Patent Application
20210040430
The present invention relates to a cell culture module.
In recent years, proteins such as enzymes, hormones, antibodies, cytokines, viruses (viral proteins) used for treatment and vaccine are industrially produced using cultured cells. However, such a protein production technology is expensive, raising medical cost. Accordingly, there have been demands for innovating technologies for culturing cells at high density and for increasing protein production, aiming at great reduction of cost.
As cells for protein production, anchorage-dependent adherent cells which adhere to a culture substrate may be sometimes used. Since such cells grow anchorage-dependently, they need to be cultured while being adhered onto the surface of a dish, plate or chamber. Conventionally, in order to culture such adherent cells in a large amount, it was preferable to increase the surface area to be adhered. However, increasing the culturing area inevitably requires to increase the space, which is responsible for increase in cost.
As a method to culture a large amount of adherent cells while decreasing the culture space, a method for culture using a microporous carrier, especially a microcarrier, has been developed (for example, PTL 1). In a cell culturing system using microcarriers, it is preferable to carry out sufficient stirring and diffusion so that the microcarriers do not aggregate together. Since this requires a volume allowing adequate agitation and diffusion of the medium in which the microcarriers are dispersed, there is an upper limit to the density at which the cells can be cultured. In order to separate the microcarrier from the medium, separation is preferably performed using a filter which can separate fine particles, possibly resulting in increased cost. Considering the foregoing, there is a demand for innovative methodology for cell culture which cultures cells at high density.
Porous polyimide films have been utilized in the prior art for filters and low permittivity films, and especially for battery-related purposes, such as fuel cell electrolyte membrane and the like. PTLs 2 to 4 describe porous polyimide films with numerous macrovoids, having excellent permeability to objects such as gases, high porosity, excellent smoothness on both surfaces, relatively high strength and, despite high porosity, excellent resistance against compression stress in the film thickness direction. All of these are porous polyimide films formed via amic acid.
The cell culture method which includes applying cells to a porous polyimide film and culturing them is reported (PTL 5).
In the case of shaking culture or stirring culture of cells using a plurality of porous polyimide films in one culture vessel or bag, respective forces received by the porous polyimide films are different in the vessel or bag. Accordingly, it has been difficult to perform cell culture for all the porous polyimide films under homogeneous conditions. In addition, in the case of shaking culture or stirring culture using porous polyimide films, it has been difficult to perform stable cell culture since stress is applied to cells growing in the films due to the continuous deformation of the shapes of the films, and the cells die.
Accordingly, it is an object of the present invention to provide means with which it is possible to apply a homogeneous culture condition to a plurality of porous polymer films and to stably culture a large amount of cells.
As a result of intensive examination in light of the problems described above, the present inventors found that it is possible to stably culture a large amount of cells by using a module including a plurality of porous polymer films and having a specific tertiary structure, and thus accomplished the present invention.
The present invention includes the following <1> to <15>.
<1>
A cell culture module comprising:
an apex part;
a bottom part;
a side part comprising a culture medium flow inlet;
a plurality of partition parts that partition a space formed by the apex part, the bottom part, and the side part, and comprise a culture medium flow inlet; and
a porous polymer film fixed to each of two or more gap spaces selected from a gap space between the apex part and a partition part adjacent thereto, a gap space between the bottom part and a partition part adjacent thereto, and a plurality of gap spaces between partition parts adjacent to each other,
wherein the porous polymer film is a porous polymer film with a three-layer structure, comprising a surface layer A and a surface layer B including a plurality of pores, as well as a macrovoid layer sandwiched between the surface layer A and the surface layer B, an average pore diameter of the pores present in the surface layer A is smaller than an average pore diameter of the pores present in the surface layer B, the macrovoid layer comprises a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by the partition wall and the surface layers A and B, and the pores in the surface layers A and B communicate with the macrovoids.
<2>
The cell culture module according to <1>, wherein at least one of gap spaces adjacent to the gap space to which the porous polymer film is fixed does not comprise a porous polymer film.
<3>
The cell culture module according to <1> or <2>, wherein 3 to 100 porous polymer films are layered and placed on each of the two or more gap spaces selected from the gap space between the apex part and the partition part adjacent thereto, the gap space between the bottom part and the partition part adjacent thereto, and the plurality of gap spaces between the partition parts adjacent to each other.
<4>
The cell culture module according to any one of <1> to <3>, wherein the porous polymer film is a porous polyimide film.
<5>
The cell culture module according to any one of <1> to <3>, wherein the porous polymer film is a porous polyethersulfone film.
<6>
The cell culture module according to any one of <1> to <5>, wherein the apex part and the bottom part comprise a culture medium flow inlet.
<7>
The cell culture module according to any one of <1> to <6>, comprising a rectangular parallelepiped shape.
<8>
The cell culture module according to any one of <1> to <6>, comprising a cube shape.
<9>
The cell culture module according to any one of <1> to <6>, comprising an ovoid shape.
<10>
A cell culture module complex, wherein the plurality of cell culture modules according to <7> or <8>are connected.
<11>
A cell culture module comprising:
a plurality of cell culture submodules; and
a casing for containing a cell culture submodule, which is used for layering and containing the plurality of cell culture submodules and comprises a culture medium flow inlet,
wherein the cell culture submodules comprise:
a porous polymer film; and
a casing for containing a porous polymer film, comprising a culture medium flow inlet, wherein the porous polymer film is fixed and contained, and
wherein the porous polymer film is a porous polymer film with a three-layer structure, comprising a surface layer A and a surface layer B including a plurality of pores, as well as a macrovoid layer sandwiched between the surface layer A and the surface layer B, an average pore diameter of the pores present in the surface layer A is smaller than an average pore diameter of the pores present in the surface layer B, the macrovoid layer comprises a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by the partition wall and the surface layers A and B, and the pores in the surface layers A and B communicate with the macrovoids.
<12>
The cell culture module according to <11>, further comprising a gap space between the plurality of layered cell culture submodules and the casing for containing a cell culture submodule.
<13>
The cell culture module according to <11> or <12>, wherein 3 to 100 porous polymer films are layered and contained in the casing for containing a porous polymer film.
<14>
The cell culture module according to any one of <11> to <13>, wherein the porous polymer film is a porous polyimide film.
<15>
The cell culture module according to any one of <11> to <13>, wherein the porous polymer film is a porous polyethersulfone film.
In accordance with the present invention, it is possible to apply a homogeneous culture condition to a plurality of porous polymer films, and to stably culture a large amount of cells.
Embodiments of the present invention will be described below with reference to the drawings as needed. The configurations of the embodiments are illustrative, and the constitution of the present invention is not limited to the specific configurations of the embodiments.
An average pore diameter of the pore present on a surface layer A (hereinafter referred to as “surface A” or “mesh surface”) in the porous polymer film used for the present invention is not particularly limited, but is, for example, 0.01 μm or more and less than 200 μm, 0.01 to 150 μm, 0.01 to 100 μm, 0.01 to 50 μm, 0.01 to 40 μm, 0.01 to 30 μm, 0.01 to 25 μm, 0.01 to 20 μm, or 0.01 to 15 μm, preferably 0.01 to 25 μm.
