US4073870A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing carbon fibers
Assignee: Teijin Ltd
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Filing: 1976-04-01
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Granted: 1978-02-14
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Expires: 1996-04-01
Abstract
Abstract A process for producing carbon fibers which comprises feeding an inert gas into a vertical furnace at about 500 to about 1,000° C. and into a transverse furnace at about 800 to about 2,000° C. connected thereto so that the inert gas flows from the transverse furnace toward the bottom of the vertical furnace and then to the top of the vertical furnace, and feeding preoxidized fibers from the top of the vertical furnace to pass the fibers countercurrent to the inert gas flow through the two furnaces to thereby carbonize the fibers. Apparatus of the type shown in the drawing for the production of carbon fibers by the above process. Carbon fibers having good performance can be produced with good efficiency.
Inventors
- 👤 Yasuo Saji
- 👤 Hideo Kurioka
- 👤 Kozo Tanaka
- 👤 Hiroyasu Ogawa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 00:30
CPC Classifications
D; D01; D01F; D01F9/00; D01F9/08; D01F9/12; D01F9/14; D01F9/20; D01F9/21; D01F9/22; D01F9/32
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
191 words
A process for producing carbon fibers which comprises feeding an inert gas into each of a vertical furnace maintained at about 500° C to about 1,000° C and a transverse furnace maintained at about 800° to about 2,000° C connected thereto so that the inert gas flows from the transverse furnace toward the bottom and then the top of the vertical furnace, and feeding preoxidized organic polymer fibers from the top of the vertical furnace to pass the fibers countercurrent to the inert gas flow through the two furnaces to thereby carbonize the fibers and obtain said carbon fibers, wherein: during the entire process within the vertical and transverse furnace the advancing direction of the fibers treated is countercurrent to the direction in which the inert gas flows; volatile components are generated in high amounts at the upper portion of the vertical furnace and there is substantially no generation of volatile components in the transverse furnace; and the feeding of the preoxidized fibers and the discharging of the inert gas containing the volatile components are carried out through the same slit whose temperature is maintained at about 200° to 400° C.
Claim 2
Dependent Claim
191 words
A process for producing carbon fibers which comprises feeding an inert gas into each of a vertical furnace maintained at about 500° C to about 1,000° C and a transverse furnace maintained at about 800° to about 2,000° C connected thereto so that the inert gas flows from the transverse furnace toward the bottom and then the top of the vertical furnace, and feeding preoxidized organic polymer fibers from the top of the vertical furnace to pass the fibers countercurrent to the inert gas flow through the two furnaces to thereby carbonize the fibers and obtain said carbon fibers, wherein: during the entire process within the vertical and transverse furnace the advancing direction of the fibers treated is countercurrent to the direction in which the inert gas flows; volatile components are generated in high amounts at the upper portion of the vertical furnace and there is substantially no generation of volatile components in the transverse furnace; and the feeding of the preoxidized fibers and the discharging of the inert gas containing the volatile components are carried out through the same slit whose temperature is maintained at about 200° to 400° C.
Claim 3
Dependent Claim
44 words
The process of claim 1 wherein said preoxidized fibers are obtained by heat treating polyacrylonitrile fibers, said polyacrylonitrile fibers being fibers of a homopolymer of acrylonitrile or a copolymer of at least about 90% by weight of acrylonitrile and a vinyl monomer copolymerizable therewith.
Claim 4
Dependent Claim
41 words
The process of claim 2 wherein the polyacrylonitrile fibers are heat treated in an oxidizing atmosphere at about 200° to about 300° C until their oxygen content becomes about 5 to about 15% by weight to thereby yield said preoxidized fiber.
Claim 5
Dependent Claim
43 words
The process of claim 2 wherein the vinyl monomer is a member selected from the group consisting of an acrylic ester, a methacrylic ester, vinyl acetate, acrylamide, N-methylolacrylamide, acrylic acid, methacrylic acid, vinylsulfonic acid, allylsulfonic acid, methallylsulfonic acid and salts of said acids.
Claim 6
Dependent Claim
29 words
The process of claim 1, wherein the generation of volatile components from preoxidized fibers is mostly completed in the temperature range of from about 500° to about 1000° C.
Claim 7
Dependent Claim
25 words
The process of claim 5, wherein said inert gas permits the volatile components to be discharged from the top of the vertical furnace without condensation.
Claim 8
Dependent Claim
26 words
The process of claim 1 wherein in the vertical furnace the preoxidized fibers are carbonized until their carbon content becomes at least about 75% by weight.
Claim 9
Dependent Claim
13 words
The process of claim 1 wherein said inert gas is nitrogen or argon.
Claim 10
Dependent Claim
17 words
The process of claim 1, wherein said preoxidized fibers are obtained by heat treating regenerated cellulose fibers.
Claim 11
Dependent Claim
22 words
The process of claim 1, wherein said vertical furnace and said transverse furnace are arranged substantially at right angles to each other.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-02-13 | 1981-08-15 | 1982-02-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-02-13 | 1985-08-15 | 1986-02-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-02-13 | 1989-08-15 | 1990-02-14 | $7700.00 | Window Closed / Lapsed |