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 productInfo
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title abstract 3
- 239000007788 liquid Substances 0.000 abstract 18
- 239000006185 dispersion Substances 0.000 abstract 12
- 239000011236 particulate material Substances 0.000 abstract 12
- 239000000758 substrate Substances 0.000 abstract 12
- 238000004873 anchoring Methods 0.000 abstract 8
- 239000007767 bonding agent Substances 0.000 abstract 8
- 238000000151 deposition Methods 0.000 abstract 8
- 239000002245 particle Substances 0.000 abstract 8
- 239000011148 porous material Substances 0.000 abstract 8
- 230000008021 deposition Effects 0.000 abstract 6
- 239000000463 material Substances 0.000 abstract 6
- 229920005989 resin Polymers 0.000 abstract 6
- 239000011347 resin Substances 0.000 abstract 6
- 230000000844 anti-bacterial effect Effects 0.000 abstract 4
- 239000003795 chemical substances by application Substances 0.000 abstract 4
- 239000011248 coating agent Substances 0.000 abstract 4
- 238000000576 coating method Methods 0.000 abstract 4
- -1 polyethylene Polymers 0.000 abstract 4
- 239000007787 solid Substances 0.000 abstract 4
- 239000005909 Kieselgur Substances 0.000 abstract 2
- 239000004698 Polyethylene Substances 0.000 abstract 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 2
- 150000001298 alcohols Chemical class 0.000 abstract 2
- 150000001412 amines Chemical class 0.000 abstract 2
- 239000003899 bactericide agent Substances 0.000 abstract 2
- 230000015572 biosynthetic process Effects 0.000 abstract 2
- 230000006835 compression Effects 0.000 abstract 2
- 238000007906 compression Methods 0.000 abstract 2
- 239000000470 constituent Substances 0.000 abstract 2
- NJLLQSBAHIKGKF-UHFFFAOYSA-N dipotassium dioxido(oxo)titanium Chemical compound [K+].[K+].[O-][Ti]([O-])=O NJLLQSBAHIKGKF-UHFFFAOYSA-N 0.000 abstract 2
- 239000002270 dispersing agent Substances 0.000 abstract 2
- 239000000835 fiber Substances 0.000 abstract 2
- 239000008394 flocculating agent Substances 0.000 abstract 2
- 230000016615 flocculation Effects 0.000 abstract 2
- 238000005189 flocculation Methods 0.000 abstract 2
- 239000011521 glass Substances 0.000 abstract 2
- 150000002334 glycols Chemical class 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 2
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- 150000002484 inorganic compounds Chemical class 0.000 abstract 2
- 229910010272 inorganic material Inorganic materials 0.000 abstract 2
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract 2
- 229910052751 metal Inorganic materials 0.000 abstract 2
- 239000002184 metal Substances 0.000 abstract 2
- 150000002739 metals Chemical class 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 2
- 239000011707 mineral Substances 0.000 abstract 2
- 239000000203 mixture Substances 0.000 abstract 2
- 230000035515 penetration Effects 0.000 abstract 2
- 239000004033 plastic Substances 0.000 abstract 2
- 229920003023 plastic Polymers 0.000 abstract 2
- 229920000647 polyepoxide Polymers 0.000 abstract 2
- 229920000573 polyethylene Polymers 0.000 abstract 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 abstract 2
- 239000004810 polytetrafluoroethylene Substances 0.000 abstract 2
- 239000000843 powder Substances 0.000 abstract 2
- 239000000126 substance Substances 0.000 abstract 2
- 239000000725 suspension Substances 0.000 abstract 2
- 229920003051 synthetic elastomer Polymers 0.000 abstract 2
- 229920003002 synthetic resin Polymers 0.000 abstract 2
- 239000000057 synthetic resin Substances 0.000 abstract 2
- 239000005061 synthetic rubber Substances 0.000 abstract 2
- 239000004753 textile Substances 0.000 abstract 2
- 229920001169 thermoplastic Polymers 0.000 abstract 2
- 229920001187 thermosetting polymer Polymers 0.000 abstract 2
- 239000004416 thermosoftening plastic Substances 0.000 abstract 2
- 235000013311 vegetables Nutrition 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 239000000080 wetting agent Substances 0.000 abstract 2
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters 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
- B01D29/111—Making filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters 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
- B01D29/13—Supported filter elements
- B01D29/15—Supported filter elements arranged for inward flow filtration
- B01D29/21—Supported 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.
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)
| 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 |
-
1964
- 1964-11-30 GB GB48642/64A patent/GB1066480A/en not_active Expired
Cited By (20)
| 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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