The average pore diameter of the pore present on a surface layer B (hereinafter referred to as “surface B” or “large pore surface”) in the porous polymer film used for the present invention is not particularly limited so long as it is larger than the average pore diameter of the pore present on the surface A, but is, for example, greater than 5 μm and 200 μm or less, 20 μm to 100 μm, 25 μm to 100 μm, 30 μm to 100 μm, 35 μm to 100 μm, 40 μm to 100 μm, 50 μm to 100 μm, or 60 μm to 100 μm, preferably 30 μm to 100 μm.
In this specification, the average pore diameter on the surface of the porous polymer film is the area average pore diameter. The area average pore diameter can be determined according to the following (1) and (2). Incidentally, the average pore diameter of the portion other than the surface of the porous polymer film can be similarly determined.
(1) From the scanning electron micrograph of the surface of the porous film, the pore area S is measured for 200 or more open pore portions, and each pore diameter d is calculated from the following Equation I assuming the pore shape as a perfect circle.
Pore Diametrer d=2×√{square root over ((S/π))} Equation I
(2) All the pore diameters obtained by the above Equation I are applied to the following Equation II to determine the area average pore diameter da when the shape of the pores is a perfect circle.
Area Average pore Diameter da=π(d3)/Σ(d2) Equation II
The thicknesses of the surface layers A and B are not particularly limited, but is, for example, 0.01 to 50 μm, preferably 0.01 to 20 μm.
The average pore diameter of macrovoids in the planar direction of the film in the macrovoid layer in the porous polymer film is not particularly limited but is, for example, 10 to 500 μm, preferably 10 to 100 μm, and more preferably 10 to 80 μm. The thicknesses of the partition wall in the macrovoid layer are not particularly limited, but is, for example, 0.01 to 50 μm, preferably 0.01 to 20 μm. In an embodiment, at least one partition wall in the macrovoid layer has one or two or more pores connecting the neighboring macrovoids and having the average pore diameter of 0.01 to 100 μm, preferably 0.01 to 50 μm. In another embodiment, the partition wall in the macrovoid layer has no pore.
The total film thickness of the porous polymer film used for the invention is not particularly limited, but may be 5 μm or more, 10 μm or more, 20 μm or more or 25 μm or more, and 500 μm or less, 300 μm or less, 100 μm or less, 75 μm or less, or 50 μm or less. It is preferably 5 to 500 μm, and more preferably 25 to 75 μm.
The film thickness of the porous polymer film used for the invention can be measured using a contact thickness gauge.
The porosity of the porous polymer film used in the present invention is not particularly limited but is, for example, 40% or more and less than 95%.
The porosity of the porous polymer film used for the invention can be determined by measuring the film thickness and mass of the porous film cut out to a prescribed size, and performing calculation from the basis weight according to the following Equation III.
Porosity %=(1−w/(S×d×D))×100 Equation III
(wherein S represents the area of the porous film, d represents the total film thickness, w represents the measured mass, and D represents the polymer density. The density is defined as 1.34 g/cm3 when the polymer is a polyimide.)
The porous polymer film used for the present invention is preferably a porous polymer film which includes a three-layer structure porous polymer film having a surface layer A and a surface layer B, the surface layers having a plurality of pores, and a macrovoid layer sandwiched between the surface layers A and B; wherein the average pore diameter of the pore present on the surface layer A is 0.01 μm to 25 μm, and the average pore diameter of the pore present on the surface layer B is 30 μm to 100 μm; wherein the macrovoid layer has a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by such a partition wall and the surface layers A and B, the thickness of the macrovoid layer, and the surface layers A and B is 0.01 to 20 μm; wherein the pores on the surface layers A and B communicate with the macrovoid, the total film thickness is 5 to 500 μm, and the porosity is 40% or more and less than 95%. In an embodiment, at least one partition wall in the macrovoide layer has one or two or more pores connecting the neighboring macrovoids with each other and having the average pore diameter of 0.01 to 100 μm, preferably 0.01 to 50 μm. In another embodiment, the partition wall does not have such pores.
The porous polymer film used for the present invention is preferably sterilized. The sterilization treatment is not particularly limited, but any sterilization treatment such as dry heat sterilization, steam sterilization, sterilization with a disinfectant such as ethanol, electromagnetic wave sterilization such as ultraviolet rays or gamma rays, and the like can be mentioned.
The porous polymer film used for the present invention is not particularly limited so long as it has the structural features described above and includes, preferably a porous polyimide film or porous polyethersulfone film (PES).
Polyimide is a general term for polymers containing imide bonds in the repeating unit, and usually it refers to an aromatic polyimide in which aromatic compounds are directly linked by imide bonds. An aromatic polyimide has an aromatic-aromatic conjugated structure via an imide bond, and therefore has a strong rigid molecular structure, and since the imide bonds provide powerful intermolecular force, it has very high levels of thermal, mechanical and chemical properties.
The porous polyimide film usable for the present invention is a porous polyimide film preferably containing polyimide (as a main component) obtained from tetracarboxylic dianhydride and diamine, more preferably a porous polyimide film composed of tetracarboxylic dianhydride and diamine. The phrase “including as the main component” means that it essentially contains no components other than the polyimide obtained from a tetracarboxylic dianhydride and a diamine, as constituent components of the porous polyimide film, or that it may contain them but they are additional components that do not affect the properties of the polyimide obtained from the tetracarboxylic dianhydride and diamine.
In an embodiment, the porous polyimide film usable for the present invention includes a colored porous polyimide film obtained by forming a polyamic acid solution composition including a polyamic acid solution obtained from a tetracarboxylic acid component and a diamine component, and a coloring precursor, and then heat treating it at 250° C. or higher.
A polyamic acid is obtained by polymerization of a tetracarboxylic acid component and a diamine component. A polyamic acid is a polyimide precursor that can be cyclized to a polyimide by thermal imidization or chemical imidization.
The polyamic acid used may be any one that does not have an effect on the invention, even if a portion of the amic acid is imidized. Specifically, the polyamic acid may be partially thermally imidized or chemically imidized.
When the polyamic acid is to be thermally imidized, there may be added to the polyamic acid solution, if necessary, an imidization catalyst, an organic phosphorus-containing compound, or fine particles such as inorganic fine particles or organic fine particles. In addition, when the polyamic acid is to be chemically imidized, there may be added to the polyamic acid solution, if necessary, a chemical imidization agent, a dehydrating agent, or fine particles such as inorganic fine particles or organic fine particles. Even if such components are added to the polyamic acid solution, they are preferably added under conditions that do not cause precipitation of the coloring precursor.
In this specification, a “coloring precursor” is a precursor that generates a colored substance by partial or total carbonization under heat treatment at 250° C. or higher.
Coloring precursors usable for the production of the porous polyimide film are preferably uniformly dissolved or dispersed in a polyamic acid solution or polyimide solution and subjected to thermal decomposition by heat treatment at 250° C. or higher, preferably 260° C. or higher, even more preferably 280° C. or higher and more preferably 300° C. or higher, and preferably heat treatment in the presence of oxygen such as air, at 250° C., preferably 260° C. or higher, even more preferably 280° C. or higher and more preferably 300° C. or higher, for carbonization to produce a colored substance, more preferably producing a black colored substance, with carbon-based coloring precursors being most preferred.
