Membranes for gas separation
US-12023633-B2 · Jul 2, 2024 · US
US10086339B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10086339-B2 |
| Application number | US-201615066697-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 10, 2016 |
| Priority date | Mar 10, 2015 |
| Publication date | Oct 2, 2018 |
| Grant date | Oct 2, 2018 |
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A polymer having a contact angle with water that is greater than or equal to 90° and a contact angle with 1,3-propane diol that is less than 90°. A pervaporation membrane comprising the polymer and a process for purifying a fermentation broth using a pervaporation membrane comprising the polymer is also described.
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The invention claimed is: 1. A pervaporation membrane comprising a polymer having a contact angle with water that is greater than or equal to 90° and a contact angle with 1,3-propane diol that is less than 90° wherein the polymer comprises allylcyclohexylamine functionalized polysiloxane or repeating units derived from an allylcyclohexylamine based acrylate. 2. The pervaporation membrane of claim 1 , wherein the polymer comprises allylcyclohexylamine functionalized polysiloxane and the membrane further comprises styrene-butyl acrylate copolymer. 3. The pervaporation membrane of claim 1 , wherein the polymer comprises a repeating unit derived from an imidazolium functionalized acrylate monomer having a dibutyl phosphate counter ion. 4. The pervaporation membrane of claim 1 , wherein the membrane has a separation factor of 1,3-propane diol relative to water of greater than or equal to 5. 5. The pervaporation membrane of claim 4 , wherein the membrane has a separation factor of 1,3-propane diol relative to glycerin greater than or equal to 1.5. 6. The process for purifying a fermentation broth comprising: contacting the broth with the pervaporation membrane of claim 1 pervaporation conditions to produce a product comprising 1,3-propane diol wherein the pervaporation membrane comprises a polymer having a contact angle with water that is greater than or equal to 90° and a contact angle with 1,3-propane diol that is less than 90° and the fermentation broth comprises 1,3-propane diol. 7. The process of claim 6 , further comprising removing solids from the fermentation broth prior to contact with the pervaporation membrane. 8. The process of claim 6 , further comprising distilling the product comprising 1,3-propane diol. 9. The process of claim 6 , wherein the pervaporation membrane has an upstream side and a downstream side and a gauge pressure on the upstream side is less than 10 atmospheres and absolute pressure on the downstream side is less than 50 millimeters of Hg. 10. The process of claim 6 , wherein the temperature of the fermentation broth is 15 to 50° C. 11. The process of claim 6 , wherein the pervaporation membrane has a mass uptake of pure water less than 1% and a mass uptake of pure 1,3-propane diol greater than 2.5%. 12. The process of claim 6 , wherein the pervaporation membrane has a separation factor of 1,3-propane diol relative to water greater than or equal to 5. 13. The process of claim 6 , wherein the polymer comprises repeating units derived from allylcyclohexylamine or tributyl phosphate. 14. The process of claim 13 , wherein the polymer comprises allylcyclohexylamine functionalized polysiloxane. 15. The process of claim 14 , wherein the membrane further comprises a styrene-butyl acrylate copolymer. 16. The process of claim 13 , wherein the polymer comprises a repeating unit derived from an allylcyclohexylamine based acrylate. 17. The process of claim 13 , wherein the polymer comprises a repeating unit derived from an imidazolium functionalized acrylate monomer having a dibutyl phosphate counter ion.
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