US2011253630A1PendingUtilityA1
Membranes with functionalized carbon nanotube pores for selective transport
Est. expiryMay 29, 2028(~1.9 yrs left)· nominal 20-yr term from priority
Y02A20/131A61M 2205/3306B01D 53/228B01D 2256/10B01D 2325/18C02F 2305/08B01D 69/148B01D 61/025C02F 1/442B01D 2323/36B01D 67/0072B01D 61/027B01D 2256/24C02F 2103/08B01D 2256/22B01D 2257/504B82Y 30/00B01D 71/027C02F 1/44B01D 2257/102A61M 1/341A61M 1/34B01D 67/00793B01D 71/0215B01D 71/0212B01D 71/024Y02C20/40
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Claims
Abstract
Provided herein composition and methods for nanoporous membranes comprising single walled, double walled, or multi-walled carbon nanotubes embedded in a matrix material. Average pore size of the carbon nanotube can be 6 nm or less. These membranes are a robust platform for the study of confined molecular transport, with applications in liquid and gas separations and chemical sensing including desalination, dialysis, and fabric formation.
Claims
exact text as granted — not AI-modified1 . A process for the preparation of a membrane of selective permeability, said process comprising:
(a) wetting with a first liquid phase a microporous support that is wettable by said first liquid phase, said first liquid phase having dissolved therein a first polymerizable species; (b) contacting said microporous support thus wetted with a second liquid phase that is at least partially immiscible with said first liquid phase and in which is dissolved a second polymerizable species, one or both of said first and second liquid phases having carbon nanotubes randomly dispersed therein of an average length; (c) causing said first and second polymerizable species to form a layer of a solid polymer over an outer surface of said microporous support; (d) sealing said layer to form a substantially continuous barrier around said nanotubes, said barrier having a thickness that is less than said average length of said nanotubes; and (e) recovering from said first and second liquid phases said microporous support with said layer adhering to said outer surface.
2 . The process of claim 1 , wherein said first and second polymerizable species are mutually reactive by interfacial polymerization to form said solid polymer that is insoluble in said first and second liquid phases and that adheres to said microporous support.
3 . The process of claim 1 , wherein steps (c) and (d) are performed in sequence, said layer of step (c) is defined as an intermediate layer and is a porous layer, and step (d) comprises forming an outer layer over said intermediate layer, said outer layer forming said barrier, and said outer layer having a thickness that is less than said average length of said nanotubes.
4 . The process of claim 1 , wherein said carbon nanotubes are single-walled carbon nanotubes.
5 . The process of claim 1 , wherein a ratio of said average length of said carbon nanotubes to said thickness of said layer is from about 1.3 to about 5.
6 . The process of claim 1 , wherein said average length of said carbon nanotubes is from about 100 nm to about 2000 nm.
7 . The process of claim 1 , wherein said carbon nanotubes have an inner diameter of about 0.4 nm to about 5 nm.
8 . The process of claim 1 , wherein said microporous support is a member selected from the group consisting of polyethersulfone, polysulfone, nylon, and polyester, and said first liquid phase is a polar phase.
9 . The process of claim 8 , wherein the second and optionally the third liquid phases are non-polar liquids.
10 . The process of claim 1 , wherein said first liquid phase is a solution of said first polymerizable species in a polar solvent selected from the group consisting of water, an alcohol, and a glycol, and said second liquid phase is a solution of said second polymerizable species in a non-polar solvent selected from the group consisting of benzene, a halobenzene, an alkyl benzene, a C 5 -C 12 alkane, a halo-substituted C 5 -C 12 alkane, and an alkyl-substituted C 5 -C 12 alkane.
11 . The process of claim 1 , wherein said first polymerizable species is an aromatic polyamine and said second polymerizable species is an aromatic polycarboxylic acid halide.
12 . The process of claim 1 , wherein said first polymerizable species is m-phenylenediamine and said second polymerizable species is trimesoyl chloride.
13 . A process for the preparation of a membrane of selective permeability, said process comprising:
(a) wetting with an aqueous phase a microporous support selected from polysulfone or polyethersulfone that is wettable by said aqueous phase, said aqueous phase having dissolved therein m-phenylenediamine; (b) contacting said microporous support thus wetted with a solvent phase that is at least partially immiscible with said aqueous phase and in which is dissolved trimesoyl chloride, one or both of said aqueous and solvent phases having carbon nanotubes randomly dispersed therein of an average length; (c) causing said m-phenylenediamine and trimesoyl chloride to form a layer of a solid polymer over an outer surface of said microporous support; (d) sealing said layer to form a substantially continuous barrier around said nanotubes, said barrier having a thickness that is less than said average length of said nanotubes; and (e) recovering from said aqueous and solvent phases said microporous support with said layer adhering to said outer surface.
14 . A membrane of carbon nanotubes formed by the process of claim 1 .
15 . A membrane with embedded carbon nanotubes, said membrane comprising a plurality of carbon nanotubes open at both ends and embedded in a solid, substantially continuous polymeric matrix, said polymeric matrix having a thickness that is less than an average of the lengths of said carbon nanotubes, said carbon nanotubes having substantially random orientations relative to said membrane and yet oriented such that at least a portion of said plurality of carbon nanotubes have both open ends protruding from said membrane to provide fluid communication through said membrane.
16 . The membrane of claim 14 , further comprising a layer of microporous material supporting said polymeric matrix.
17 . The membrane of claim 14 , wherein a ratio of said average of the lengths of said carbon nanotubes to said thickness of said polymeric matrix is from about 1.3 to about 5.
18 . A method for desalination of water, said method comprising passing said water through a membrane comprising a plurality of nanotubes open at both ends and embedded in a solid, substantially continuous polymeric matrix, said polymeric matrix having a thickness that is less than an average of the lengths of said nanotubes, said nanotubes having substantially random orientations relative to said membrane and yet oriented such that at least a portion of said plurality of nanotubes have both open ends protruding from said membrane to provide fluid communication through said membrane.
19 . The method of claim 18 , wherein said membrane further comprises a layer of microporous material supporting said polymeric matrix.
20 . The method of claim 18 , wherein the ratio of said average of the lengths of said nanotubes to said thickness of said polymeric matrix is from about 1.3 to about 5.
21 . The method of claim 18 , wherein said polymeric matrix has a substantially planar exposed outer surface and contains from about 2.5×10 8 to about 1×10 12 nanotubes per square centimeter of said exposed outer surface.Join the waitlist — get patent alerts
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