# US 8,465,565 B2 · Polyethylene membrane and method of its production > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 8,465,565 B2 - Document ID: US8465565B2 - Status: Granted - Kind: B2 - Application number: 12/866,872 - Filed: 2009-02-20 - Published: 2010-12-16 - Granted: 2013-06-18 - Earliest claimed: 2008-02-22 - Assignees: Lydall Solutech B.V. - Applicants: Gijsbertus Hendrikus Maria Calis; Hendrik Derk Hoving - Inventors: Gijsbertus Hendrikus Maria Calis; Hendrik Derk Hoving - Web page: https://patentgrep.com/patent/US8465565B2 ## CPC - B01D 71/261: {Polyethylene} - B01D 39/1623: {of synthetic origin} - B01D 39/2017: {the material being filamentary or fibrous} - B01D 39/2041: {the material being filamentary or fibrous} - B01D 39/2058: {the material being particulate} - B01D 39/2082: {the material being filamentary or fibrous} - B01D 46/543: {using membranes} - B01D 67/002: {from melts} - B01D 67/0027: {by stretching} - B01D 67/0086: {Mechanical after-treatment} - B01D 69/02: characterised by their properties - B01D 2239/0241: comprising electrically conductive fibres or particles - B01D 2239/025: comprising nanofibres - B01D 2239/0407: comprising particulate additives, e.g. adsorbents - B01D 2239/0442: Antimicrobial, antibacterial, antifungal additives - B01D 2239/045: Deodorising additives - B01D 2239/0457: Specific fire retardant or heat resistant properties - B01D 2239/064: The fibres being mixed - B01D 2239/065: More than one layer present in the filtering material - B01D 2239/0654: Support layers - B01D 2239/1208: Porosity - B01D 2239/1225: Fibre length - B01D 2239/1233: Fibre diameter - B01D 2239/1241: Particle diameter - B01D 2239/1291: Other parameters - B01D 2325/20: Specific permeability or cut-off range - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) ## Abstract The invention relates to a porous membrane having a particle filtration value of at least 10 under U.S. Military Standard MIL-STD-282 (1956), where the porous membrane is a polyethylene membrane. The membranes according to the invention are particularly useful for filters such as ASHRAE filters, HEPA filters and ULPA filters for example in heating, ventilating, respirators and air conditioning applications. ## Claims ### Claim 1 A gas filtration media, comprising a multilayered polyethylene membrane having a particle filtration, PF, value calculated according to the formula: PF=(-log(Penetration (%)/100)/Pressure loss (mm H2O))×100 in which the Penetration (%)=100-Collection efficiency at a Pressure loss (unit: mm H2O) measured when air is flowing through the membrane at a flow velocity of 5.3 cm/second and a collection efficiency (unit: %) measured using dioctyl phthalate having a particle size of 0.3 μm (U.S. Military Standard MIL-STD-282 (1956)), the PF value of the membrane is at least 20, and wherein the membrane has a porosity of at least 88 vol-%, a thickness of greater than 10 μm to less than 200 μm, and an average pore size of at least 0.5 μm, wherein the polyethylene is stretched in a transverse directions by a factor of at least 10 times the area and in the machine direction alone is stretched by a factor of at least 2.5 times the area. ### Claim 2 (depends on 1) Membrane according to claim 1, wherein the membrane is a freestanding membrane. ### Claim 3 (depends on 1) Membrane according to claim 1, wherein the pressure loss according to U.S. Military Standard MIL-STD-282 (1956) is at least 3 mm H2O and less than 30 mm H2O when the air is passing through the membrane at a flow velocity of 5.3 cm/sec. ### Claim 4 (depends on 1) Membrane according to claim 1, wherein a Gurley value according to ISO 5636-5 is less than 5 s/50 ml. ### Claim 5 (depends on 4) Membrane according to claim 4, wherein the collection efficiency is at least 90%, when air is flowing through the membrane at a flow velocity of 5.3 cm/second and a collection efficiency (unit: %) measured using dioctyl phthalate having a particle size of 0.3 μm (U.S. Military Standard MIL-STD-282 (1956)). ### Claim 6 (depends on 1) Membrane according to claim 1, wherein said porous polyethylene membrane is a stretched polyethylene membrane having a multi layered structure of fibril webs, wherein a cross-section of the membrane has 1 to 12 fibril webs/30 μm. ### Claim 7 (depends on 6) Membrane according to claim 6 having a combination of microfibers with internal