US4025610A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for denitrifying coke
Assignee: JFE Engineering Corp
•
Filing: 1974-12-13
•
Granted: 1977-05-24
•
Expires: 1994-12-13
Abstract
Abstract A grain coke is packed in a vertical furnace between a pair of opposite electrodes for passing current through the coke, thus heating the same to a temperature of above 1400° C, preferably 1500° C for more than 10 minutes. Coke is loaded into the furnace from an upper portion and heat treated coke is cooled and then discharged from the bottom. Inert or reducing gas may be introduced into the lower portion of the furnace and discharged from the upper portion thereby cooling heat treated coke and preheating loaded coke.
Inventors
- 👤 Gyoichi Suzuki
- 👤 Ryo Ando
- 👤 Hideyuki Yoshikoshi
- 👤 Seishiro Nagaoka
- 👤 Yogiro Yamaoka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 23:22
CPC Classifications
C; C10; C10B; C10B19/00; C10L; C10L9/00; C10L9/08
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
101 words
A method for denitrifying metallurgical coke, wherein a metallurgical coke is packed into a vertical furnace having a coke loading opening at the upper end thereof and a coke discharge opening at the lower end thereof, characterized in that an electric current is passed along the coke loading-discharge line in said furnace between a pair of electrodes positioned at the upper and lower portions of said furnace in a downward and an upward direction, respectively, to generate Joule heat in said packed coke at a temperature greater than 1400° C. for more than 10 minutes in an inert or reducing atmosphere.
Claim 2
Independent Claim
101 words
A method for denitrifying metallurgical coke, wherein a metallurgical coke is packed into a vertical furnace having a coke loading opening at the upper end thereof and a coke discharge opening at the lower end thereof, characterized in that an electric current is passed along the coke loading-discharge line in said furnace between a pair of electrodes positioned at the upper and lower portions of said furnace in a downward and an upward direction, respectively, to generate Joule heat in said packed coke at a temperature greater than 1400° C. for more than 10 minutes in an inert or reducing atmosphere.
Claim 3
Dependent Claim
13 words
The method of claim 1, wherein said temperature is greater than 1500° C.
Claim 4
Dependent Claim
18 words
The method of claim 1, wherein the particle size of said metallurgical coke is less than 20 mm.
Claim 5
Dependent Claim
19 words
The method of claim 1, wherein the particle size of said metallurgical coke is from 1 to 10 mm.
Claim 6
Dependent Claim
36 words
The method according to claim 1 wherein said coke powder is continuously loaded into the upper portion of a vertical furnace, and the heat treated coke is continuously discharged from the lower portion of the furnace.
Claim 7
Dependent Claim
61 words
The method according to claim 1 wherein inert or reducing gas is admitted into the lower portion of said furnace and discharged from the upper portion of said furnace for cooling heat treated coke, and the heat of the atmosphere discharged from the furnace is used to preheat the grain coke before it is loaded in the heating zone of furnace.
Claim 8
Dependent Claim
52 words
The method according to claim 6 wherein the gas in the furnace is circulated by a blower installed in a circulating conduit connected between the upper end and the lower end of said furnace and the dust in said gas is removed by dust removing means also installed in said circulating conduit.
Claim 9
Dependent Claim
34 words
The method according to claim 7 wherein a heat exchanger is provided in said circulating conduit for preheating the coke to be loaded in said furnace by the heat recovered by said heat exchanger.
Claim 10
Dependent Claim
62 words
The method according to claim 1 wherein said grain coke has a particle size of less than 5 mm, furnace atmosphere is introduced into the lower portion of said furnace for cooling heat treated coke, then discharged to the outside of said furnace and again introduced into the upper portion of said furnace for preheating the coke loaded in said upper portion.
Claim 11
Dependent Claim
69 words
The method according to claim 1 wherein the coke is packed in said furnace with such grain size distribution that the resistance to the flow of furnace atmosphere through the packed grain coke decreases towards the furnace wall thereby selectively recovering the heat generated in the packed coke at portions thereof near said furnace wall and preventing local overheating of the packed coke due to nonuniform distribution of current.
Claim 12
Dependent Claim
94 words
Apparatus for denitrifying metallurgical coke, comprising a vertical furnace having a coke loading opening at the upper end thereof and a coke discharge opening at the lower end thereof, characterized in that a pair of electrodes are positioned in said furnace, one electrode being positioned at the upper portion thereof in a downward direction and the other electrode of the pair being positioned at the lower portion thereof in an upward direction, whereby electric current passed between said electrodes heats said metallurgical coke packed in said furnace by Joule heat generated by said current.
Claim 13
Dependent Claim
94 words
Apparatus for denitrifying metallurgical coke, comprising a vertical furnace having a coke loading opening at the upper end thereof and a coke discharge opening at the lower end thereof, characterized in that a pair of electrodes are positioned in said furnace, one electrode being positioned at the upper portion thereof in a downward direction and the other electrode of the pair being positioned at the lower portion thereof in an upward direction, whereby electric current passed between said electrodes heats said metallurgical coke packed in said furnace by Joule heat generated by said current.
Claim 14
Dependent Claim
34 words
The apparatus according to claim 11 which further comprises a gas inlet port near said discharge opening for admitting inert gas or reducing gas and a gas discharge opening near said coke loading opening.
Claim 15
Dependent Claim
34 words
The apparatus according to claim 11 wherein said furnace is of the vertical type and said electrodes close the coke loading opening and the discharge opening thereby operating said furnace as a batch type.
Claim 16
Dependent Claim
32 words
The apparatus according to claim 11 wherein said furnace is of a vertical type and said electrodes are spaced from the furnace wall thereby permitting continuous loading and discharging of the coke.
Claim 17
Dependent Claim
36 words
The apparatus according to claim 14 wherein the electrode positioned at the discharge opening is provided with a flange and the discharge opening is defined between said flange and the lower end of the furnace wall.
Claim 18
Dependent Claim
60 words
The apparatus according to claim 11 wherein said furnace is provided with a gas inlet opening near said coke discharge opening and a gas discharge opening near said coke loading opening, and said apparatus further comprises a circulating conduit connected between said gas inlet opening and said gas discharge opening and a blower connected in series with said circulating conduit.
Claim 19
Dependent Claim
36 words
The apparatus according to claim 16 wherein said circulating conduit includes a pair of annular manifolds encircling said furnace and said annular manifolds are connected to said gas inlet opening and said gas discharge opening, respectively.
Claim 20
Dependent Claim
27 words
The apparatus according to claim 16 wherein said circulating conduit further includes a dust collector and a heat exchanger which are connected in series with said blower.
Claim 21
Dependent Claim
37 words
The apparatus according to claim 13 wherein a heating zone is defined between said pair of electrodes and bypass conduits are provided for said furnace on the outside thereof for bypassing furnace gas around said heating zone.
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) | 1980-05-23 | 1980-11-22 | 1981-05-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-05-23 | 1984-11-22 | 1985-05-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-05-23 | 1988-11-22 | 1989-05-24 | $7700.00 | Window Closed / Lapsed |