METHOD FOR PRODUCING POROUS HOLLOW FIBER MEMBRANE FOR HUMIDIFICATION

Abstract

A method for producing a porous hollow fiber membrane for humidification, the method comprising dry-wet spinning a spinning dope comprising a water-soluble organic solvent solution composed of polyphenylsulfone resin and hydrophilic polyvinylpyrrolidone using water as a core liquid; then performing a crosslinking treatment at 120 to 220° C. for 1 to 20 hours; and then dipping the resultant in an acidic solution with a concentration of 5 to 500 ppm. The obtained porous hollow fiber membrane has improved hydrophilicity without impairing the wettability of the porous hollow fiber membrane. Since, humidification performance of the porous hollow fiber membrane alone can be improved, it is effective as a humidifying membrane for fuel cells.

Claims

1. A method for producing a porous hollow fiber membrane for humidification, the method comprising: dry-wet spinning a spinning dope comprising a water-soluble organic solvent solution composed of polyphenylsulfone resin and hydrophilic polyvinylpyrrolidone using water as a core liquid; then performing a crosslinking treatment at 120 to 220° C. for 1 to 20 hours; and then dipping the resultant in an acidic solution containing an acid at a concentration of 5 to 500 ppm.

2. The method for producing a porous hollow fiber membrane for humidification according to claim 1, wherein hydrophilic polyvinylpyrrolidone is used at a ratio of 50 to 150 parts by weight, based on 100 parts by weight of the polyphenylsulfone resin.

3. The method for producing a porous hollow fiber membrane for humidification according to claim 1, wherein an autoclave treatment is performed prior to the crosslinking treatment.

4. The method for producing a porous hollow fiber membrane for humidification according to claim 1, which is used as a humidifying membrane for fuel cells.

Description

BRIEF DESCRIPTION OF DRAWING

[0016] FIG. 1: Graphs comparing the water vapor permeability coefficient and contact angle measured for hollow fiber membranes obtained in the Example and Comparative Examples

EMBODIMENTS FOR CARRYING OUT THE INVENTION

[0017] The polyphenylsulfone resin has a repeating unit represented as follows:

##STR00001##

i.e., it has a biphenylene group and no isopropylidene group. In practice, commercial products, such as the RADEL R series produced by Amoco, can be used as they are.

[0018] To a spinning dope comprising polyphenylsulfone resin as a film-forming component, hydrophilic polyvinylpyrrolidone and a water-soluble organic solvent are added to form a spinning dope. As the water-soluble organic solvent, an aprotic polar solvent, such as dimethylformamide, dimethylacetamide, or N-methyl-2-pyrrolidone, is used. The polyphenylsulfone resin is used at a concentration of about 10 to 40 wt. %, preferably about 15 to 30 wt. %, in the spinning dope. A porous hollow fiber membrane having a desired pore size and membrane strength cannot be obtained outside this concentration range.

[0019] As the polyvinylpyrrolidone added as a hydrophilic highmolecular substance, one having a molecular weight of about 1000 (K-15) to 1200000 (K-90), preferably about 10000 (K-30) to 1200000 (K-90), is used at a ratio of about 50 to 150 parts by weight, preferably about 50 to 100 parts by weight, based on 100 parts by weight of the polyphenylsulfone resin. The addition of polyvinylpyrrolidone at such a ratio more or less affects structure control, such as the surface pore size of the porous membrane; however, more than that, it achieves an effect of reducing the air permeability rate of the porous membrane, i.e., improving gas barrier properties, and improving the water vapor permeability rate.

[0020] Dry-wet spinning using such a spinning dope is carried out using water as a core liquid. The porous hollow fiber membrane coagulated in water or an aqueous coagulation solution is washed with water, and washed with hot water in an autoclave at 121° C. for about 30 to 90 minutes, followed by a crosslinking treatment. The crosslinking treatment of polyvinylpyrrolidone is carried out at about 120 to 220° C., preferably about 150 to 190° C., more preferably about 175 to 190° C., for about 1 to 20 hours, preferably about 5 to 12 hours.

[0021] If the crosslinking treatment is not carried out, the elution of hydrophilizing substances cannot be suppressed even when the acid treatment is performed, and it is difficult to ensure wettability, as shown in the decrease of the water vapor permeability coefficient shown in Comparative Example 3, provided later.

