Microporous hydrophilic membrane
A hydrophilic microporous membrane comprising a thermoplastic resin, having been subjected to hydrophilizing treatment and having a maximum pore size of 0 to 100 nm, wherein when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa, an average permeation rate (liter/m 2 /h) for 5 minutes from the start of filtration (briefly referred to as globulin permeation rate A) satisfies the following formula (1) and an average permeation rate (liter/m 2 /h) for 5 minutes from the time point of 55 minutes after the start of filtration (briefly referred to as globulin permeation rate B) satisfies the following formula (2): Globulin permeation rate A >0.0015 ×maximum pore size (nm) 2.75 (1) Globulin permeation rate B /globulin permeation rate A >0.2 . (2)
1. A hydrophilic microporous membrane comprising a thermoplastic resin, having been contacted with a hydrophilic vinyl monomer having one vinyl group after generation of radicals by irradiation with ionizing radiation in order to be subjected to hydrophilizing treatment by a graft polymerization reaction, and having a maximum pore size of 10 to 100 nm,
wherein said hydrophilic microporous membrane has a coarse structure layer with a higher open pore ratio and a fine structure layer with a lower open pore ratio which are formed in one piece, wherein said coarse structure layer exists on at least one side of the membrane surface and has a thickness of 2 μm or more and a thickness of said fine structure layer is 50% or more of the whole membrane thickness,
wherein when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa, an average globulin permeation rate A (liter/m 2 /h) for 5 minutes from the start of filtration satisfies the following formula (1) and an average globulin permeation rate B (liter/m 2 /h) for 5 minutes from the time point of 55 minutes after the start of filtration satisfies the following formula (2):
Globulin permeation rate A>0.0015 maximum pore size (nm) 2.75 (1)
Globulin permeation rate B /globulin permeation rate A >0.2 (2).
2. The hydrophilic microporous membrane according to claim 1 having a maximum pore size of 10 to 70 nm.
3. The hydrophilic microporous membrane according to claim 2 having a receding contact angle of water of 0 to 20 degrees.
4. The hydrophilic microporous membrane according to claim 1 having a maximum pore size of 10 to 36 nm.
5. The hydrophilic microporous membrane according to claim 4 having a receding contact angle of water of 0 to 20 degrees.
6. The hydrophilic microporous membrane according to claim 4 , wherein an accumulated permeation volume in three hours after the start of filtration is 50 liter/m 2 or more when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa.
7. The hydrophilic microporous membrane according to claim 1 having a receding contact angle of water of 0 to 20 degrees.
8. The hydrophilic microporous membrane according to claim 1 , wherein a logarithmic reduction value of porcine parvovirus at the time point by which 55 liter/m 2 has been permeated from the start of filtration is 3 or more.
9. The hydrophilic microporous membrane according to claim 1 , wherein both of a logarithmic reduction value of porcine parvovirus at the time point by which 5 liter/m 2 has been permeated from the start of filtration and a logarithmic reduction value of porcine parvovirus at the time point by which further 5 liter/m 2 has been permeated after 50 liter/m 2 is permeated are 3 or more.
10. The hydrophilic microporous membrane according to claim 9 , wherein an accumulated permeation volume in three hours after the start of filtration is 50 liter/m 2 or more when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa.
11. The hydrophilic microporous membrane according to claim 1 , wherein an accumulated permeation volume in three hours after the start of filtration is 50 liter/m 2 or more when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa.
12. The hydrophilic microporous membrane according to claim 1 , wherein the thickness of the coarse structure layer is 3 μm or more.
13. The hydrophilic microporous membrane according to claim 1 , wherein the thickness of the coarse structure layer is 5 μm or more.
14. The hydrophilic microporous membrane according to claim 1 , wherein the thermoplastic resin is polyvinylidene fluoride.
15. The hydrophilic microporous membrane according to claim 1 , wherein the hydrophilizing treatment is a graft polymerization reaction of a hydrophilic vinyl monomer having one vinyl group to the surface of the pores of the hydrophilic microporous membrane.
16. The hydrophilic microporous membrane according to claim 15 , wherein the hydrophilic vinyl monomer contains a hydroxyl group.
17. The hydrophilic microporous membrane according to claim 1 , wherein the adsorption amount per 1 g of the membrane is 3 mg or less when dead-end filtration at a constant pressure of 0.3 MPa is performed using a 0.01 wt % bovine immunoglobulin solution and a filtrate of 50 liter/m 2 from the start of filtration is collected.
18. A method for removing a virus from a liquid containing a physiologically active substance, comprising filtering the liquid through the hydrophilic microporous membrane according to claim 1 .