Production of low carbon footprint magnesia

Patent metadata

Field	Value
Publication number	US-11401168-B2
Application number	US-201716320579-A
Country	US
Kind code	B2
Filing date	Jul 20, 2017
Priority date	Jul 27, 2016
Publication date	Aug 2, 2022
Grant date	Aug 2, 2022

Abstract

A process for producing magnesia can include contacting CO2-containing emissions with a magnesium-containing material to produce magnesium carbonate; subjecting the magnesium carbonate to calcination to produce a CO2 by-product and magnesia; and recycling at least a portion of the CO 2 by-product for contacting the magnesium-containing material to produce the magnesium carbonate. The magnesium-containing material can include mining residues, such as phyllosilicate or chrysotile mining residue, and the magnesium carbonate produced can include precipitated nesquehonite that is subjected to calcination to produce the magnesia.

First claim

The invention claimed is:

1. A process for producing magnesia, comprising:
contacting a CO 2 -containing gas with a natural magnesium-containing material to produce magnesium carbonate;
subjecting the magnesium carbonate to indirect-heated calcination to produce a CO 2 by-product and magnesia; and
directly recycling at least a portion of the CO 2 by-product for contacting the natural magnesium-containing material to produce the magnesium carbonate, the CO 2 by-product having a higher CO 2 concentration than the CO 2 -containing gas.

2. The process of claim 1 , wherein the step of contacting further comprises providing the natural magnesium-containing material in an aqueous slurry and contacting the CO 2 -containing gas and the portion of the CO 2 by-product with the aqueous slurry.

3. The process of claim 2 , comprising recovering precipitated magnesium carbonate from the aqueous slurry and subjecting the precipitated magnesium carbonate to the calcination step.

4. The process of claim 1 , further comprising:
in the contacting step, producing a carbonate loaded slurry comprising precipitable carbonates and substantially free of precipitated alkaline earth metal carbonates;
separating the carbonate loaded slurry into an aqueous phase comprising the precipitable carbonates and a solid phase;
precipitating the magnesium carbonate from the aqueous phase; and
separating the magnesium carbonate from the aqueous phase.

5. The process of claim 1 , wherein the CO 2 -containing gas comprises CO 2 -containing emissions that are directly used as they are produced from a plant.

6. The process of claim 1 , wherein the step of contacting the CO 2 -containing gas with the natural magnesium-containing material comprises:
subjecting the natural magnesium-containing material to dehydroxylation to reduce a water content of the natural magnesium-containing material and to produce a heat-activated material; and

contacting the heat-activated material with the CO 2 -containing gas.

7. The process of claim 6 , wherein CO 2 derived from the heat activation pre-treatment is supplied to the contacting step.

8. The process of claim 6 , wherein the dehydroxylation is performed at a temperature from approximately 600 to 700 degrees Celsius and for a duration of approximately 20 to 60 minutes.

9. The process of claim 1 , wherein the natural magnesium-containing material is contacted with a CO 2 feed stream that includes a plurality of CO 2 source streams.

10. The process of claim 9 , further comprising controlling the relative quantity of each CO 2 source stream in the CO 2 feed stream.

11. The process of claim 10 , wherein the controlling is performed according to pressure, temperature and/or composition of the CO 2 source streams.

12. The process of claim 9 , wherein the CO 2 feed stream further comprises CO 2 derived from an additional magnesia production train.

13. The process of claim 1 , wherein the natural magnesium-containing material comprises at least one of basalt, peridotite, serpentinized peridotite, ophiolitic rock, mafic rock, ultramafic rocks, peridot, pyroxene, olivine, serpentine, and/or brucite.

14. The process of claim 13 , wherein the natural magnesium-containing material is a magnesium-containing particulate material having a magnesium content between about 1 wt % and about 35 wt %.

15. The process of claim 1 , wherein the contacting step comprises contacting the CO 2 -containing gas with the natural magnesium-containing material in at least one carbonation unit at a carbonation temperature between about 10° C. and about 40° C. and a carbonation pressure between about 1 bar and about 20 bars, for carbonation thereof to produce magnesium carbonates and a CO 2 depleted gas.

16. The process of any one of claim 1 , further comprising:
subjecting the natural magnesium-containing material to size reduction prior to carbonation to provide a particle size of at most 75 microns.

17. The process of claim 16 , wherein subjecting the natural magnesium-containing material to size reduction comprises:
grinding a starting material to provide a particle size between about 200 microns and about 1000 microns to produce a sized material;
removing a magnetic fraction from the sized material to produce a non-magnetic fraction; and
grinding the non-magnetic fraction to produce the natural magnesium-containing material having the particle size of at most 75 microns.

18. The process of claim 1 , further comprising:
recovering a CO 2 -containing by-product stream from calcination; and
subjecting the CO 2 -containing by-product to water removal to produce a treated CO 2 by-product stream prior to contacting the treated CO 2 by-product stream as the portion of the CO 2 by-product with the natural magnesium-containing material.

19. The process of claim 18 , wherein a CO 2 content of the portion of the CO 2 by-product is greater than a CO 2 content of the CO 2 -containing gas.

20. The process of claim 1 , wherein the natural magnesium-containing material is serpentine.

Assignees

• Inst Nat Rech Scient

Inventors

• Mercier Guy
• Pasquier Louis-César
• Kemache Nassima
• Cecchi Emmanuelle
• Blais Jean-François

Classifications

• C01F5/02 Primary

  Magnesia · CPC title

• C01F5/24

  Magnesium carbonates · CPC title

• C01F5/06 Primary

  by thermal decomposition of magnesium compounds (calcining magnesite or dolomite C04B2/10) · CPC title

• C01B32/50

  Carbon dioxide · CPC title