nanofibers, wherein the microfibers having a size of 1-10 μm and length of 5-50 μm and the nanofibers having a size 10-150 nm in thickness and 2-20 μm in length. ### Claim 8 (depends on 1) Membrane according to claim 1, wherein the porous polyethylene membrane comprises at least one component selected from the group consisting of flame retardants, fillers, electrically conducting materials, anti fouling additives, and anti odor additives. ### Claim 9 (depends on 1) Membrane according to claim 1, wherein the porous polyethylene film comprises at least 50 wt-% polyethylene and about 1-50 wt-% of component(s) selected from the group consisting of metal, metal oxide, ceramic powder, oxidized PE, PEO, PTFE, micronized wax blends, PE copolymers, activated carbon, carbon black, polymeric resins other than PE, and combinations thereof. ### Claim 10 (depends on 9) Membrane according to claim 9, further comprising an additive selected from the group consisting of active carbon, carbon black, graphite, high surface area metallic powders, carbon nanotubes, synthetic oxides, naturally occurring oxides, hydroxides and fiber material. ### Claim 11 (depends on 1) Membrane according to claim 1, wherein at least 20 wt-% and less than 80 wt-% of the porous polyethylene film is UHMWPE, and at least 5 wt-% and less than 80 wt-% of the porous polyethylene film is HMWPE. ### Claim 12 (depends on 1) Membrane according to claim 1 having an air-permeable support member laminated on at least one surface of said membrane, wherein the support member is a laminate comprising a nonwoven, woven, spunweb, web and/or grid member, and the support member comprises a material selected from the group consisting of PET, ECTFE, PA, PBT, PPS, PP, PE, ePTFE, UHMWPE, and copolymers comprising any one of these, mixed cellulose ester, polyvinylchloride, cellulose triacetate, ceramic, and glass, and the support member and the membrane being bonded to each other by ultrasonic welding, gluing, thermo bonding or by laser welding. ### Claim 13 A method of preparing a gas filtration membrane comprising the steps of: providing a mixture of a solvent and a polyethylene optionally with a further component, wherein the polyethylene optionally with the further component is about 5 to 30 weight percent of the total weight of the solvent, extruding a membrane from the mixture, removing the solvent to form a base member, and stretching the membrane by a factor of at least 2.5 to 10 times the original length in a machine direction at a deformation speed of less than 30 mm/s and by a factor of 3 to 10 times the original length in a transverse direction at a speed that provides the membrane for use as a gas filtration media having a PF value of more than 20, a porosity of at least 88 vol-% and an average pore size of at least 0.5 μm. ### Claim 14 (depends on 13) Method according to claim 13, wherein the solvent is removed by evaporation before stretching of the base member. ### Claim 15 (depends on 1) An air filter pack comprising a pleated membrane according to claim 1. ### Claim 16 (depends on 13) Method according to claim 13, wherein the step of stretching the membrane in the machine direction is conducted simultaneously to the stretching in the transverse direction. ### Claim 17 Gas filtration membrane prepared by a process comprising: extruding a solution comprising a polyethylene polymer having a solids content of 10 to 25 weight percent to form a porous multilayered structure; stretching the porous polyethylene multilayered structure in a transverse direction by a factor of at least 10 times the extruded width and in the machine direction by a factor of at least 2.5 times the extruded length to form a membrane, wherein the membrane has a particle filtration, PF, value calculated according to the formula: PF=(-log(Penetration (%)/100)/Pressure loss (mm H2O))×100 in which the Penetration (%)=100-Collection efficiency at a Pressure loss (unit: mm H2O) measured when air is flowing through the membrane at a flow velocity of 5.3 cm/second and a collection efficiency (unit: %) measured using dioctyl phthalate having a particle size of 0.3 μm (U.S. Military Standard MIL-STD-282 (1956)), the PF value of the membrane is at least 20, and wherein the membrane has a porosity of at least 88 vol-%, a thickness of greater than 10 μm to less than 200 μm and an average pore size of at least 0.5 μm.