The coloring precursor, when being heated, first appears as a carbonized compound, but compositionally it contains other elements in addition to carbon, and also includes layered structures, aromatic crosslinked structures and tetrahedron carbon-containing disordered structures.
Carbon-based coloring precursors are not particularly restricted, and for example, they include tar or pitch such as petroleum tar, petroleum pitch, coal tar and coal pitch, coke, polymers obtained from acrylonitrile-containing monomers, ferrocene compounds (ferrocene and ferrocene derivatives), and the like. Of these, polymers obtained from acrylonitrile-containing monomers and/or ferrocene compounds are preferred, with polyacrylonitrile being preferred as a polymer obtained from an acrylonitrile-containing monomer.
Moreover, in another embodiment, examples of the porous polyimide film which may be used for the preset invention also include a porous polyimide film which can be obtained by molding a polyamic acid solution derived from a tetracarboxylic acid component and a diamine component followed by heat treatment without using the coloring precursor.
The porous polyimide film produced without using the coloring precursor may be produced, for example, by casting a polyamic acid solution into a film, the polyamic acid solution being composed of 3 to 60% by mass of polyamic acid having an intrinsic viscosity number of 1.0 to 3.0 and 40 to 97% by mass of an organic polar solvent, immersing or contacting in a coagulating solvent containing water as an essential component, and imidating the porous film of the polyamic acid by heat treatment. In this method, the coagulating solvent containing water as an essential component may be water, or a mixed solution containing 5% by mass or more and less than 100% by mass of water and more than 0% by mass and 95% by mass or less of an organic polar solvent. Further, after the imidation, one surface of the resulting porous polyimide film may be subjected to plasma treatment.
The tetracarboxylic dianhydride which may be used for the production of the porous polyimide film may be any tetracarboxylic dianhydride, selected as appropriate according to the properties desired. Specific examples of tetracarboxylic dianhydrides include biphenyltetracarboxylic dianhydrides such as pyromellitic dianhydride, 3,3′,4,4′-biphenyltetracarboxylic dianhydride (s-BPDA) and 2,3,3′,4′-biphenyltetracarboxylic dianhydride (a-BPDA), oxydiphthalic dianhydride, diphenylsulfone-3,4,3′,4′-tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)sulfide dianhydride, 2,2-bis(3,4-dicarboxyphenyl)-1,1,1,3,3,3-hexafluoropropane dianhydride, 2,3,3′,4′-benzophenonetetracarboxylic dianhydride, 3,3′,4,4′-benzophenonetetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)methane dianhydride, 2,2-bis(3,4-dicarboxyphenyl)propane dianhydride, p-phenylenebis(trimellitic acid monoester acid anhydride), p-biphenylenebis(trimellitic acid monoester acid anhydride), m-terphenyl-3,4,3′,4′-tetracarboxylic dianhydride, p-terphenyl-3,4,3′,4′-tetracarboxylic dianhydride, 1,3-bis(3,4-dicarboxyphenoxy)benzene dianhydride, 1,4-bis(3,4-dicarboxyphenoxy)benzene dianhydride, 1,4-bis(3,4-dicarboxyphenoxy)biphenyl dianhydride, 2,2-bis[(3,4-dicarboxyphenoxy)phenyl]propane dianhydride, 2,3,6,7-naphthalenetetracarboxylic dianhydride, 1,4,5,8-naphthalenetetracarboxylic dianhydride, 4,4′-(2,2-hexafluoroisopropylidene)diphthalic dianhydride, and the like. Also preferably used is an aromatic tetracarboxylic acid such as 2,3,3′,4′-diphenylsulfonetetracarboxylic acid. These may be used alone or in appropriate combinations of two or more.
Particularly preferred among these are at least one type of aromatic tetracarboxylic dianhydride selected from the group consisting of biphenyltetracarboxylic dianhydride and pyromellitic dianhydride. As a biphenyltetracarboxylic dianhydride there may be suitably used 3,3′,4,4′-biphenyltetracarboxylic dianhydride.
As diamine which may be used for the production of the porous polyimide film, any diamine may be used. Specific examples of diamines include the following.
1) Benzenediamines with one benzene nucleus, such as 1,4-diaminobenzene(paraphenylenediamine), 1,3-diaminobenzene, 2,4-diaminotoluene and 2,6-diaminotoluene;
2) diamines with two benzene nuclei, including diaminodiphenyl ethers such as 4,4′-diaminodiphenyl ether and 3,4′-diaminodiphenyl ether, and 4,4′-diaminodiphenylmethane, 3,3′-dimethyl-4,4′-diaminobiphenyl, 2,2′-dimethyl-4,4′-diaminobiphenyl, 2,2′-bis(trifluoromethyl)-4,4′-diaminobiphenyl, 3,3′-dimethyl-4,4′-diaminodiphenylmethane, 3,3′-dicarboxy-4,4′-diaminodiphenylmethane, 3,3′,5,5′-tetramethyl-4,4′-diaminodiphenylmethane, bis(4-aminophenyl)sulfide, 4,4′-diaminobenzanilide, 3,3′-dichlorobenzidine, 3,3′-dimethylbenzidine, 2,2′-dimethylbenzidine, 3,3′-dimethoxybenzidine, 2,2′-dimethoxybenzidine, 3,3′-diaminodiphenyl ether, 3,4′-diaminodiphenyl ether, 4,4′-diaminodiphenyl ether, 3,3′-diaminodiphenyl sulfide, 3,4′-diaminodiphenyl sulfide, 4,4′-diaminodiphenyl sulfide, 3,3′-diaminodiphenylsulfone, 3,4′-diaminodiphenylsulfone, 4,4′-diaminodiphenylsulfone, 3,3′-diaminobenzophenone, 3,3′-diamino-4,4′-dichlorobenzophenone, 3,3′-diamino-4,4′-dimethoxybenzophenone, 3,3′-diaminodiphenylmethane, 3,4′-diaminodiphenylmethane, 4,4′-diaminodiphenylmethane, 2,2-bis(3-aminophenyl)propane, 2,2-bis(4-aminophenyl)propane, 2,2-bis(3-aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 2,2-bis(4-aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 3,3′-diaminodiphenyl sulfoxide, 3,4′-diaminodiphenyl sulfoxide and 4,4′-diaminodiphenyl sulfoxide;
