Patent US3863000A successfully refreshed from Google Patents.
US3863000A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of manufacturing a tough thermoplastic resin foam
Assignee: Furukawa Electric Co Ltd
•
Filing: 1972-10-18
•
Granted: 1975-01-28
•
Expires: 1992-10-18
Abstract
Abstract A method of manufacturing a tough thermoplastic resin foam having a low density and large cell size which comprises extruding a mixture of a thermoplastic resin and foaming agent through an extruder at temperatures slightly higher than the softening point of the mixture to create foam nuclei, and thereafter slowly cooling the extruded mixture to make the foam nuclei grow and form cells more than 5 mm in diameter.
Inventors
- 👤 Akira Kasai
- 👤 Mitsuo Inui
- 👤 Nobuo Hoshino
- 👤 Kenichi Hattori
- 👤 Naonori Shiina
- 👤 Hiroyuki Nakae
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 06:48
CPC Classifications
B; B29; B29C; B29C44/00; B29C44/34; B29C44/36; B29C44/46; B29C44/50; B29C44/505; B29C48/00; B29C48/25; B29C48/92; B29C2948/00; B29C2948/92; B29C2948/92009; B29C2948/92114; B29C2948/92323; B29C2948/92428; B29L; B29L2007/00; Y; Y10; Y10S; Y10S264/00; Y10S264/13; Y10S264/14
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
34 words
A method according to claim 1 wherein said cooling is carried out at such a rate that the growth of cells is completed in 2 to 25 minutes after the extrusion of said mixture.
Claim 2
Dependent Claim
39 words
A method according to claim 1 wherein the thermoplastic resin is one selected from the group consisting of polyolefins, copolymers of olefins, polystyrene, copolymers of styrene, polyvinyl chloride, copolymers of vinyl chloride, acrylic resin, polyamide, polyester, polyacetal and polycarbonate.
Claim 3
Dependent Claim
23 words
A method according to claim 3 wherein the polyolefin is one selected from the group consisting of polyethylene, polypropylene, polybutene and copolymers thereof.
Claim 4
Dependent Claim
21 words
A method according to claim 4 wherein the polyethylene is high density polyethylene having a melt index of less than 1.
Claim 5
Dependent Claim
43 words
A method according to claim 1 wherein the volatile foaming agent is one selected from the group consisting of hydrocarbons, halogenated hydrocarbons, alcohols, ethers and esters and mixtures thereof, all having a boiling point lower than the softening point of the thermoplastic resin.
Claim 6
Dependent Claim
12 words
A method according to claim 6 wherein the halogenated hydrocarbon is trichloromonofluoroethane.
Claim 7
Dependent Claim
33 words
A method according to claim 1 wherein the volatile foaming agent is used in an amount of 6 to 15 parts by weight based on 100 parts by weight of the thermoplastic resin.
Claim 8
Dependent Claim
35 words
A method according to claim 1 wherein a material selected from the group consisting of calcium carbonate, clay, talc, zinc white, silicate, glass powders, carbon black and wooden powders is used as a nucleating agent.
Claim 9
Dependent Claim
22 words
A method according to claim 1 wherein said mixture is extruded in the form of any of a rod, pipe and board.
Claim 10
Dependent Claim
20 words
A method according to claim 1 wheRein said extruded mixture is expanded to a thickness of 10 to 200 mm.
Claim 11
Dependent Claim
29 words
A method according to claim 1 wherein the thermoplastic resin is incorporated with an additive selected from the group consisting of a pigment, antioxidant, ultraviolet absorber and flame retardant.
Claim 12
Independent Claim
224 words
A method of manufacturing a tough thermoplastic resin foam having a low density and large cell size which comprises a. introducing into an extruder a thermoplastic resin, 2 to 20 parts by weight of a volatile foaming agent based on 100 parts by weight of said resin and soluble in said resin at extruding temperature and less than 3 parts by weight of a nucleating agent based on 100 parts by weight of said resin, b. extruding into the atmosphere the mixture in the form of a board through a die orifice at a temperature between the softening or melting point of said mixture and a temperature 20*C higher than the softening or melting point of the thermoplastic resin itself, c. cooling the surfaces of the board rapidly by blowing cooled gas, spraying liquid, placing the board in contact with a cooled metal material or fixing a cooling sheet-like material to form skin layers on both sides thereof, and d. cooling the board with skin layers slowly to cause the formation of foam nuclei therein and to make cells grow more than 5 mm in average cell diameter by permitting the extruded mixture to stand in the open air or placing it in a heat transfer medium, while taking up the board at a speed less than the extrusion speed at the die orifice.
Claim 13
Dependent Claim
35 words
A method according to claim 13 wherein said slow cooling is carried out at such a rate that the growth of cells is completed in 2 to 25 minutes after the extrusion of said board.
Claim 14
Independent Claim
270 words
A method of manufacturing a board formed of tough thermoplastic resin foam surfaced on both sides thereof with hard skin layers about 1 mm thick, more than 50 percent of cells of the resin foam having a diameter of more than 5 mm, the thickness of the board being between about 10 to 200 mm and the density of the board being between about 0.05 to 0.3 g./cc., which comprises: a. Introducing into an extruder a thermoplastic resin, 2 to 20 parts of a volatile foaming agent based on 100 parts of said resin and soluble in said resin at extruding temperature and less than 3 parts by weight of a nucleating agent based on 100 parts by weight of said resin, b. extruding into the atmosphere the mixture in the form of a board through a die orifice at a temperature between the softening or melting point of said mixture and a temperature 20*C higher than the softening or melting point of said thermoplastic resin, c. cooling the surfaces of the board rapidly by blowing cooled gas, spraying liquid, placing the board in contact with a cooled metal material or fixing a cooling sheet-like material to form skin layers on both sides therof, and d. cooling the board with skin layers slowly to cause the formation of foam nuclei therein and to make cells grow more than 5 mm in average cell diameter by permitting the extruded mixture to stand in the open air or placing it in a heat transfer medium, while taking up the board at a speed less than the extrusion speed at the die orifice.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1978-01-27 | 1978-07-29 | 1979-01-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-01-27 | 1982-07-29 | 1983-01-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-01-27 | 1986-07-29 | 1987-01-28 | $7700.00 | Window Closed / Lapsed |