Material for neutralising and/or hardening liquids, a method for producing same, and uses
US-2024293793-A1 · Sep 5, 2024 · US
US2022288555A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022288555-A1 |
| Application number | US-202017607966-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 4, 2020 |
| Priority date | May 2, 2019 |
| Publication date | Sep 15, 2022 |
| Grant date | — |
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Processes for making magnesium-containing layered double hydroxides from a magnesium phosphate-containing mineral are disclosed, as well as a magnesium-containing layered double hydroxides and their uses.
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1 . A process for the preparation of a magnesium-containing layered double hydroxide, the process comprising the step of: a) using a magnesium phosphate-containing mineral as a source of Mg 2+ ions in a process of preparing a layered double hydroxide. 2 . The process of claim 1 , wherein the magnesium phosphate-containing mineral is struvite or a magnesium phosphate-containing mineral derived from struvite (e.g. bobierrite). 3 . The process of claim 1 or 2 , wherein Mg 2+ ions are generated in step a) by contacting the magnesium phosphate-containing mineral with an aqueous solution (e.g. water). 4 . The process of claim 3 , wherein the temperature of the aqueous solution is 5-120° C., preferably 30-95° C. 5 . The process of claim 1 , wherein the magnesium phosphate-containing mineral is struvite or a magnesium phosphate-containing mineral derived from struvite, and the Mg 2+ ions are generated in step a) by contacting the magnesium phosphate-containing mineral with an aqueous solution for 30-75 minutes at a temperature of 55-90° C., and wherein the process of step a) is a coprecipitation process. 6 . The process of any preceding claim, wherein step a) comprises mixing the Mg 2+ ions with: M′, wherein M′ is one or more trivalent or tetravalent cations, X, wherein X one or more anions, and optionally M, wherein M is a monovalent or divalent cation other than Mg 2+ , in an aqueous reaction medium (e.g. water) at a pH sufficient to form a layered double hydroxide. 7 . The process of claim 6 , wherein the pH of the aqueous reaction medium is 9.5-13.0. 8 . The process of claim 6 or 7 , wherein the temperature of the aqueous reaction medium is 5-80° C. 9 . The process of any one of claims 6 to 8 , wherein the formed layered double hydroxide is aged in the aqueous reaction medium for 1-200 hours. 10 . The process of any one of claims 6 to 9 , wherein the temperature of the aqueous reaction medium is 65-85° C. and the formed layered double hydroxide is aged in the aqueous reaction medium for 1-24 hours (such as 2-8 hours). 11 . The process of any one of claims 6 to 10 , wherein M′ is selected from Al 3+ , Ga 3+ , Y 3+ , In 3+ , Fe 3+ , Co 3+ , Ni 3+ , Mn 3+ , Cr 3+ , Ti 3+ , V 3+ , La 3+ , Sn 4+ , Ti 4+ and Zr 4+ . 12 . The process of any one of claims 6 to 11 , wherein M is selected from Li + , Ca 2+ , Zn 2+ , Fe 2+ , Ni 2+ , Co 2+ , Mn 2+ and Cu 2+ . 13 . The process of any one of claims 6 to 12 , wherein M′ is Al 3+ and M is absent or is Zn 2+ . 14 . The process of any one of claims 6 to 13 , wherein X is selected from a halide, an inorganic oxyanion, an anionic surfactant, an anionic chromophore and an anionic UV absorber. 15 . The process of any one of claims 6 to 14 , wherein X is one or more of carbonate, phosphate, sulfate and nitrate. 16 . The process of any one of claims 6 to 15 , wherein X is one or more of carbonate and phosphate. 17 . The process of any one of claims 6 to 15 , wherein X is carbonate. 18 . The process of any preceding claim, wherein the layered double hydroxide is a phosphate-containing layered double hydroxide and step a) further comprises using the magnesium phosphate-containing mineral as a source of phosphate ions in the process of preparing the layered double hydroxide. 19 . A magnesium-containing layered double hydroxide obtainable by the process of any preceding claim. 20 . A magnesium-containing-layered double hydroxide having a specific surface area of 80 m 2 g -1 and a tap density of at least 0.25 g cm −3 . 21 . The magnesium-containing layered double hydroxide as claimed in claim 19 or 20 , wherein the layered double hydroxide has a specific surface area of ≥100 m 2 g −1 . 22 . The magnesium-containing layered double hydroxide as claimed in claim 19 , 20 or 21 , wherein the layered double hydroxide has a tap density of at least 0.30 g cm −3 . 23 . The magnesium-containing layered double hydroxide as claimed in any one of claims 19 to 22 , wherein the layered double hydroxide is a MgAl layered double hydroxide or a MgZnAl layered double hydroxide, optionally wherein carbonate accounts for >75 wt % of all interlayer anions present in the layered double hydroxide. 24 . The magnesium-containing layered double hydroxide as claimed in any one of claims 19 to 23 , wherein the layered double hydroxide is a magnesium aluminium carbonate layered double hydroxide. 25 . Use of the magnesium-containing layered double hydroxide as claimed in any one of claims 19 to 23 as a sorbent, a catalytic support or as a filler in a composite material. 26 . A thermally-treated (e.g. calcined) magnesium-containing layered double hydroxide as claimed in claims 19 to 23 .
Layered double hydroxide, e.g. comprising nitrate, sulfate or carbonate ions as intercalating anions · CPC title
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by d-values or two theta-values, e.g. as X-ray diagram · CPC title
Chemical treatments not covered by groups B01J20/3007 - B01J20/3078 · CPC title
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