US4017585A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Fluid bed calcination process
Assignee: Dorr Oliver Inc
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Filing: 1974-10-29
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Granted: 1977-04-12
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Expires: 1994-10-29
Abstract
Abstract Phosphate rock is calcined under conditions calculated to completely oxidize the carbon and sulfur in the rock. Calcination is also conducted at elevated temperature to eliminate cadmium metal, a poisonous substance in fertilizers, from the calcined rock product. A fluid bed system for eliminating cadmium metal in the calcination of phosphate rock involves a two-vessel system in which an independent cadmium removal vessel served by a separate fluidizing air stream carries out volatilization of cadmium, while preheating, precalcining and cooling is conducted in another multi-bed reactor which is served by a separate fluidizing air stream.
Inventors
- 👤 Peter A. Angevine
- 👤 David W. Leyshon
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 07:31
CPC Classifications
C; C01; C01B; C01B25/00; C01B25/01
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
254 words
A process for calcining phosphate rock containing contaminating quantities of the heavy metal cadmium comprising, preheating the phosphate rock in a primary chamber wherein the rock is fluidized by a first gas stream at a temperature of from about 700° C to about 800° C, the exhaust gas from said primary chamber being conducted to the stack, transferring the rock to a secondary chamber countercurrent to said first gas stream wherein fuel is injected into said chamber for combustion and the rock is fluidized by said first gas stream at a temperature of from about 450° C to about 500° C, transferring the rock for calcining to a tertiary chamber wherein fuel is injected for combustion to attain a temperature in the range from about 1000° C to about 1150° C to volatilize the cadmium and the rock is fluidized by a second gas stream flowing in parallel with said first gas stream, the exhaust gas and volatilized cadmium from said tertiary chamber being handled separately from the exhaust gas from said primary chamber so that the cadmium may be condensed therefrom for separate disposal, transferring the calcined rock to a cooling chamber for fluidization in said first gas stream, said calcined rock being cooled to a temperature of from about 450° C to about 500° C and the fluidizing gas being heated by said rock to this temperature range, discharging the cooled calcined rock from said cooling chamber and conducting the heated fluidizing gas to the secondary chamber as the fluidizing gas therefor.
Claim 2
Dependent Claim
254 words
A process for calcining phosphate rock containing contaminating quantities of the heavy metal cadmium comprising, preheating the phosphate rock in a primary chamber wherein the rock is fluidized by a first gas stream at a temperature of from about 700° C to about 800° C, the exhaust gas from said primary chamber being conducted to the stack, transferring the rock to a secondary chamber countercurrent to said first gas stream wherein fuel is injected into said chamber for combustion and the rock is fluidized by said first gas stream at a temperature of from about 450° C to about 500° C, transferring the rock for calcining to a tertiary chamber wherein fuel is injected for combustion to attain a temperature in the range from about 1000° C to about 1150° C to volatilize the cadmium and the rock is fluidized by a second gas stream flowing in parallel with said first gas stream, the exhaust gas and volatilized cadmium from said tertiary chamber being handled separately from the exhaust gas from said primary chamber so that the cadmium may be condensed therefrom for separate disposal, transferring the calcined rock to a cooling chamber for fluidization in said first gas stream, said calcined rock being cooled to a temperature of from about 450° C to about 500° C and the fluidizing gas being heated by said rock to this temperature range, discharging the cooled calcined rock from said cooling chamber and conducting the heated fluidizing gas to the secondary chamber as the fluidizing gas therefor.
Claim 3
Dependent Claim
163 words
A process for calcining cadmium-contaminated phosphate rock which is to be employed in the manufacture of phosphoric acid, the phosphate rock also containing significant quantities of the impurities carbon and sulfur, the calcination process to be connected in such a way as to avoid increasing the corrosive nature of the product phosphoric acid and removing the undesirable cadmium from the phosphate rock product, comprising, calcining the phosphate rock in a fluidized bed reactor at a temperature of from about 1000° C to about 1150° C while employing a detention time in the calcining fluidized bed of from 30 to 200 minutes to volatize the cadmium and so remove it from the phosphate rock as a vapor for disposal, maintaining oxidizing conditions in said reactor by controlling the exhaust gas from said reactor to contain at least about 0.5%, by volume, of oxygen so that the carbon and sulfur impurities are essentially completely oxidized and the formation of corrosive sulfide constituents is thereby prevented.
Claim 4
Dependent Claim
163 words
A process for calcining cadmium-contaminated phosphate rock which is to be employed in the manufacture of phosphoric acid, the phosphate rock also containing significant quantities of the impurities carbon and sulfur, the calcination process to be connected in such a way as to avoid increasing the corrosive nature of the product phosphoric acid and removing the undesirable cadmium from the phosphate rock product, comprising, calcining the phosphate rock in a fluidized bed reactor at a temperature of from about 1000° C to about 1150° C while employing a detention time in the calcining fluidized bed of from 30 to 200 minutes to volatize the cadmium and so remove it from the phosphate rock as a vapor for disposal, maintaining oxidizing conditions in said reactor by controlling the exhaust gas from said reactor to contain at least about 0.5%, by volume, of oxygen so that the carbon and sulfur impurities are essentially completely oxidized and the formation of corrosive sulfide constituents is thereby prevented.
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) | 1980-04-11 | 1980-10-11 | 1981-04-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-04-11 | 1984-10-11 | 1985-04-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-04-11 | 1988-10-11 | 1989-04-12 | $7700.00 | Window Closed / Lapsed |