Hollow fiber membranes for solubilizing a gas into a liquid, devices for same, and processes of same
A hollow fiber membrane is disclosed that includes both a porous hollow fiber and a nonporous film coating. The hollow fiber membrane is suitable for use in solubilizing gases into liquids. This can include for example carbonation of an aqueous liquid by CO 2 gas. Systems, methods, and devices are disclosed.
1. A system for solubilizing a liquid with a gas comprising:
a shell containing a bundle of hollow fiber membranes;
a liquid source; and
a gas source;
wherein each hollow fiber membrane comprises:
a mesoporous hollow fiber comprising a hydrophobic fluorinated polymer; and
a nanoscopic perfluorinated film;
wherein the mesoporous hollow fiber has an average pore diameter from about 0.05 to about 3 microns;
wherein the nanoscopic perfluorinated film has an average thickness from about 25 to about 500 nanometers;
wherein the mesoporous hollow fiber comprises:
an outer surface defining an outer diameter of the mesoporous hollow fiber;
a lumen having an inner surface defining an inner diameter of the mesoporous hollow fiber; and
an annular wall having a wall thickness extending from the inner surface of the lumen to the outer surface of the fiber; and
wherein the nanoscopic perfluorinated film at least partially coats one or both of:
the outer surface of the mesoporous hollow fiber; and
the inner surface of the lumen;
wherein the shell has a shell side and a lumen side, the shell side defined by the shell and the outer surfaces of the bundle of hollow fiber membranes, and the lumen side defined by the inner surfaces of the lumens of the bundle of hollow fiber membranes;
wherein the liquid source is configured to supply a liquid to one of the shell side and lumen side of the shell; and
wherein the gas source is configured to supply a gas to the other of the shell side and lumen side of the shell.
2. The system of claim 1 , wherein the nanoscopic perfluorinated film at least partially coats the outer surface of the mesoporous hollow fibers of the bundle of hollow fiber membranes.
3. The system of claim 1 , wherein the shell comprises:
a first end;
a second end;
an inlet port in fluid communication with the shell side of the shell; and
an outlet port in fluid communication with the shell side of the shell;
wherein the hollow fiber membranes of the bundle of hollow fiber membranes are substantially aligned along the lengths of the hollow fiber membranes and extend through the length of the shell from the first end to the second end; and
wherein the first end and the second end of the shell comprise binding material effectively interconnecting the lumen of adjacent hollow fiber membranes.
4. The system of claim 1 further comprising:
a gas; and
a liquid initially free of the gas;
wherein the gas source is configured to supply the gas at a pressure to the lumen side of the shell;
wherein the liquid source is configured to supply the liquid initially free of the gas to the shell side of the shell; and
wherein the shell is configured to enable the pressurized gas to diffuse through the pores of the mesoporous hollow fibers and permeate through the nanoscopic perfluorinated film and providing microscale size bubbles of the gas into the liquid such that the liquid subsequently contains at least a portion of the gas.
5. The system of claim 4 , wherein the pressurized gas comprises one or both of CO 2 and N 2 .
6. The system of claim 4 , wherein the liquid comprises water.
7. The system of claim 4 , wherein the nanoscopic perfluorinated film comprises polytetrafluoroethylene (PTFE).
8. The system of claim 4 , wherein the nanoscopic perfluorinated film has an average thickness of about 75 to about 150 nanometers.
9. The system of claim 4 , wherein the hydrophobic fluorinated polymer comprises polyvinylidene difluoride (PVDF).
10. The system of claim 4 , wherein the nanoscopic perfluorinated film has an average thickness of about 50 to about 200 nanometers.
11. The system of claim 4 , wherein the average inner diameter of the mesoporous hollow fibers of the bundle of hollow fiber membranes is in a range of from about 75 to about 200 micrometers.
12. The system of claim 4 , wherein the average outer diameter of the mesoporous hollow fibers of the bundle of hollow fiber membranes is in a range of from about 150 to about 400 micrometers.
13. The system of claim 4 , wherein the average wall thickness of the mesoporous hollow fibers of the bundle of hollow fiber membranes is in a range of from about 25 to about 100 micrometers.