3) diamines with three benzene nuclei, including 1,3-bis(3-aminophenyl)benzene, 1,3-bis(4-aminophenyl)benzene, 1,4-bis(3-aminophenyl)benzene, 1,4-bis(4-aminophenyl)benzene, 1,3-bis(4-aminophenoxy)benzene, 1,4-bis(3-aminophenoxy)benzene, 1,4-bis(4-aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)-4-trifluoromethylbenzene, 3,3′-diamino-4-(4-phenyl)phenoxybenzophenone, 3,3′-diamino-4,4′-di(4-phenylphenoxy)benzophenone, 1,3-bis(3-aminophenyl sulfide)benzene, 1,3-bis(4-aminophenyl sulfide)benzene, 1,4-bis(4-aminophenyl sulfide)benzene, 1,3-bis(3-aminophenylsulfone)benzene, 1,3-bis(4-aminophenylsulfone)benzene, 1,4-bis(4-aminophenylsulfone)benzene, 1,3-bis[2-(4-aminophenyl)isopropyl]benzene, 1,4-bis[2-(3-aminophenyl)isopropyl]benzene and 1,4-bis[2-(4-aminophenyl)isopropyl]benzene; 4) diamines with four benzene nuclei, including 3,3′-bis(3-aminophenoxy)biphenyl, 3,3′-bis(4-aminophenoxy)biphenyl, 4,4′-bis(3-aminophenoxy)biphenyl, 4,4′-bis(4-aminophenoxy)biphenyl, bis[3-(3-aminophenoxy)phenyl]ether, bis[3-(4-aminophenoxy)phenyl]ether, bis[4-(3-aminophenoxy)phenyl]ether, bis [4-(4-aminophenoxy)phenyl]ether, bis[3-(3-aminophenoxy)phenyl]ketone, bis[3-(4-aminophenoxy)phenyl]ketone, bis[4-(3-aminophenoxy)phenyl]ketone, bis[4-(4-aminophenoxy)phenyl]ketone, bis[3-(3-aminophenoxy)phenyl]sulfide, bis[3-(4-aminophenoxy)phenyl]sulfide, bis[4-(3-aminophenoxy)phenyl]sulfide, bis[4-(4-aminophenoxy)phenyl]sulfide, bis[3-(3-aminophenoxy)phenyl]sulfone, bis[3-(4-aminophenoxy)phenyl]sulfone, bis[4-(3-aminophenoxy)phenyl]sulfone, bis [4-(4-aminophenoxy)phenyl]sulfone, bis[3-(3-aminophenoxy)phenyl]methane, bis[3-(4-aminophenoxy)phenyl]methane, bis[4-(3-aminophenoxy)phenyl]methane, bis[4-(4-aminophenoxy)phenyl]methane, 2,2-bis[3-(3-aminophenoxy)phenyl]propane, 2,2-bis[3-(4-aminophenoxy)phenyl]propane, 2,2-bis[4-(3-aminophenoxy)phenyl]propane, 2,2-bis[4-(4-aminophenoxy)phenyl]propane, 2,2-bis[3-(3-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 2,2-bis[3-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 2,2-bis[4-(3-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane and 2,2-bis[4-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane.
These may be used alone or in mixtures of two or more. The diamine used may be appropriately selected according to the properties desired.
Preferred among these are aromatic diamine compounds, with 3,3′-diaminodiphenyl ether, 3,4′-diaminodiphenyl ether, 4,4′-diaminodiphenyl ether, paraphenylenediamine, 1,3-bis(3-aminophenyl)benzene, 1,3-bis(4-aminophenyl)benzene, 1,4-bis(3-aminophenyl)benzene, 1,4-bis(4-aminophenyl)benzene, 1,3-bis(4-aminophenoxy)benzene and 1,4-bis(3-aminophenoxy)benzene being preferred for use. Particularly preferred is at least one type of diamine selected from the group consisting of benzenediamines, diaminodiphenyl ethers and bis(aminophenoxy)phenyl.
From the viewpoint of heat resistance and dimensional stability under high temperature, the porous polyimide film which may be used for the invention is preferably formed from a polyimide obtained by combination of a tetracarboxylic dianhydride and a diamine, having a glass transition temperature of 240° C. or higher, or without a distinct transition point at 300° C. or higher.
From the viewpoint of heat resistance and dimensional stability under high temperature, the porous polyimide film which may be used for the invention is preferably a porous polyimide film comprising one of the following aromatic polyimides.
(i) An aromatic polyimide comprising at least one tetracarboxylic acid unit selected from the group consisting of biphenyltetracarboxylic acid units and pyromellitic acid units, and an aromatic diamine unit,
(ii) an aromatic polyimide comprising a tetracarboxylic acid unit and at least one type of aromatic diamine unit selected from the group consisting of benzenediamine units, diaminodiphenyl ether units and bis(aminophenoxy)phenyl units, and/or,
(iii) an aromatic polyimide comprising at least one type of tetracarboxylic acid unit selected from the group consisting of biphenyltetracarboxylic acid units and pyromellitic acid units, and at least one type of aromatic diamine unit selected from the group consisting of benzenediamine units, diaminodiphenyl ether units and bis(aminophenoxy)phenyl units.
The porous polyimide film used in the present invention is preferably a three-layer structure porous polyimide film having a surface layer A and a surface layer B, the surface layers having a plurality of pores, and a macrovoid layer sandwiched between the surface layers A and B; wherein an average pore diameter of the pores present in the surface layer A is 0.01 μm to 25 μm, and the mean pore diameter present on the surface layer B is 30 μm to 100 μm; wherein the macrovoid layer has a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by such a partition wall and the surface layers A and B; wherein the thickness of the macrovoid layer, and the surface layers A and B is 0.01 to 20 μm, wherein the pores on the surface layers A and B communicate with the macrovoid, the total film thickness is 5 to 500 μm, and the porosity is 40% or more and less than 95%. In this case, at least one partition wall in the macrovoid layer has one or two or more pores connecting the neighboring macrovoids and having the average pore diameter of 0.01 to 100 μm, preferably 0.01 to 50 μm.
For example, porous polyimide films described in WO2010/038873, Japanese Unexamined Patent Publication (Kokai) No. 2011-219585 or Japanese Unexamined Patent Publication (Kokai) No. 2011-219586 may be used for the present invention.
The porous polyethersulfone film which may be used for the present invention contains polyethersulfone and typically consists substantially of polyethersulfone. Polyethersulfone may be synthesized by the method known to those skilled in the art. For example, it may be produced by a method wherein a dihydric phenol, an alkaline metal compound and a dihalogenodiphenyl compound are subjected to polycondensation reaction in an organic polar solvent, a method wherein an alkaline metal di-salt of a dihydric phenol previously synthesized is subjected to polycondensation reaction dihalogenodiphenyl compound in an organic polar solvent or the like.
Examples of an alkaline metal compound include alkaline metal carbonate, alkaline metal hydroxide, alkaline metal hydride, alkaline metal alkoxide and the like. Particularly, sodium carbonate and potassium carbonate are preferred.
Examples of a dihydric phenol compound include hydroquinone, catechol, resorcin, 4,4′-biphenol, bis(hydroxyphenyl)alkanes (such as 2,2-bis(hydroxyphenyl)propane, and 2,2-bis(hydroxyphenyl)methane), dihydroxydiphenylsulfones, dihydroxydiphenyl ethers, or those mentioned above having at least one hydrogen on the benzene rings thereof substituted with a lower alkyl group such as a methyl group, an ethyl group, or a propyl group, or with a lower alkoxy group such as a methoxy group, or an ethoxy group. As the dihydric phenol compound, two or more of the aforementioned compounds may be mixed and used.
