WO2017179705A1 - Container for cell suspension preparation, and preparation method for cell suspension - Google Patents

Container for cell suspension preparation, and preparation method for cell suspension Download PDF

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Publication number
WO2017179705A1
WO2017179705A1 PCT/JP2017/015292 JP2017015292W WO2017179705A1 WO 2017179705 A1 WO2017179705 A1 WO 2017179705A1 JP 2017015292 W JP2017015292 W JP 2017015292W WO 2017179705 A1 WO2017179705 A1 WO 2017179705A1
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WIPO (PCT)
Prior art keywords
container
cell suspension
space
mesh sheet
cell
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PCT/JP2017/015292
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French (fr)
Japanese (ja)
Inventor
林 真司
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株式会社カネカ
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Publication of WO2017179705A1 publication Critical patent/WO2017179705A1/en

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M1/00Apparatus for enzymology or microbiology
    • C12M1/12Apparatus for enzymology or microbiology with sterilisation, filtration or dialysis means
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M3/00Tissue, human, animal or plant cell, or virus culture apparatus
    • C12M3/06Tissue, human, animal or plant cell, or virus culture apparatus with filtration, ultrafiltration, inverse osmosis or dialysis means
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M3/00Tissue, human, animal or plant cell, or virus culture apparatus
    • C12M3/08Apparatus for tissue disaggregation
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/02Separating microorganisms from their culture media

