Method for improving quality of titanium-containing feedstock
US-2015368753-A1 · Dec 24, 2015 · US
US2023331578A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023331578-A1 |
| Application number | US-202018026828-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 17, 2020 |
| Priority date | Sep 17, 2020 |
| Publication date | Oct 19, 2023 |
| Grant date | — |
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A preparation method of a porous oxide is provided, which includes: preparing the porous oxide with a polyester polyol as a raw material. The porous oxide prepared by the preparation method in the present application has characteristics such as uniform and adjustable pore sizes and controllable distribution of mesopores, micropores, and macropores.
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What is claimed is: 1 . A preparation method of a porous oxide, comprising: preparing the porous oxide with a polyester polyol as a raw material. 2 . The preparation method according to claim 1 , comprising: in an atmosphere comprising a gas A, roasting the raw material comprising the polyester polyol to obtain the porous oxide, wherein the gas A is at least one selected from the group consisting of an air, a nitrogen, an inert gas, and an oxygen. 3 . The preparation method according to claim 2 , wherein the roasting is conducted at 350° C. to 900° C. for 1.5 h to 25 h. 4 . The preparation method according to claim 1 , comprising: subjecting a raw material comprising an oxygen-containing acid ester and a polyol to a transesterification reaction to obtain the polyester polyol. 5 . The preparation method according to claim 4 , wherein the oxygen-containing acid ester is at least one selected from the group consisting of a compound with a chemical formula shown in formula I and a compound with a chemical formula shown in formula II: M(OR 1 ) n 1 formula I O═P(OR 2 ) n 2 formula II wherein M is a metallic element or a non-metallic element excluding P; R 1 and R 2 each are independently at least one selected from the group consisting of C 1 -C 8 alkyl groups; and n 1 is 2 to 8 and n 2 is 2 to 8. 6 . The preparation method according to claim 5 , wherein M is at least one selected from the group consisting of B, Si, Ge, Al, Ti, Fe, Sn, V, Ga, Zr, Cr, Sb, and W. 7 . The preparation method according to claim 4 , wherein there are no less than two hydroxyl groups in the polyol. 8 . The preparation method according to claim 4 , wherein the polyol comprises at least one selected from the group consisting of ethylene glycol (EG), diethylene glycol (DEG), triethylene glycol (TEG), tetraethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 1,6-hexanediol, polyethylene glycol (PEG) 200, PEG 400, PEG 600, PEG 800, 1,4-cyclohexanediol, 1,4-cyclohexanedimethanol (1,4-CHDM), 1,4-benzenedimethanol, glycerol, trimethylolpropane, pentaerythritol, xylitol, and sorbitol. 9 . The preparation method according to claim 4 , wherein the transesterification reaction is conducted for 2 h to 10 h at 80° C. to 180° C. under a stirring in an inert atmosphere. 10 . A porous oxide, wherein the porous oxide is prepared by the preparation method according to claim 1 . 11 . The porous oxide according to claim 10 , wherein the porous oxide has a pore size of 0.4 nm to 80 nm and a specific surface area (SSA) of 150 m 2 /g to 1,500 m 2 /g. 12 . The porous oxide according to claim 10 , wherein the porous oxide comprises a micropore with a pore size of 0.4 nm to 2.0 nm. 13 . The porous oxide according to claim 10 , wherein the porous oxide comprises a mesopore with a pore size of 2.0 nm to 50 nm. 14 . The porous oxide according to claim 10 , wherein the porous oxide comprises a macropore with a pore size of 50 nm to 80 nm. 15 . The porous oxide according to claim 10 , wherein the preparation method of the porous oxide comprises: in an atmosphere comprising a gas A, roasting the raw material comprising the polyester polyol to obtain the porous oxide, wherein the gas A is at least one selected from the group consisting of an air, a nitrogen, an inert gas, and an oxygen. 16 . The porous oxide according to claim 15 , wherein the roasting in the preparation method of the porous oxide is conducted at 350° C. to 900° C. for 1.5 h to 25 h. 17 . The porous oxide according to claim 10 , wherein the preparation method of the porous oxide comprises: subjecting a raw material comprising an oxygen-containing acid ester and a polyol to a transesterification reaction to obtain the polyester polyol. 18 . The porous oxide according to claim 17 , wherein the oxygen-containing acid ester is at least one selected from the group consisting of a compound with a chemical formula shown in formula I and a compound with a chemical formula shown in formula II: M(OR 1 ) n 1 formula I O═P(OR 2 ) n 2 formula II wherein M is a metallic element or a non-metallic element excluding P; R 1 and R 2 each are independently at least one selected from the group consisting of C 1 -C 8 alkyl groups; and n 1 is 2 to 8 and n 2 is 2 to 8. 19 . The preparation method according to claim 18 , wherein M is at least one selected from the group consisting of B, Si, Ge, Al, Ti, Fe, Sn, V, Ga, Zr, Cr, Sb, and W. 20 . The preparation method according to claim 17 , wherein there are no less than two hydroxyl groups in the polyol.
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Methods for preparing oxides or hydroxides in general (particular individual oxides or hydroxides, see the relevant groups of subclasses C01B - C01G or C25B, according to the element combined with the oxygen or hydroxy group) · CPC title
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