US4414095A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Mesophase pitch using steam cracker tar (CF-6)
Assignee: Exxon Mobil Corp
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Filing: 1981-06-12
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Granted: 1983-11-08
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Expires: 2001-06-12
Abstract
Abstract A feedstock for carbon artifact manufacture is obtained from a steam cracker tar by heat soaking the steam cracker tar or a vacuum stripped steam cracker tar with a polycondensed aromatic oil thereby providing a pitch suitable for carbon artifact manufacture.
Inventors
- 👤 Ghazi Dickakian
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 18:08
CPC Classifications
C; C10; C10C; C10C3/00
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
85 words
A process for preparing a pitch suitable for carbon fiber manufacture comprising: providing a steam cracker tar or a vacuum stripped steam cracker tar; adding a polycondensed aromatic pitch oil boiling in an approximate range of 400° C. to 600° C. to said steam cracker tar or vacuum stripped steam cracker tar to provide a mixture; and heat soaking said mixture at temperatures in the range of from about 350° C. to about 430° C. whereby a pitch suitable for carbon artifact manufacture is obtained.
Claim 2
Dependent Claim
85 words
A process for preparing a pitch suitable for carbon fiber manufacture comprising: providing a steam cracker tar or a vacuum stripped steam cracker tar; adding a polycondensed aromatic pitch oil boiling in an approximate range of 400° C. to 600° C. to said steam cracker tar or vacuum stripped steam cracker tar to provide a mixture; and heat soaking said mixture at temperatures in the range of from about 350° C. to about 430° C. whereby a pitch suitable for carbon artifact manufacture is obtained.
Claim 3
Dependent Claim
44 words
The process of claim 1 wherein said polycondensed aromatic oil having a boiling point range of from about 400° C. to about 600° C. is added in amounts ranging from about 5 wt. % to about 60 wt. % based on the total mixture.
Claim 4
Dependent Claim
44 words
The process of claim 1 wherein said polycondensed aromatic oil having a boiling point range of from about 400° C. to about 600° C. is added in amounts ranging from about 30 wt. % to about 50 wt. % based on the total mixture.
Claim 5
Dependent Claim
23 words
The process of claim 2 or 3 including adding a dealkylation catalyst selected from heavy metal halides, Lewis acids and Lewis acid salts.
Claim 6
Dependent Claim
12 words
The process of claim 3 wherein the catalyst is AlCl 3 .
Claim 7
Dependent Claim
19 words
The process of claim 1 including vacuum stripping said heat soaked mixture when a steam cracker tar is provided.
Claim 8
Dependent Claim
117 words
A process of preparing a pitch from a steam cracker tar comprising: providing a steam cracker tar; heating said steam cracker tar at temperatures ranging from about 150° C. to about 430° C. at reduced pressures for times sufficient to remove from about 10 wt. % to about 50 wt. % of low boiling substances in said tar thereby providing a vacuum stripped steam cracker tar; adding from about 5 wt. % to about 60 wt. % of an aromatic oil having a boiling point ranging from about 400° C. to about 600° C. to provide a mixture; heat soaking said mixture at temperatures ranging from about 350° C. to about 430° C. to provide a pitch.
Claim 9
Dependent Claim
117 words
A process of preparing a pitch from a steam cracker tar comprising: providing a steam cracker tar; heating said steam cracker tar at temperatures ranging from about 150° C. to about 430° C. at reduced pressures for times sufficient to remove from about 10 wt. % to about 50 wt. % of low boiling substances in said tar thereby providing a vacuum stripped steam cracker tar; adding from about 5 wt. % to about 60 wt. % of an aromatic oil having a boiling point ranging from about 400° C. to about 600° C. to provide a mixture; heat soaking said mixture at temperatures ranging from about 350° C. to about 430° C. to provide a pitch.
Claim 10
Dependent Claim
28 words
The process of claim 6 wherein from about 0.025 wt. % to about 1.0 wt. % of AlCl 3 is added to the mixture prior to heat soaking.
Claim 11
Dependent Claim
68 words
A process for preparing a pitch suitable for carbon fiber manufacture comprising: providing a steam cracker tar; adding a polycondensed aromatic pitch oil boiling in an approximate range of 400° C. to 600° C. to said steam cracker tar to provide a mixture; heat soaking said mixture at temperatures in the range of from about 350° C. to about 430° C.; and vacuum stripping said heat soaked mixture.
Claim 12
Dependent Claim
68 words
A process for preparing a pitch suitable for carbon fiber manufacture comprising: providing a steam cracker tar; adding a polycondensed aromatic pitch oil boiling in an approximate range of 400° C. to 600° C. to said steam cracker tar to provide a mixture; heat soaking said mixture at temperatures in the range of from about 350° C. to about 430° C.; and vacuum stripping said heat soaked mixture.
Claim 13
Dependent Claim
28 words
The process of claim 9 wherein from about 0.025 wt. % to about 1.0 wt. % of AlCl 3 is added to the mixture prior to heat soaking.
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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) | 1986-11-07 | 1987-05-09 | 1987-11-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-11-07 | 1991-05-09 | 1991-11-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-11-07 | 1995-05-09 | 1995-11-08 | $7700.00 | Window Closed / Lapsed |