US4009232A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for the production of carbon microspheres 1-20 μ in diameter
Assignee: Kureha Corp
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Filing: 1974-03-12
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Granted: 1977-02-22
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Expires: 1994-03-12
Abstract
Abstract Discrete carbon microspheres having a particle diameter on the order of 1-20 μ are obtained by a process involving the steps of homogeneously mixing a pitch having a softening point of 70° - 250° C, a nitrobenzene-insoluble content of not more than 25% and an H/C ratio of 0.2- 1.0 with an aromatic solvent compatible with said pitch and dispersing the resultant mixture in an aqueous solution of a surface active agent with agitation and at a temperature to maintain the viscosity at 200-5000 cps to form microspheres of the pitch/solvent mixture. The dispersion is then cooled to solidify the microspheres. The microspheres 1-20 μ in diameter are then separated from the solution and from the finer particles and contacted an organic solvent which is incompatible with the pitch to extract the first-mentioned aromatic solvent from the microspheres. The resultant pitch microspheres are then contacted with an oxidizing agent to render them infusible and baked in an atmosphere of an inert gas to carbonize same.
Inventors
- 👤 Zenya Shiiki
- 👤 Masaaki Nakao
- 👤 Kunihiko Katori
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 08:10
CPC Classifications
C; C01; C01B; C01B32/00
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
227 words
A method for the production of discrete carbon microspheres having a particle size of 1-20 μ comprising: a. mixing a pitch having a softening point of 70°-250° C, a nitrobenzene-insoluble content of not more than 25% and a H/C ratio of 0.2-1.0 with a water-insoluble aromatic solvent having a boiling point of 70°-250° C to produce a homogeneous pitch/solvent mixture of more than 50% by weight pitch, said mixing being conducted at a temperature of 100°-200° C to maintain a viscosity of 200-5000 cps; b. dispersing said pitch/solvent mixture with agitation in an aqueous solution of a surface active agent to form an aqueous dispersion of said pitch/solvent mixture in the form of microspheres, said solution being at a temperature sufficient to retain said viscosity of said pitch/solvent mixture at 200-5000 cps; c. cooling said aqueous dispersion to solidify said microspheres; d. separating said solidified pitch/solvent microspheres having a particle size of 1-20 μ from said aqueous solution and from particles having diameters smaller than 1 μ; e. extracting said aromatic solvent from said microspheres by contacting said microspheres with an organic solvent compatible with said aromatic solvent, but incompatible with said pitch; f. contacting said microspheres with an oxidizing agent to render said microspheres infusible; and g. heating said microspheres in an inert gas atmosphere to produce carbon microspheres having a particle size of 1-20 μ.
Claim 2
Independent Claim
227 words
A method for the production of discrete carbon microspheres having a particle size of 1-20 μ comprising: a. mixing a pitch having a softening point of 70°-250° C, a nitrobenzene-insoluble content of not more than 25% and a H/C ratio of 0.2-1.0 with a water-insoluble aromatic solvent having a boiling point of 70°-250° C to produce a homogeneous pitch/solvent mixture of more than 50% by weight pitch, said mixing being conducted at a temperature of 100°-200° C to maintain a viscosity of 200-5000 cps; b. dispersing said pitch/solvent mixture with agitation in an aqueous solution of a surface active agent to form an aqueous dispersion of said pitch/solvent mixture in the form of microspheres, said solution being at a temperature sufficient to retain said viscosity of said pitch/solvent mixture at 200-5000 cps; c. cooling said aqueous dispersion to solidify said microspheres; d. separating said solidified pitch/solvent microspheres having a particle size of 1-20 μ from said aqueous solution and from particles having diameters smaller than 1 μ; e. extracting said aromatic solvent from said microspheres by contacting said microspheres with an organic solvent compatible with said aromatic solvent, but incompatible with said pitch; f. contacting said microspheres with an oxidizing agent to render said microspheres infusible; and g. heating said microspheres in an inert gas atmosphere to produce carbon microspheres having a particle size of 1-20 μ.
Claim 3
Dependent Claim
23 words
The method of claim 1, wherein said aromatic solvent is selected from the group consisting of benzene, toluene xylene, naphthalene, tetralin and methylnaphthalene.
Claim 4
Dependent Claim
30 words
The method of claim 1, wherein said surface active agent is selected from the group consisting of anionic surface active agents, cationic surface active agents and nonionic surface active agents.
Claim 5
Dependent Claim
44 words
The method of claim 3, wherein said anionic surface active agent is selected from the group consisting of fatty acid salts, olefin-sulfuric acid esters, long-chain alcohol-sulfuric acid esters, fatty-acid alkyl-sulfuric acid esters, alkyl sulfonic acid salts, alkylbenzene-sulfonic acid salts and lower alkylnaphthalene-sulfonic acid salts.
Claim 6
Dependent Claim
29 words
The method of claim 3, wherein said cationic surface active agent is selected from the group consisting of long-chain primary amine salts, alkyltrimethyl ammonium salts and dialkyldimethyl ammonium salts.
Claim 7
Dependent Claim
26 words
The method of claim 3, wherein said nonionic surface active agent is selected from the group consisting of polyoxyethylenealkyl ethers, polyoxyethylene alkylphenyl esters and polyoxylethylene-alkylnaphthyl ethers.
Claim 8
Dependent Claim
20 words
The method of claim 1, wherein said organic solvent is selected from the group consisting of alcohols and paraffinic hydrocarbons.
Claim 9
Dependent Claim
19 words
The method of claim 7, wherein said alcohol is selected from the group consisting of methanol, ethanol and propanol.
Claim 10
Dependent Claim
21 words
The method of claim 7, wherein said paraffinic hydrocarbon is selected from the group consisting of hexane, heptane and light naphtha.
Claim 11
Dependent Claim
26 words
The method of claim 1, wherein said oxidizing agent is selected from the group consisting of nitric acid, sulfuric acid, chromic acid, permanganates and hyprochlorous acid.
Claim 12
Dependent Claim
33 words
The method of claim 1, wherein said cooling is carried out in the presence of a water-soluble organic solvent added to the aqueous dispersion in step c to facilitate separating the solidified microspheres.
Claim 13
Dependent Claim
13 words
The method of claim 11, wherein said water-soluble organic solvent is an alcohol.
Claim 14
Dependent Claim
35 words
The method of claim 1, wherein said pitch microspheres are rendered infusible by dispersing said microspheres in water containing 0.001-0.1% of a surface active agent and subsequently adding said oxdizing agent to the aqueous dispersion.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-02-22 | 1980-08-23 | 1981-02-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-02-22 | 1984-08-23 | 1985-02-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-02-22 | 1988-08-23 | 1989-02-22 | $7700.00 | Window Closed / Lapsed |