Composition for co2 gas separation membrane, co2 gas separation membrane and method for producing same, and co2 gas separation membrane module
US-2017232398-A1 · Aug 17, 2017 · US
US10173178B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-10173178-B1 |
| Application number | US-201615138400-A |
| Country | US |
| Kind code | B1 |
| Filing date | Apr 26, 2016 |
| Priority date | Apr 27, 2015 |
| Publication date | Jan 8, 2019 |
| Grant date | Jan 8, 2019 |
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A carbon dioxide membrane structure, a method of making the same, and a carbon dioxide separator including the same. The membrane structure may include a carbon dioxide separation membrane containing PVA and a carrier, and a polysulfone-based support having an average pore size ranging from about 40 to about 90 μm.
Opening claim text (preview).
The invention claimed is: 1. A carbon dioxide separation membrane comprising: a base polymer comprising poly vinyl alcohol (PVA); a carrier selected from: imidazole; and benzimidazole; a cross-linker comprising DETA wherein the carbon dioxide separation membrane is configured to operate at temperatures ranging from about 80° C. to about 150° C. 2. The membrane of claim 1 , wherein the membrane has a PVA to carrier mol ratio ranging from about 5:1 to about 10:1. 3. A carbon dioxide separation membrane comprising: a base polymer comprising poly vinyl alcohol (PVA); and a carrier comprising PANI, wherein the membrane has a PVA to carrier mol ratio ranging from about 275:1 to about 325:1, and wherein the carbon dioxide separation membrane is configured to operate at temperatures ranging from about 80° C. to about 150° C. 4. The membrane of claim 1 , wherein the membrane is configured to operate at a temperature ranging from about 100 to about 140° C. 5. The membrane of claim 1 , wherein the PVA is at least about 99% hydrolyzed. 6. The membrane of claim 1 , wherein from about 20% to about 25% of monomers of the PVA are cross-linked. 7. The membrane of claim 1 , wherein the carrier comprises imidazole. 8. The membrane of claim 1 , wherein the carrier comprises benzimidazole. 9. The membrane of claim 3 , wherein the membrane is configured to operate at a temperature ranging from about 100 to about 140° C. 10. The membrane of claim 3 , wherein the PVA is at least about 99% hydrolyzed. 11. The membrane of claim 3 , wherein from about 20% to about 25% of monomers of the PVA are cross-linked. 12. The membrane of claim 3 , further comprising a cross-linker selected from: formaldehyde; DETA; DETA and formaldehyde; potassium hydroxide and formaldehyde; and gultaraldehyde and potassium hydroxide. 13. The membrane of claim 12 , wherein when the cross-linker is formaldehyde.
characterised by specific membranes · CPC title
In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction · CPC title
Cross-linking · CPC title
by chemical reactions (in-situ polymerisation, polycondensation, cross-linking or reaction for manufacturing composite membranes B01D69/125) · CPC title
Devices · CPC title
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