[0022] The crosslinked porous hollow fiber membrane is further subjected to the acid treatment by dipping it in an acidic solution with a concentration of about 5 to 500 ppm, preferably about 50 to 300 ppm.

[0023] For the acid treatment, sulfuric acid; hydrohalogenic acids, such as hydrochloric acid, hydrobromic acid, and hydroiodic acid; halogen oxo acids, such as hypochlorous acid; sulfonic acids, such as fluorosulfonic acid and methanesulfonic acid; nitric acid; phosphoric acid; boric acid; hexafluoroantimonic acid; tetrafluoroboric acid; hexafluorophosphoric acid; carboxylic acids, such as acetic acid; ascorbic acid; and the like are used.

[0024] The acid treatment is followed by a drying treatment, thereby producing a porous hollow fiber membrane. The acid treatment is carried out at about 60 to 110° C., preferably about 70 to 100° C., for about 24 to 150 hours. After the acid treatment, a drying treatment is carried out at about 40 to 60° C. for about 12 to 48 hours.

[0025] When the acid treatment is carried out, the wettability of the porous hollow fiber membrane is significantly improved, as shown in the comparison results of the Example and Comparative Example 2. However, if the concentration of the acid used in the acid treatment is higher than the above range, the physical properties of the porous hollow fiber membrane are reduced, which is not preferable.

EXAMPLES

[0026] The following describes the present invention with reference to Examples.

Example

[0027] 20 parts by weight of polyphenylsulfone resin (RADEL R-5000, produced by Solvay Specialty Polymers) and 15 parts by weight of polyvinylpyrrolidone (Kollidon 30, produced by BASF) were dissolved in 65 parts by weight of dimethylformamide to prepare a membrane-forming dope. Next, water was discharged as a core liquid to the inside nozzle of a double annular spinning nozzle, and the membrane-forming dope was discharged from the outside of the double annular spinning nozzle using a gear pump. After the discharged membrane-forming dope was coagulated in a water coagulation liquid, and then taken up on a hollow fiber membrane bobbin using a winder. After the hollow fiber membrane was taken up, the hollow fiber membrane was subjected to an autoclave treatment at 121° C. for 60 minutes.

[0028] The hollow fiber membrane after the autoclave treatment was placed in a thermostatic chamber and heated at 175° C. for 9 hours to crosslink the polyvinylpyrrolidone. Then, the porous hollow fiber membrane after the crosslinking treatment was dipped in a sulfuric acid aqueous solution with a concentration of 300 ppm, and an acid treatment was carried out at 80° C. for 150 hours. After completion of the dipping, the porous hollow fiber membrane was placed in a thermostatic chamber and dried at 55° C. for 24 hours.

[0029] The obtained porous hollow fiber membrane was used to perform a water vapor permeability test and to measure the water contact angle of the hollow fiber membrane. As a result, the water vapor permeability coefficient was 0.168 g/min/cm.sup.2/MPa and the contact angle was 71.39°.

Comparative Example 1

[0030] When neither the crosslinking treatment nor the acid treatment was carried out in the Example, the obtained porous hollow fiber membrane had a water vapor permeability coefficient of 0.102 g/min/cm.sup.2/MPa and a contact angle of 81.10°.

Comparative Example 2

[0031] When the acid treatment was not carried out in the Example, the obtained porous hollow fiber membrane had a water vapor permeability coefficient of 0.120 g/min/cm.sup.2/MPa and a contact angle of 79.30°.

Comparative Example 3

[0032] When the crosslinking treatment was not carried out in the Example, the obtained porous hollow fiber membrane had a water vapor permeability coefficient of 0.066 g/min/cm.sup.2/MPa and a contact angle of 82.42°.

INDUSTRIAL APPLICABILITY

[0033] The porous hollow fiber membrane obtained by the production method according to the present invention has improved hydrophilicity without impairing the wettability of the porous hollow fiber membrane. Therefore, the porous hollow fiber membrane alone has high humidification performance, and is thus effectively used as a porous hollow fiber membrane used in a humidifying membrane module for fuel cells.