Method of and system for separating volatile siloxane from feed mixture
Various embodiments disclosed relate to methods of separating a volatile siloxane from a liquid mixture. In various embodiments, the method includes contacting a first side of a first hydrophobic membrane with a liquid feed mixture including a polymer and at least one volatile siloxane. The method can also include contacting a second side of the membrane with a sweep medium including at least one of a sweep gas, a sweep liquid, and a vacuum, to produce a permeate mixture on the second side of the membrane and a retentate mixture on the first side of the membrane, wherein the permeate mixture is enriched in the volatile siloxane, and the retentate mixture is depleted in the volatile siloxane.
1. A method of separating a volatile siloxane from a liquid mixture, the method comprising:
contacting a first side of a first hydrophobic membrane with a liquid feed mixture comprising a polymer and at least one volatile siloxane, wherein the feed mixture is free of an organopolysiloxane emulsion; and
contacting a second side of the membrane with a sweep medium comprising at least one of a sweep gas, a sweep liquid, and a vacuum, to produce a permeate mixture on the second side of the membrane and a retentate mixture on the first side of the membrane, wherein the permeate mixture is enriched in the volatile siloxane, and the retentate mixture is depleted in the volatile siloxane.
2. The method of claim 1 , wherein the retentate mixture is depleted in the volatile siloxane by about 1 wt % to about 99.9 wt %, as compared to the liquid feed mixture.
3. The method of claim 1 , wherein the first hydrophobic membrane is nonporous.
4. The method of claim 1 , wherein the first hydrophobic membrane is a dense silicone membrane.
5. The method of claim 1 , wherein the first hydrophobic membrane has a thickness of about 1 μm to about 300 μm.
6. The method of claim 1 , wherein the first hydrophobic membrane is an unsupported membrane.
7. The method of claim 1 , wherein the first hydrophobic membrane is a hollow fiber membrane module comprising a bundle of hollow fibers, wherein the fibers collectively have a bore-side and a shell-side, wherein either
the first side of the hollow fiber membrane is the bore-side and the second side of the hollow fiber membrane is the shell-side, or
the first side of the hollow fiber membrane is the shell-side and the second side of the hollow fiber membrane is the bore-side.
8. The method of claim 1 , wherein the sweep liquid comprises an organosilicon fluid comprising at least one of an organosiloxane and an organosilane.
9. The method of claim 8 , wherein the organosilicon fluid comprises at least one silicon-bonded group chosen from a substituted or unsubstituted (C 1 -C 20 )hydrocarbyl interrupted or terminated with 0, 1, 2, or 3 groups selected from —O—, —NH—, and —S—, substituted or unsubstituted (C 1 -C 20 )alkyl, substituted or unsubstituted (C 6 -C 20 )aryl, and a substituted or unsubstituted polyether.
10. The method of claim 1 , further comprising desorbing the volatile siloxane from the permeate mixture and recirculating the desorbed permeate mixture into contact with the second side of the first hydrophobic membrane.
11. The method of claim 1 , wherein the polymer of the liquid feed mixture is an organopolysiloxane.
12. The method of claim 1 , wherein the volatile siloxane comprises at least one of a cyclosiloxane and a linear siloxane.
13. The method of claim 12 , wherein the cyclosiloxane is a substituted or unsubstituted cyclosiloxane having about 4 to 20 —Si—O— units in the ring or rings thereof.
14. A method of separating a volatile siloxane from a liquid mixture, the method comprising:
contacting a first side of a first hydrophobic membrane with a liquid feed mixture comprising a polymer and at least one volatile siloxane, wherein the feed mixture is free of an organopolysiloxane emulsion, the first hydrophobic membrane comprises a dense silicone membrane having a thickness of about 1 μm to about 300 μm, and the liquid feed mixture has a temperature of about −40° C. to about 250° C.; and
contacting a second side of the membrane with a sweep medium comprising at least one of a sweep gas, a sweep liquid, and a vacuum, to produce a permeate mixture on the second side of the membrane and a retentate mixture on the first side of the membrane, wherein the permeate mixture is enriched in the volatile siloxane, and the retentate mixture is depleted in the volatile siloxane by about 40 wt % to about 99 wt %, as compared to the liquid feed mixture.
15. A system for separating a volatile siloxane from a liquid mixture, the system comprising:
a first hydrophobic membrane;
a liquid feed mixture comprising a polymer and at least one volatile siloxane, the liquid feed mixture contacting a first side of the first hydrophobic membrane, wherein the feed mixture is free of an organopolysiloxane emulsion;
a sweep medium comprising at least one of a sweep gas, a sweep liquid, and a vacuum, the sweep medium contacting a second side of the membrane;
a permeate mixture on the second side of the membrane, the permeate mixture formed by the contacting, wherein the permeate mixture is enriched in the volatile siloxane;
a retentate mixture on the first side of the membrane, the retentate mixture formed by the contacting, wherein the retentate mixture is depleted in the volatile siloxane.