Periodic mesoporous organosilica-doped nanocomposite membranes and systems including same
US-11260352-B2 · Mar 1, 2022 · US
US12458932B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12458932-B2 |
| Application number | US-202318315663-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 11, 2023 |
| Priority date | May 11, 2023 |
| Publication date | Nov 4, 2025 |
| Grant date | Nov 4, 2025 |
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A filtration membrane including a first layer having a triamine-functionalized copper oxide polysilicate mesoporous material, a second layer including a polysulfone, and a third layer including a polyester terephthalate. The triamine-functionalized copper oxide polysilicate mesoporous material includes a copper oxide polysilicate backbone and a silicon atom of a silicon-containing triamine bonded to a silicate group in the copper oxide polysilicate backbone. The copper oxide polysilicate backbone is datively bonded to one or more tetramines, and the silicon-containing triamine and one or more tetramines are covalently cross-linked with terephthaloyl chloride to form a polyamide.
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The invention claimed is: 1 . A filtration membrane, comprising: a first layer comprising a triamine-functionalized copper oxide polysilicate mesoporous material, wherein the triamine-functionalized copper oxide polysilicate mesoporous material comprises a copper oxide polysilicate backbone and a silicon atom of a silicon-containing triamine bonded to a silicate group in the copper oxide polysilicate backbone, wherein the copper oxide polysilicate backbone is datively bonded to one or more tetramines, wherein the silicon-containing triamine and the one or more tetramines are covalently cross-linked with terephthaloyl chloride to form a polyamide, a second layer comprising a polysulfone; and a third layer comprising a polyester terephthalate. 2 . The filtration membrane of claim 1 , wherein the silicon atom of the silicon-containing triamine is covalently bonded to a silicate group of the copper oxide polysilicate backbone. 3 . The filtration membrane of claim 1 , wherein an amino terminus of the tetramine is coordinated to one or more copper atoms in the copper oxide polysilicate backbone. 4 . The filtration membrane of claim 1 , wherein the silicon-containing triamine and the one or more tetramines are covalently cross-linked with the terephthaloyl chloride through at least one of a primary amine of the silicon-containing triamine and a secondary amine of the silicon-containing triamine, and at least one of a primary amine of the tetramine and a secondary amine of the tetramine. 5 . The filtration membrane of claim 1 , wherein the one or more of the tetramines are covalently cross-linked with the terephthaloyl chloride through one or more primary amine of the tetramine and one or more secondary amine of the tetramine. 6 . The filtration membrane of claim 1 , wherein the silicon-containing triamine is N 1 -(3-trimethoxysilylpropyl) diethylenetriamine. 7 . The filtration membrane of claim 1 , wherein the tetramine is N,N′-bis(3-aminopropyl) ethylenediamine. 8 . The filtration membrane of claim 1 , wherein the membrane comprises the triamine-functionalized copper oxide polysilicate mesoporous material in an amount of 0.01% by weight to 0.2% by weight. 9 . The filtration membrane of claim 1 , wherein the copper oxide polysilicate mesoporous material has a hierarchical structure of MCM-41. 10 . The filtration membrane of claim 1 , wherein the silicon-containing triamine and the one or more tetramines are covalently cross-linked with the terephthaloyl chloride with interfacial polymerization. 11 . The filtration membrane of claim 1 , wherein the polysulfone and polyester terephthalate are prepared by phase inversion. 12 . The filtration membrane of claim 1 , wherein carbon, nitrogen, oxygen, copper, and silicon are uniformly distributed in the first layer. 13 . The filtration membrane of claim 1 , wherein the membrane has an average surface roughness from 7 nm to 17 nm. 14 . The filtration membrane of claim 1 , wherein the membrane has a water contact angle from 80° to 60°. 15 . The filtration membrane of claim 1 , wherein the membrane has a rate of flux from 15 L m −2 h −1 to 85 L m −2 h −1 at a pressure of 25 bar. 16 . A nanofiltration method, comprising: contacting an aqueous composition with the filtration membrane of claim 1 , wherein the aqueous composition comprises at least water, one or more salts, and one or more pharmaceuticals, collecting a permeate passing through the filtration membrane to obtain a purified composition having a reduced amount of the salts and the pharmaceuticals. 17 . The filtration membrane of claim 1 , wherein the membrane has a rejection profile of salts from 55% by weight to 99% by weight. 18 . The filtration membrane of claim 17 , wherein the salts are MgCl 2 , MgSO 4 , CaCl 2 , Na 2 SO 4 , and NaCl. 19 . The filtration membrane of claim 1 , wherein the membrane has a rejection profile of pharmaceuticals from 60% by weight to 80% by weight. 20 . The filtration membrane of claim 19 , wherein the pharmaceuticals are caffeine, sulfamethoxazole, amitriptyline, and loperamide.
by interfacial polymerisation · CPC title
Sulfur oxides · CPC title
Organic compounds not provided for in groups B01D2257/00 - B01D2257/602 · CPC title
Polyarylates · CPC title
Inorganic halogen compounds · CPC title
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