US4863708A
Expired / Lapsed
US
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Process for producing carbon fibers and the carbon fibers produced by the process
Assignee: Kureha Corp
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Filing: 1989-01-03
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Granted: 1989-09-05
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Expires: 2009-01-03
Abstract
Abstract Disclosed herein is a process for producing pitch-based carbon fibers having the specific properties comparable to those of polyacrylonitrile(PAN)-based carbon fibers, wherein an optically isotropic pitch obtained by polymerizing naphthalene at a temperature of not more than 330° C. and heating the thus obtained polymeric material at a temperature of 330° to 440° C. while introducing an inert gas thereinto to remove volatile components therefrom, is subjected to melt-spinning, infusibilization (therosetting) and carbonization and the thus obtained carbonized-fibers are subjected to heat treatment at a temperature of not less that 900° C. to obtain the carbon fibers.
Inventors
- 👤 Ikuo Seo
- 👤 Yasuo Sakaguchi
- 👤 Ken Kashiwadate
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 17:54
CPC Classifications
C; C10; C10C; C10C3/00; D; D01; D01F; D01F9/00; D01F9/08; D01F9/12; D01F9/14; D01F9/20; D01F9/24
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
245 words
In a process for producing carbon fibers comprising polymerizing naphthalene at a temperature of not more than 330° C. in the presence of a Lewis acid catalyst for 0.5 to 100 hours, after removing the catalyst from reaction mixture, heating the thus obtained polymeric material under an atmospheric pressure or a reduced pressure while introducing an inert gas thereinto to remove volatile components therefrom, thereby obtaining a pitch for melt-spinning, melt-spinning pitch fibers from the thus obtained pitch, infusibilizing the thus obtained pitch fibers, carbonizing the thus infusibilized fibers by heating to a temperature of 900° C. or less in an inert atmosphere and subjecting the thus obtained carbon fibers to heat treatment at a temperature of not less than 900° C., the improvements comprising (1) heat-treating a polymeric material of naphthalene at a temperature of 330° to 440° C. for not more than 40 minutes to produce an optically isotropic pitch having a softening point of 180° to 200° C., an atomic ratio of hydrogen to carbon (H/C) of 0.6 to 0.8 and an average molecular weight of 800 to 1500, and containing 35 to 45% by weight of benzene-insoluble without containing any quinoline-insolubles and (2) melt-spinning pitch fibers from said optically isotropic pitch, and infusibilizing and carbonizing the pitch fibers, thereby obtaining carbon fibers having an apparent crystallite size (L c (002)) of 15 to 200 Å and an interlayer spacing (d 002 ) of 3.371 to 3.47 Å measured by X-ray diffractometry.
Claim 2
Dependent Claim
245 words
In a process for producing carbon fibers comprising polymerizing naphthalene at a temperature of not more than 330° C. in the presence of a Lewis acid catalyst for 0.5 to 100 hours, after removing the catalyst from reaction mixture, heating the thus obtained polymeric material under an atmospheric pressure or a reduced pressure while introducing an inert gas thereinto to remove volatile components therefrom, thereby obtaining a pitch for melt-spinning, melt-spinning pitch fibers from the thus obtained pitch, infusibilizing the thus obtained pitch fibers, carbonizing the thus infusibilized fibers by heating to a temperature of 900° C. or less in an inert atmosphere and subjecting the thus obtained carbon fibers to heat treatment at a temperature of not less than 900° C., the improvements comprising (1) heat-treating a polymeric material of naphthalene at a temperature of 330° to 440° C. for not more than 40 minutes to produce an optically isotropic pitch having a softening point of 180° to 200° C., an atomic ratio of hydrogen to carbon (H/C) of 0.6 to 0.8 and an average molecular weight of 800 to 1500, and containing 35 to 45% by weight of benzene-insoluble without containing any quinoline-insolubles and (2) melt-spinning pitch fibers from said optically isotropic pitch, and infusibilizing and carbonizing the pitch fibers, thereby obtaining carbon fibers having an apparent crystallite size (L c (002)) of 15 to 200 Å and an interlayer spacing (d 002 ) of 3.371 to 3.47 Å measured by X-ray diffractometry.
