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US4111791A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of highly aromatic extract oil

Assignee: Phillips Petroleum Co
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Filing: 1977-02-24
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Granted: 1978-09-05
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Expires: 1997-02-24
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Abstract

Abstract In a system wherein a topped crude catalytic cracking system and a gas oil catalytic cracking system are operated, and the heavy cycle oils from each system are combined and the combined heavy cycle oil stream is solvent extracted to provide an aromatic extract suitable as feed for a carbon black operation, the aromaticity of the extract is increased by passing a substantial portion of the topped crude heavy cycle oil to the gas oil fractionator and recovering a heavy cycle oil from the gas oil fractionator as charge to solvent extraction.

Inventors

  • 👤 Edgar D. Davis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 23:54
CPC Classifications
C; C10; C10G; C10G55/00; C10G55/02; C10G55/06; C10G51/00; C10G51/06

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 206 words
A process comprising (a) passing a topped crude stream to a first catalytic cracking zone wherein said stream is subjected to catalytic cracking to produce an effluent of cracked products; (b) passing the effluent obtained in step (a) to a first fractionation zone wherein the cracked products from the first catalytic cracking zone are separated into separate distillate fractions comprising light hydrocarbons, gasoline, light cycle oil, heavy cycle oil and a catalyst-containing bottoms product; (c) passing a substantial portion of said heavy cycle oil obtained in step (b) to a second fractionation zone; (d) passing a gas oil stream to a second catalytic cracking zone wherein said gas oil stream is subjected to catalytic cracking to produce an effluent of cracked products; (e) passing the effluent obtained in step (d) to said second fractionation zone wherein the cracked products from the second catalytic cracking zone and the heavy cycle oil from step (b) are separated into separate distillate fractions comprising light hydrocarbons, gasoline, light cycle oil, heavy cycle oil and a catalyst-containing bottoms product; and (f) passing said heavy cycle oil obtained in step (e) to a solvent extraction zone wherein the oil is separated into an aromatics-containing extract phase and into a paraffin-containing raffinate phase.
Claim 2
Dependent Claim 206 words
A process comprising (a) passing a topped crude stream to a first catalytic cracking zone wherein said stream is subjected to catalytic cracking to produce an effluent of cracked products; (b) passing the effluent obtained in step (a) to a first fractionation zone wherein the cracked products from the first catalytic cracking zone are separated into separate distillate fractions comprising light hydrocarbons, gasoline, light cycle oil, heavy cycle oil and a catalyst-containing bottoms product; (c) passing a substantial portion of said heavy cycle oil obtained in step (b) to a second fractionation zone; (d) passing a gas oil stream to a second catalytic cracking zone wherein said gas oil stream is subjected to catalytic cracking to produce an effluent of cracked products; (e) passing the effluent obtained in step (d) to said second fractionation zone wherein the cracked products from the second catalytic cracking zone and the heavy cycle oil from step (b) are separated into separate distillate fractions comprising light hydrocarbons, gasoline, light cycle oil, heavy cycle oil and a catalyst-containing bottoms product; and (f) passing said heavy cycle oil obtained in step (e) to a solvent extraction zone wherein the oil is separated into an aromatics-containing extract phase and into a paraffin-containing raffinate phase.
Claim 3
Dependent Claim 53 words
The process of claim 1 wherein the bottoms product obtained in step (b) is further separated into a decant oil portion and a slurry oil portion, and wherein said slurry oil portion is recycled to said first catalytic cracking zone, and wherein said decant oil portion is passed to said second fractionation zone.
Claim 4
Dependent Claim 21 words
The process of claim 1 wherein said bottoms product obtained in step (e) is recycled to said second catalytic cracking zone.
Claim 5
Dependent Claim 27 words
The process of claim 1 wherein at least a portion of said paraffin-containing raffinate phase obtained in step (f) is recycled to said second catalytic cracking zone.
Claim 6
Dependent Claim 57 words
The process of claim 1 wherein said first catalytic cracking step is conducted at a temperature in the range of 870°-960° F and a conversion level of about 30-60 percent, and said second catalytic cracking step is conducted at a temperature in the range of 905°-970° F and a conversion level in the range of 50-80 percent.
Claim 7
Dependent Claim 23 words
The process of claim 1 wherein all of said heavy cycle oil obtained in step (b) is passed to said second fractionation zone.
Claim 8
Dependent Claim 41 words
The process of claim 1 wherein a further portion of said heavy cycle oil obtained in step (b) is combined with said heavy cycle oil obtained in step (e) and the resulting combined stream is passed to said solvent extraction zone.
Claim 9
Dependent Claim 27 words
The process of claim 7 wherein the amount of said heavy cycle oil obtained in step (b) is not greater than 10 percent of said combined stream.
Claim 10
Dependent Claim 28 words
The process of claim 7 wherein the amount of said heavy cycle oil obtained in step (b) is not greater than about 7 percent of said combined stream.

References Cited (Backward Citations)

US3190828A Cited
US3303123A Cited
US3591485A Cited
US3928173A 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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