Carbon dioxide chemical sequestration from industrial emissions by carbonation
Techniques are described for chemical sequestration of carbon dioxide and production of precipitated magnesium carbonate. The process can include contacting carbon dioxide from industrial emissions with water and magnesium-containing particulate material, such as serpentinite, which is thermally pre-treated and has a particle size of at most 75 microns. The process can also include separation of the loaded aqueous stream from the solids, followed by precipitation of magnesium carbonate material that includes carbon and oxygen from industrial emissions and magnesium from serpentinite or chrysotile mining residue, for example.
1. A process for sequestering carbon dioxide and producing magnesium carbonate, the process comprising:
thermally pre-treating a magnesium-containing particulate material where 90% of the solid particles have a particle size equal to or less than about 75 μm, for dehydroxylation thereof, to produce a pre-treated magnesium-containing particulate material;
contacting the pre-treated magnesium-containing particulate material with water and a carbon dioxide containing gas, to form a loaded slurry and a carbon dioxide depleted gas;
separating the loaded slurry from the carbon dioxide depleted gas;
separating the loaded slurry into at least a loaded aqueous stream and a solids-enriched stream;
subjecting the loaded aqueous stream to precipitation to form a precipitation slurry comprising magnesium carbonate precipitates; and
subjecting the precipitation slurry to separation to produce a precipitated magnesium carbonate material and a precipitate depleted stream.
2. The process of claim 1 , wherein the loaded slurry has mass concentration between 25 g/L and 300 g/L in grams of total solids per liter of the loaded slurry.
3. The process of claim 1 , further comprising drying the precipitated magnesium carbonate material to form a dried product.
4. The process of claim 1 , further comprising recycling at least a portion of the precipitate depleted stream for contacting the pre-treated magnesium-containing particulate material and the carbon dioxide containing gas.
5. The process of claim 4 , further comprising recycling at least a portion of the solids-enriched stream back for contacting the carbon dioxide containing gas and the precipitate depleted stream.
6. The process of claim 1 , wherein the magnesium-containing particulate material further has a median particle size between about 10 μm and about 45 μm.
7. The process of claim 6 , further comprising crushing and/or grinding the magnesium-containing particulate material to obtain the particle size equal to or less than about 75 μm and the median particle size between about 10 μm and about 45 μm.
8. The process of claim 1 , wherein the carbon dioxide containing gas comprises industrial emissions and has a carbon dioxide concentration between 1% and 30%.
9. The process of claim 1 , wherein the step of contacting the pre-treated magnesium-containing particulate material with water and a carbon dioxide containing gas is performed in a carbonation unit at a carbonation temperature between about 10° C. and about 40° C. and at a carbonation pressure between about 1 bar and about 12 bars.
10. The process of claim 1 , wherein the loaded slurry is substantial free of precipitated magnesium carbonate particles.
11. The process of claim 10 , wherein the loaded slurry is substantial free of precipitated calcium carbonate particles.
12. The process of claim 11 , wherein the loaded slurry is substantial free of any precipitated alkaline earth metal carbonates.
13. The process of claim 1 , wherein the precipitating is performed at a precipitation temperature between about 20° C. and about 80° C. for a precipitation time between about 0.5 hours and about 12 hours.
14. The process of claim 1 , wherein the magnesium-containing particulate material comprises serpentinite.
15. The process of claim 1 , wherein the magnesium-containing particulate material comprises mining residue.
16. The process of claim 1 , further comprising grinding the solids-enriched stream to produce a pre-ground material and then recycling at least a portion of the pre-ground material back for contacting the carbon dioxide containing gas.
17. The process of claim 1 , wherein the precipitated magnesium carbonate material is at least 95 wt % in hydrated form.
18. The process of claim 1 , wherein the thermally pre-treating is performed in a thermal pre-treatment unit, the contacting and the separating of the loaded slurry from the carbon dioxide depleted gas re performed in a carbonation unit, the separating of the loaded slurry into at least a loaded aqueous stream and a solids-enriched stream is performed in a separation unit, and the precipitation is performed in a precipitation unit.
19. A process for sequestering carbon dioxide and producing magnesium carbonate, the process comprising:
contacting a dehydroxylated magnesium-containing particulate material with water and a carbon dioxide containing gas, to form a loaded slurry and a carbon dioxide depleted gas;
separating the loaded slurry from the carbon dioxide depleted gas;
separating the loaded slurry into at least a loaded aqueous stream and a solids-enriched stream;
subjecting the loaded aqueous stream to precipitation to form a precipitation slurry comprising magnesium carbonate precipitates; and
subjecting the precipitation slurry to separation to produce a precipitated magnesium carbonate material and a precipitate depleted stream.
20. The process of claim 19 , wherein the loaded slurry has mass concentration between 25 g/L and 300 g/L in grams of total solids per liter of the loaded slurry; 90% of the dehydroxylated magnesium-containing particulate material has a particle size equal to or less than about 75 μm; the carbon dioxide containing gas comprises industrial emissions and has a carbon dioxide concentration between 1% and 30%; the step of contacting the dehydroxylated magnesium-containing particulate material with water and a carbon dioxide containing gas is performed in a carbonation unit at a carbonation temperature between about 10° C. and about 40° C. and at a carbonation pressure between about 1 bar and about 12 bars; the loaded slurry is substantial free of precipitated magnesium carbonate particles; and the precipitating is performed at a precipitation temperature between about 20° C. and about 80° C. for a precipitation time between about 0.5 hours and about 12 hours.