US3959084A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for cooling of coke
Assignee: Dravo Corp
•
Filing: 1974-09-25
•
Granted: 1976-05-25
•
Expires: 1994-09-25
Abstract
Abstract Upon discharge from a coke oven, highly heated coke is cooled by charging the hot coke to a shaft cooler wherein it is contacted with an inert cooling gas to a temperature of between 600°-800°F, the coke then being discharged through a pressure retention device and to a quench bunker by means of a feeding device, with the coke further cooled to a temperature of below 300°F by water sprays, while preventing entrance of steam into the shaft cooler. The feed means and quench bunker are enclosed so as to prevent discharge to the atmosphere of steam produced on contact of the spray with the coke as well as particulate material carried thereby. The coke at below 300°F is then fed to a conveyor for removal from the cooling area.
Inventors
- 👤 John Gordon Price
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 13:45
CPC Classifications
C; C10; C10B; C10B39/00; C10B39/02; C10B39/04
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
121 words
The method of cooling coke from incandescent temperature to a temperature where it may be transported in open air on a conveyor belt which comprises initially reducing the temperature from said incandescent temperature to a range between 600°F and 800°F by inert gas circulating therethrough in a first enclosure and thereafter immediately cooling it in a second enclosure by direct transfer of heat from the coke to water where the latent heat of vaporization of the water as liquid to steam effects the primary reduction of temperature of the coke from the range of 600°F to 800°F to a temperature between about 200°-300°F, below the temperature where steam and hot coke react, and excluding steam so produced from said first enclosure.
Claim 2
Independent Claim
121 words
The method of cooling coke from incandescent temperature to a temperature where it may be transported in open air on a conveyor belt which comprises initially reducing the temperature from said incandescent temperature to a range between 600°F and 800°F by inert gas circulating therethrough in a first enclosure and thereafter immediately cooling it in a second enclosure by direct transfer of heat from the coke to water where the latent heat of vaporization of the water as liquid to steam effects the primary reduction of temperature of the coke from the range of 600°F to 800°F to a temperature between about 200°-300°F, below the temperature where steam and hot coke react, and excluding steam so produced from said first enclosure.
Claim 3
Dependent Claim
46 words
The method of cooling coke defined in claim 1, wherein partially cooled coke at a temperature between 600°-800°F is continuously charged to the second enclosure for reduction of the temperature thereof to a temperature between about 200°-300°F, below the temperature where steam and hot coke react.
Claim 4
Dependent Claim
43 words
The method of cooling coke defined in claim 1, wherein coke is removed from said second enclosure at a temperature between about 200°-300°F and carries residual water therewith such that the coke, when further cooled to ambient temperature, will contain about 2-3% moisture.
References Cited (Backward Citations)
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Cited
US3774315A
Cited
US3800428A
Cited
US3843458A
Cited
US3809619A
Cited
US3795987A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-05-25 | 1979-11-24 | 1980-05-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-25 | 1983-11-24 | 1984-05-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-25 | 1987-11-24 | 1988-05-25 | $7700.00 | Window Closed / Lapsed |