on the substrate sheet. The anchoring layer material consists of a bonding agent and a particulate material in a dispersing liquid. The bonding agent is preferably a liquid, or a solid which may be rendered liquid by appropriate treatment. Liquid thermosetting resins, e.g. polyepoxide resins, are preferred. In such cases, curing agents for these resins (preferably organic amines) are incorporated in the mixture. Amongst thermoplastic solid bonding agents, polyethylene, polytetrafluoroethylene and synthetic rubbers are preferred. The particulate material of the anchoring layer may be any of those used for the microporous layer (see below). When the later microporous layer is to enter the pores of the substrate sheet the anchoring-layer particles are non-fibrous; when coating is intended, the particles are fibrous. The dispersing liquid used in the anchoring layer material can be any of those used in applying the microporous layer, or any inert liquid. The microporous layer dispersion consists of a particulate material and optionally a bonding agent or a wetting agent in the dispersing liquid. Particulate material of a fibrous or like character is preferred, e.g. fibres of mineral, vegetable or synthetic origin; certain inorganic compounds, especially potassium titanate; glass; metals; and clays with needle-like particles. Optionally, non-fibrous particles such as diatomaceous earth may be included, and may even form the major constituent. Bactericides and like substances may be included. The dispersing liquid may be selected from: water, alcohols, glycols, hydrocarbons. The degree of flocculation of the dispersion is controlled, and may be varied by adding a dispersing agent or a flocculating agent before or after deposition. The dispersion may be agitated during deposition. The depth of penetration should not exceed 2 or 3 fibre diameters. Preferably a differential pressure is maintained across the element during deposition, which takes place several times; between one application and the next, the element is removed from the dispersion and a differential pressure applied to set the layer. Adhesion is effected by heating (e.g. a curing oven, or inward hot gaseous flow through the tubular element) or by standing at room temperature. A bactericidal layer (e.g. of Ag Br) may be applied to the element afterwards.ALSO:A process for the manufacture of a corrugated microporous filter element comprises treating a porous substrate sheet in selected areas intended as the bases of corrugation folds, to reduce porosity by at least 10% relative to other areas of the sheet, folding the sheet along these areas and intermediate areas to form corrugations having base folds to a radius of curvature of at least 0.025 inch, applying to the corrugated sheet a dispersion comprising a suspending liquid and a particulate material, and causing the dispersion to flow through the sheet, thus depositing particulate material either on the substrate or within its pores, or both, to form a microporous layer. The maximum pore diameter may be 25 microns. The substrate sheet is preferably paper, optionally in two or more layers, and optionally resin-impregnated. Other materials include: plastics; textiles; felts and the like; porous sintered powder sheets; two wire-mesh sheets sintered together. The "reduction of porosity" may be effected by compression during formation of the corrugations, or by coating or impregnating (e.g. with synthetic resins). In the latter case a backing layer, or strips, having finer pores, may be applied permanently or temporarily to the reverse of the substrate sheet. If the corrugated sheet is to be used flat, the layer-forming suspension is applied to it in that form, but if it is to be used in tubular form its ends are joined and sealed prior to the application. The sheet may be impregnated with a setting agent for the corrugations prior to forming them, if necessary. For maximum adhesion of the microporous layer, a prior anchoring layer is laid down on the substrate sheet. The anchoring layer material consists of a bonding agent and a particulate material in a dispersing liquid. The bonding agent is preferably a liquid, or a solid which may be rendered liquid by appropriate treatment. Liquid thermosetting resins, e.g. polyepoxide resins, are preferred. In such cases, curing agents for these resins (preferably organic amines) are incorporated in the mixture. Amongst thermoplastic solid bonding agents, polyethylene, polytetrafluoroethylene and synthetic rubbers are preferred. The particulate material of the anchoring layer may be any of those used for the microporous layer (see below). When the later microporous layer is to enter the pores of the substrate sheet the anchoring-layer particles are non-fibrous; when coating is intended, the particles are fibrous. The dispersing liquid used in the anchoring layer material can be any of those used in applying the microporous layer, or any inert liquid. The microporous layer dispersion consists of a particulate material and optionally a bonding agent or a wetting agent in the dispersing liquid. Particulate material of a fibrous or like character is preferred, e.g. fibres of mineral, vegetable or synthetic origin; certain inorganic compounds, especially potassium titanate; glass; metals; and clays with needle-like particles. Optionally, non-fibrous particles such as diatomaceous earth may be included, and may even form the major constituent. Bactericides and like substances may be included. The dispersing liquid may be selected from: water, alcohols, glycols, hydrocarbons. The degree of flocculation of the dispersion is controlled, and may be varied by adding a dispersing agent or a flocculating agent before or after deposition. The dispersion may be agitated during deposition. The depth of penetration should not exceed 2 or 3 fibre diameters. Preferably a differential pressure is maintained across the element during deposition, which takes place several times; between one application and the next, the element is removed from the dispersion and a differential pressure applied to set the layer. Adhesion is effected by heating (e.g. a curing oven, or inward hot gaseous flow through the tubular element) or by standing at room temperature. A bactericidal layer (e.g. of Ag Br) may be applied to the element afterwards.
GB48642/64A 1963-12-05 1964-11-30 Process for preparing filters having a microporous layer attached thereto and product Expired GB1066480A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US32829763A 1963-12-05 1963-12-05

