Inorganic dual-layer microporous supported membranes
Abstract
The present invention provides for a dual-layer inorganic microporous membrane capable of molecular sieving, and methods for production of the membranes. The inorganic microporous supported membrane includes a porous substrate which supports a first inorganic porous membrane having an average pore size of less than about 25 Å and a second inorganic porous membrane coating the first inorganic membrane having an average pore size of less than about 6 Å. The dual-layered membrane is produced by contacting the porous substrate with a surfactant-template polymeric sol, resulting in a surfactant sol coated membrane support. The surfactant sol coated membrane support is dried, producing a surfactant-templated polymer-coated substrate which is calcined to produce an intermediate layer surfactant-templated membrane. The intermediate layer surfactant-templated membrane is then contacted with a second polymeric sol producing a polymeric sol coated substrate which is dried producing an inorganic polymeric coated substrate. The inorganic polymeric coated substrate is then calcined producing an inorganic dual-layered microporous supported membrane in accordance with the present invention.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . An inorganic microporous supported membrane, comprising:
a macroporous support; a templated porous intermediate layer coating the support; and a microporous layer coating the templated porous intermediate layer such that the microporous layer is capable of molecular sieving.
2 . The inorganic microporous supported membrane as claimed in claim 1 , wherein:
the templated porous intermediate layer is an inorganic surfactant-templated silica layer; and the microporous layer is an inorganic silica layer.
3 . The inorganic microporous supported membrane as claimed in claim 2 , wherein:
the surfactant-templated porous intermediate layer having an average pore size of less than about 20 Å; and the microporous layer having an average pore size of less than about 5 Å.
4 . The inorganic microporous supported membrane as claimed in claim 1 , wherein:
the templated porous intermediate layer including an amphiphilic block copolymer.
5 . An inorganic microporous supported membrane, comprising:
a porous substrate; a first inorganic porous membrane coating the substrate having an average pore size of less than about 25 Å; and a second inorganic porous membrane coating the first inorganic membrane having an average pore size of less than about 6 Å.
6 . The inorganic microporous supported membrane as claimed in claim 5 , wherein:
the first inorganic porous membrane has a pore diameter in a range of about 10 to 20 Å.
7 . The inorganic microporous supported membrane as claimed in claim 6 , wherein:
the first inorganic porous membrane includes a surfactant-templated material.
8 . The inorganic microporous supported membrane as claimed in claim 7 , wherein:
the surfactant-templated material is prepared from silica polymers and a surfactant powder.
9 . The inorganic microporous supported membrane as claimed in claim 5 , wherein:
the second inorganic porous membrane is an inorganic silica membrane.
10 . The inorganic microporous supported membrane as claimed in claim 5 , wherein:
the first inorganic porous membrane has a thickness of less than about 100 Å.
11 . The inorganic microporous supported membrane as claimed in claim 5 , wherein:
the second inorganic porous membrane has an average pore size of between 2 and 5 Å.
12 . The inorganic microporous supported membrane as claimed in claim 5 , wherein:
the second inorganic porous membrane has an average pore size of between 3 and 4 Å.
13 . The inorganic microporous supported membrane as claimed in claim 5 , wherein:
the second inorganic porous membrane has a thickness less than about 100 nm.
14 . The inorganic microporous supported membrane as claimed in claim 5 , wherein the porous substrate is an alumina substrate.
15 . The inorganic microporous supported membrane as claimed in claim 6 , wherein:
the porous substrate has an average pore diameter ranging between 30 to 60 Å.
16 . A method for producing an inorganic dual-layered microporous supported membrane capable of molecular sieving, the method comprising:
contacting a porous substrate with a surfactant-template polymeric sol resulting in a surfactant sol coated membrane support; drying the surfactant sol coated membrane support producing a surfactant-templated polymeric coated substrate; calcining the surfactant-templated polymeric coated substrate to produce an intermediate layer surfactant membrane; contacting the intermediate layer surfactant templated membrane with a second polymeric sol producing a polymeric sol coated substrate; and drying the polymeric sol coated substrate producing an inorganic polymeric coated substrate; calcining the inorganic polymeric coated substrate producing the inorganic dual-layered microporous supported membrane.
