JP5134480B2 - Epoxy resin porous membrane and method for producing the same - Google Patents

Description

  The present invention relates to a porous epoxy resin membrane having pores communicating with a three-dimensional network skeleton and a method for producing the same.

  Epoxy resins have excellent chemical resistance and are inexpensive, and for example, in Patent Document 1, they are applied as separation media for column chromatography.

  In Patent Document 1, an epoxy resin and a curing agent are dissolved in a porogen to prepare a uniform solution, and this solution is poured into a mold and heated to polymerize the epoxy resin and polymerize the epoxy resin. After separating the porogen from the phase, the porogen is removed to obtain a porous epoxy resin. According to the method of Patent Document 1, a monolithic porous body having pores communicating with a three-dimensional network skeleton can be obtained.

International Publication WO 2006/073173

  However, since the manufacturing method disclosed in Patent Document 1 can only obtain a porous body having a uniform pore size in the thickness direction, the amount of permeate is maintained in separation membrane applications for ion separation and the like. However, it was difficult to improve the separation performance.

  An object of the present invention is to provide an epoxy resin porous membrane capable of improving the separation performance while maintaining the amount of permeate, and a method for producing the same.

  As a result of extensive research, the inventors of the present invention filled a solution containing an epoxy resin, a curing agent and a porogen between a pair of sheet materials, and heated only one of the sheet materials, so that the pore diameter gradually increased in the thickness direction. The inventors have found that a film having an asymmetric structure can be obtained, and have completed the present invention.

  That is, the epoxy resin porous membrane of the present invention is an epoxy resin porous membrane having pores communicating with a three-dimensional network skeleton, and the pore diameter of the pores from one surface of the membrane It is characterized by gradually increasing in the thickness direction over the other surface.

  According to the porous epoxy resin membrane of the present invention, since the pore diameter gradually increases in the thickness direction (asymmetric structure), the separation performance can be improved while maintaining the permeate amount.

  In the epoxy resin porous membrane of the present invention, the average pore diameter in the vicinity of the other surface is preferably 2 to 100 times the average pore diameter in the vicinity of the one surface. This is because both the maintenance of the permeate amount and the improvement of the separation performance can be easily realized.

  In the epoxy resin porous membrane of the present invention, the average pore diameter in the vicinity of the other surface is 0.2 to 5 μm, and the average pore diameter in the vicinity of the one surface is 0.02 to 0.5 μm. There may be. In this case, in the vicinity of the other surface, since the average pore diameter of the pores is 0.2 to 5 μm, it is possible to prevent a decrease in the film strength while maintaining a high permeate amount. Further, in the vicinity of the one surface, since the average pore diameter of the pores is 0.02 to 0.5 μm, the resistance of the permeate flow can be reduced and the separation performance can be improved.

  The method for producing an epoxy resin porous membrane of the present invention is a method for producing an epoxy resin porous membrane having pores communicating with a three-dimensional network skeleton, and a solution containing an epoxy resin, a curing agent and a porogen Filling step between a pair of sheet materials, a reaction-induced phase separation step in which only one of the sheet materials is heated to phase-separate the epoxy resin polymer and porogen while polymerizing the epoxy resin, And a removal step of removing porogen from the cured product obtained in the reaction-induced phase separation step.

  According to the production method of the present invention, since the solution containing the epoxy resin, the curing agent, and the porogen is filled between the pair of sheet materials, sedimentation of the porogen in the solution can be prevented. Thereby, since the porogen is surely present in the solution in the vicinity of the contact surface with the sheet material in the reaction-induced phase separation step, pores can be formed also on the film surface and in the vicinity thereof. Further, in the reaction-induced phase separation step, only one of the sheet materials is heated, and therefore, between the film surface (one surface) on the one sheet material side and the film surface (the other surface) on the other sheet material side. Thus, a temperature difference occurs. As a result, a structure (asymmetric structure) is obtained in which the pore diameter gradually increases in the thickness direction from one surface of the membrane to the other surface, so that the separation performance can be improved while maintaining the permeate amount. An epoxy resin porous membrane can be provided.

  In the production method of the present invention, in the reaction-induced phase separation step, it is preferable to heat the one sheet material and cool the other sheet material. This is because the temperature difference between the one surface and the other surface can be increased, so that an asymmetric structure can be realized more easily. In this case, it is preferable to perform the heating and cooling so that the temperature difference between the one sheet material and the other sheet material is 10 to 200 ° C. Since the average pore diameter in the vicinity of the other surface can be 2 to 100 times the average pore diameter in the vicinity of the one surface, it is easy to maintain both the amount of permeate and improve the separation performance. This is because it can be realized.