Claim 3
Dependent Claim
31 words
The process according to claim 1, wherein the heat-treatment of said polymeric material of naphthalene is carried out at a temperature of 350° to 420° C. for 1 to 30 minutes.
Claim 4
Dependent Claim
94 words
The process according to claim 1, wherein carbonized fibers obtained form said optically isotropic pitch are subjected to heat treatment at a temperature of 900° to 1600° C., thereby producing carbon fibers having a preferred orientation (22°) of larger than 50°, an apparent crystallite size (L c (002)) of 15 to 50 Å and an interlayer spacing (d 002 ) of 3.44 to 3.47 Å measured by X-ray diffractometry and also having a tensile strength of not less than 200 kgf/mm 2 and a Young's modulus of not less than 9500 kgf/mm 2 .
Claim 5
Dependent Claim
101 words
The process according to claim 1, wherein carbonized fibers obtained from said optically isotropic pitch are subjected to heat treatment at a temperature of over 1600° C. and below 2000° C., thereby producing carbon fibers having a preferred orientation (22°) of 30° to 50°, an apparent crystallite size (L c (002)) of over 50 Å and less than 80 Å and an interlayer spacing (d 002 ) of 3.43 to 3.45 Å, measured by X-ray diffractometry and also having a tensile strength of not less than 250 kgf/mm 2 and a Young's modulus of not less than 15000 kgf/mm 2 .
Claim 6
Dependent Claim
99 words
The process according to claim 1, wherein carbonized fibers obtained from said optically isotropic pitch are subjected to heat treatment at a temperature of not less than 2000° C., thereby producing carbon fibers having a preferred orientation (22°) of below 30°, an apparent crystallite size (L c (002)) of over 80 Å and not more than 200 Å and an interlayer spacing (d 002 ) of 3.371 to 3.440 Å measured by X-ray diffractometry and also having a tensile strength of not less than 300 kgf/mm 2 and a Young's modulus of not less than 20000 kgf/mm 2 .
Claim 7
Dependent Claim
98 words
A process for producing an optically isotropic pitch which is melt-spinnable and a precursor for carbon fibers, comprising polymerizing naphthalene at a temperature of not more than 330° C. in the presence of a Lewis acid catalyst consisting essentially of aluminum chloride or boron trifuluoride, or 0.5 to 100 hours and after removing said catalyst from the reaction mixture, heating the thus obtained polymeric material to a temperature of 330° to 440° C. for not more than 40 minutes while introducing an inert gas thereinto under an atmospheric pressure or a reduced pressure to remove volatile components therefrom.
Claim 8
Dependent Claim
98 words
A process for producing an optically isotropic pitch which is melt-spinnable and a precursor for carbon fibers, comprising polymerizing naphthalene at a temperature of not more than 330° C. in the presence of a Lewis acid catalyst consisting essentially of aluminum chloride or boron trifuluoride, or 0.5 to 100 hours and after removing said catalyst from the reaction mixture, heating the thus obtained polymeric material to a temperature of 330° to 440° C. for not more than 40 minutes while introducing an inert gas thereinto under an atmospheric pressure or a reduced pressure to remove volatile components therefrom.
Claim 9
Dependent Claim
63 words
An optically isotropic pitch which is melt-spinnable and a precursor for carbon fibers, having a softening point of 180° to 200° C., an atomic ratio of hydrogen to carbon of 0.6 to 0.8 and an average molecular weight of 800 to 1500, and containing 35 to 45% by weight of benzene-insolubles without containing any quinoline-insolubles, produced by the process according to claim 6.
Claim 10
Dependent Claim
19 words
The process according to claim 1, wherein the Lewis acid catalyst consists essentially of aluminum chloride or boron trifluoride.
Claim 11
Dependent Claim
16 words
The process according to claim 1, wherein the Lewis acid catalyst consists essentially of aluminum chloride.
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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) | 1992-09-04 | 1993-03-06 | 1993-09-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-09-04 | 1997-03-06 | 1997-09-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-09-04 | 2001-03-06 | 2001-09-05 | $7700.00 | Window Closed / Lapsed |