Polyethersulfone may be a commercially available product. Examples of a commercially available product include SUMIKAEXCEL 7600P, SUMIKAEXCEL 5900P (both manufactured by Sumitomo Chemical Company, Limited).
The logarithmic viscosity of the polyethersulfone is preferably 0.5 or more, more preferably 0.55 or more from the viewpoint of favorable formation of a macrovoid of the porous polyethersulfone membrane; and it is preferably 1.0 or less, more preferably 0.9 or less, further preferably 0.8 or less, particularly preferably 0.75 or less from the viewpoint of the easy production of a porous polyethersulfone film.
Further, from the viewpoints of heat resistance and dimensional stability under high temperature, it is preferred that the porous polyethersulfone film or polyethersulfone as a raw material thereof has a glass transition temperature of 200° C. or higher, or that a distinct glass transition temperature is not observed.
The method for producing the porous polyethersulfone film which may be used for the present invention is not particularly limited. For example, the film may be produced by a method including the following steps:
a step in which polyethersulfone solution containing 0.3 to 60% by mass of polyethersulfone having logarithmic viscosity of 0.5 to 1.0 and 40 to 99.7% by mass of an organic polar solvent is casted into a film, immersed in or contacted with a coagulating solvent containing a poor solvent or non-solvent of polyethersulfone to produce a coagulated film having pores; and
a step in which the coagulated film having pores obtained in the above-mentioned step is heat-treated for coarsening of the aforementioned pores to obtain a porous polyethersulfone film;
wherein the heat treatment includes the temperature of the coagulated film having the pores is raised higher than the glass transition temperature of the polyethersulfone, or up to 240° C. or higher.
The porous polyethersulfone film which can be used in the present invention is preferably a porous polyethersulfone film having a surface layer A, a surface layer B, and a macrovoid layer sandwiched between the surface layers A and B,
wherein the macrovoid layer has a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by such a partition wall and the surface layers A and B, the macrovoids having the average pore diameter in the planar direction of the film of 10 to 500 μm;
wherein the thickness of the macrovoid layer is 0.1 to 50 μm,
each of the surface layers A and B has a thickness of 0.1 to 50 μm,
wherein one of the surface layers A and B has a plurality of pores having the average pore diameter of more than 5 μm and 200 μm or less, while the other has a plurality of pores having the average pore diameter of 0.01 μm or more and less than 200 μm,
wherein one of the surface layers A and B has a surface aperture ratio of 15% or more while other has a surface aperture ratio of 10% or more,
wherein the pores of the surface layers A and B communicate with the macrovoids,
wherein the porous polyethersulfone film has total film thickness of 5 to 500 μm and a porosity of 50 to 95%.
In this specification, a “cell culture module” refers to a cell culture substrate applicable to a cell culture vessel and a cell culture device.
A cell culture vessel and a cell culture device in which the cell culture module of the present invention can be used are not particularly limited, but, for example, the cell culture module can be used in a cell culture vessel and a cell culture device which are commercially available. For example, the cell culture module can be used in a culture device including a culture vessel composed of a flexible bag, and can be used in the state of floating in the culture vessel. In addition, for example, it is possible to apply the cell culture module to a stirring culture type vessel such as a spinner flask, and to culture cells. In addition, as for a culture vessel, it may be applicable to an open vessel and a closed vessel. For example, any of a petri dish, a flask, plastic bag, a test tube, and a large tank for cell culture may be used, as appropriate. These include, for example, Cell Culture Dish manufactured by BD Falcon, and Nunc Cell Factory manufactured by Thermo Scientific. A sterilized bottle, for example, a simple columnar vessel such as a storage bottle manufactured by Coming, Inc. can also be efficiently used as a culture vessel by using a shaking device such as an orbital shaker or a program shaker. Similarly, use of a shaker enables a petri dish or a flask to be used as a culture vessel.
It is preferred that the configuration member of the cell culture module of the present invention, except the porous polymer films, has enough strength not to be deformed by movement of the culture medium under stirring culture, shaking culture conditions, and that the member is formed of a non-flexible material. Moreover, it is preferred that the configuration member is formed of a material which does not affect the growth of cells in cell culture. Examples of such materials include, for example, polymers such as polyolefins (for example, polyethylene and polypropylene), nylon, polyester, polystyrene, polycarbonate, polymethyl methacrylate, and polyethylene terephthalate; and metals such as stainless steel and titanium, but are not limited thereto.
One mode of the cell culture module of the present invention is a cell culture module including:
an apex part;
a bottom part;
a side part including a culture medium flow inlet;
a plurality of partition parts that partition a space formed by the apex part, the bottom part, and the side part, and include a culture medium flow inlet; and
a porous polymer film fixed to each of two or more gap spaces selected from a gap space between the apex part and a partition part adjacent thereto, a gap space between the bottom part and a partition part adjacent thereto, and a plurality of gap spaces between partition parts adjacent to each other,
wherein the porous polymer film is a porous polymer film with a three-layer structure, including a surface layer A and a surface layer B including a plurality of pores, as well as a macrovoid layer sandwiched between the surface layer A and the surface layer B, the average pore diameter of the pores present in the surface layer A is smaller than the average pore diameter of the pores present in the surface layer B, the macrovoid layer includes a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by the partition wall and the surface layers A and B, and the pores in the surface layers A and B communicate with the macrovoids.
Hereinafter, the cell culture module also refers to “cell culture module A”.
A “partition part” in the cell culture module of the present invention is generally planar. An “apex part” in the cell culture module of the present invention is a part present in the uppermost part generally vertical to the extending direction of the partition part, and the shape of the apex part is not particularly limited. A “bottom part” in the cell culture module of the present invention is a part present in the lowermost part generally vertical to the extending direction of the partition part, and the shape of the bottom part is not particularly limited. In the cell culture module of the present invention, a “side part” is a portion, other than the apex part and the bottom part, configuring the periphery of the cell culture module, and the shape of the side part is not particularly limited.
The apex and bottom parts of the cell culture module A may include culture medium flow inlets. The numbers and shapes of the culture medium flow inlets present in the apex and bottom parts are not particularly limited as long as a culture medium is favorably supplied into the interior of the module. Moreover, the sizes thereof are not particularly limited unless cultured cells and the culture medium are prevented from passing. Preferably, each of the apex and bottom parts includes a plurality of culture medium flow inlets.
The side part of the cell culture module A includes culture medium flow inlets. The number and shapes of the culture medium flow inlets present in the side part are not particularly limited as long as a culture medium is favorably supplied into the interior of the module. Moreover, the sizes thereof are not particularly limited unless cultured cells and the culture medium are prevented from passing. Preferably, the side part includes a plurality of culture medium flow inlets.
The number of the partition parts of the cell culture module A is not particularly limited, but is preferably 2 to 50, more preferably 2 to 30, still more preferably 2 to 20, and particularly preferably 2 to 10. The number and shapes of the culture medium flow inlets included in the partition part are not particularly limited unless a culture medium is prevented from favorably moving. Moreover, the sizes thereof are not particularly limited unless cultured cells and the culture medium are prevented from passing.
