Patent US4127472A successfully refreshed from Google Patents.
US4127472A
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US
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Process for preparing a raw material for the manufacture of needle coke
Assignee: Nippon Steel Chemical and Materials Co Ltd
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Filing: 1977-11-22
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Granted: 1978-11-28
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Expires: 1997-11-22
Abstract
Abstract In mixing coal tar and/or coal tar pitch with aromatic and aliphatic solvents at atmospheric pressure and at a temperature between 15 DEG C and 140 DEG C to prepare a raw material for the manufacture of needle coke, the mixing ratio of the aromatic and aliphatic solvents and their quantities of addition to the coal tar and/or coal tar pitch are adjusted so that insoluble substances precipitate in a pitch zone. A supernatant obtained by separating the insoluble substances is distilled, and hydrocarbons consisting substantially of aromatic compounds and freed of the insoluble substances are obtained. Then the hydrocarbons are used as the raw material for the manufacture of needle coke.
Inventors
- 👤 Wataru Migitaka
- 👤 Hirofumi Sunago
- 👤 Yukiyosi Ogawa
- 👤 Takanori Nisihata
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 06:25
CPC Classifications
C; C10; C10B; C10B57/00; C10B57/04; C10B57/045; C10B55/00
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
112 words
A process for preparing a raw material for the manufacture of needle coke comprising the steps of mixing coal tar and/or coal tar pitch with aromatic and aliphatic solvents at atmospheric pressure and at a temperature between 15° C. and 140° C., with the mixing ratio of the aromatic and aliphatic solvents and their quantities of addition to the coal tar and/or coal tar pitch being adjusted so that insoluble substances precipitate in a pitch zone, distilling a supernatant obtained by separating the insoluble substances, obtaining hydrocarbons consisting substantially of aromatic compounds and freed of the insoluble substances, and using the hydrocarbons as the raw material for the manufacture of needle coke.
Claim 2
Dependent Claim
112 words
A process for preparing a raw material for the manufacture of needle coke comprising the steps of mixing coal tar and/or coal tar pitch with aromatic and aliphatic solvents at atmospheric pressure and at a temperature between 15° C. and 140° C., with the mixing ratio of the aromatic and aliphatic solvents and their quantities of addition to the coal tar and/or coal tar pitch being adjusted so that insoluble substances precipitate in a pitch zone, distilling a supernatant obtained by separating the insoluble substances, obtaining hydrocarbons consisting substantially of aromatic compounds and freed of the insoluble substances, and using the hydrocarbons as the raw material for the manufacture of needle coke.
Claim 3
Dependent Claim
17 words
A process according to claim 1, wherein the coal tar pitch used is soft coal tar pitch.
Claim 4
Dependent Claim
28 words
A process according to claim 1, wherein the aromatic solvent is at least one member selected from the group consisting of creosote oil, wash oil, and anthracene oil.
Claim 5
Dependent Claim
22 words
A process according to claim 1, wherein the aromatic solvent is delayed coker by-product oil obtained when preparing raw coal pitch coke.
Claim 6
Dependent Claim
36 words
A process according to claim 1, wherein the aromatic solvent has an initial boiling point of not lower than 80° C. and accomplishes 95 percent by volume distillation at a temperature not higher than 400° C.
Claim 7
Dependent Claim
37 words
A process according to claim 1, wherein the aromatic solvent preferably has an initial boiling point of not lower than 140° C. and accomplishes 95 percent by volume distillation at a temperature not higher than 350° C.
Claim 8
Dependent Claim
55 words
A process according to claim 1, wherein the aromatic solvent more preferably has an initial boiling point of not lower than 140° C. and accomplishes at least 60 percent by volume distillation at a temperature between 200° C. and 230° C. and 95 percent by volume distillation at a temperature not higher than 300° C.
Claim 9
Dependent Claim
26 words
A process according to claim 1, wherein the aliphatic solvent is at least one member selected from the group consisting of industrial gasoline, naphtha and kerosene.
Claim 10
Dependent Claim
36 words
A process according to claim 1, wherein the aliphatic solvent has an initial boiling point of not lower than 30° C. and accomplishes 90 percent by volume distillation at a temperature not higher than 350° C.
Claim 11
Dependent Claim
37 words
A process according to claim 1, wherein the aliphatic solvent preferably has an initial boiling point of not lower than 150° C. and accomplishes 95 percent by volume distillation at a temperature not higher than 320° C.
Claim 12
Dependent Claim
38 words
A process according to claim 1, wherein the aliphatic solvent more preferably has an initial boiling point of not lower than 150° C. and accomplishes 95 percent by volume distillation at a temperature not higher than 250° C.
Claim 13
Dependent Claim
21 words
A process according to claim 1, wherein the mixing is effected in the temperature range between 70° C. and 140° C.
Claim 14
Dependent Claim
21 words
A process according to claim 1, wherein the separation is effected in the temperature range between 20° C. and 100° C.
Claim 15
Dependent Claim
21 words
A process according to claim 1, wherein the separation is accomplished by the gravity settling method or the liquid cyclone method.
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) | 1981-11-27 | 1982-05-29 | 1982-11-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-11-27 | 1986-05-29 | 1986-11-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-11-27 | 1990-05-29 | 1990-11-28 | $7700.00 | Window Closed / Lapsed |