# US 11,998,878 B2 · Composite hollow fiber and related methods and products > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,998,878 B2 - Document ID: US11998878B2 - Status: Granted - Kind: B2 - Application number: 16/817,351 - Filed: 2020-03-12 - Published: 2020-09-17 - Granted: 2024-06-04 - Earliest claimed: 2019-03-15 - Assignees: Entegris, Inc. - Applicants: Entegris, Inc. - Inventors: Sina Bonyadi - Web page: https://patentgrep.com/patent/US11998878B2 ## CPC - B01D 69/107: {Organic support material} - B01D 67/0016: {Coagulation} - B01D 69/08: Hollow fibre membranes (manufacture of hollow fibres D01D5/24, D01F1/08) - B01D 69/12: Composite membranes; Ultra-thin membranes - B01D 71/261: {Polyethylene} - B01D 71/641: {Polyamide-imides} - C02F 1/442: {by nanofiltration} - C02F 1/444: {by ultrafiltration or microfiltration} - B01D 61/14: Ultrafiltration; Microfiltration - B01D 71/56: Polyamides, e.g. polyester-amides - 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) - C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes) ## Abstract Described are composite hollow fibers filter membranes that include a porous polymeric hollow fiber support and a filter layer; methods of making the composite hollow fibers and using the composite hollow fibers as a filter membrane; methods of making a filter component or filter from the composite hollow fiber; and filter components and filters that contain the composite hollow fibers as filter membranes. ## Claims ### Claim 1 A composite hollow fiber filter membrane comprising: a polymeric, microporous, hollow fiber support comprising: an outer surface, an inner surface, a thickness extending between the outer surface and the inner surface, and micropores; and a porous polymeric filter layer that is not cured and comprises coagulated polymer precipitated onto the outer surface, wherein the porous polymeric filter layer has a porosity in a range from 60% to 85%, wherein the porous polymeric filter layer includes pores having an average pore size in a range from 10 nanometers to 8 microns, wherein the composite hollow fiber filter membrane exhibits a retention that exceeds 90% for monolayer coverages of 0.5%, 1.0%, 1.5%, and 2.0%, wherein the coagulated polymer is selected from the group consisting of polyimides, polyamides, polyamide-imides, and polysulfones, wherein the hollow fiber support (in the absence of the porous polymeric filter layer) has a thickness of from about 20 to 200 microns and is thicker than the porous polymeric filter layer, wherein the composite hollow fiber filter membrane is configured to filter a solvent selected from the group consisting of propylene glycol methyl ether (PGME), propylene glycol methylether acetate (PGMEA), and cyclohexanone, and wherein the porous polymeric filter layer is resistant to the solvent selected from the group consisting of propylene glycol methyl ether (PGME), propylene glycol methylether acetate (PGMEA), and cyclohexanone. ### Claim 2 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the porous polymeric filter layer includes the pores having the average pore size that is smaller than an average pore size of the micropores of the hollow fiber support. ### Claim 3 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the hollow fiber support has an average pore size of less than 10 microns. ### Claim 4 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the hollow fiber support (in the absence of the porous polymeric filter layer) has a thickness in a range from 30 to 150 microns. ### Claim 5 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the hollow fiber support comprises polyolefin or nylon. ### Claim 6 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the porous polymeric filter layer penetrates the thickness of the hollow fiber support to a depth of not greater than 2 microns. ### Claim 7 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the coagulated polymer is formed by immersion precipitation of filter layer polymer on the hollow fiber support. ### Claim 8 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the porous polymeric filter layer comprises polymer that is soluble in solvent selected from the group consisting of n-methyl pyrrolidone (NMP), dimethylformamide (DMF), dimethylacetamide (DMAc), and combinations thereof. ### Claim 9 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the coagulated polymer comprises polymer selected from the group consisting of polyimide and polyamide-imide. ### Claim 10 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the composite membrane has a flux in a range from 20 to 8000 LMH/bar and bubble point in a range from 50-500 psi measured using ethoxy-nonafluorobutane (HFE 7200) at