A method of fixing a porous polymer film to a gap space is not particularly limited. For example, the porous polymer film is fixed by being sandwiched between an apex part and a partition part adjacent thereto, between a bottom part and a partition part adjacent thereto, and between partition parts adjacent to each other. For example, at least one place of the porous polymer film is fixed to at least one place of the apex, bottom, or partition part forming the gap space by an optional method (for example, adhesion with an adhesive, or fixation using a fastener). The fixation of the porous polymer film to the gap space can prevent stress from being applied to cells to be grown in the porous polymer film, resulting in suppression of apoptosis or the like, enabling stable culture of a large amount of cells.
The porous polymer film can be fixed in an optional form to the gap space. In one embodiment, the porous polymer film is a layered body of a plurality of porous polymer films. The layered porous polymer films may be small pieces. The shape of the small pieces may be an optional shape such as, for example, a circular, elliptical, quadrangular, triangular, polygonal, or string shape. Preferably, the small pieces of the layered porous polymer films have a generally square shape. The size of the small pieces may be an optional size. When the small pieces have a generally square shape, the length thereof is not particularly limited but is, for example, 80 mm or less, 50 mm or less, 30 mm or less, 20 mm or less, or 10 mm or less.
When the porous polymer film fixed to the gap space is a layered body of the plural porous polymer films, the layered body is preferably a layered body of two or more, three or more, four or more, or five or more, and 100 or less, 50 or less, 40 or less, 30 or less, 20 or less, 15 or less, or 10 or less porous polymer films, more preferably a layered body of 3 to 100 porous polymer films, and more preferably a layered body of 5 to 50 porous polymer films.
When the porous polymer film fixed to the gap space is a layered body of the plural porous polymer films, insoles may be disposed between the porous polymer films. A culture medium can be efficiently supplied to between the layered porous polymer films by disposing the insoles. The insoles are not particularly limited as long as having the function of forming optional spaces between the layered porous polymer films and efficiently supplying a medium. For example, a planar structure having a mesh structure can be used as such an insole. For example, a mesh made of polystyrene, polycarbonate, polymethyl methacrylate, polyethylene terephthalate, or stainless steel can be used as the material of the insoles. However, the material is not limited thereto. When the insoles having a mesh structure are possessed, openings to such a degree that a culture medium can be supplied to between the layered porous polymer films may be included, and can be selected if appropriate.
In one embodiment, porous polymer films fixed to gap spaces may be processed into a three-dimensional shape rather than a planar shape, and used. For example, the porous polymer films, i) which are folded up, ii) which are wound into a roll-like shape, iii) of which the sheets or small pieces are linked in a thready structure, or iv) which are tied into a rope-like shape, may be used.
The entire shape of the cell culture module A is not particularly limited. Cell culture modules having various entire shapes can be produced by changing the shapes of members configuring apex, bottom, side, and partition parts. From the viewpoint of the easiness of stirring in culture, the easiness of production, or the like, the entire shape of the cell culture module A is preferably an n-prism shape (for example, n=3 to 6), a cylindrical shape, a spheroid shape, an ovoid shape, or a spherical shape, and more preferably a rectangular parallelepiped shape, a cube shape, or an ovoid shape. When cell culture modules have an n-prism shape or a cylindrical shape, the corners of the modules may be chamfered in order to lessen impact at the time of the collision between the modules and to avoid damage to the modules.
Preferably, at least one of gap spaces adjacent to a gap space to which a porous polymer film is fixed does not include a porous polymer film. For example, when a porous polymer film is fixed to a gap space between an apex part a partition part adjacent thereto, there is only one adjacent gap space, and therefore, the space does not include a porous polymer film. For example, when a porous polymer film is fixed to a gap space between a bottom part and a partition part adjacent thereto, there is only one adjacent gap space, and therefore, the space does not include a porous polymer film. For example, when a porous polymer film is fixed to a gap space between partition parts adjacent to each other, there are two gap spaces adjacent to each other, and therefore, neither thereof includes a porous polymer film or either thereof does not include a porous polymer film. A gap space including no porous polymer film functions as a clearance for passage of a culture medium. A culture medium is supplied from a culture medium flow inlet to a clearance for passage of a culture medium, present in the interior of the cell culture module A. The culture medium supplied to the clearance for passage of a culture medium can pass through a culture medium flow inlet present in a partition part and can efficiently come into contact with a porous polymer film.
The cell culture module A may include arrangement means for arranging the apex part, the partition part, and the bottom part at regular spacings in order to dispose gap spaces between the apex part and the partition part adjacent thereto, between the bottom part and the partition part adjacent thereto, and between the partition parts adjacent to each other. The shape of the arrangement means is not particularly limited, but is determined depending on the configuration of the cell culture module, as appropriate. For example, a mount stage of partition parts adjacent to each other, disposed on a partition part, as illustrated in
Mount stages 9 for mounting the adjacent first partition part 5 are disposed on the top surface of the second partition part 6. The mount stages 9 function as arrangement means for arranging the first partition part 5 and the second partition part 6 at a regular spacing. The mount stages 9 allow a gap space in which a porous polymer film is not placed to be formed between the second partition part 6 and the first partition part 5. The gap space functions as a clearance for passage of a culture medium. A culture medium supplied from a culture medium flow inlet present in each of the apex part 2, the bottom part 3, and the side part 4 to the clearance for passage of a culture medium can pass through the culture medium flow inlet 8 present in each of the first partition part 5 and the second partition part 6, and can efficiently come into contact with the porous polymer film layered bodies 7a and 7b. The number, positions, and shapes of the mount stages are not particularly limited. The mount stages may be disposed on the undersurface of the adjacent first partition part 5 rather than on the top surface of the second partition part 6. Moreover, the mount stages may be disposed on the inner wall surface of the side part of the vessel, formed by the bottom part 3 and the side part 4.
When the cell culture module A has a rectangular parallelepiped shape or a cube shape, a plurality of cell culture modules may be linked, resulting in formation of a cell culture module complex.
a bottom part having a culture medium flow inlet;
a side part having a culture medium flow inlet;
five partition parts that partition a space formed by the apex part, the bottom part, and the side part, and have culture medium flow inlets; and
a porous polymer film fixed to each of four gap spaces selected from a gap space between the apex part and a partition part adjacent thereto, a gap space between the bottom part and a partition part adjacent thereto, and a plurality of gap spaces between partition parts adjacent to each other,
wherein at least one of the gap spaces adjacent to the gap space to which the porous polymer film is fixed does not include a porous polymer film.
Accordingly, the cell culture module complex can be regarded as one embodiment of the cell culture module A.
