Gas separation device with nanocomposite membrane
US-9815019-B1 · Nov 14, 2017 · US
US10105655B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10105655-B2 |
| Application number | US-201815889705-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 6, 2018 |
| Priority date | Feb 19, 2016 |
| Publication date | Oct 23, 2018 |
| Grant date | Oct 23, 2018 |
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A semi-porous composite membrane and a method of manufacturing the semi-porous composite membrane. The semi-porous composite membrane includes a base supporting substrate comprising α-Al 2 O 3 , an outer layer comprising silica, and an intermediate layer comprising crystalline fibers of boehmite, and at least one of a secondary metal oxide and a synthetic polymer, wherein the intermediate layer is disposed between the base supporting substrate and the outer layer. The crystalline fibers of boehmite are a length of 5-150 nm. The semi-porous composite membrane may be employed in membrane reactors.
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The invention claimed is: 1. A membrane reactor, comprising: a semi-porous composite membrane in the form of a tube, wherein the semi-porous composite membrane comprises: a base supporting substrate comprising α-Al 2 O 3 ; an outer layer comprising silica; and an intermediate layer comprising crystalline fibers of α-Al 2 O 3 which are a length of 5-150 nm and at least one of a secondary metal oxide and a synthetic polymer, wherein the intermediate layer is disposed between the base supporting substrate and the outer layer; wherein the semi-porous composite membrane has a permeance of 4.0×10 −8 mol·m −2 ·s −1 ·Pa −1 to 1.0×10 −6 mol·m −2 ·s −1 ·Pa −1 for He and H 2 from at least one gas of Ar, N 2 , and CO. 2. The membrane reactor of claim 1 , wherein the secondary metal oxide is at least one metal oxide selected from the group consisting of lanthanum oxide, zirconium dioxide, calcium oxide, and gallium oxide. 3. The membrane reactor of claim 1 , wherein the base supporting substrate is a porous base supporting substrate. 4. The membrane reactor of claim 3 , wherein the porous base supporting substrate comprises pores having an average diameter of 50 nm to 160 nm. 5. The membrane reactor of claim 1 , wherein the intermediate layer comprises pores of which 70%-95% of a total number of the pores have a pore size distribution from 2 nm to 70 nm. 6. The membrane reactor of claim 1 , wherein the outer layer is a silica membrane. 7. The membrane reactor of claim 6 , wherein the silica membrane is a porous silica membrane comprising pores having an average pore diameter of 0.1 nm to 2 nm. 8. The membrane reactor of claim 1 , wherein the synthetic polymer is present and is at least one polymer selected from the group consisting of polyvinyl alcohol, polyethylene glycol, polyvinyl pyrrolidone, polyacrylic acid, polyacrylamide, poly(N-(2-hydroxypropyl) methacrylamide, and polyoxazoline.
Details relating to membrane preparation · CPC title
Supported membranes; Membrane supports · CPC title
Specific permeability or cut-off range · CPC title
Aluminium oxide · CPC title
Polyamides, e.g. polyester-amides · CPC title
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