  In the production method of the present invention, in the reaction-induced phase separation step, the one sheet material may be heated to 80 to 160 ° C, and the other sheet material may be cooled to -50 to 80 ° C. In this case, since the average pore diameter of the pores in the vicinity of the one surface can be set to 0.02 to 0.5 μm, the resistance of the permeate flow can be reduced and the separation performance can be improved. Moreover, since the average pore diameter of the pores in the vicinity of the other surface can be set to 0.2 to 5 μm, it is possible to prevent a decrease in the film strength while maintaining a high permeate amount.

  In the reaction-induced phase separation step, when heating the one sheet material and cooling the other sheet material, the heating and cooling treatment time is preferably 10 to 300 minutes. If it is in the said range, after ensuring the intensity | strength of a film | membrane, ensuring of the hole diameter for making the maintenance of a permeate amount and improvement of a separation performance compatible will become easy.

  In the reaction-induced phase separation step, when heating the one sheet material and cooling the other sheet material, after the heating and cooling, the cooling is stopped and only the heating is continued. Is preferred. This is because the vicinity of the other surface can be sufficiently cured, so that it is easy to ensure the strength of the film. In this case, it is preferable that the processing time of the heating after stopping the cooling is 0.5 to 5 hours. This is because it is easier to ensure the strength of the film.

  In the manufacturing method of this invention, it is preferable to further include the drying process which further hardens | cures the hardened | cured material from which the porogen was removed after the said removal process. This is because it is easy to ensure the strength of the film because crosslinking with a curing agent can be sufficiently performed. In this case, in the drying step, the cured product is preferably dried at an atmospheric temperature of 50 to 160 ° C. for 0.5 to 20 hours. This is because it is easier to ensure the strength of the film.

  In the production method of the present invention, the porogen content in the solution may be 20 to 80% by weight in the filling step. Since the pore diameter and porosity of the obtained membrane can be set to appropriate values, for example, when applied to a support membrane of a composite reverse osmosis membrane, it is easy to maintain the amount of permeate and improve separation performance. is there.

  In the production method of the present invention, the sheet material is preferably a glass sheet. This is because the glass sheet has high heat resistance, high releasability with respect to the cured epoxy resin, and can be recycled, so that the manufacturing cost can be easily reduced. However, not only glass but also a sheet material having high heat resistance and high releasability can be preferably used.

  In the manufacturing method of this invention, it is preferable that the space | interval of the said pair of sheet material after the said filling process is 0.1-5 mm. This is because when the thickness is 0.1 mm or more, it is easy to secure the strength of the film, and when the thickness is 5 mm or less, the precipitation of the porogen can be easily prevented.

  Hereinafter, preferred embodiments of the present invention will be described. The epoxy resin porous membrane of the present invention is an epoxy resin porous membrane having pores communicating with a three-dimensional network skeleton, wherein the pore diameter is from one side of the membrane to the other side of the membrane. It is characterized by gradually increasing in the thickness direction over the surface. According to the present invention, since the pore diameter gradually increases in the thickness direction (asymmetric structure), the separation performance can be improved while maintaining the permeate amount.

  The thickness of the porous epoxy resin membrane of the present invention is preferably 0.1 mm or more from the viewpoint of membrane strength, and preferably 5 mm or less from the viewpoint of ease of handling, ease of processing, and securing the amount of permeate.

  The porosity of the epoxy resin porous membrane of the present invention is preferably 20% or more from the viewpoint of maintaining the amount of permeated liquid, and preferably 80% or less from the viewpoint of improving separation performance and ensuring membrane strength. In addition, the said porosity is measured with the auto pore 9520 type | model apparatus by Shimadzu Corporation by the mercury intrusion method.

  In the epoxy resin porous membrane of the present invention, the average pore diameter in the vicinity of the other surface is preferably 2 to 100 times the average pore diameter in the vicinity of the one surface, and 10 to 100 times. More preferably. This is because both the maintenance of the permeate amount and the improvement of the separation performance can be easily realized. The “average pore diameter in the vicinity of the surface” means a cross-sectional observation of the film with a transmission electron microscope (S-4800, manufactured by Hitachi High-Technologies Corporation, magnification: 4000 times), a visual field width of 60 μm, and a thickness direction from the surface. In addition, for pores existing within a depth range of 1/5 to 1/100 of the thickness of the film, an average obtained by image processing using free software “Image J” or “Photoshop” manufactured by Adobe Point to the hole diameter.

