Highly microporous polymers and methods for producing and using the same
The present invention provides microporous polymers and methods for producing and using the same. In particular, microporous polymers of the present invention are highly porous as indicated by a Gurley air permeability flow rate of about 4 seconds or less per mL of air flow per 25 micron of microporous polymer thickness per square inch.
1. A method of producing a microporous polymer film comprising:
dissolving a polymer having a polymer free surface energy in a low surface tension liquid to form a polymer solution;
forming an approximately saturated solution by adding, to the polymer solution, a high surface tension liquid having a surface tension equal to or in excess of the polymer surface free energy; the forming being conducted at a temperature less than or equal to the lower of a boiling temperature of the approximately saturated solution or a melt temperature of the polymer;
placing the approximately saturated solution in a layer at the forming temperature on a generally planar substrate having a substrate surface free energy at least equal to the surface tension of the low surface tension liquid;
urging the low surface tension liquid into a non-wetting relation to the polymer by cooling the approximately saturated solution to increase surface tension of the solvent to form a gelled polymer having a surface tension which exceeds the surface free energy of the polymer material, causing the low surface tension liquid to tend to bead within the gelled polymer; and
evaporating the low surface tension liquid from the gelled polymer to form a film defining a plurality of pores, such that sufficient low surface tension liquid is partially removed from the gelled polymer to form the film defining the plurality of pores, the low surface tension liquid being evaporated at temperatures not to exceed the lower of a boiling temperature of the approximately saturated solution and of the melt temperature of the polymer.
2. The method of claim 1 , wherein the solubility of the polymer material in the solution is about 25% v/v or less relative to the total volume of the solvent in the solution.
3. The method of claim 1 , wherein the ratio of the low surface tension liquid relative to the high surface tension liquid is less than or equal to between 9:1 to 99:1 v/v.
4. The method of claim 1 , wherein
the volume of the high surface tension liquid is selected in a ratio to the polymer material to approximate a desired void volume ratio between the a volume of the plurality of pores and the combined total volume of the polymer material and the volume of the plurality of pores.
5. The method of claim 1 , wherein the low surface tension liquid is one of a group of a ketone, ester, ether, aldehyde, amine, amide, nitrile, cyanate, nitrite, nitrate, nitro- or nitroso-compound, thiol, sulfide, sulfonium, sulfate, sulfonyl compound, sulfinyl compound, thio-compounds, and a mixture of two or more thereof.
6. The method of claim 5 , wherein the ketone is selected from a group consisting of acetone, methyl ethyl ketone, pentanone, hexanone, cyclic ketone, and a mixture of two or more thereof.
7. The method of claim 1 , wherein the high surface tension liquid is selected from a group consisting of:
acetamide, acetophenone, adiponitrile, aniline, benzaldehyde, benzyl benzoate, benzonitrile, benzophenone, bromine, bromobenzene, tribromomethane, bromophenol, carbon disulfide, chloroacetic acid, chlorobenzene, chlorophenol, diethylaniline, diethylene glycol, dimethylaniline, dimethyl phenyl pyrazolane, dimethyl sulfoxide, diphenylamine, ethylaniline, ethylene bromide, ethylene glycol, formamide, formic acid, furfural, γ-butyrolactone, glycerin, glycerol, methylaniline, methyl benzoate, methylene iodide, nitric acid, nitrobenzene, nitromethane, phenol, phosphorous tribromide, phosphorous tri-iodide, propylene glycol, pyridine, pyridazine, quinoline, sulfuric acid, tetrabromomethane, toluene, xylene, water, and a mixture of two or more thereof.
8. The method of claim 7 , wherein the high surface tension liquid is water.
9. The method of claim 1 , wherein the thickness of the layer is about 500 μm or less.
10. The method of claim 1 , wherein the surface tension of the solvent is at least about 35 dynes/cm at 25° C.
11. The method of claim 1 , wherein the gelled polymer is formed at a temperature of about 40° C. or less.
12. The method of claim 11 , wherein the low surface tension liquid is removed from the gelled polymer at a temperature of about 30° C. or less.
13. The method of claim 1 , wherein the gelled polymer is formed at a temperature of about 5° C. or less relative to forming temperature of the approximately saturated solution.
14. The method of claim 1 , wherein the solvent is removed at a temperature of about 5° C. or less relative to the forming temperature of the approximately saturated solution.
15. The method of claim 1 , wherein the solubility of the polymer material in the low surface tension liquid is about 10% v/v or less.
16. The method of claim 1 , the forming the approximately saturated solution-includes one of heating the mixture, subjecting the mixture to high shear mixing, or a combination thereof