US4057490A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Thermal cracking process employing crushed oil shale as fuel
Assignee: Gulf Research and Development Co
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Filing: 1976-07-12
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Granted: 1977-11-08
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Expires: 1996-07-12
Abstract
Abstract In the thermal cracking of a hydrocarbon feed oil to produce a product including ethylene, the feed oil is passed together with entrained hot solids through a high temperature cracking zone. Coke-laden hot solids are recovered and passed to a burner zone together with crushed oil shale as supplementary fuel. An acidic material, such as HF catalyst from an alkylation unit, can also be employed as supplementary fuel. The acidic material will react with alkaline components in the oil shale to form stable neutral salts which circulate as heat carrier solids.
Inventors
- 👤 Francis Edmund Wynne, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 21:41
CPC Classifications
C; C10; C10G; C10G9/00; C10G9/28; C10G9/30
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
101 words
In a process for thermal cracking of a hydrocarbon feed oil to produce a product including ethylene, propylene and 1,3-butadiene wherein said feed oil is passed together with entrained hot catalytically inert solids through a cracking zone at a temperature between 1,430° and 2,500° F. for a residence time of 0.05 to 2 seconds and coke-laden hot solids are recovered and passed to a burner zone operated at a temperature above 1,700° F. together with supplementary fuel, the improvement wherein said supplementary fuel comprises crushed oil shale and said entrained hot catalytically inert solids includes solids derived from said shale oil.
Claim 2
Dependent Claim
101 words
In a process for thermal cracking of a hydrocarbon feed oil to produce a product including ethylene, propylene and 1,3-butadiene wherein said feed oil is passed together with entrained hot catalytically inert solids through a cracking zone at a temperature between 1,430° and 2,500° F. for a residence time of 0.05 to 2 seconds and coke-laden hot solids are recovered and passed to a burner zone operated at a temperature above 1,700° F. together with supplementary fuel, the improvement wherein said supplementary fuel comprises crushed oil shale and said entrained hot catalytically inert solids includes solids derived from said shale oil.
Claim 3
Dependent Claim
30 words
The process of claim 1 including the additional step of charging an acidic material to said burner zone, said crushed oil shale containing alkaline materials which neutralize said acidic material.
Claim 4
Dependent Claim
26 words
The process of claim 2 wherein said acidic material is hydrogen fluoride which is neutralized by CaO in said oil shale to form CaFl 2 .
Claim 5
Dependent Claim
14 words
The process of claim 3 wherein the entrained hot solids includes CaFl 2 .
Claim 6
Dependent Claim
18 words
The process of claim 1 wherein the residence time in the cracking zone is 0.05 to 0.5 seconds.
Claim 7
Dependent Claim
22 words
The process of claim 1 wherein the product stream leaving the cracking zone is immediately quenched to a temperature below 1,300° F.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-11-07 | 1981-05-09 | 1981-11-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-11-07 | 1985-05-09 | 1985-11-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-11-07 | 1989-05-09 | 1989-11-08 | $7700.00 | Window Closed / Lapsed |