  In the epoxy resin porous membrane of the present invention, the average pore diameter in the vicinity of the other surface is 0.2 to 5 μm (preferably 0.5 to 2 μm), and the average pore diameter in the vicinity of the one surface is May be 0.02 to 0.5 μm (preferably 0.05 to 0.2 μm). When the average pore diameter in the vicinity of the other surface is 0.2 to 5 μm, it is possible to prevent a decrease in film strength while maintaining a high permeate amount. In addition, when the average pore diameter in the vicinity of the one surface is 0.02 to 0.5 μm, it is possible to reduce the flow resistance of the permeate and improve the separation performance. When the average pore diameter in the vicinity of the one surface is 0.5 μm or less, when the epoxy resin porous membrane of the present invention is applied to the support membrane of the composite reverse osmosis membrane, the skin layer forming material is applied. It becomes easy.

  The epoxy resin porous membrane of the present invention is an inexpensive and chemical-resistant separation membrane, a composite reverse osmosis membrane supporting membrane for the purpose of desalination such as seawater and brine, and ultrafiltration for filtering fine particles, etc. It can be suitably used for a membrane or the like. Moreover, since it is excellent in heat resistance, it can be used in harsh environments. In addition, about the specific example of the constituent material of the epoxy resin porous membrane of this invention, it illustrates by description of the manufacturing method of the epoxy resin porous membrane of this invention hereafter.

  Next, the manufacturing method of the epoxy resin porous membrane of this invention is demonstrated. The method for producing an epoxy resin porous membrane of the present invention is a method for producing an epoxy resin porous membrane having pores communicating with a three-dimensional network skeleton, and a pair of a solution containing an epoxy resin, a curing agent and a porogen. A filling step of filling between the sheet materials, a reaction-induced phase separation step in which only one of the sheet materials is heated to polymerize the epoxy resin and phase-separate the polymer of the epoxy resin and the porogen, and the reaction induction And a removal step of removing porogen from the cured product obtained in the phase separation step.

  According to the production method of the present invention, since the solution containing the epoxy resin, the curing agent, and the porogen is filled between the pair of sheet materials, sedimentation of the porogen in the solution can be prevented. Thereby, since the porogen is surely present in the solution in the vicinity of the contact surface with the sheet material in the reaction-induced phase separation step, pores can be formed also on the film surface and in the vicinity thereof. Further, in the reaction-induced phase separation step, only one of the sheet materials is heated, and therefore, between the film surface (one surface) on the one sheet material side and the film surface (the other surface) on the other sheet material side. Thus, a temperature difference occurs. As a result, a structure (asymmetric structure) is obtained in which the pore diameter gradually increases in the thickness direction from one surface of the membrane to the other surface, so that the separation performance can be improved while maintaining the permeate amount. An epoxy resin porous membrane can be provided.

  Epoxy resins that can be used in the present invention include bisphenol A type epoxy resins, brominated bisphenol A type epoxy resins, bisphenol F type epoxy resins, bisphenol AD type epoxy resins, stilbene type epoxy resins, biphenyl type epoxy resins, and bisphenol A novolak types. Epoxy resin, cresol novolac type epoxy resin, diaminodiphenylmethane type epoxy resin, polyphenyl base epoxy resin such as tetrakis (hydroxyphenyl) ethane base, fluorene-containing epoxy resin, triglycidyl isocyanurate, heteroaromatic ring (for example, triazine ring) Aromatic epoxy resins such as epoxy resins containing aliphatic glycidyl ether type epoxy resins, aliphatic glycidyl ester type epoxy resins, alicyclic glycerides. Jill ether type epoxy resin, aromatic epoxy resins such as alicyclic glycidyl ester type epoxy resins. In this invention, these 1 type may be used and multiple types may be used. Of these, bisphenol A type epoxy resin, bisphenol F type epoxy resin, and bisphenol A novolac type epoxy resin, which have high film forming properties and are easily porous, are preferable.

