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US4111794A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of producing pitch coke

Assignee: Rain Carbon Germany GmbH
•
Filing: 1977-03-31
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Granted: 1978-09-05
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Expires: 1997-03-31
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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 17:36
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)

US2775549A Cited
US3617515A Cited
DE2064695A1 Cited
US3799865A Cited
DE2434295A1 Cited

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

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