A cell culture module including:
a plurality of cell culture submodules; and
a casing for containing a cell culture submodule, which is used for layering and containing the plurality of cell culture submodules and includes a culture medium flow inlet,
wherein the cell culture submodules include:
a porous polymer film; and
a casing for containing a porous polymer film, including a culture medium flow inlet, wherein the porous polymer film is fixed and contained, and
wherein the porous polymer film is a porous polymer film with a three-layer structure, including a surface layer A and a surface layer B including a plurality of pores, as well as a macrovoid layer sandwiched between the surface layer A and the surface layer B, the average pore diameter of the pores present in the surface layer A is smaller than the average pore diameter of the pores present in the surface layer B, the macrovoid layer includes a partition wall bonded to the surface layers A and B, and a plurality of macrovoids surrounded by the partition wall and the surface layers A and B, and the pores in the surface layers A and B communicate with the macrovoids.
Hereinafter, the cell culture module is also referred to as a “cell culture module B”.
The shape of the membrane-like porous polymer film can be prevented from being continuously deformed because a porous polymer film is fixed and contained in a casing. This can prevent stress from being applied to cells to be grown in the porous polymer film, resulting in suppression of apoptosis or the like, enabling stable culture of a large amount of cells. A method of fixing a porous polymer film into a casing for containing a porous polymer film is not particularly limited. For example, the porous polymer film is fixed by being sandwiched between the apex and bottom parts of the casing. For example, at least one place of the porous polymer film is fixed to at least one place in the casing by an optional method (for example, adhesion with an adhesive, or fixation using a fastener).
The shape of the porous polymer film contained in the casing is not particularly limited. In one embodiment, the porous polymer film is a layered body of a plurality of porous polymer films. The layered porous polymer films may be small pieces. The shape of the small pieces may be an optional shape such as, for example, a circular, elliptical, quadrangular, triangular, polygonal, or string shape. Preferably, the small pieces of the layered porous polymer films have a generally square shape. The size of the small pieces may be an optional size. When the small pieces have a generally square shape, the length thereof is not particularly limited but is, for example, 80 mm or less, 50 mm or less, 30 mm or less, 20 mm or less, or 10 mm or less.
When the porous polymer film contained in the casing is a layered body of the plural porous polymer films, the layered body is preferably a layered body of two or more, three or more, four or more, or five or more, and 100 or less, 50 or less, 40 or less, 30 or less, 20 or less, 15 or less, or 10 or less porous polymer films, more preferably a layered body of 3 to 100 porous polymer films, and particularly preferably a layered body of 5 to 50 porous polymer films. In the layered body, insoles may be disposed between the porous polymer films. A culture medium can be efficiently supplied to between the layered porous polymer films by disposing the insoles. The insoles are not particularly limited as long as having the function of forming optional spaces between the layered porous polymer films and efficiently supplying a medium. For example, a planar structure having a mesh structure can be used as such an insole. For example, a mesh made of polystyrene, polycarbonate, polymethyl methacrylate, polyethylene terephthalate, or stainless steel can be used as the material of the insoles. However, the material is not limited thereto. When the insoles having a mesh structure are possessed, openings to such a degree that a culture medium can be supplied to between the layered porous polymer films may be included, and can be selected if appropriate.
In one embodiment, porous polymer films contained in a casing may be processed into a three-dimensional shape rather than a planar shape, and used. For example, the porous polymer films, i) which are folded up, ii) which are wound into a roll-like shape, iii) of which the sheets or small pieces are linked in a thready structure, or iv) which are tied into a rope-like shape, may be used.
The casing for containing a porous polymer film, which contains a porous polymer film, includes culture medium flow inlets. A cell culture medium is supplied into the interior of the casing, and discharged to the exterior thereof through the flow inlets. The number and shapes of the culture medium flow inlets are not particularly limited. Moreover, the sizes thereof are not particularly limited unless cultured cells and the culture medium are prevented from passing.
The culture medium flow inlets in the casing for containing a porous polymer film may have a mesh-like structure. Moreover, the casing itself containing a porous polymer film may have a mesh shape. Examples of the structure having a mesh shape include, but are not limited to, those having structures having longitudinal, transverse, and/or oblique grating patterns wherein each opening forms a culture medium flow inlet which allows the fluid to pass therethrough.
In the cell culture module B, a plurality of cell culture submodules are contained in a casing for containing a cell culture submodule. The number of the layered cell culture submodules is preferably 2 or more, 3 or more, 4 or more, or 5 or more, and 30 or less, 15 or less, or 10 or less, more preferably 2 to 15, particularly preferably 3 to 10.
The casing for containing a cell culture submodule includes culture medium flow inlets. A cell culture medium is supplied into the interior of the casing, and discharged to the exterior thereof through the flow inlets. The number and shapes of the culture medium flow inlets are not particularly limited. Moreover, the sizes thereof are not particularly limited unless cultured cells and the culture medium are prevented from passing. Preferably, the casing for containing a cell culture submodule includes a plurality of culture medium flow inlets.
The cell culture module B preferably includes gap spaces between the plurality of layered cell culture submodules and the casing for containing a cell culture submodule. The gap spaces function as clearances for passage of a culture medium. A culture medium is supplied from the culture medium flow inlets present in the casing for containing a cell culture submodule to the clearances for passage of a culture medium, present in the interior of the cell culture module B.
The culture medium supplied to the clearances for passage of a culture medium can pass through the culture medium flow inlets present in the casing for containing a porous polymer film and can efficiently come into contact with the porous polymer films.
The cell culture module of the present invention illustrated in
All documents mentioned in this specification are incorporated herein by reference in their entirety.
Examples of the present invention described below are only for illustration, and are not intended to limit the technical scope of the present invention. The technical scope of the present invention is limited only by the descriptions of claims. Change of the present invention, for example, addition, deletion, and substitution of a constituent feature of the present invention can be made without departing from the gist of the present invention.
The porous polyimide film used in the following examples and comparative examples was prepared by forming a polyamic acid solution composition including a polyamic acid solution obtained from 3,3′,4,4′-biphenyltetracarboxylic dianhydride (s-BPDA) as a tetracarboxylic acid component and 4,4′-diaminodiphenyl ether (ODA) as a diamine component, and polyacrylamide as a coloring precursor, and performing heat treatment at 250° C. or higher. The resulting porous polyimide film was a three-layer structure porous polyimide film having a surface layer A and a surface layer B, the surface layers having a plurality of pores, and a macrovoid layer sandwiched between the surface layers A and B; wherein the average pore diameter of the pore present on the surface layer A was 19 um, the average pore diameter of the pore present on the surface layer B was 42 um, and the film thickness was 25 um, and the porosity was 74%.
Cell Culture Using Cell Culture Module Complex 10
Cell culture was performed using a cell culture module complex 10 illustrated in
Conditioned/suspended anti-human IL-8 antibody producing CHO-DP12 cells (ATCC CRL-12445) were float-cultured in a medium (BalanCD (Trademark) CHO Growth A) and culture was continued until viable cell count per mL was 3.51×106 cells/mL (total cell number of 3.83×106 cells/mL, viable cell rate of 92%).