  Curing agents that can be used in the present invention include aromatic amines (for example, metaphenylenediamine, diaminodiphenylmethane, diaminodiphenylsulfone, benzyldimethylamine, dimethylaminomethylbenzene), aromatic acid anhydrides (for example, phthalic anhydride, Aromatic curing agents such as trimellitic anhydride, pyromellitic anhydride, phenol resin, phenol novolac resin, heteroaromatic ring-containing amines (for example, triazine ring-containing amines), aliphatic amines (for example, ethylenediamine, Diethylenetriamine, triethylenetetramine, tetraethylenepentamine, iminobispropylamine, bis (hexamethylene) triamine, 1,3,6-trisaminomethylhexane, polymethylenediamine, trimethylhexamethylenediamine , Polyether diamine, etc.), alicyclic amines (isophorone diamine, menthane diamine, N-aminoethylpiperazine, 3,9-bis (3-aminopropyl) 2,4,8,10-tetraoxaspiro (5, 5) Non-aromatic such as undecane adduct, bis (4-amino-3-methylcyclohexyl) methane, bis (4-aminocyclohexyl) methane and their modified products), aliphatic polyamidoamines composed of polyamines and dimer acids A curing agent is mentioned. In this invention, these 1 type may be used and multiple types may be used. Of these, alicyclic amines, aliphatic amines, and aromatic amines are preferable from the viewpoint of reactivity.

  The porogen that can be used in the present invention refers to a solvent that can dissolve an epoxy resin and a curing agent and can cause reaction-induced phase separation after the epoxy resin and the curing agent are polymerized. Examples include cellosolves such as cellosolve and ethyl cellosolve, esters such as ethylene glycol monomethyl ether acetate and propylene glycol monomethyl ether acetate, and glycols such as polyethylene glycol and polypropylene glycol. Of these, polyethylene glycol and polypropylene glycol are preferred from the viewpoint of phase separation.

  Moreover, even if it is insoluble or hardly soluble at room temperature with each epoxy resin or curing agent, a solvent in which a reaction product of the epoxy resin and the curing agent is soluble can be used as a porogen. Examples of such porogen include brominated bisphenol A type epoxy resin (“Epicoat 5058” manufactured by Japan Epoxy Resin Co., Ltd.).

  In this invention, it is preferable that the addition ratio of the hardening | curing agent with respect to the epoxy resin in a solution has a hardening | curing agent equivalent of 0.6 or more with respect to 1 equivalent of epoxy groups from a viewpoint of film | membrane intensity | strength. Moreover, it is preferable that a hardening | curing agent equivalent is 1.5 or less with respect to 1 equivalent of epoxy groups from a viewpoint of preventing the residue of an unreacted hardening | curing agent. In the present invention, in addition to the curing agent described above, a curing accelerator may be added to the solution in order to obtain the desired porous structure. As the curing accelerator, known ones can be used, for example, tertiary amines such as triethylamine and tributylamine, 2-phenol-4-methylimidazole, 2-ethyl-4-methylimidazole, and 2-phenol. Examples include imidazoles such as -4,5-dihydroxyimidazole.

  The porosity, pore size, pore size distribution, etc. of the epoxy resin porous membrane obtained in the present invention are the types and ratios of the raw materials such as epoxy resin, curing agent, porogen, etc., or heating in the reaction-induced phase separation step described later. Since it varies depending on reaction conditions such as temperature and cooling temperature, it is necessary to create a phase diagram of the system and select the optimum conditions in order to obtain the porosity, pore size, and pore size distribution of the target porous membrane. preferable. In addition, by controlling the molecular weight, molecular weight distribution, system viscosity, crosslinking reaction rate, etc. of the epoxy resin polymer during phase separation, the co-continuous structure of epoxy resin and porogen is fixed in a specific state, and a stable porous structure Can be obtained.

  In the production method of the present invention, in the reaction-induced phase separation step, it is preferable to heat the one sheet material and cool the other sheet material. This is because the temperature difference between the one surface and the other surface can be increased, so that an asymmetric structure can be realized more easily. In this case, it is preferable to perform the heating and cooling so that the temperature difference between the one sheet material and the other sheet material is 10 to 200 ° C. (more preferably, 50 to 150 ° C.). Since the average pore diameter in the vicinity of the other surface can be 2 to 100 times the average pore diameter in the vicinity of the one surface, it is easy to maintain both the amount of permeate and improve the separation performance. This is because it can be realized. In addition, it is preferable that the temperature of a sheet | seat material is made into the average value of the value measured ten places at random.

