Patent US2406995A successfully refreshed from Google Patents.
Patent US4404092A successfully refreshed from Google Patents.
US4404092A
Expired / Lapsed
US
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Delayed coking process
Assignee: Mobil Oil AS
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Filing: 1982-02-12
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Granted: 1983-09-13
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Expires: 2002-02-12
Abstract
Abstract The liquid yield of a delayed coking process is improved by controlling the temperature of the vapor space above the carbonizing mass so that that incipient coking and cracking of the vapors is reduced. The temperature is preferably controlled by introducing a quenching liquid into the vapor space; suitable liquids for this purpose include water, coker feedstock and the bottoms fraction derived from the coker products.
Inventors
- 👤 Costandi A. Audeh
- 👤 Tsoung-Yuan Yan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 15:22
CPC Classifications
C; C10; C10B; C10B55/00; C10G; C10G9/00; C10G9/005
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
137 words
In a delayed coking process in which a heated heavy hydrocarbon feedstock is introduced into the bottom of a coker drum to form a carbonizing mass at a temperature of at least 450° C. in which the delayed coking reaction occurs to form coke and gas and vapor phase products which are removed from the vapor space above the carbonizing mass through an outlet the improvement which comprises: maintaining the temperature of the vapor space substantially below 450° C. by introducing a quenching liquid into the vapor space of the coker drum in the region of the outlet, whereby the temperature of vapor space is maintained at its lowest in the region of the outlet and at its highest in the region of the interface with the carbonizing mass and liquid products are obtained in improved yield.
Claim 2
Dependent Claim
137 words
In a delayed coking process in which a heated heavy hydrocarbon feedstock is introduced into the bottom of a coker drum to form a carbonizing mass at a temperature of at least 450° C. in which the delayed coking reaction occurs to form coke and gas and vapor phase products which are removed from the vapor space above the carbonizing mass through an outlet the improvement which comprises: maintaining the temperature of the vapor space substantially below 450° C. by introducing a quenching liquid into the vapor space of the coker drum in the region of the outlet, whereby the temperature of vapor space is maintained at its lowest in the region of the outlet and at its highest in the region of the interface with the carbonizing mass and liquid products are obtained in improved yield.
Claim 3
Dependent Claim
26 words
A process according to claim 1 in which the temperature of the vapor space is maintained at about 425° C. in the region of the outlet.
Claim 4
Dependent Claim
37 words
A process according to claim 1 in which the temperature of the vapor space is maintained by introducing a quenching liquid comprising water into the vapor space of the coker drum in the region of the outlet.
Claim 5
Dependent Claim
43 words
A process according to claim 1 in which the temperature of the vapor space is maintained by introducing a quenching liquid comprising heavy hydrocarbon feedstock for the coking process into the vapor space of the coker drum in the region of the outlet.
Claim 6
Dependent Claim
48 words
A process according to claim 1 in which the temperature of the vapor space is maintained by introducing a quenching liquid comprising a bottoms fraction derived by fractionation of the vapor phase coker products into the vapor space of the coker drum in the region of the outlet.
Claim 7
Dependent Claim
60 words
A process according to claim 1 in which the temperature of the vapor space is maintained by introducing a quenching liquid comprising a mixture of a heavy hydrocarbon feedstock for the coking process and a bottoms fraction derived by fractionation of the vapor phase coker products into the vapor space of the coker drum in the region of the outlet.
Claim 8
Dependent Claim
120 words
A delayed coking process in which heated petroleum residua is introduced into a coking drum to form a carbonizing mass at a temperature of at least 450° C. to form coke and a vapor phase which is maintained at a temperature substantially equal to the carbonizing mass temperature in the region of the interface between the vapor phase and carbonizing mass; withdrawing hot vapor from the coker drum through a vapor outlet above the carbonizing mass; introducing quenching water into the vapor phase in the region of the vapor outlet to maintain an outlet vapor temperature below about 425° C. with progressively hotter temperature towards the carbonizing mass; and recovering liquid hydrocarbon products from the vapor phase in improved yield.
Claim 9
Dependent Claim
120 words
A delayed coking process in which heated petroleum residua is introduced into a coking drum to form a carbonizing mass at a temperature of at least 450° C. to form coke and a vapor phase which is maintained at a temperature substantially equal to the carbonizing mass temperature in the region of the interface between the vapor phase and carbonizing mass; withdrawing hot vapor from the coker drum through a vapor outlet above the carbonizing mass; introducing quenching water into the vapor phase in the region of the vapor outlet to maintain an outlet vapor temperature below about 425° C. with progressively hotter temperature towards the carbonizing mass; and recovering liquid hydrocarbon products from the vapor phase in improved yield.
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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) | 1986-09-12 | 1987-03-14 | 1987-09-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-09-12 | 1991-03-14 | 1991-09-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-09-12 | 1995-03-14 | 1995-09-13 | $7700.00 | Window Closed / Lapsed |