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US3992285A
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Process for the conversion of hydrocarbonaceous black oil
Assignee: Universal Oil Products Co
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Filing: 1974-09-23
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Granted: 1976-11-16
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Expires: 1994-09-23
Abstract
Abstract A process for the conversion of a hydrocarbonaceous black oil, wherein the terminal heating of the black oil before conversion is performed by the admixture of said black oil with a gas comprising steam and having a temperature greater than the hydrocarbon conversion temperature.
Inventors
- 👤 Leroi E. Hutchings
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 02:06
CPC Classifications
C; C10; C10G; C10G47/00; C10G45/00; C10G45/02; C10G45/24; C10G45/26
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
78 words
A process for the desulfurization of a hydrocarbonaceous black oil containing sulfur and asphaltic material which comprises preheating said oil by indirect heat exchange to a temperature not in excess of about 550°F., commingling with the preheated oil a steam-containing gas in sufficient amount and of sufficient temperature to raise the oil to a desulfurization temperature of from about 600°F. to about 800°F., and contacting the thus heated oil at a hydrocarbon conversion conditions with a desulfurization catalyst.
Claim 2
Dependent Claim
78 words
A process for the desulfurization of a hydrocarbonaceous black oil containing sulfur and asphaltic material which comprises preheating said oil by indirect heat exchange to a temperature not in excess of about 550°F., commingling with the preheated oil a steam-containing gas in sufficient amount and of sufficient temperature to raise the oil to a desulfurization temperature of from about 600°F. to about 800°F., and contacting the thus heated oil at a hydrocarbon conversion conditions with a desulfurization catalyst.
Claim 3
Dependent Claim
57 words
The process of claim 1 further characterized in that said hydrocarbon conversion conditions comprise a pressure from about 500 psig. to about 5000 psig., a temperature from about 600°F. to about 900°F., a hydrogen gas circulation rate from about 1000 SCFB to about 20,000 SCFB and a steam rate from about 1000 SCFB to about 20,000 SCFB.
Claim 4
Dependent Claim
42 words
The process of claim 1 further characterized in that at least a portion of the steam condensate formed during the admixture of the black oil with the steam is removed from the mixture before the black oil is contacted with the catalyst.
Claim 5
Dependent Claim
24 words
The process of claim 1 further characterized in that said black oil is derived from tar sand, shale or any other inorganic oil-bearing substance.
References Cited (Backward Citations)
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US3330760A
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US3565787A
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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) | 1979-11-16 | 1980-05-17 | 1980-11-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-11-16 | 1984-05-17 | 1984-11-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-11-16 | 1988-05-17 | 1988-11-16 | $7700.00 | Window Closed / Lapsed |