# US 5,702,658 A · Bicomponent polymer fibers made by rotary process > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,702,658 A - Document ID: US5702658A - Status: Granted - Kind: A - Application number: 08/608,795 - Filed: 1996-02-29 - Granted: 1997-12-30 - Earliest claimed: 1996-02-29 - Assignees: Owens Corning Fiberglas Technology, Inc. - Inventors: Michael T. Pellegrin; Patrick M. Gavin; Patrick L. Ault; James E. Loftus; Randall M. Haines; Virgil Morris - Web page: https://patentgrep.com/patent/US5702658A ## CPC - D01D 5/18: by means of rotating spinnerets - D01D 5/34: Core-skin structure; Spinnerette packs therefor - D01F 8/04: from synthetic polymers - D01D: MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS - D01F: CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS ## Abstract In a method for making bicomponent polymer fibers, first and second molten polymers are supplied to a rotating spinner having an orificed peripheral wall. The molten polymers are centrifuged through the orifices as molten bicomponent polymer streams. The streams are cooled to make bicomponent polymer fibers. ## Claims ### Claim 1 A method for making multicomponent fibers of thermoplastic material comprising: supplying at least first and second molten thermoplastic materials to a rotating spinner having an orificed peripheral wall; centrifuging the molten thermoplastic materials through the orifices as molten multicomponent streams of thermoplastic material; and cooling the streams to make multicomponent fibers of thermoplastic material. ### Claim 2 (depends on 1) The method of claim 1 in which the multicomponent fibers are bicomponent fibers and the melting point of the first thermoplastic material is different from the melting point of the second thermoplastic material by an amount greater than about 10.degree. C. ### Claim 3 (depends on 2) The method of claim 2 in which the melting point of the first thermoplastic material is different from the melting point of the second thermoplastic material by an amount greater than about 25.degree. C. ### Claim 4 (depends on 1) The method of claim 1 in which the multicomponent fibers are bicomponent fibers and the coefficient of thermal expansion of the first thermoplastic material is different from the coefficient of thermal expansion of the second thermoplastic material by an amount greater than about 5.0 ppm/.degree.C. ### Claim 5 (depends on 4) The method of claim 4 in which the coefficient of thermal expansion of the first thermoplastic material is different from the coefficient of thermal expansion of the second thermoplastic material by an amount greater than about 10.0 ppm/.degree.C. ### Claim 6 (depends on 1) The method of claim 1 in which the multicomponent fibers are bicomponent fibers having an average outside diameter of from about 5 microns to about 50 microns. ### Claim 7 (depends on 6) The method of claim 6 in which the bicomponent fibers have an average outside diameter of from about 5 microns to about 35 microns. ### Claim 8 (depends on 1) The method of claim 1 in which the multicomponent fibers are bicomponent fibers and the viscosity of the first thermoplastic material is different from the viscosity of the second thermoplastic material by a factor within the range of from about 5 to about 1000. ### Claim 9 (depends on 1) The method of claim 1 in which the multicomponent fibers are bicomponent fibers, and additionally comprising the steps of collecting the bicomponent polymer fibers as a wool pack and subjecting the wool pack to a temperature greater than the melting point of the second polymer but less than the melting point of the first polymer. ### Claim 10 (depends on 1) The method of claim 1 in which the multicomponent fibers are bicomponent fibers and the melting point of the first polymer is different from the melting point of the second polymer by an amount greater than about 10.degree. C., the coefficient of thermal expansion of the first polymer is different from the coefficient of thermal expansion of the second polymer by an amount greater than about 2.0 ppm/.degree.C., and the fibers have an average outside diameter of from about 5 microns to about 50 microns. ### Claim 11 (depends on 10) The method of claim 10 in which the bicomponent fibers of thermoplastic material comprise, by weight, from about 40% to about 60% first thermoplastic material and from about 40% to about 60% second thermoplastic material. ### Claim 12 (depends on 10) The method of claim 10 in which the first thermoplastic material is a polymer selected from the group consisting of poly(phenylene sulfide), poly(ethylene terephthalate), poly(butylene terephthalate), polycarbonate, polyamide, and mixtures thereof. ### Claim 13 (depends on 10) The method of claim 10 in which the second thermoplastic material is a polymer selected from the group consisting of polyethylene, polypropylene, polystyrene, asphalt, and mixtures thereof. ### Claim 14 A method for making bicomponent fibers of thermoplastic material comprising: supplying first and second molten thermoplastic materials to a rotating spinner having an orificed peripheral wall, where the melting point of the first thermoplastic material is different from the melting point of the second thermoplastic material by an mount greater than about 10.degree. C.; centrifuging the molten thermoplastic materials through the orifices as molten bicomponent streams of thermoplastic material; and cooling the streams to make bicomponent fibers of thermoplastic material. ### Claim 15 (depends on 14) The method of claim 14 in which the coefficient of thermal expansion of the first thermoplastic material is different from the coefficient of thermal expansion of the second thermoplastic material by an amount greater than about 2.0 ppm/.degree.C. ### Claim 16 (depends on 14) The method of claim 14 in which the bicomponent fibers have an average outside diameter of from about 5 microns to about 50 microns. ### Claim 17 (depends on 14) The method of claim 14 in which the first thermoplastic material is a polymer selected from the group consisting of poly(phenylene sulfide), poly(ethylene terephthalate), poly(butylene terephthalate), polycarbonate, polyamide, and mixtures thereof. ### Claim 18 (depends on 14) The method of claim 14 in which the second thermoplastic material is a polymer selected from the group consisting of polyethylene, polypropylene, polystyrene, asphalt, and mixtures thereof. ### Claim 19 A method for making bicomponent fibers of thermoplastic material comprising: supplying first and second molten thermoplastic materials to a rotating spinner having an orificed peripheral wall, where, the first thermoplastic material is a material selected from the group consisting of poly(phenylene sulfide), poly(ethylene terephthalate), poly(butylene terephthalate), polycarbonate, polyamide, polyethylene, polypropylene, polystyrene, asphalt, and mixtures thereof, and the second thermoplastic material is a different material selected from the group consisting of poly(phenylene sulfide), poly(ethylene terephthalate), poly(butylene terephthalate), polycarbonate, polyamide, polyethylene, polypropylene, polystyrene, asphalt, and mixtures thereof; centrifuging the molten thermoplastic materials through the orifices as molten bicomponent streams of thermoplastic material; and cooling the streams to make bicomponent fibers of thermoplastic material. ### Claim 20 (depends on 19) The method of claim 19 in which the melting point of the first thermoplastic material is different from the melting point of the second thermoplastic material by an amount greater than about 10.degree. C., and in which the viscosity of the first thermoplastic material is different from the viscosity of the second thermoplastic material by a factor within the range of from about 5 to about 1,000.