The three cell culture module complexes 10 were added into a bottle type sterilized vessel (manufactured by Corning, Inc.) having an internal volume of 150 mL, 53.3 mL of a medium for culturing a CHO cell monolayer KBM270 (manufactured by Kohjin Bio Co., Ltd.) was added into the bottle type sterilized vessel, and the three cell culture module complexes 10 were immersed in the medium at a shaking rate of 35 rpm for 10 minutes in a CO2 incubator using a program shaker (manufactured by KENIS LIMITED). A liquid mixture of 4.0 mL of CHO DP-12 floating cell culture medium (total cell number of 3.83×106 cells/mL, viable cell count of 3.51×106 cells/mL, dead cell count of 3.23×105 cells/mL, and viable cell rate of 92%) and 22.6 mL of medium for floating cells (BalanCD (Trademark) CHO Growth A) was added, and cells were adsorbed for about 14 hours using a program shaker (manufactured by KENIS LIMITED) under a rotational condition of 35 rpm (expected average viable cell adsorption number of 5.30×104 cells per sheet). The cell adsorption ratio calculated from the collected medium was 95%.
Then, the medium was removed, 40 mL of a medium for culturing a CHO cell monolayer KBM270 (manufactured by Kohjin Bio Co., Ltd.) was added, and culture was started. Three days after the start of the culture, the vessel was transferred to an electromagnetic orbital shaker (for a CO2 incubator, manufactured by AS ONE Corporation), and the culture was continued at a shaking rate of 200 rpm. Medium replacement was performed every day, and the amounts of consumed glucose, produced lactic acid, lactate dehydrogenase, and produced antibody per day in the medium were measured using Cedex Bio (manufactured by Roche Diagnostics K.K.). It was confirmed that glucose was consumed with time, and an antibody and lactic acid were continuously produced. The amounts of consumed glucose and produced lactic acid for 3 days after the start of the culture are set forth in Table 1. It was confirmed that the culture was stably performed.
Cell Culture Using Cell Culture Module 20
Cell culture was performed using a cell culture module 20 illustrated in
Conditioned/suspended anti-human IL-8 antibody producing CHO-DP12 cells (ATCC CRL-12445) were float-cultured using a medium (BalanCD (Trademark) CHO Growth A) and culture was continued until viable cell count per mL was 5.41×106 cells/mL (total cell number of 6.16×106 cells/mL, viable cell rate of 88%).
The five sterilized cell culture modules 20 were added into a bottle type sterilized vessel (manufactured by Corning, Inc.) having an internal volume of 150 mL, 26.7 mL of a medium for culturing a CHO cell monolayer KBM270 (manufactured by Kohjin Bio Co., Ltd.) was added into the bottle type sterilized vessel, and the five sterilized cell culture modules 20 were immersed in the medium at a shaking rate of 35 rpm for 10 minutes in a CO2 incubator using a program shaker (manufactured by KENIS LIMITED). Then, a liquid mixture of 6.0 mL of CHO DP-12 floating cell culture medium (total cell number of 6.16×106 cells/mL, viable cell count of 5.41×106 cells/mL, dead cell count of 7.51×105 cells/mL, and viable cell rate of 88%) and 7.3 mL of medium for floating cells (BalanCD (Trademark) CHO Growth A) was added, and cells were adsorbed for about 14 hours using a program shaker (manufactured by KENIS LIMITED) under a rotational condition of 35 rpm (cell adsorption number of 5.30×104 cells per sheet). The cell adsorption ratio calculated from the collected medium was 88%.
Then, the medium was removed, 40 mL of a medium for culturing a CHO cell monolayer KBM270 (manufactured by Kohjin Bio Co., Ltd.) was added, and culture was started. Two days after the start of the culture, the vessel was transferred to an electromagnetic orbital shaker (for a CO2 incubator, manufactured by AS ONE Corporation), and the culture was continued at a shaking rate of 200 rpm. Medium replacement was performed every day, and the amounts of consumed glucose, produced lactic acid, lactate dehydrogenase, and produced antibody per day in the medium were measured using Cedex Bio (manufactured by Roche Diagnostics K.K.). It was confirmed that glucose was consumed with time, and an antibody and lactic acid were continuously produced. Variations with time of the amount of produced antibody are illustrated in
Thirty cell culture submodules 30 illustrated in
Conditioned/suspended anti-human IL-8 antibody producing CHO-DP12 cells (ATCC CRL-12445) were float-cultured using a medium (BalanCD (Trademark) CHO GROWTH A) and culture was continued until viable cell count per mL was 2.0×106 cells/mL.
Porous polyimide films having a long and narrow shape of 0.3 cm×2.5 cm were prepared and subjected to dry heat sterilization. Then, the 11 to 12 porous polyimide films were placed in a petri dish of 20 cm2, 4 mL of the floating culture medium described above was poured, and the porous polyimide films were sufficiently moisturized with a cell suspension. Then, the petri dish was left standing in a CO2 incubator. After 2 hours, the petri dish was taken out of the incubator, the cell suspension was sucked and removed, 4 mL of medium (2% FBS-supplemented IMDM) was then added, and culture was further continued in the CO2 incubator. The medium was replaced at a pace of every two days.
Seven days after the start of the culture, the number of cells, cultured using CCK8 (Cell Countinig Kit 8; solution reagent manufactured by Dojindo Laboratories Co., Ltd.), on the porous polyimide films in the three petri dishes was calculated as a cell count per area. On the next day, the culture in one of the three petri dishes was further continued for 2 days on an as-is basis (hereinafter referred to as “culture 1”).
In one of the remaining two petri dishes, the porous polyimide film on which the cells grew was transferred into an oxygen permeable culture bag (manufactured by NIPRO CORPORATION) along with the culture medium, and sealed aseptically with a heat sealer. Then, the cells were subjected to shaking culture for 2 days in a shaker placed in a CO2 incubator set to cause 20 to 30 vibrations per minute (hereinafter referred to as “culture 2”).
Further, the porous polyimide film contained in the remaining petri dish was aseptically cut into about 0.3 cm x 0.3 cm strips with scissors. Then, an overcoat having a size of about 1 cm×1 cm and made of 30 # nylon mesh was prepared, the cut porous polyimide films were contained in the overcoat, and the overcoat was aseptically sealed with a heat sealer. The obtained cell culture module was transferred along with the medium into an oxygen permeable culture bag (manufactured by NIPRO CORPORATION), and the oxygen permeable culture bag was aseptically sealed with the heat sealer. Then, the cells were subjected to shaking culture for 2 days in a shaker placed in a CO2 incubator set to cause 20 to 30 vibrations per minute (hereinafter referred to as “culture 3”).
The densities of the cells subjected to the cultures 1 to 3 were calculated using CCK8. The results are set forth in Table 2. In the culture 2 in which the shaking culture was performed without fixing the porous polyimide film, a marked decrease in cell count was observed. This is considered to be caused by exhibition by cells due to apoptosis or the like, resulting from stress applied to the cells growing in the porous polyimide film because of the continuous deformation of the shape of the porous polyimide film. In contrast, the decrease in cell count observed in the culture 2 was suppressed in the culture 3 in which the shaking culture was performed in a state in which the porous polyimide film was contained and fixed in the overcoat.
The cell culture module of the present invention can be preferably used for stable cell culture and substance production.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2018-010105 | Jan 2018 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2019/002375 | 1/24/2019 | WO | 00 |