  In the production method of the present invention, in the reaction-induced phase separation step, the one sheet material is heated to 80 to 160 ° C (preferably 100 to 140 ° C), and the other sheet material is -50 to 80 ° C ( Preferably, it may be cooled to -20 to 10 ° C. By heating the one sheet material at 80 to 160 ° C., the average pore diameter of the pores in the vicinity of the one surface can be set to 0.02 to 0.5 μm, thereby reducing the resistance of the permeate flow. In addition, separation performance can be improved. Further, by cooling the other sheet material to −50 to 80 ° C., the average pore diameter of the pores in the vicinity of the other surface can be set to 0.2 to 5 μm, so that the permeate amount was kept high. In the above, a decrease in film strength can be prevented.

  In the reaction-induced phase separation step, when the one sheet material is heated and the other sheet material is cooled, the heating and cooling treatment time is preferably 10 to 300 minutes, preferably 10 to 60 minutes. It is more preferable that If it is in the said range, after ensuring the intensity | strength of a film | membrane, ensuring of the hole diameter for making the maintenance of a permeate amount and improvement of a separation performance compatible will become easy.

  In the reaction-induced phase separation step, when heating the one sheet material and cooling the other sheet material, after the heating and cooling, the cooling is stopped and only the heating is continued. Is preferred. This is because the vicinity of the other surface can be sufficiently cured, so that it is easy to ensure the strength of the film. In this case, the heating treatment time after stopping the cooling is preferably 0.5 to 5 hours, and more preferably 1 to 3 hours. This is because it is easier to ensure the strength of the film.

  In the manufacturing method of this invention, it is preferable to further include the drying process which further hardens | cures the hardened | cured material from which the porogen was removed after the said removal process. This is because it is easy to ensure the strength of the film because crosslinking with a curing agent can be sufficiently performed. In this case, in the drying step, the cured product is preferably dried at an atmospheric temperature of 50 to 160 ° C. (more preferably 80 to 160 ° C.) for 0.5 to 20 hours (more preferably 1 to 10 hours). . This is because it is easier to ensure the strength of the film.

  In the production method of the present invention, in the filling step, the porogen content in the solution may be 20 to 80% by weight (preferably 55 to 75% by weight). Since the pore diameter and porosity of the obtained membrane can be set to appropriate values, for example, when applied to a support membrane of a composite reverse osmosis membrane, it is easy to maintain the amount of permeate and improve separation performance. is there.

  The sheet material that can be used in the present invention is not particularly limited as long as it can be uniformly heated (or cooled) at the contact interface with the solution and has releasability with respect to the cured epoxy resin. , Sheet materials coated with silicone-based release agents, fluorine-based release agents, hydrocarbon-based release agents, etc., and glass sheets can be used. May be. Of these, a glass sheet is preferable. This is because the glass sheet has high heat resistance, high releasability, and can be recycled, so that the manufacturing cost can be easily reduced. Moreover, when using glycols as a porogen, precipitation of this glycols can be prevented effectively. Note that. The thickness of the sheet material is, for example, 0.1 to 10 mm, and preferably 0.8 to 2.0 mm from the viewpoints of recyclability and handleability.

  In the manufacturing method of this invention, it is preferable that the space | interval of the said pair of sheet material after the said filling process is 0.1-5 mm, and it is more preferable that it is 0.1-0.5 mm. This is because when the thickness is 0.1 mm or more, it is easy to secure the strength of the film, and when the thickness is 5 mm or less, the precipitation of the porogen can be easily prevented. In addition, it is preferable to make the space | interval of a sheet material into the average value of the value measured ten places at random.

  Next, preferred embodiments of the method for producing an epoxy resin porous membrane of the present invention will be described with reference to the drawings. 1A to F to be referred to are schematic process diagrams for explaining an example of the method for producing the porous epoxy resin membrane of the present invention.

  First, the solution 1 (refer FIG. 1A) containing an epoxy resin, a hardening | curing agent, and a porogen is prepared. Although the preparation method is not particularly limited, it is preferable to prepare a solution 1 by dissolving the epoxy resin in the porogen and then adding a curing agent thereto to obtain a uniform solution.

