Organic compound, perovskite precursor solution, perovskite film, perovskite cell, and electric apparatus
US-2025386725-A1 · Dec 18, 2025 · US
US11261088B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11261088-B2 |
| Application number | US-202017033788-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 26, 2020 |
| Priority date | Oct 17, 2019 |
| Publication date | Mar 1, 2022 |
| Grant date | Mar 1, 2022 |
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A method for production of ammonium phosphate from phosphate rock slurry. The method includes: introducing flue gas containing SO2 into a phosphate rock slurry, to yield an absorption solution; evaporating waste ammonia water containing 10-20 wt. % ammonia to yield ammonia gas; introducing the ammonia gas into the absorption solution at a temperature of 110-135° C. until a neutralization degree of the absorption solution reaches 1.5-1.6, thus yielding an ammonium phosphate solution and calcium sulfate; separating the calcium sulfate from the ammonium phosphate solution; and introducing the ammonium phosphate solution to a granulator for granulation to yield ammonium phosphate granules; drying and sieving the ammonium phosphate granules, thereby yielding ammonium phosphate.
Opening claim text (preview).
What is claimed is: 1. A method, comprising: 1) introducing flue gas containing SO 2 and oxygen into an absorption tower, and pumping a phosphate rock slurry comprising Ca 10 (PO 4 ) 6 F 2 into the absorption tower to contact the flue gas, whereby a first absorption solution comprising sulfuric acid and 20-25 wt. % of water is yielded; 2) transferring the absorption solution obtained in 1) into a neutralization tank, and reacting phosphate rock with sulfuric acid in the first absorption solution to obtain a second absorption solution comprising phosphoric acid and calcium sulfate; 3) evaporating waste ammonia water containing 10-20 wt. % ammonia to yield ammonia gas; 4) introducing the ammonia gas into the second absorption solution at a temperature of 110-135° C. until a neutralization degree of the second absorption solution reaches 1.5-1.6, thus yielding an ammonium phosphate solution and calcium sulfate; 5) separating the calcium sulfate from the ammonium phosphate solution; and 6) introducing the ammonium phosphate solution to a granulator for granulation to yield ammonium phosphate granules; drying and sieving the ammonium phosphate granules, thereby yielding ammonium phosphate. 2. The method of claim 1 , wherein the phosphate rock slurry has a solid content of 35-55 wt. %, and is prepared by: grinding a phosphate rock using a ball mill until more than 90% of phosphate rock powders pass through a 100-mesh sieve; and mixing the phosphate rock powders with water in a surge tank. 3. The method of claim 2 , wherein the flue gas comprises 10-25% (v/v) of O 2 and less than or equal to 3% (v/v) of SO 2 ; the phosphate rock slurry has a pH value of 4-6; the phosphate rock slurry and the flue gas are introduced to an absorption tower in a liquid-gas ratio of 8-12 L/m 3 , and a temperature in the absorption tower is 25-60° C.
Ammonium phosphates · CPC title
Purification of calcium sulfates · CPC title
Sulfates of Ca from gases containing sulfur oxides · CPC title
characterised by a specific solution or suspension · CPC title
Phosphates · CPC title
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