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US4320107A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing carbon fibers

Assignee: SANKO GAS CHEMICAL Co Ltd
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Filing: 1979-11-23
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Granted: 1982-03-16
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Expires: 1999-11-23
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Abstract

Abstract A fibrous carbon is prepared by dissolving coal in a hydrocarbon solvent by heating under hydrogen pressure, by subjecting to melt spinning a solvent-refined coal obtained by successively removing insoluble residues and the solvent from the resultant solution, by making the fiber thus obtained non-fusible, and then by subjecting same to carbonization. The melt spinning may be effected by mixing a highly aromatic bituminous substance with the solvent refined coal. Alternatively, the solvent-refined coal may be pretreated prior to melt spinning by extracting it with a non-aromatic solvent to remove soluble components therefrom.

Inventors

  • 👤 Mikio Oyabu
  • 👤 Kenji Fukuda
  • 👤 Keiichi Hirata

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 20:28
CPC Classifications
D; D01; D01F; D01F9/00; D01F9/08; D01F9/12; D01F9/14; D01F9/145; D01F9/15

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 115 words
A process for producing carbon fibers which comprises: (a) providing as a starting material a solid solvent-refined coal having a softening point of from 200° C. to 250° C. and an insolubles content of 0.5% by weight or less, said solid solvent-refined coal being obtained by hydrogenating coal in a hydrocarbon solvent at a temperature of 300°-500° C. under a hydrogen pressure of 3-300 Kg/cm 2 and eliminating the hydrocarbon solvent; (b) subjecting said solvent-refined coal to melt spinning to form a fiber; (c) heating said fiber in air at a rate of 3-10° C./minute to render said fiber non-fusible; and (d) carbonizing said non-fusible fiber in an inert atmosphere to form said carbon fiber.
Claim 2
Dependent Claim 115 words
A process for producing carbon fibers which comprises: (a) providing as a starting material a solid solvent-refined coal having a softening point of from 200° C. to 250° C. and an insolubles content of 0.5% by weight or less, said solid solvent-refined coal being obtained by hydrogenating coal in a hydrocarbon solvent at a temperature of 300°-500° C. under a hydrogen pressure of 3-300 Kg/cm 2 and eliminating the hydrocarbon solvent; (b) subjecting said solvent-refined coal to melt spinning to form a fiber; (c) heating said fiber in air at a rate of 3-10° C./minute to render said fiber non-fusible; and (d) carbonizing said non-fusible fiber in an inert atmosphere to form said carbon fiber.
Claim 3
Dependent Claim 33 words
A process according to claim 1 in which said heating to render said fiber non-fusible is effected at a temperature 60° to 80° C. higher than the softening point of said solvent-refined coal.

References Cited (Backward Citations)

US3959448A Cited
US3629379A Cited
US3767741A Cited
US4146576A Cited
US4055583A Cited
US4210517A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-03-15 1985-09-14 1986-03-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-03-15 1989-09-14 1990-03-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-03-15 1993-09-14 1994-03-16 $7700.00 Window Closed / Lapsed

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