  Next, as shown in FIG. 1A, the solution 1 is filled between a pair of glass sheets 2a and 2b. The filling method is not particularly limited. For example, a spacer (not shown) such as a double-sided tape is provided on the peripheral edge of the glass sheet 2b so that the cured product obtained from the solution 1 can ensure a certain thickness. Then, the solution 1 may be applied to the portion surrounded by the spacer on the glass sheet 2b, and the solution 1 and the glass sheet 2a may be brought into close contact with each other by placing the glass sheet 2a thereon. In the state where the solution 1 is sandwiched between the glass sheets 2a and 2b, the distance S between the glass sheets 2a and 2b is preferably 0.1 to 5 mm as described above, and preferably 0.1 to 0.5 mm. More preferably. That is, it is preferable to adjust the thickness of the spacer so that the distance S between the glass sheets 2a and 2b is within the above range.

  Next, as shown in FIG. 1B, the glass sheet 2b is heated by the hot plate 3, and the tray 5 filled with the refrigerant 4 such as ice water is placed on the glass sheet 2a to cool the glass sheet 2a. Thereby, since the hole diameter of the hole in the vicinity of the film surface 1a on the cooled glass sheet 2a side becomes larger than the hole diameter in the vicinity of the film surface 1b on the heated glass sheet 2b side, A membrane is obtained.

  After performing the heating and cooling for a predetermined time, as shown in FIG. 1C, the tray 5 (see FIG. 1B) is removed to stop the cooling, and only the heating by the hot plate 3 is continued. Thereby, since the hardening of the vicinity of the film surface 1a can fully be performed, it becomes easy to ensure the strength of the film.

  After performing the said heating for predetermined time, as shown to FIG. 1D, the obtained hardened | cured material 6 is released from glass sheet 2a, 2b. At this time, it is preferable to use the glass sheets 2a and 2b as the sheet material as in the present embodiment because the releasability is improved.

  Then, as shown to FIG. 1E, the hardened | cured material 6 is immersed in the water 8 in the water tank 7, and a porogen is removed. As the solvent for removing the porogen, a solvent other than water (for example, DMF, DMSO, THF, etc.) may be used as long as the porogen can be eluted without damaging the membrane.

  And the epoxy resin porous membrane 10 shown to FIG. 1F is obtained by performing the drying process which further hardens | cures the hardened | cured material 6 from which the porogen was removed, and fully performing bridge | crosslinking by a hardening | curing agent.

  As mentioned above, although preferable embodiment of this invention was described, this invention is not limited to the said embodiment. For example, the spacer can be a glass bead having a uniform particle diameter or a metal plate having a uniform thickness. In the reaction-induced phase separation step, it is also possible to provide a difference between the set temperatures of one surface and the other surface using a press. As a cooling method at that time, it is also possible to use cold air. It is also possible to perform the reaction-induced phase separation step in a low temperature atmosphere and heat only one surface with a hot plate or the like. In the porogen removal step, a method of immersing in a solvent or a method of removing by flowing a solvent may be used. At that time, the use of ultrasonic irradiation or the like can remove the porogen more efficiently.

  Examples of the present invention will be described below. In addition, this invention is not limited to a following example.

  An epoxy resin porous membrane was manufactured according to the steps of FIGS. As the epoxy resin, bisphenol A type epoxy resin (“Epicoat 828” manufactured by Japan Epoxy Resin Co., Ltd.) was used. As the curing agent, bis (4-aminocyclohexyl) methane (manufactured by Tokyo Chemical Industry Co., Ltd.) was used. Polyethylene glycol 200 (manufactured by Tokyo Chemical Industry Co., Ltd.) was used, and glass sheets made of soda glass were used as the glass sheets 2a and 2b.

  First, 50 g of porogen was added to 23.3 g of epoxy resin, and this was stirred and dissolved at 2000 rpm for 5 minutes by a rotating / revolving mixer (trade name “Awatori Netaro” ARE-250) to prepare an epoxy resin / porogen solution. Next, 5.2 g of a curing agent was added to the epoxy resin / porogen solution, and this was stirred and dissolved at 2000 rpm for 10 minutes by the autorotation / revolution mixer to prepare Solution 1.

  Next, after two sheets of double-sided tape are laminated and pasted on the peripheral edge of the glass sheet 2b, the solution 1 is applied to the part surrounded by the double-sided tape on the glass sheet 2b, and the glass sheet 2a is applied thereon. The solution 1 and the glass sheet 2a were adhered to each other. In this state, the distance S between the glass sheets 2a and 2b was 800 μm.