a temperature of 25 degrees Celsius. ### Claim 11 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the porous polymeric filter layer penetrates partially into the thickness of the hollow fiber support. ### Claim 12 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the porous polymeric filter layer penetrates substantially into the thickness of the hollow fiber support. ### Claim 13 (depends on 1) The composite hollow fiber filter membrane of claim 1, wherein the porous polymeric filter layer includes the pores having the average pore size that is larger than an average pore size of the micropores of the hollow fiber support. ### Claim 14 A method of preparing a composite hollow fiber filter membrane comprising a polymeric, microporous, hollow fiber support and a porous polymeric filter layer, the method comprising: placing a polymer solution coating on an outer surface of the polymeric, microporous, hollow fiber support, the polymer solution comprising a polymer selected from the group consisting of polyimides, polyamides, polyamide-imides, and polysulfones dissolved in solvent and excluding curing reagents, and contacting the polymer solution coating with coagulation solution to cause dissolved polymer of the polymer solution coating to form a layer of coagulated polymer on the outer surface, the layer of coagulated polymer precipitated onto the outer surface and penetrating partially into a thickness of the polymeric, microporous, hollow fiber support, wherein the porous polymeric filter layer has a porosity in a range from 60% to 85%, wherein the porous polymeric filter layer includes pores having an average pore size in a range from 10 nanometers to 8 microns, wherein the composite hollow fiber filter membrane exhibits a retention that exceeds 90 for monolayer coverages of 0.5%, 1.0%, 1.5%, and 2.0% %, wherein the polymeric, microporous, hollow fiber support (in the absence of the porous polymeric filter layer) has a thickness of from about 20 to 200 microns and is thicker than the porous polymeric filter layer, wherein the composite hollow fiber filter membrane is configured to filter a solvent selected from the group consisting of propylene glycol methyl ether (PGME), propylene glycol methylether acetate (PGMEA), and cyclohexanone, and wherein the porous polymeric filter layer is resistant to the solvent selected from the group consisting of propylene glycol methyl ether (PGME), propylene glycol methylether acetate (PGMEA), and cyclohexanone. ### Claim 15 (depends on 14) The method of claim 14 further comprising, during placing: passing the polymeric, microporous, hollow fiber support through a central opening of an annular die, and passing the polymer solution through an annular opening of the annular die to place the polymer solution coating on the outer surface. ### Claim 16 (depends on 14) The method of claim 14, further comprising allowing for an amount of evaporation of the polymer solution coating before contacting the polymer solution coating with the coagulation solution. ### Claim 17 (depends on 14) The method of claim 14, wherein the coagulated polymer comprises polymer selected from the group consisting of polyimide and polyamide-imide. ### Claim 18 A filter comprising a composite hollow fiber filter membrane comprising: a polymeric, microporous, hollow fiber support comprising: an outer surface, an inner surface, a thickness extending between the outer surface and the inner surface, and micropores; and a porous polymeric filter layer that is not cured and comprises coagulated polymer precipitated onto the outer surface, wherein the porous polymeric filter layer has a porosity in a range from 60% to 85%, wherein the porous polymeric filter layer includes pores having an average pore size in a range from 10 nanometers to 8 microns, wherein the composite hollow fiber filter membrane exhibits a retention that exceeds 90 for monolayer coverages of 0.5%, 1.0%, 1.5%, and 2.0% %, wherein the coagulated polymer is selected from the group consisting of polyimides, polyamides, polyamide-imides, and poly sulfones, wherein the hollow fiber support (in the absence of the porous polymeric filter layer) has a thickness of from about 20 to 200 microns and is thicker than the porous polymeric filter layer, wherein the composite hollow fiber filter membrane is configured to filter a solvent selected from the group consisting of propylene glycol methyl ether (PGME), propylene glycol methylether acetate (PGMEA), and cyclohexanone, and wherein the porous polymeric filter layer is resistant to the solvent selected from the group consisting of propylene glycol methyl ether (PGME), propylene glycol methylether acetate (PGMEA), and cyclohexanone.