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US4058451A Expired / Lapsed US ⏱️ 0.0 years remaining

Combination process for producing high quality metallurgical coke

Assignee: Honeywell UOP LLC
•
Filing: 1976-08-23
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Granted: 1977-11-15
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Expires: 1996-08-23
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Abstract

Abstract A process for producing high quality metallurgical coke from hydrocarbonaceous charge stock containing coke precursors which comprises: (a) admixing said hydrocarbonaceous charge with a hereinafter described hydrocarbonaceous recycle stream; (b) introducing the resulting admixture into a coking zone maintained at coking conditions to produce coke and a hydrocarbonaceous effluent having a reduced level of coke precursors; (c) introducing at least a portion of said hydrocarbonaceous effluent into a hydrodesulfurization zone maintained at hydrodesulfurization conditions; (d) recycling at least a portion of the resultant desulfurized hydrocarbon of step (c) to step (a) as said hydrocarbonaceous recycle stream.

Inventors

  • 👤 Frank Stolfa

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 15:55
CPC Classifications
C; C10; C10B; C10B57/00; C10B57/04; C10B57/045; C10B55/00; C10G; C10G69/00; C10G69/02; C10G69/06

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 166 words
A process for producing high quality metallurgical coke from a sulfur-containing reduced crude oil which comprises: a. admixing said reduced crude oil with a hydrocarbon recycle stream formed as hereinafter set forth; b. introducing the resulting mixture into a coking zone maintained at coking conditions to produce coke and a hydrocarbon effluent having a reduced level of coke precursors; c. separating the coke from the hydrocarbon effluent and recovering the same; d. introducing the hydrocarbon effluent to a flash zone and therein vaporizing hydrocarbons boiling up to about 400° F.; e. hydrodesulfurizing the remainder of said effluent boiling above about 400° F.; f. fractionating the resultant desulfurized remainder of the hydrocarbon effluent to separate therefrom hydrocarbons boiling up to about 650° F., leaving a desulfurized hydrocarbon bottoms fraction boiling above about 650° F.; and g. supplying at least a portion of said desulfurized bottoms fraction boiling above about 650° F., to step (a) as said hydrocarbon recycle stream for admixture with the reduced crude oil therein.
Claim 2
Dependent Claim 166 words
A process for producing high quality metallurgical coke from a sulfur-containing reduced crude oil which comprises: a. admixing said reduced crude oil with a hydrocarbon recycle stream formed as hereinafter set forth; b. introducing the resulting mixture into a coking zone maintained at coking conditions to produce coke and a hydrocarbon effluent having a reduced level of coke precursors; c. separating the coke from the hydrocarbon effluent and recovering the same; d. introducing the hydrocarbon effluent to a flash zone and therein vaporizing hydrocarbons boiling up to about 400° F.; e. hydrodesulfurizing the remainder of said effluent boiling above about 400° F.; f. fractionating the resultant desulfurized remainder of the hydrocarbon effluent to separate therefrom hydrocarbons boiling up to about 650° F., leaving a desulfurized hydrocarbon bottoms fraction boiling above about 650° F.; and g. supplying at least a portion of said desulfurized bottoms fraction boiling above about 650° F., to step (a) as said hydrocarbon recycle stream for admixture with the reduced crude oil therein.
Claim 3
Dependent Claim 34 words
The process of claim 1 further characterized in that said coking conditions include a pressure from about 20 psig. to about 75 psig. and a temperature from about 875° F. to about 975° F.
Claim 4
Dependent Claim 35 words
The process of claim 1 further characterized in that said hydrodesulfurization is effected at a pressure from about 500 psig. to about 1200 psig., and a temperature from about 600° F. to about 800° F.

References Cited (Backward Citations)

US2901417A Cited
US2789085A Cited
US2793172A Cited
US3369992A Cited
US3475323A Cited
US3707462A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-11-14 1981-05-16 1981-11-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-11-14 1985-05-16 1985-11-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-11-14 1989-05-16 1989-11-15 $7700.00 Window Closed / Lapsed

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