US4824362A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for operation of flash smelting furnace
Assignee: Sumitomo Metal Mining Co Ltd
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Filing: 1988-02-11
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Granted: 1989-04-25
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Expires: 2008-02-11
Abstract
Abstract A method of operating a flash smelting furnace which includes a reaction shaft, a concentrate burner disposed at the top of the reaction shaft, a settler disposed with one end thereof connected to the lower part of the reaction shaft, an uptake disposed as connected to the other end of the settler, and at least one lance pipe disposed through the ceiling of the settler between the reaction shaft and the uptake and adapted to permit forced supply of at least powdery raw materials and a reaction gas into the melt in the settler includes the steps of blowing the powdery raw materials containing only a small amount of incombustible substances and the reaction gas into the reaction shaft through the concentrate burner, blowing powdery raw materials containing at least incombustible substances through the lance pipe, and employing means capable of at least retaining the heat of the melt.
Inventors
- 👤 Takayoshi Kimura
- 👤 Yasuo Ojima
- 👤 Yoshiaki Mori
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 03:58
CPC Classifications
F; F27; F27B; F27B9/00; C; C22; C22B; C22B5/00; C22B5/02; C22B15/00; C22B5/12; C22B5/14
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
255 words
A method of producing a copper or nickel-containing matte from a powdered concentrate which contains a copper or nickel sulfide ore in an apparatus which includes a vertical reaction shaft that has a concentrate burner at an upper end thereof and forms a lower end, a horizontal settler which is connected at a first end thereof to a said lower end of said reaction shaft and has a ceiling and a second end, and an uptake shaft connected to said second end of said settler, said method comprising the steps of (a) blowing a reaction gas and a powdery raw material which includes said powdered concentrate through said concentrate burner so that said powdered concentrate will react with said reaction gas as said powdered concentrate descends within said reaction shaft, thereby providing in said settler a lower liquid layer of copper or nickel-containing matte, an upper liquid layer of slag and a hot waste gas containing dust, (b) providing at least one downwardly-extending lance pipe in said ceiling of said settler, (c) jointly blowing said powdered concentrate, recycled dust, powdery auxiliary fuel and a reaction gas through each lance pipe at a speed of 50 to 150 m/s and into said slag layer in said settler, thereby providing additional slag, copper or nickel-containing matte and hot waste gas, (d) removing said hot waste gas from said settler through said uptake shaft, (e) recovering said dust from said hot waste gas, and (f) recycling at least some of said recovered dust for use in step (c).
Claim 2
Independent Claim
255 words
A method of producing a copper or nickel-containing matte from a powdered concentrate which contains a copper or nickel sulfide ore in an apparatus which includes a vertical reaction shaft that has a concentrate burner at an upper end thereof and forms a lower end, a horizontal settler which is connected at a first end thereof to a said lower end of said reaction shaft and has a ceiling and a second end, and an uptake shaft connected to said second end of said settler, said method comprising the steps of (a) blowing a reaction gas and a powdery raw material which includes said powdered concentrate through said concentrate burner so that said powdered concentrate will react with said reaction gas as said powdered concentrate descends within said reaction shaft, thereby providing in said settler a lower liquid layer of copper or nickel-containing matte, an upper liquid layer of slag and a hot waste gas containing dust, (b) providing at least one downwardly-extending lance pipe in said ceiling of said settler, (c) jointly blowing said powdered concentrate, recycled dust, powdery auxiliary fuel and a reaction gas through each lance pipe at a speed of 50 to 150 m/s and into said slag layer in said settler, thereby providing additional slag, copper or nickel-containing matte and hot waste gas, (d) removing said hot waste gas from said settler through said uptake shaft, (e) recovering said dust from said hot waste gas, and (f) recycling at least some of said recovered dust for use in step (c).
Claim 3
Dependent Claim
19 words
A method according to claim 1, wherein said reaction gas in steps (a) and (c) consists of hot air.
Claim 4
Dependent Claim
19 words
A method according to claim 1, wherein said reaction gas in steps (a) and (c) consists of oxygen-enriched air.
Claim 5
Dependent Claim
23 words
A method according to claim 1, wherein said powdery raw material in step (a) includes recycled dust from step (f) and a flux.
References Cited (Backward Citations)
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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) | 1992-04-24 | 1992-10-24 | 1993-04-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-04-24 | 1996-10-24 | 1997-04-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-04-24 | 2000-10-24 | 2001-04-25 | $7700.00 | Window Closed / Lapsed |