  Next, while heating the glass sheet 2b with the hot plate 3 set to 120 degreeC, the tray 5 filled with the refrigerant | coolant 4 (ice water) was set | placed on the glass sheet 2a, and the glass sheet 2a was cooled. Thereby, the glass sheet 2a was cooled to 0.2 degreeC. This state was maintained for about 1 hour, after which the tray 5 was removed, cooling was stopped, and only heating with the hot plate 3 was continued for about 2 hours.

  After performing the said heating, it stood still to room temperature and the obtained hardened | cured material 6 was released from glass sheet 2a, 2b. Subsequently, the cured product 6 was immersed in water 8 overnight to remove the porogen. And the drying process which further hardens | cures the hardened | cured material 6 from which the porogen was removed at 50 degreeC atmospheric temperature for about 4 hours was performed, and the epoxy resin porous membrane 10 with a thickness of 850 micrometers was obtained. Sectional SEM images of the obtained epoxy resin porous membrane 10 are shown in FIGS. 2A is a cross-sectional SEM image in the vicinity of the film surface 1a on the glass sheet 2a side, FIG. 2B is a cross-sectional SEM image of the intermediate layer having a depth of about 400 μm from the film surface 1a, and FIG. It is a cross-sectional SEM image of the vicinity of the film | membrane surface 1b at the side of the sheet | seat 2b. As shown in FIGS. 2A to 2C, a structure was observed in which the pore diameter gradually increased in the thickness direction from the film surface 1b to the film surface 1a. 2A and 2C were measured by the above average pore diameter measurement method, the average pore diameter of the pores shown in FIG. 2A was 5 μm, and the average pore diameter of the pores shown in FIG. 2C was measured. Was 0.5 μm.

A to F are schematic process diagrams for explaining an example of the method for producing the porous epoxy resin membrane of the present invention. AC is a cross-sectional SEM image of the epoxy resin porous membrane of the Example of this invention.

Explanation of symbols

1 Solution 1a, 1b Film surface 2a, 2b Glass sheet 3 Hot plate 4 Refrigerant 5 Tray 6 Cured product 7 Water tank 8 Water 10 Epoxy resin porous film S Interval

Claims (12)

A method for producing an epoxy resin porous membrane having pores communicating with a three-dimensional network skeleton,
A filling step of filling a solution containing an epoxy resin, a curing agent and a porogen between a pair of sheet materials;
A reaction-induced phase separation step of phase-separating the polymer of the epoxy resin and the porogen while polymerizing the epoxy resin by heating only one of the sheet materials;
A method for producing an epoxy resin porous membrane comprising a removing step of removing the porogen from the cured product obtained in the reaction-induced phase separation step. The method for producing a porous epoxy resin membrane according to claim 1 , wherein, in the reaction-induced phase separation step, the one sheet material is heated and the other sheet material is cooled. 3. The epoxy resin porous membrane according to claim 2 , wherein in the reaction-induced phase separation step, the heating and cooling are performed so that a temperature difference between the one sheet material and the other sheet material is 10 to 200 ° C. 4. Manufacturing method. In Reaction-induced phase separation process, and heating the one of the sheet material to 80 to 160 ° C., the epoxy resin porous membrane according to claim 2 or 3 cooling said other sheet material -50～80 ° C. Production method. The method for producing an epoxy resin porous membrane according to any one of claims 2 to 4 , wherein, in the reaction-induced phase separation step, the heating and cooling treatment time is 10 to 300 minutes. The method for producing an epoxy resin porous membrane according to any one of claims 2 to 5 , wherein, in the reaction-induced phase separation step, after the heating and cooling, the cooling is stopped and only the heating is continued. . The method for producing an epoxy resin porous membrane according to claim 6 , wherein the heating treatment time after the cooling is stopped is 0.5 to 5 hours. After the removing step, the production method of the epoxy resin porous membrane according to any one of claims 1 to 7, wherein the porogen further comprises a drying step to further cure the cured product is removed. The method for producing an epoxy resin porous membrane according to claim 8 , wherein in the drying step, the cured product is dried at an atmospheric temperature of 50 to 160 ° C. for 0.5 to 20 hours. In the filling step, the production method of the epoxy resin porous membrane according to any one of the solution ~ claim 1, wherein the content of the said porogen is 20 to 80 wt% of 9. The method for producing a porous epoxy resin membrane according to any one of claims 1 to 10 , wherein the sheet material is a glass sheet. The method for producing an epoxy resin porous membrane according to any one of claims 1 to 11 , wherein an interval between the pair of sheet materials after the filling step is 0.1 to 5 mm.

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