Methods and systems for treatment of lime to form vaterite
US-12077447-B2 · Sep 3, 2024 · US
US9505629B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9505629-B2 |
| Application number | US-201414461201-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 15, 2014 |
| Priority date | Aug 19, 2013 |
| Publication date | Nov 29, 2016 |
| Grant date | Nov 29, 2016 |
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Disclosed is a method of preparing calcium carbonate using a direct carbonation reaction. The method includes dissolving fuel gas desulfurization gypsum into an ammonia solution, performing a filtering process after making a carbonation reaction by feeding carbon dioxide into the ammonia solution in which the fuel gas desulfurization gypsum is dissolved, and performing a filtering process after precipitating the calcium carbonate by maintaining a filtered solution in a stationary state.
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What is claimed is: 1. A method of preparing calcium carbonate using a direct carbonation reaction, the method comprising: dissolving flue gas desulfurization gypsum into an ammonia solution; performing a filtering process to obtain a filtered solution after making a carbonation reaction by feeding carbon dioxide into the ammonia solution in which the flue gas desulfurization gypsum is dissolved; and performing a filtering process to obtain solid-phase calcium carbonate after precipitating the calcium carbonate by maintaining the filtered solution in a stationary state, wherein a solid dosage of the flue gas desulfurization gypsum to the ammonia solution is in a range of 5 g/L to 20 g/L, wherein the calcium carbonate includes vaterite crystals having 100% whiteness, and wherein the direct carbonation reaction is performed at normal temperature and normal pressure. 2. The method of claim 1 , wherein an ammonia concentration in the ammonia solution is in a range of 4% by volume to 12% by volume. 3. The method of claim 1 , wherein the dissolving of the flue gas desulfurization gypsum into the ammonia solution comprises performing an agitating process at a rate in a range of 350 rpm to 450 rpm for five minutes. 4. The method of claim 1 , wherein a concentration of the flue gas desulfurization gypsum in the ammonia solution in which the flue gas desulfurization gypsum is in a range of 30 mM to 110 mM. 5. The method of claim 1 , wherein the carbon dioxide is fed at a flow rate in a range of 1 L/min to 3 L/min. 6. The method of claim 1 , wherein the carbonation reaction is performed for five minutes to 20 minutes. 7. The method of claim 1 , wherein the carbonation reaction is completed at pH 7. 8. The method of claim 1 , wherein the filtering process is performed by a 0.2 μm membrane filter. 9. The method of claim 8 , wherein the 0.2 μm membrane filter includes cellulose acetate. 10. The method of claim 1 , further comprising crystallizing the filtered solution after precipitating the calcium carbonate. 11. The method of claim 1 , further comprising adjusting a pH of the ammonia solution, in which the flue gas desulfurization gypsum is dissolved, to at least 9.0 in the carbonation reaction.
Aggregated particles or particles with an intergrown morphology · CPC title
by d-values or two theta-values, e.g. as X-ray diagram · CPC title
cube-like · CPC title
Compositional purity · CPC title
Three-dimensional structures · CPC title
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