Monolayer, composite, gas separation material, filter, gas separation device and method for manufacturing composite
US-12128366-B2 · Oct 29, 2024 · US
US12465895B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12465895-B2 |
| Application number | US-202519243771-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 20, 2025 |
| Priority date | Dec 19, 2022 |
| Publication date | Nov 11, 2025 |
| Grant date | Nov 11, 2025 |
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A membrane including a polysulfone/polyethylene terephthalate (PSf/PET) support and an active layer on an outer surface of the PSf/PET support. The active layer comprises reacted units of a diacyl chloride compound, a tetra-amine compound, and a nanocomposite including graphitic carbon nitride and polypyrrole. The membrane of the present disclosure is self-cleaning following exposure to radiation and finds application in water decontamination and de-salination.
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The invention claimed is: 1 . A porous water decontamination membrane, comprising: a polysulfone/polyethylene terephthalate (PSf/PET) support; and a crosslinked polyamide active layer on an outer surface of the PSf/PET support, wherein the crosslinked polyamide active layer comprises reacted units of: a diacyl chloride compound; a tetra-amine compound; and a homogeneous nanocomposite comprising graphitic carbon nitride nanosheets and polypyrrole; wherein the graphitic carbon nitride nanosheets are bonded to at least one terminal end of the polypyrrole in the nanocomposite. 2 . The membrane of claim 1 , wherein the graphitic carbon nitride nanosheets has triazine and hepta zine rings. 3 . The membrane of claim 1 , wherein the graphitic carbon nitride nanosheets have a thickness of 10-100 nm. 4 . The membrane of claim 1 , wherein the diacyl chloride compound is an aromatic ring substituted with two acyl chloride groups. 5 . The membrane of claim 1 , wherein the tetra-amine compound is a linear or branched aliphatic amine with of 2-50 carbons and four amine groups. 6 . The membrane of claim 1 , wherein the membrane has 0.01 to 5 wt % of the nanocomposite based on the total weight of the crosslinked polyamide active layer. 7 . The membrane of claim 1 , wherein particles of the crosslinked polyamide active layer have a globular shape. 8 . The membrane of claim 1 , wherein particles of the crosslinked polyamide active layer are not agglomerated. 9 . The membrane of claim 1 , wherein particles of the crosslinked polyamide active layer have an average size of 50-200 nm. 10 . The membrane of claim 1 , having 50-70 at. % carbon, 25-35 at. % sulfur, 5-15 at. % oxygen, and 1-10 at. % nitrogen, based on a total number of atoms in the membrane. 11 . The membrane of claim 1 , having a surface roughness of less than 24 nm. 12 . The membrane of claim 1 , having a water contact angle of less than 90°. 13 . The membrane of claim 1 , wherein the crosslinked polyamide active layer covers at least 95% of the outer surface of the polysulfone/polyethylene terephthalate (PSf/PET) support. 14 . The membrane of claim 1 , wherein the membrane is porous, having pores with an average diameter of less than 1 nm. 15 . The membrane of claim 1 , having a permeate flux of 40 to 100 L m −2 h −1 at 10-30 bar. 16 . The membrane of claim 1 , wherein the membrane rejects at least 60% of inorganic salts. 17 . The membrane of claim 1 , wherein the membrane is self-cleaning following exposure to radiation. 18 . The membrane of claim 17 , wherein the radiation is from 400-700 nm.
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