Publications (1)

Publication Number Publication Date
GB1066480A true GB1066480A (en) 1967-04-26

Family

ID=23280382

Family Applications (1)

Application Number Title Priority Date Filing Date
GB48642/64A Expired GB1066480A (en) 1963-12-05 1964-11-30 Process for preparing filters having a microporous layer attached thereto and product

Country Status (1)

Country Link
GB (1) GB1066480A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4101423A (en) 1975-04-04 1978-07-18 Millipore Corporation Tubular filtration element and method of making it
GB2182071B (en) * 1985-10-25 1989-11-08 Scott & Fyfe Ltd Composite sheet material
US6106897A (en) * 1996-08-09 2000-08-22 Scapa Group Plc Polymer pore structure
GB2316015B (en) * 1996-08-10 2000-08-30 Scapa Group Plc Polymer pore structure
WO2018089877A1 (en) * 2016-11-14 2018-05-17 3M Innovative Properties Company Air filters comprising metal-containing polymeric sorbents
JP2019513539A (en) * 2016-03-14 2019-05-30 スリーエム イノベイティブ プロパティズ カンパニー Air filter containing polymeric sorbent for reactive gases
US10960341B2 (en) 2016-03-14 2021-03-30 3M Innovative Properties Company Air filters comprising polymeric sorbents for aldehydes
US11014070B2 (en) 2016-03-14 2021-05-25 3M Innovative Properties Company Composite granules including polymeric sorbent for reactive gases
CN115069098A (en) * 2022-08-23 2022-09-20 佛山(华南)新材料研究院 Alumina fiber filter membrane and preparation method thereof
WO2025031684A1 (en) * 2023-08-08 2025-02-13 Hydac Filter Systems Gmbh Process for the manufacture of a filter
WO2025031685A1 (en) * 2023-08-08 2025-02-13 Hydac Filter Systems Gmbh Process for the manufacture of a filter

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4101423A (en) 1975-04-04 1978-07-18 Millipore Corporation Tubular filtration element and method of making it
GB2182071B (en) * 1985-10-25 1989-11-08 Scott & Fyfe Ltd Composite sheet material
US6106897A (en) * 1996-08-09 2000-08-22 Scapa Group Plc Polymer pore structure
GB2316015B (en) * 1996-08-10 2000-08-30 Scapa Group Plc Polymer pore structure
US11000827B2 (en) 2016-03-14 2021-05-11 3M Innovative Properties Company Air filters comprising polymeric sorbents for reactive gases
US11014070B2 (en) 2016-03-14 2021-05-25 3M Innovative Properties Company Composite granules including polymeric sorbent for reactive gases
JP7010452B2 (en) 2016-03-14 2022-02-10 スリーエム イノベイティブ プロパティズ カンパニー Air filter containing polymer sorbent for reactive gas
EP3429725A4 (en) * 2016-03-14 2019-11-13 3M Innovative Properties Company Air filters comprising polymeric sorbents for reactive gases
JP2019513539A (en) * 2016-03-14 2019-05-30 スリーエム イノベイティブ プロパティズ カンパニー Air filter containing polymeric sorbent for reactive gases
US10960341B2 (en) 2016-03-14 2021-03-30 3M Innovative Properties Company Air filters comprising polymeric sorbents for aldehydes
US11045787B2 (en) 2016-03-14 2021-06-29 3M Innovative Properties Company Composite granules including polymeric sorbent for aldehydes
JP2020500694A (en) * 2016-11-14 2020-01-16 スリーエム イノベイティブ プロパティズ カンパニー Air filter containing metal-containing polymer adsorbent
WO2018089877A1 (en) * 2016-11-14 2018-05-17 3M Innovative Properties Company Air filters comprising metal-containing polymeric sorbents
US11103822B2 (en) 2016-11-14 2021-08-31 3M Innovative Properties Company Air filters comprising metal-containing polymeric sorbents
CN109922870B (en) * 2016-11-14 2021-11-02 3M创新有限公司 Air Filters Containing Metal-Containing Polymer Adsorbents
CN109922870A (en) * 2016-11-14 2019-06-21 3M创新有限公司 Air filter comprising the polymer absorbant containing metal
CN115069098A (en) * 2022-08-23 2022-09-20 佛山(华南)新材料研究院 Alumina fiber filter membrane and preparation method thereof
CN115069098B (en) * 2022-08-23 2022-11-08 佛山(华南)新材料研究院 A kind of alumina fiber filter membrane and preparation method thereof
WO2025031684A1 (en) * 2023-08-08 2025-02-13 Hydac Filter Systems Gmbh Process for the manufacture of a filter
WO2025031685A1 (en) * 2023-08-08 2025-02-13 Hydac Filter Systems Gmbh Process for the manufacture of a filter

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