Patent US4366047A successfully refreshed from Google Patents.
US4366047A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Combination hydrorefining, heat-treating and hydrocracking process
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1981-06-02
•
Granted: 1982-12-28
•
Expires: 2001-06-02
Abstract
Abstract A process for upgrading a heavy hydrocarbonaceous oil is provided in which the oil is hydrorefined, heat-treated and hydrocracked to increase the selectivity of the hydrocracked product to components boiling in the range of 350° to 675° F.
Inventors
- 👤 William E. Winter
- 👤 Bong H. Chang
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 23:30
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/12
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
162 words
A process for upgrading a heavy hydrocarbonaceous oil feed, which comprises the steps of: (a) contacting said oil feed with added hydrogen in the presence of a hydrorefining catalyst at hydrorefining conditions, in a hydrorefining zone; (b) heat-treating at least a portion of the entire effluent of said hydrorefining zone, said portion including normally liquid hydrocarbons and hydrogen, in a heat-treating zone, in the absence of a catalyst at conditions such as to avoid any significant cracking of said normally liquid hydrocarbons, said conditions including a temperature in the range of about 500° to about 720° F., for a period of time ranging from about 0.25 hour to about 6 hours; (c) passing at least a portion of the entire heat-treated effluent, including hydrogen and normally liquid hydrocarbons, to a hydrocracking zone; (d) subjecting said portion of heat-treated effluent to hydrocracking conditions in the presence of a hydrocracking catalyst in said hydrocracking zone, and (e) recovering a hydrocracked normally liquid hydrocarbonaceous product.
Claim 2
Dependent Claim
162 words
A process for upgrading a heavy hydrocarbonaceous oil feed, which comprises the steps of: (a) contacting said oil feed with added hydrogen in the presence of a hydrorefining catalyst at hydrorefining conditions, in a hydrorefining zone; (b) heat-treating at least a portion of the entire effluent of said hydrorefining zone, said portion including normally liquid hydrocarbons and hydrogen, in a heat-treating zone, in the absence of a catalyst at conditions such as to avoid any significant cracking of said normally liquid hydrocarbons, said conditions including a temperature in the range of about 500° to about 720° F., for a period of time ranging from about 0.25 hour to about 6 hours; (c) passing at least a portion of the entire heat-treated effluent, including hydrogen and normally liquid hydrocarbons, to a hydrocracking zone; (d) subjecting said portion of heat-treated effluent to hydrocracking conditions in the presence of a hydrocracking catalyst in said hydrocracking zone, and (e) recovering a hydrocracked normally liquid hydrocarbonaceous product.
Claim 3
Dependent Claim
26 words
The process of claim 1 wherein said heavy hydrocarbonaceous oil feed of step (a) has an atmospheric pressure boiling point of at least about 650° F.
Claim 4
Dependent Claim
25 words
The process of claim 1 wherein said heavy hydrocarbonaceous oil feed of step (a) has at least 10 weight percent constituents boiling above 900° F.
Claim 5
Dependent Claim
23 words
The process of claim 1 wherein said heat-treating conditions of step (b) include a temperature ranging from about 500° to about 690° F.
Claim 6
Dependent Claim
26 words
The process of claim 1 wherein said heat-treating of step (b) is conducted for a period of time ranging from about 0.5 to about 3 hours.
Claim 7
Dependent Claim
34 words
The process of claim 1 wherein said hydrorefining conditions in step (a) include a temperature ranging from about 600° to about 900° F. and a pressure ranging from about 50 to about 3500 psig.
Claim 8
Dependent Claim
34 words
The process of claim 1 wherein said hydrocracking conditions of step (d) include a temperature ranging from about 400° to about 900° F. and a pressure ranging from about 500 to about 3500 psig.
References Cited (Backward Citations)
US2889263A
Cited
US3055823A
Cited
US3509044A
Cited
US3730875A
Cited
US4298457A
Cited
US4292168A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-12-27 | 1986-06-28 | 1986-12-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-12-27 | 1990-06-28 | 1990-12-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-12-27 | 1994-06-28 | 1994-12-28 | $7700.00 | Window Closed / Lapsed |