Methods to Rapidly Deposit Thin Films (or Coatings) of Microporous Material on Supports Using Thermally Induced Self-Assembly
US-2015246318-A1 · Sep 3, 2015 · US
US2016296883A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016296883-A1 |
| Application number | US-201415100513-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 26, 2014 |
| Priority date | Nov 29, 2013 |
| Publication date | Oct 13, 2016 |
| Grant date | — |
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Metal organic framework membranes can be used in gas separation applications.
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1 . A thin film membrane comprising a zeolite-like metal-organic framework, wherein the thin film membrane has a selectivity for CO 2 over H 2 . 2 . The thin film membrane of claim 1 , wherein the thin film membrane is anionic. 3 . The thin film membrane of claim 1 , wherein the thin film membrane has a zeolite-like topology. 4 . The thin film membrane of claim 1 , wherein the thin film membrane is on a support. 5 . The thin film membrane of claim 4 , wherein the support is a porous ceramic substrate. 6 . (canceled) 7 . The thin film membrane of claim 1 , wherein the permeance of the thin film membrane is higher for CO 2 than for CH 4 . 8 - 10 . (canceled) 11 . The thin film membrane of claim 1 , wherein the permeance of the thin film membrane is higher for CO 2 than for N 2 . 12 . (canceled) 13 . The thin film membrane of claim 1 , wherein the permeance of the thin film membrane is higher for CO 2 than for O 2 . 14 . (canceled) 15 . The thin film membrane of claim 1 , wherein the thickness of the thin-film membrane is between 20 and 100 μm. 16 . (canceled) 17 . The thin film membrane of claim 1 , wherein the zeolite-like metal-organic framework includes a linker and a metal. 18 . The thin film membrane of claim 17 , wherein the metal includes a transition metal, group 13 metal or a lanthanide metal. 19 . The thin film membrane of claim 17 , wherein the linker includes a heteroaromatic group. 20 . A method for preparing a zeolite-like metal-organic framework membrane comprising contacting a substrate with a solution mixture of carboxylic acid, an imidazole or a pyrimidine, a metal salt, and a nitric acid to form a zeolite-like metal-organic framework membrane. 21 . The method of claim 20 , wherein the zeolite-like metal-organic framework membrane is anionic. 22 . The method of claim 20 , wherein the zeolite-like metal-organic framework membrane has a sodalite topology. 23 . (canceled) 24 . The method of claim 20 , further comprising activating the substrate. 25 . The method of claim 20 , further comprising heating the reagent while contacting with the substrate. 26 . The method of claim 20 , further comprising contacting the substrate with acetonitrile after contacting with the reagent. 27 . The method of claim 20 , further comprising modifying the zeolite-like metal-organic framework membrane through cation exchange with an alkali metal ion or alkaline earth metal ion. 28 - 29 . (canceled) 30 . A method of separating gases comprising passing a mixture of gases through a thin film membrane comprising a zeolite-like metal-organic framework, wherein the thin film membrane has a selectivity for CO 2 over H 2 . 31 - 45 . (canceled)
characterised by specific membranes · CPC title
by controlled crystallisation, e,.g. hydrothermal growth · CPC title
Membrane materials having negatively charged functional groups · CPC title
Molecular sieves (carbon B01D71/021) · CPC title
characterised by their properties · CPC title
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