Claims
- 1. A process for the preparation of a pitch-based carbon fiber having a micro-structure comprising strip-like structural units extended in the longitudinal direction of the fiber, wherein the fractal dimension D of the arrangement of the strip like structural units in the cross-section of the fiber has a fractal structure satisfying the requirement of the following formula (2) relative to the observation scale r satisfying the requirement of the following formula (1) with respect to the cross-section of the fiber
- E/2.5 r E/25 (1)
- 2.0 D 1.05 (2)
- wherein E in the formula (1) stands for a smallest principal radius of gyration of cross-sectioned area of the fiber, which comprises melt-spinning a pitch having an optically anisotropic region occupancy ratio of at least 50% by using a spinneret apparatus comprising a spinning nozzle including an introduction hole portion and a fine hole portion and at least one stationary element selected from the group consisting of a stationary dividing element and a stationary kneading element, arranged upstream of the introduction hole portion of the nozzle, and simultaneously satisfying the requirements of the following formulae (5), (6) and (7), and rendering the spun fiber infusible and carbonizing the fiber: ##EQU4##
- 150.degree..ltoreq..crclbar..ltoreq.180.degree. (6)
- L.sub.c .multidot..eta./W>20 (7)
- wherein n stands for the viscosity (poise) of the spun pitch in the spinning nozzle, S(l) stands for the cross-sectional area (mm.sup.2) of the nozzle hole at a distance l (mm) measured in the direction toward the outlet of the spinning nozzle from the most downstream position of the stationary element as the origin, l.sub.O stands for a distance (mm) between the most downstream point of said element and the outlet of the spinning nozzle, l.sub.c stands for the length (mm) of the fine hole portion, O stands for the angle (degree) of introduction to the fine hole portion from the introduction hole portion, and Q stands for the quantity (g/min) of the pitch extruded per hole of the spinning nozzle.
- 2. A process according to claim 1, wherein for spinning the pitch, a spinning nozzle having a hole shape having a central distance Ln of a wet edge and a width Wn of the wet edge, in which at least one of Ln satisfies the requirements of the following two formulae, is used:
- Ln<10 mm (8)
- 1.0<Ln/Wn.ltoreq.20 (9)
- 3. A process according to claim 1, wherein the optically anisotropic region occupancy ratio of the pitch is at least 90%.
- 4. A process according to claim 1, wherein the melt-spinning is conducted at a temperature lower than 360.degree. C.
- 5. A process according to claim 1, wherein the melting point of the pitch as determined by the Mettler method is 280.degree. to 340.degree. C.
- 6. A process according to claim 1, wherein iodine is doped in an amount of at least 1.0% by weight into the melt-spun pitch fiber, the pitch fiber is treated with air maintained at a temperature lower than 350.degree. C. to be infusibilized, and the pitch fiber is heated in an inert atmosphere to be carbonized.
- 7. A process according to claim 6, wherein the amount of iodine doped is more than 3% by weight.
- 8. A process according to claim 6, wherein the infusibilization of the pitch fiber is effected at a temperature higher than 100.degree. C.
- 9. A process according to claim 1, wherein at the step of carbonizing the melt-spun pitch fiber to form a carbon fiber, the pitch fiber is treated in the co-presence of iodine and oxygen and then carbonized in an inert atmosphere.
- 10. A process according to claim 9, wherein the iodine concentration in the gas mixture is at least 0.01 mole % and the oxygen concentration is at least 1%.
- 11. A process according to claim 9, wherein the treatment with the iodine/oxygen gas mixture is effected at a temperature of 100.degree. to 400.degree. C.
- 12. A process according to claim 1, wherein the melt-spun pitch fiber is treated with ozone, infusibilized in the presence of at least iodine, and then carbonized in an inert atmosphere.
- 13. A process according to claim 12, wherein iodine is doped in an amount of at least 1.0% by weight into the ozone-treated pitch fiber, and the pitch fiber is then infusibilized in air at a temperature of lower than 350.degree. C.
- 14. A process according to claim 13, wherein the infusibilization of the pitch fiber is effected at a temperature higher than 100.degree. C.
- 15. A process according to claim 12, wherein the ozone-treated pitch fiber is infusibilized in a gas mixture of iodine and oxygen.
- 16. A process according to claim 15, wherein the treatment with the iodine/oxygen gas mixture is effected at a temperature of 100.degree. to 400.degree. C.
- 17. A process according to claim 1, wherein the carbonization is effected in an inert atmosphere at a temperature higher than 1000.degree. C.
- 18. A process according to claim 17, wherein the carbonization is effected in an inert atmosphere at a temperature higher than 1800.degree. C.
Parent Case Info
This is a division of application Ser. No. 281,245, filed Dec. 7, 1988, now U.S. Pat. No. 5,047,292.
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Divisions (1)
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281245 |
Dec 1988 |
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