Compositions and Methods for the Capture of Carbon Dioxide and/or the Generation of Silica

Patent metadata

Field	Value
Publication number	US-2025256971-A1
Application number	US-202519052136-A
Country	US
Kind code	A1
Filing date	Feb 12, 2025
Priority date	Feb 12, 2024
Publication date	Aug 14, 2025
Grant date	—

Abstract

Described herein are methods of using silicate materials, including silicate materials obtained from nature, synthesized, and/or obtained from industrial waste streams, to capture and store carbon dioxide. In some embodiments, the methods can also be used to form silica (e.g., high purity silica). In some embodiments, the methods can also be used to produce hydrogen.

First claim

What is claimed is:

1 . A process comprising:
(a) reacting a silicate precursor with an aqueous carbonate or bicarbonate solution having an alkaline pH under conditions effective to generate a stable carbonate precipitate and soluble silicate product; (b) reacting the soluble silicate product with carbon dioxide under conditions effective to form a soluble carbonate or bicarbonate and silicic acid; and (c) thermally decomposing the silicic acid to produce silica and water.

2 . The process of claim 1 , wherein the alkaline pH comprises a pH of 8 or more, such as a pH of from 8 to 14, a pH of from 9 to 14, a pH of from 8 to 13, a pH of from 9 to 13, a pH of from 8 to 12, or a pH of from 9 to 12.

3 . The process of claim 1 , wherein the stable carbonate precipitate comprises calcium carbonate, magnesium carbonate, iron carbonate, or a combination thereof.

4 . The process of claim 3 , wherein the stable carbonate precipitate comprises calcium carbonate, magnesium carbonate, or a combination thereof.

5 . The process of claim 1 , wherein the stable carbonate precipitate further comprises a transition metal ion present within the silicate precursor.

6 . The process of claim 1 , wherein the silicate precursor is selected from the group consisting of a nesosilicate, a sorosilicate, an inosilicate (a single chain inosilicate or a double chain inosilicate), a cyclosilicate, a phyllosilicate, or a tectosilicate.

7 . The process of claim 1 , wherein the silicate precursor comprises a calcium silicate.

8 . The process of claim 7 , wherein the calcium silicate comprises wollastonite or pseudo-wollastonite.

9 . The process of claim 1 , wherein an aqueous carbonate or bicarbonate solution comprises aqueous sodium bicarbonate.

10 . The process of claim 1 , wherein the soluble silicate product comprises a sodium silicate, such as sodium metasilicate (Na 2 SiO 3 ).

11 . The process of claim 1 , wherein step (a) is performed at an elevated temperature and/or pressure, such as a temperature of from greater than room temperature (20° C.) (e.g., a temperature of from greater than 20° C. to 400° C.).

12 . The process of claim 11 , wherein step (a) is performed at a temperature of at least 100° C., such as a temperature of from 100° C. to 400° C., a temperature of from 100° C. to 300° C., a temperature of from 150° C. to 400° C., or a temperature of from 150° C. to 300° C.

13 . The process of claim 1 , wherein step (b) is performed at an elevated temperature and/or pressure, such as a temperature of from greater than room temperature (20° C.) (e.g., a temperature of from greater than 20° C. to 400° C.).

14 . The process of claim 13 , wherein step (b) is performed at a temperature of at least 50° C., such as a temperature of from 50° C. to 400° C., a temperature of from 50° C. to 300° C., a temperature of from 50° C. to 200° C., or a temperature of from 50° C. to 100° C.

15 . The process of claim 1 , wherein step (c) comprises heating the silicic acid to a temperature of at least 50° C., such as a temperature of at least 80° C., or a temperature of at least 100° C.

16 . The process of claim 15 , wherein step (c) comprises heating the silicic acid to a temperature of from 50° C. to 200° C., such as a temperature of from 50° C. to 150° C., a temperature of from 50° C. to 100° C., a temperature of from 50° C. to 150° C., a temperature of from 50° C. to 100° C., a temperature of from 100° C. to 200° C., a temperature of from 100° C. to 170° C., or a temperature of from 100° C. to 150° C.

17 . The process of claim 1 , further comprising reacting a silicate feedstock material with water vapor under conditions effective to generate hydrogen gas and the silicate precursor.

18 . The process of claim 17 , wherein the silicate feedstock material comprises a silicate that comprises a reduced metal cation or metal (e.g., a transition metal or reduced transition metal cation such as Fe metal or an Fe 2+ ion).

19 . The process of claim 17 , wherein the silicate feedstock material comprises an industrial waste product, such as steel slag or fly ash.

20 . The process of claim 17 , wherein the reaction of the silicate feedstock material with water vapor is performed at an elevated temperature and/or pressure, such as a temperature of from 600° C. to 900° C.

Assignees

• Ohio State Innovation Foundation

Inventors

• Zhai Shang
• Fan Liang-Shih
• Shank Kyle
• Cole David

Classifications

• C01B32/60

  Preparation of carbonates or bicarbonates in general (of percarbonates C01B15/10; of specific carbonates or bicarbonates according to the cation C01B-C01G) · CPC title

• C01F11/18

  Carbonates · CPC title

• C01F5/24

  Magnesium carbonates · CPC title

• C01B33/126 Primary

  Preparation of silica of undetermined type · CPC title

• C01B3/061 Primary

  by reaction of water with metal oxides · CPC title