Membranes for gas separation
US-12023633-B2 · Jul 2, 2024 · US
US10279320B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10279320-B2 |
| Application number | US-201415021847-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 16, 2014 |
| Priority date | Sep 16, 2013 |
| Publication date | May 7, 2019 |
| Grant date | May 7, 2019 |
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The present invention relates to a water treatment membrane including a support; and a polymer layer including a copolymer containing a hydrophobic repeating unit and a hydrophilic repeating unit including an ion exchange functional group on the support, wherein the polymer layer has ion exchange capacity (IEC) of 0.02 meq/g to 2.4 meq/g, and to a water treatment module, which have excellent salt rejection and permeate flow properties.
Opening claim text (preview).
The invention claimed is: 1. A water treatment membrane comprising: a support; and a polymer layer on the support, the polymer layer including a copolymer containing a hydrophobic repeating unit and a hydrophilic repeating unit including an ion exchange functional group, wherein: the polymer layer has ion exchange capacity (IEC) of 0.02 meq/g to 2.4 meq/g; the hydrophilic repeating unit has the following Chemical Formula 3: wherein: G in each repeating unit is a functional group selected from the group consisting of: R 5 has an ion exchange functional group that is —SO 3 M, —CO 3 M or —PO 3 M where M is H, Na or K; and the hydrophobic repeating unit has the following Chemical Formula 4: wherein: H in each repeating unit is a functional group selected from the group consisting of: and * in Chemical Formula 3 and 4 is a site at which repeating units are connected and no separate atoms or molecules are present at the site. 2. The water treatment membrane of claim 1 , wherein a molar ratio of the hydrophilic repeating unit and the hydrophobic repeating unit is 1:9 to 1:1. 3. The water treatment membrane of claim 1 , wherein the copolymer has a weight average molecular weight of 30,000 to 1,000,000. 4. The water treatment membrane of claim 1 , wherein the polymer layer has a thickness of 0.1 μm to 200 μm. 5. The water treatment membrane of claim 1 , which has initial salt rejection of 97% or greater, and initial permeate flow of 38 to 48 gallon/ft 2 ·day when a sodium chloride (NaCl) solution having a concentration of 32,000 ppm passes therethrough under a pressure of 800 psi. 6. The water treatment membrane of claim 1 comprising one or more active layers on the polymer layer. 7. The water treatment membrane of claim 1 , which is a microfiltration membrane, an ultrafiltration membrane, a nanofiltration membrane or a reverse osmosis membrane. 8. A water treatment module comprising the water treatment membrane of claim 1 . 9. A method for manufacturing a water treatment membrane comprising: coating a support using a solution including a copolymer containing a hydrophobic repeating unit and a hydrophilic repeating unit including an ion exchange functional group, and a solvent; and carrying out phase transition by immersing the coated support in a non-solvent, wherein: the copolymer is a copolymer containing a hydrophobic repeating unit and a hydrophilic repeating unit including an ion exchange functional group, wherein: G is any one or more functional groups selected from the group consisting of the following functional groups: R 5 has an ion exchange functional group that is —SO 3 M, —CO 3 M or —PO 3 M where M is H, Na or K; and the hydrophobic repeating unit has the following Chemical Formula 4: wherein: H is any one or more functional groups selected from the group consisting of the following functional groups: and * in Chemical Formula 3 and 4 is a site at which repeating units are connected and no separate atoms or molecules are present at the site. 10. The method for manufacturing a water treatment membrane of claim 9 , wherein the non-solvent is selected from the group consisting of distilled water that is distilled once, distilled water that is distilled three times, alcohols, and a mixture thereof. 11. The water treatment membrane of claim 1 , wherein: the hydrophilic repeating unit is: and the hydrophobic repeating unit is: 12. The method for manufacturing a water treatment membrane of claim 9 , wherein: the hydrophilic repeating unit is: and the hydrophobic repeating unit is:
Hydrophilization · CPC title
Specific ratios of components used · CPC title
Hydrophobization · CPC title
Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74 (rubbers in general B01D71/24) · CPC title
Ultrafiltration · CPC title
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