US4111794A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of producing pitch coke
Assignee: Rain Carbon Germany GmbH
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Filing: 1977-03-31
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Granted: 1978-09-05
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Expires: 1997-03-31
Abstract
Abstract Manufacture of pitch coke with needle-like structure by mixing pyrolysis oil condensate formed in the process with a coal-tar pitch having a softening point between 70° and 150° C, filtering the mixture at a temperature 100° to 200° C above the softening point, heating the filtrate to a temperature between 450° and 525° C in a tubular heater and coking the heated filtrate in a coking drum, passing volatile pyrolysis products from the drum to a fractionating column for separation of pyrolysis oil condensate from non-condensible gas.
Inventors
- 👤 Gerhard Pietzka
- 👤 Harald Tillmanns
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 10:32
CPC Classifications
C; C10; C10B; C10B55/00
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
218 words
Method for the manufacture of pitch coke with needle-like structure which comprises: (a) mixing pyrolysis oil condensate formed in the coking of coal-tar pitch with a coal-tar pitch having a softening point between 70° and 150° C. in the proportion of 70 to 95% by weight coal-tar pitch and 5 to 30% by weight pyrolysis oil condensate, (b) filtering said mixture of condensate and pitch at a temperature 100° C. to 200° above the softening point of the pitch, (c) passing the filtrate in a restricted stream through a heating zone and heating the filtrate therein to a temperature between about 450° and 525° C., (d) discharging the thus heated filtrate to a coking chamber wherein the heated filtrate forms a non-volatile carbonaceous residue as coke and volatile vapor and gas, (e) releasing the volatile vapor and gas from the coking chamber and passing the vapor and gas to a fractionating zone with an overhead temperature of between about 150° and 200° C. at pressures of about 0.5 to 2.0 bar and a bottom temperature of about 300° C., in which the vapor is condensed to form pyrolysis oil condensate, (f) withdrawing said condensate from the fractioning zone, and returning at least a part of said condensate for mixing with additional incoming coal-tar pitch prior to said filtering.
Claim 2
Dependent Claim
218 words
Method for the manufacture of pitch coke with needle-like structure which comprises: (a) mixing pyrolysis oil condensate formed in the coking of coal-tar pitch with a coal-tar pitch having a softening point between 70° and 150° C. in the proportion of 70 to 95% by weight coal-tar pitch and 5 to 30% by weight pyrolysis oil condensate, (b) filtering said mixture of condensate and pitch at a temperature 100° C. to 200° above the softening point of the pitch, (c) passing the filtrate in a restricted stream through a heating zone and heating the filtrate therein to a temperature between about 450° and 525° C., (d) discharging the thus heated filtrate to a coking chamber wherein the heated filtrate forms a non-volatile carbonaceous residue as coke and volatile vapor and gas, (e) releasing the volatile vapor and gas from the coking chamber and passing the vapor and gas to a fractionating zone with an overhead temperature of between about 150° and 200° C. at pressures of about 0.5 to 2.0 bar and a bottom temperature of about 300° C., in which the vapor is condensed to form pyrolysis oil condensate, (f) withdrawing said condensate from the fractioning zone, and returning at least a part of said condensate for mixing with additional incoming coal-tar pitch prior to said filtering.
Claim 3
Dependent Claim
18 words
Method according to claim 1, wherein the coal-tar pitch has a softening point between 80° and 150° C.
Claim 4
Dependent Claim
24 words
Method according to claim 1, wherein at least two coal-tar pitches are used, the softening points of which differ by more than 20 K.
Claim 5
Dependent Claim
14 words
Method according to claim 1, wherein the pitch filtrate is coked by delayed coking.
Claim 6
Dependent Claim
13 words
Method according to claim 1, wherein said heating zone is a tubular heater.
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) | 1981-09-04 | 1982-03-06 | 1982-09-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-09-04 | 1986-03-06 | 1986-09-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-09-04 | 1990-03-06 | 1990-09-05 | $7700.00 | Window Closed / Lapsed |