Definitions

  • the present invention relates to a method for preparing a cell suspension by removing impurities from an enzyme-treated solution of a cell-containing sample such as a collected biological tissue, and a cell suspension preparation container for use in the method.
  • Patent Document 1 discloses a blood processing filter including a flexible container having an inlet and an outlet for blood and a sheet-like blood processing filter material arranged so that the inside of the container is separated from the inlet side and the outlet side. It is disclosed.
  • Patent Document 2 discloses a spiral-shaped primary flow path connecting the primary side inlet and the primary side outlet and extending from the membrane periphery to the center of the membrane, and 2 filtrates permeated through the filtration membrane.
  • a plate-type membrane module for collecting a low-molecular-weight substance concentration measurement sample in blood in which a secondary-side flow path leading to a secondary-side outlet is formed is disclosed.
  • Patent Document 3 when specific tissue stem cells are obtained from a tissue piece collected from a living tissue using a puncture needle, (1) the pore size is passed through a filter of 200 to 300 ⁇ m in a closed system. A step of removing blood cell components, (2) a step of washing with a phosphate buffer containing an antibiotic, (3) a step of subjecting the obtained tissue piece to enzyme treatment to form a cell suspension, and (4) a specific gravity A step of separating light cells from the target cells by floating; (5) a step of passing the suspension of the target cells again through a filter having a pore size of 250 to 300 ⁇ m; and (6) a filter having a pore size of 20 to 40 ⁇ m. It is disclosed to perform a step of passing, (7) centrifugation and / or a step of obtaining a target cell from a cell suspension by passing through a 400-500 nm filter.
  • the separation operation using a filter as disclosed in Patent Documents 1 and 2 is performed to remove undesirable components such as aggregates and leukocytes from a liquid tissue such as blood, and a part of the separation operation is performed inside the filter. Intended to leave.
  • a separation operation using a filter is performed to remove impurities such as undigested material from an enzyme-treated product of adipose tissue, the filter is clogged at an early stage. Therefore, in order to obtain a sufficient amount of cells, a filter having a large area must be used.
  • the apparatus tends to be large, leading to high costs and further limiting the facilities that can be used.
  • Patent Document 3 describes the use of a syringe-like device for enzyme treatment of living tissue in a closed system, but specific means for supplying enzymes to living tissue while maintaining the closed system. Is not disclosed. In order to actually supply an enzyme to a living tissue while maintaining a closed system inside the syringe-like device, a complicated device is required and it is considered that the realization is not easy.
  • an object of the present invention is to provide a method for preparing a cell suspension easily from a cell-containing sample such as a living tissue with a high cell recovery rate, and a container used therefor.
  • the present inventors have provided a mesh sheet for removing impurities from an enzyme-treated solution of a cell-containing sample such as a living tissue, and suspended the cell without causing clogging or the like.
  • the present inventors have found a container having a constitution capable of preparing a liquid and a method for preparing a cell suspension using the container.
  • the enzyme treatment solution may be obtained by performing an enzyme treatment of the cell-containing sample inside the container, or may be prepared outside the container.
  • the gist of the present invention is as follows.
  • a cell suspension preparation container A container body containing an internal space capable of holding liquid; A mesh sheet arranged to divide the internal space into a first space and a second space; A charging unit provided in the container body, and formed with a liquid charging port into the first space; A discharge part provided in the container body, and formed with a discharge port for liquid from the second space; With The container in which 90- ⁇ is less than 50, where ⁇ (°) is a narrow angle formed between the flow direction of the liquid discharged from the discharge port and the normal line of the surface along the mesh sheet . (2) The container according to (1), wherein the mesh sheet has a pore diameter of 50 to 300 ⁇ m. (3) The container according to (1) or (2), wherein the container body has flexibility.
  • a cell suspension preparation container A container body containing an internal space capable of holding liquid; A mesh sheet arranged to divide the internal space into a first space and a second space; A charging unit provided in the container body, and formed with a liquid charging port into the first space; A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
  • the container body includes a first side wall and a second side wall facing each other with the mesh sheet interposed therebetween, The first side wall and the mesh sheet surround the first space; The second side wall and the mesh sheet surround the second space;
  • the insertion portion is disposed between the peripheral portion of the first side wall and the peripheral portion of the mesh sheet so as to communicate the first space and the outside via the input port,
  • the discharge part is arranged between the peripheral part of the second side wall and the peripheral part of the mesh sheet so as to communicate the second space and the outside through the discharge port,
  • the said container by which said 1st side wall, said 2nd side wall, and said mesh sheet are integrated in the peripheral part.
  • the charging unit and the discharging unit are disposed at positions facing the container body, and the first side wall and the second of the end of the charging unit on the first space side
  • the width along the direction facing the side wall is W1
  • the width of the end of the discharge portion on the second space side along the direction in which the first side wall and the second side wall face each other is W2
  • the average value of W1 and W2 is W
  • the distance between the end of the input portion on the first space side and the end of the discharge portion on the second space side is D
  • D The container according to (7), wherein D / W is 12 or more.
  • a method for preparing a cell suspension from a cell-containing sample (A) a container body containing an internal space capable of holding a liquid; A mesh sheet arranged to divide the internal space into a first space and a second space; A charging unit provided in the container body, and formed with a liquid charging port into the first space; A discharge part provided in the container body, and formed with a discharge port for liquid from the second space; A cell-containing sample and an enzyme are introduced through the inlet, and an enzyme treatment solution is generated by performing an enzyme reaction in the first space, and / or an enzyme treatment of the cell-containing sample is conducted through the inlet.
  • the process of adding liquid (B)
  • the enzyme treatment liquid is passed through the mesh sheet to remove impurities, a cell suspension is generated on the second space side, and the generated cell suspension is discharged through the discharge port.
  • a process comprising the steps of: (11) When the narrow angle formed by the flow direction of the cell suspension discharged through the discharge port and the normal of the surface along the mesh sheet is ⁇ (°) in step (b)
  • (12) The method according to (10) or (11), wherein the container is the container according to any one of (1) to (9).
  • the cell-containing sample is one or more selected from the group consisting of fat, skin, blood vessel, cornea, oral cavity, kidney, liver, pancreas, heart, nerve, muscle, prostate, intestine, amniotic membrane, placenta and umbilical cord.