17 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the step of calcining the inorganic polymeric coated substrate includes:
calcining the inorganic polymeric coated substrate at a first temperature producing a dual-layered supported membrane;
further calcining the dual-layered supported membrane at a second temperature to produce the inorganic dual-layered microporous supported membrane.
18 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 17 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining under a vacuum.
19 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 18 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining under a vacuum of less than about 6 pounds per square inch absolute (psia).
20 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 18 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining under a vacuum of less than about 4 psia.
21 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 17 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining at a temperature ranging from 200 to 400° C.
22 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 21 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining at a temperature ranging from 250 to 350° C.
23 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 17 , wherein:
the step of calcining the dual-layered inorganic supported membrane includes calcining at a temperature ranging from 300 to 600° C.
24 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 23 , wherein:
the step of calcining the dual-layered inorganic supported membrane includes calcining at a temperature ranging from 400 to 500° C.
25 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 24 , wherein:
the step of calcining the dual-layered inorganic supported membrane includes calcining for between about 30 to 90 minutes.
26 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining under a vacuum.
27 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 26 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining under a vacuum of less than about 6 pounds per square inch absolute (psia).
28 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 27 , wherein:
the step of calcining the inorganic polymeric coated substrate includes calcining under a vacuum of less than about 4 pounds per square inch absolute (psia).
29 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the step of heating the surfactant-template membrane substrate includes heating at a temperature between 500 to 600° C.
30 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 29 , wherein:
the step of heating the surfactant-template membrane substrate includes heating for between about 30 to 90 minutes.
31 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the step of calcining the surfactant-templated polymeric coated substrate includes calcining at a temperature between 100-150° C.
32 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the surfactant-template polymeric sol comprises silica polymers.
33 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the second polymeric sol comprises silica polymers.
34 . The method for producing the inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein:
the surfactant-template polymeric sol is prepared and deposited under conditions of low condensation rate; and the second polymeric sol is prepared and deposited under a condition of low condensation rate.
35 . The method for producing an inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein the method is performed under Class 100 clean room conditions.
36 . The method for producing an inorganic dual-layered microporous supported membrane as claimed in claim 16 , wherein the step of drying the surfactant sol coated membrane support is performed under conditions of low relative pressure of the liquid constituents.
37 . A method for producing a supported membrane capable of molecular sieving, comprising:
preventing a subsequently deposited top microporous sol from penetrating further into the support including:
modifying a surface of the support; and
depositing the top microporous membrane on a modified support producing the supported membrane capable of molecular sieving.
38 . The method for producing a supported membrane as claimed in claim 37 , wherein:
the step of modifying a surface of the support includes:
depositing an intermediate membrane on the surface.
39 . The method for producing a supported membrane as claimed in claim 38 , wherein:
the step of depositing the intermediate membrane includes depositing an inorganic surfactant-templated silica intermediate layer having an average pore size of less than 25 Å.
40 . The method for producing a supported membrane as claimed in claim 38 , wherein:
the step of depositing the intermediate membrane includes:
depositing a surfact-template sol onto the support;
drying the surfactant sol coated support;
calcining the dried surfactant sol coated support resulting in a surfactant supported membrane.
41 . The method for producing a supported membrane as claimed in claim 38 , wherein:
the step of depositing an intermediate membrane including:
removing the surfactant-template by heating the surfactant supported membrane producing the modified support.
42 . The method for producing a supported membrane as claimed in claim 38 , wherein:
the step of depositing the top microporous membrane includes:
depositing an inorganic polymeric sol on the modified support;
drying the polymeric sol coated support resulting in an inorganic polymeric sol coated support;
calcining the inorganic polymeric sol coated support resulting in a dual-layered supported membrane;
further calcining the dual-layered supported membrane resulting in the supported membrane capable of molecular sieving.Join the waitlist — get patent alerts
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