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US4014980A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for manufacturing graphite whiskers using condensed polycyclic hydrocarbons

Assignee: Kureha Corp
•
Filing: 1975-07-29
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Granted: 1977-03-29
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Expires: 1995-07-29
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Abstract

Abstract A method for manufacturing graphite whiskers which comprises: mixing one or more of gasified compounds having a condensed polycyclic structure of two to five benzene rings with a large amount of inert gas containing a small amount of CO, CO 2 or H 2 O; heating said gas mixture at 700° to 1200° C and a substantially atmospheric pressure to generate precursory carbon whiskers comprised of numerous carbon crystals orientated in a form of single sheet which is rolled up like a scroll or a plurality of separate sheets rolled in concentric relationships; and graphitizing said carbon whiskers at temperatures of 2700° to 3000° C in an atmosphere of inert gas.

Inventors

  • 👤 Hiroto Fujimaki
  • 👤 Haruhisa Hayashi
  • 👤 Takashi Kawahara

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 11:16
CPC Classifications
D; D01; D01F; D01F9/00; D01F9/08; D01F9/12; D01F9/14; D01F9/20; D01F9/24; C; C30; C30B; C30B25/00; C30B25/005; C30B29/00; C30B29/02

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 223 words
A method for manufacturing graphite whiskers having a diameter of from 1 to 50 microns, a tensile strength of at least 1,000 kg/mm 2 and a modulus of elasticity of at least 5 × 10 4 kg/mm 2 , which comprises the steps of gasifying one or more liquefied organic compounds having a condensed polycyclic structure of substantially two to five benzene rings, the atomic ratio of H/C thereof being 1 at most; mixing the gasified substance derived from one part by volume of the liquefied organic compound with 500 to 5000 parts by volume of an inert gas mixed with 0.1 to 5 parts by volume of an active gas selected from the group consisting of carbon monoxide, carbon dioxide and water vapor; passing the resulting gaseous mixture at a substantially atmospheric pressure through a reaction furnace containing therein a heat-resistant substrate to deposit thereon thermally cracked carbon nuclei at a temperature of from 700° to about 890° C. for a period of at least 5 minutes, followed by 900° to 1200° C. to obtain precursory carbon whiskers at a growing velocity of at least 0.5 mm per minute; and graphitizing the precursory carbon whiskers in another furnace at a temperature of from 2700° to 3000° C. for a period of from 1 to 10 minutes in an atmosphere of inert gas.
Claim 2
Independent Claim 223 words
A method for manufacturing graphite whiskers having a diameter of from 1 to 50 microns, a tensile strength of at least 1,000 kg/mm 2 and a modulus of elasticity of at least 5 × 10 4 kg/mm 2 , which comprises the steps of gasifying one or more liquefied organic compounds having a condensed polycyclic structure of substantially two to five benzene rings, the atomic ratio of H/C thereof being 1 at most; mixing the gasified substance derived from one part by volume of the liquefied organic compound with 500 to 5000 parts by volume of an inert gas mixed with 0.1 to 5 parts by volume of an active gas selected from the group consisting of carbon monoxide, carbon dioxide and water vapor; passing the resulting gaseous mixture at a substantially atmospheric pressure through a reaction furnace containing therein a heat-resistant substrate to deposit thereon thermally cracked carbon nuclei at a temperature of from 700° to about 890° C. for a period of at least 5 minutes, followed by 900° to 1200° C. to obtain precursory carbon whiskers at a growing velocity of at least 0.5 mm per minute; and graphitizing the precursory carbon whiskers in another furnace at a temperature of from 2700° to 3000° C. for a period of from 1 to 10 minutes in an atmosphere of inert gas.
Claim 3
Dependent Claim 30 words
The method according to claim 1, wherein the liquefied organic compound having a condensed polycyclic structure is one selected from the group consisting of anthracene, phenanthrene, chrysene, fluoranthene and pyrene.
Claim 4
Dependent Claim 14 words
The method according to claim 1, wherein the liquified organic compound comprises anthracene oil.
Claim 5
Dependent Claim 24 words
The method according to claim 1, wherein the liquefied organic compound comprises a 300° to 450° C distillate fraction obtained from desulfurized coal tar.
Claim 6
Dependent Claim 29 words
The method according to claim 1, wherein the liquefied organic compound comprises a 300° to 450° C distillate fraction obtained from a desulfurized residue of thermally cracked petroleum oil.
Claim 7
Dependent Claim 22 words
The method according to claim 5, wherein the petroleum oil is one selected from the group consisting of crude oil and naphtha.
Claim 8
Dependent Claim 21 words
The method according to claim 1, wherein the inert gas is one selected from the group consisting of nitrogen and argon.

References Cited (Backward Citations)

CA556074A Cited
US3057687A Cited
US3347776A Cited
US3378345A Cited
US3411949A Cited
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US3531249A Cited
US3442617A Cited
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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) 1980-03-28 1980-09-27 1981-03-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-03-28 1984-09-27 1985-03-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-03-28 1988-09-27 1989-03-29 $7700.00 Window Closed / Lapsed

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