← Back to Patent Explorer
US4497705A Expired / Lapsed US ⏱️ 0.0 years remaining

Fluid coking with solvent separation of recycle oil

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1983-08-17
•
Granted: 1985-02-05
•
Expires: 2003-08-17
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A fluid coking process is provided in which a stream of heavy oil product, which typically is recycled to the coking zone, is first subjected to solvent separation to separate it into a high Conradson carbon product and a lower Conradson carbon product and, thereafter, at least a portion of the lower Conradson carbon product is recovered and the high Conradson carbon product is recycled to the coking zone.

Inventors

  • 👤 Harold N. Weinberg
  • 👤 Charles Rebick
  • 👤 Kenneth O. McElrath

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 19:47
CPC Classifications
C; C10; C10B; C10B55/00; C10G; C10G55/00; C10G55/02; C10G55/04

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 193 words
In a fluid coking process comprising the steps of: (a) contacting a carbonaceous chargestock with hot fluidized solids in a fluidized bed contained in a coking zone at coking conditions to produce coke which deposits on said fluidized solids and a vapor phase product, including heavy and light normally liquid hydrocarbons, and (b) passing said vapor phase product of step (a) to a scrubbing zone and separating at least a portion of said heavy hydrocarbons from said vapor phase product in said scrubbing zone, said separated hydrocarbons having a Conradson carbon content ranging from about 5 to about 50 weight percent, the improvement which comprises: (c) subsequently contacting at least a portion of said separated hydrocarbons, said portion of separated hydrocarbons having a Conradson carbon content ranging from about 5 to about 50 weight percent, with a solvent in a solvent separation zone at separation conditions to separate said heavy hydrocarbons into a high Conradson carbon hydrocarbonaceous product and a low Conradson carbon hydrocarbonaceous product; (d) recycling at least a portion of said high Conradson carbon product to said coking zone, and (e) recovering said low Conradson carbon hydrocarbonaceous product of step (c).
Claim 2
Dependent Claim 193 words
In a fluid coking process comprising the steps of: (a) contacting a carbonaceous chargestock with hot fluidized solids in a fluidized bed contained in a coking zone at coking conditions to produce coke which deposits on said fluidized solids and a vapor phase product, including heavy and light normally liquid hydrocarbons, and (b) passing said vapor phase product of step (a) to a scrubbing zone and separating at least a portion of said heavy hydrocarbons from said vapor phase product in said scrubbing zone, said separated hydrocarbons having a Conradson carbon content ranging from about 5 to about 50 weight percent, the improvement which comprises: (c) subsequently contacting at least a portion of said separated hydrocarbons, said portion of separated hydrocarbons having a Conradson carbon content ranging from about 5 to about 50 weight percent, with a solvent in a solvent separation zone at separation conditions to separate said heavy hydrocarbons into a high Conradson carbon hydrocarbonaceous product and a low Conradson carbon hydrocarbonaceous product; (d) recycling at least a portion of said high Conradson carbon product to said coking zone, and (e) recovering said low Conradson carbon hydrocarbonaceous product of step (c).
Claim 3
Dependent Claim 30 words
The process of claim 1 wherein the initial atmospheric pressure boiling point of said heavy hydrocarbons separated from said vapor phase product ranges from about 650° to about 975° F.
Claim 4
Dependent Claim 14 words
The process of claim 1 wherein said solvent separation is a solvent extraction process.
Claim 5
Dependent Claim 14 words
The process of claim 1 wherein said solvent separation is a solvent deasphalting process.
Claim 6
Dependent Claim 25 words
The process of claim 1 wherein said carbonaceous chargestock comprises a hydrocarbonaceous oil having a Conradson carbon content of at least about 5 weight percent.
Claim 7
Dependent Claim 31 words
The process of claim 1 wherein said coking conditions include a temperature ranging from about 850° to about 1800° F. and a pressure ranging from about 0 to about 150 psig.
Claim 8
Dependent Claim 20 words
The process of claim 1 wherein said coking conditions include a temperature ranging from about 900° to about 1200° F.
Claim 9
Dependent Claim 19 words
The process of claim 1 wherein said coking zone is the sole coking zone in said fluid coking process.

References Cited (Backward Citations)

US3172840A Cited
US2700637A Cited
US2727853A Cited
US2777802A Cited
US2901413A Cited
US2890999A Cited
US2943995A Cited
US2926129A Cited
US3247095A Cited
US3661543A Cited
US3707462A Cited
US4057487A Cited
US4213848A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-02-05 1988-08-06 1989-02-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-02-05 1992-08-06 1993-02-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-02-05 1996-08-06 1997-02-05 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag