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US4207167A Expired / Lapsed US ⏱️ 0.0 years remaining

Combination hydrocarbon cracking, hydrogen production and hydrocracking

Assignee: Phillips Petroleum Co
•
Filing: 1978-03-21
•
Granted: 1980-06-10
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Expires: 1998-03-21
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Abstract

Abstract A used hydrocarbon cracking catalyst having coke laydown thereon is regenerated under conditions to produce a gas rich in carbon monoxide which, together with steam, is subjected to a shift reaction to produce carbon dioxide and hydrogen, and oil cracked with said catalyst produces vapors which are fractionated to yield gases, cracked gasoline, a light-cycle oil, a heavy-cycle oil and bottoms, at least one of the light and heavy cycle oils is hydrocracked with the hydrogen earlier produced.

Inventors

  • 👤 Ralph W. Bradshaw

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 12:22
CPC Classifications
C; C10; C10G; C10G69/00; C10G69/02; C10G69/04; C01; C01B; C01B3/00; C01B3/02; C01B3/06; C01B3/12; C10G47/00

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 169 words
A process for producing a hydrocracked oil which comprises in a cracking zone cracking a hydrocarbon oil in the presence of a catalyst, fractionating cracked vapors thus produced to obtain a cycle oil and hydrocracking said cycle oil in the presence of hydrogen obtained as follows: regenerating in a regenerator in said cracking zone spent catalyst as obtained from said cracking and having coke laydown thereon, under conditions to combust said coke to produce a flue gas containing carbon monoxide, recovering said flue gas from said regenerator, adding at least one of water and steam to quench said recovered flue gas and as needed to adjust the temperature of said flue gas and to provide steam reactant; in an ensuing water shift reaction, subjecting said recovered flue gas containing carbon monoxide and now containing steam to a water shift reaction to produce carbon dioxide and hydrogen recovering hydrogen from said water shift reaction product and using said hydrogen, thus obtained and recovered, for said hydrocracking of said cycle oil.
Claim 2
Dependent Claim 169 words
A process for producing a hydrocracked oil which comprises in a cracking zone cracking a hydrocarbon oil in the presence of a catalyst, fractionating cracked vapors thus produced to obtain a cycle oil and hydrocracking said cycle oil in the presence of hydrogen obtained as follows: regenerating in a regenerator in said cracking zone spent catalyst as obtained from said cracking and having coke laydown thereon, under conditions to combust said coke to produce a flue gas containing carbon monoxide, recovering said flue gas from said regenerator, adding at least one of water and steam to quench said recovered flue gas and as needed to adjust the temperature of said flue gas and to provide steam reactant; in an ensuing water shift reaction, subjecting said recovered flue gas containing carbon monoxide and now containing steam to a water shift reaction to produce carbon dioxide and hydrogen recovering hydrogen from said water shift reaction product and using said hydrogen, thus obtained and recovered, for said hydrocracking of said cycle oil.
Claim 3
Dependent Claim 32 words
An operation according to claim 1 wherein the product of the hydrocracking is fractionated to recover a series of hydrocarbons and hydrogen and wherein the hydrogen is recycled to the hydrocracking operation.

References Cited (Backward Citations)

US2518775A Cited
US2572734A Cited
US3172839A Cited
US3193488A Cited
US3245900A Cited
US3284338A Cited
US3691063A Cited
US3816298A Cited
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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) 1983-06-10 1983-12-10 1984-06-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-06-10 1987-12-10 1988-06-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-06-10 1991-12-10 1992-06-10 $7700.00 Window Closed / Lapsed

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