Patent US3957484A successfully refreshed from Google Patents.
US3957484A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Fluid bed roasting of metal sulphides at high temperatures
Assignee: Individual
•
Filing: 1974-09-18
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Granted: 1976-05-18
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Expires: 1994-09-18
Abstract
Abstract An improved method for agglomerative fluid bed roasting of metal sulphide particles. The sulphide particles are fed as an aqueous slurry through the freeboard of the roaster onto the surface of a bed of roasted calcine agglomerate particles fluidized by a free oxygen-bearing gas. Slurry water is evaporated in the bed and the sulphides are roasted therein. The feed rates of sulphide, water and free oxygen-containing gas are controlled to ensure temperatures in the roaster such that fusion occurs during roasting and agglomerated calcine particles are formed with regular, rounded surfaces. Calcine particles small enough to become entrained in the roaster off-gases are readily disengaged therefrom in cyclones to provide substantially dust-free SO2-bearing gas. A preferred practice of the method is feeding substantially the stoichiometric amount of free oxygen to convert the sulphide to SO2 and metal oxide, thereby producing on the one hand a roasted oxide calcine substantially devoid of sulphur and on the other hand an SO2-bearing gas substantially devoid of free oxygen. The method is particularly advantageous in the roasting of pyrrhotite concentrates and other sulphide concentrates containing pyrrhotite such as those derived from the nickel-copper ores of the Sudbury Basin.
Inventors
- 👤 Simon Otto Fekete
- 👤 Colin Bruce MacKenzie
- 👤 Philip George Thornhill
- 👤 Edward Howard Coulter
- 👤 Kenneth Leslie Agnew
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 19:56
CPC Classifications
C; C22; C22B; C22B1/00; C22B1/02; C22B1/10
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
171 words
A method for roasting particulate metal sulphides in a fluid bed reactor containing a fluidized bed of hot roasted calcine particles and a freeboard space between the bed and the top of the reactor comprising: i. feeding a free oxygen-containing gas upwardly through the reactor thereby maintaining the fluidized bed; ii. feeding an aqueous slurry of metal sulphide particles onto the surface of the fluidized bed thereby supplying both water and sulphide to the bed, iii. both evaporating a majority of the slurry water in the hot bed thereby forming agglomerates of sulphide particles that become dispersed in the bed as evaporation occurs and roasting the sulphide, while controlling the rates of feeding free oxygencontaining gas, water and sulphide to the bed to control temperatures in the bed and in the freeboard space such that fusion occurs during roasting thereby forming roasted calcine agglomerate particles of controlled size and rounded shape, iv. recovering the roasted calcine agglomerate particles from the bed, and v. recovering sulphur dioxide-containing gas from the freeboard space.
Claim 2
Independent Claim
171 words
A method for roasting particulate metal sulphides in a fluid bed reactor containing a fluidized bed of hot roasted calcine particles and a freeboard space between the bed and the top of the reactor comprising: i. feeding a free oxygen-containing gas upwardly through the reactor thereby maintaining the fluidized bed; ii. feeding an aqueous slurry of metal sulphide particles onto the surface of the fluidized bed thereby supplying both water and sulphide to the bed, iii. both evaporating a majority of the slurry water in the hot bed thereby forming agglomerates of sulphide particles that become dispersed in the bed as evaporation occurs and roasting the sulphide, while controlling the rates of feeding free oxygencontaining gas, water and sulphide to the bed to control temperatures in the bed and in the freeboard space such that fusion occurs during roasting thereby forming roasted calcine agglomerate particles of controlled size and rounded shape, iv. recovering the roasted calcine agglomerate particles from the bed, and v. recovering sulphur dioxide-containing gas from the freeboard space.
Claim 3
Dependent Claim
34 words
A method as claimed in claim 1 including passing said sulphur dioxide-containing gas through a cyclone thereby removing entrained calcine agglomerate particles therefrom and producing a substantially clean gas for subsequent sulphur recovery therefrom.
Claim 4
Dependent Claim
33 words
Method according to claim 2 in which the metal sulphide is in the form of a mineral concentrate and the mineral is selected from the group comprising pyrrhotite, pentlandite, chalcopyrite and mixtures thereof.
Claim 5
Dependent Claim
20 words
Method according to claim 3 in which the metal sulphide is an iron sulphide concentrate consisting predominantly of nickeliferous pyrrhotite.
Claim 6
Dependent Claim
25 words
Method according to claim 3 in which the metal sulphide is a nickel-copper sulphide concentrate consisting predominantly of a mixture of pyrrhotite, pentlandite and chalcopyrite.
Claim 7
Dependent Claim
22 words
Method according to claim 2 in which the free oxygen-containing gas is selected from the group comprising air, oxygen-enriched air, and oxygen.
Claim 8
Dependent Claim
22 words
Method according to claim 2, comprising feeding the aqueous slurry vertically through the freeboard and centrally onto the surface of the bed.
Claim 9
Dependent Claim
64 words
Method according to claim 2, comprising feeding the aqueous slurry at a preselected pulp density, feeding auxiliary cooling water onto the surface of the bed, and adjusting the flow rate of the cooling water to compensate for variations in the flow of slurry water resulting from variations in the pulp density of the slurry from the preselected value, thereby maintaining substantially steady bed temperatures.
Claim 10
Dependent Claim
64 words
Method according to claim 2 and additionally comprising controlling the feed rates of sulphide and free oxygen-containing gas with respect to one another such that free oxygen is supplied in substantially the stoichiometric quantity required to roast all the metal sulphide to sulphur dioxide and metal oxide thereby producing roasted calcine substantially devoid of sulphur and sulphur dioxide-bearing gas substantially devoid of free oxygen.
Claim 11
Dependent Claim
19 words
Method according to claim 9 in which the metal sulphide is nickeliferous pyrrhotite and the metal oxide is hematite.
Claim 12
Dependent Claim
127 words
Method according to claim 2 in which the metal sulphide is nickeliferous pyrrhotite, the free oxygen-containing gas is air, and additionally comprising, i. feeding the aqueous slurry at a preselected pulp density vertically through the freeboard and centrally onto the surface of the bed, ii. controlling the feed rate of pyrrhotite relative to that of air such that the free oxygen supplied is substantially the stoichiometric amount required to roast the pyrrhotite to hematite and sulphur dioxide. iii. feeding auxiliary cooling water onto the surface of the bed at a controlled rate and adjusting the rate to control the bed temperature at a preselected level, thereby producing roasted calcine agglomerate particles of controlled size substantially devoid of sulphur and sulphur dioxide-containing gas substantially devoid of free oxygen.
Claim 13
Dependent Claim
32 words
Method according to claim 11, and additionally comprising treating the roasted calcine in a sulphating atmosphere at elevated temperature and subsequently leaching the sulphated calcine in aqueous solution to dissolve nickel therefrom.
Claim 14
Dependent Claim
32 words
Method according to claim 11, and additionally comprising treating the roasted calcine in a reducing atmosphere at elevated temperature and subsequently leaching the reduced calcine in ammoniacal solution to dissolve nickel therefrom.
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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) | 1979-05-18 | 1979-11-17 | 1980-05-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-18 | 1983-11-17 | 1984-05-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-18 | 1987-11-17 | 1988-05-18 | $7700.00 | Window Closed / Lapsed |