  • the discharge port is connected to a cell suspension treatment apparatus capable of washing and concentrating the cell suspension in a closed system;
  • C The method according to any one of (10) to (14), further comprising a step of washing and concentrating the cell suspension discharged from the discharge port with the device in a closed system to obtain a cell concentrate. the method of.
  • a cell suspension can be prepared in a closed system without an open system operation such as centrifugation from a cell-containing sample such as a collected biological tissue or an enzyme-treated solution of a cell-containing sample. it can. Further, by using the cell suspension preparation container of the present invention in the method, it is possible to prepare a cell suspension with an excellent throughput and cell recovery rate without causing clogging of the mesh. .
  • FIG. 1 is a cross-sectional view taken along line AA of the cell suspension preparation container 1 of FIG. 1-1.
  • FIG. 2 is a cross-sectional view taken along the line BB of the cell suspension preparation container 1 of FIG. 1-1.
  • FIG. 1 is a perspective view showing a state in which a liquid is placed in the internal space 13 of the cell suspension preparation container 1 of the present invention shown in FIG. 1-1.
  • FIG. 2 is a cross-sectional view taken along the line CC of the cell suspension preparation container 1 of FIG. 2-1.
  • FIG. 2 is a schematic end view of the vicinity of a discharge part 31 of a CC line cutting part of the cell suspension preparation container 1 of FIG.
  • FIG. 1 It is the schematic of one Embodiment of the cell suspension processing apparatus connected to the container for cell suspension preparation of this invention.
  • ⁇ (°) is the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet
  • ⁇ (°) is the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet
  • FIG. 8 shows an enzyme treatment container 810 for preparing an enzyme treatment solution by containing a cell-containing sample and an enzyme, and a cell suspension containing the prepared enzyme treatment solution.
  • 1 is a schematic diagram showing a configuration of a cell suspension preparation system 800 including a cell suspension preparation container 1 according to an embodiment of the present invention and a collection container 820 that collects the generated cell suspension. is there.
  • FIGS. 1-1 to 1-3 are schematic views showing one embodiment of the cell suspension preparation container of the present invention.
  • the cell suspension preparation container 1 of this embodiment is arranged so that a container body 10 containing an internal space 13 capable of holding a liquid and the internal space 13 are divided into a first space 11 and a second space 12.
  • the mesh sheet 40, the container main body 10 and the charging section 21 provided with the liquid inlet 20 into the first space 11, and the container main body 10 and the liquid from the second space 12 are provided.
  • the discharge part 31 in which the discharge port 30 of this was formed is provided.
  • FIGS. 1-1 to 1-3 schematically show an example of the shape of the cell suspension preparation container 1 of the present embodiment when no contents are contained in the internal space 13.
  • FIGS. 2-1 and 2-2 show an example of the shape when the liquid is filled in the internal space 13 of the cell suspension preparation container 1 of the present embodiment.
  • the depiction of the liquid is omitted for simplicity of illustration.
  • the discharge port 30 needs to be sealed, but depiction of means for sealing is also omitted.
  • the container body 10 that constitutes the outer shell of the internal space 13 that can hold the liquid can be provided with a mesh sheet 40 in the manner described later, and should not affect the cells that are held inside.
  • the container body 10 and the mesh sheet 40 include, for example, a first side wall 15 and a second side wall 16 that face each other with the mesh sheet 40 therebetween, and the first side wall 15 and the mesh sheet 40 surround the first space 11.
  • the second side wall 16 and the mesh sheet 40 can be configured to surround the second space 12.
  • FIGS. 1-1 to 1-3 represent such embodiments.
  • the first side wall 15, the second side wall 16, and the mesh sheet 40 are integrated at the first side wall peripheral part 150, the second side wall peripheral part 160 and the mesh sheet peripheral part 41.
  • the container body 10 is made of a transparent or translucent material because the state of the cell suspension inside can be visually observed. In addition, it is preferable that at least a part, preferably the whole, be flexible because the internal cell suspension can be physically separated by clamping as necessary. It is preferable that the container main body 10 does not contain an adhesive at a portion exposed to the internal space 13. When the container main body 10 includes the first side wall 15 and the second side wall 16, the manufacturing process can be simplified if the material of the side wall can be bonded by thermal fusion without using an adhesive. This is preferable because it does not need to consider the influence of the adhesive on the cells.
  • the material of the container body 10 include vinyl chloride, soft vinyl chloride, polyurethane, ethylene-vinyl acetate copolymer, polyolefin such as polyethylene and polypropylene, hydrogenated product of styrene-butadiene-styrene copolymer, and Examples thereof include thermoplastic elastomers such as styrene-isoprene-styrene copolymers or hydrogenated products thereof, and mixtures of thermoplastic elastomers with polyolefins and softeners such as ethylene-ethyl acrylate. It is preferable that the inner surface defining the internal space 13 of the container body 10 is pear-finished because residual liquid can be reduced when the cell suspension is discharged.
  • the mesh sheet 40 is disposed so as to divide the internal space 13 into a first space 11 and a second space 12.
  • As the mesh sheet one that can allow liquid such as water to pass therethrough, and preferably allows necessary cells to pass therethrough is used.
  • the mesh sheet 40 preferably has a pore diameter in the range of 50 to 300 ⁇ m. If the pore size is in such a range, contaminants such as undigested tissue clumps and debris contained in the enzyme-treated product of living tissue are removed without causing clogging of the mesh, and only necessary cells are removed. Can be passed.
  • the pore diameter is preferably 50 ⁇ m or more, more preferably 95 ⁇ m or more, preferably 300 ⁇ m or less, more preferably 200 ⁇ m or less.
  • the mesh sheet 40 preferably has a hole area ratio of 40% or more, particularly 45% or more because clogging is difficult to occur.
  • “mesh” refers to a material having a network structure in which a plurality of pores penetrating from one surface to the other surface are two-dimensionally arranged in a planar shape.
  • the mesh include, but are not limited to, one in which fibers are woven so as to form a network structure, and a membrane in which a plurality of pores penetrating in the thickness direction are formed.
  • the mesh also includes what is generally called a “screen”.
  • a sheet made of mesh is referred to as a “mesh sheet”.
  • the “mesh” is a material that does not have the network structure and has three-dimensional pores (for example, a fibrous porous medium or a sponge-like structure, does not have the network structure, and has a three-dimensional structure.
  • the material of the mesh sheet 40 is a synthetic resin material such as nylon, polyester, rayon, polyolefin, polystyrene, acrylic resin, polycarbonate, polyacrylamide, polyurethane, vinyl chloride, etc. from the viewpoint of material safety, stability, and availability.
  • an inorganic material such as hydroxyapatite, glass, alumina, and titania
  • a metal such as stainless steel, titanium, and aluminum.
  • the combination is not particularly limited, but synthetic polymers such as polyolefin, polystyrene, acrylic resin, nylon, polyester, polycarbonate, polyacrylamide, polyurethane, vinyl chloride, hydroxyapatite, glass,
  • a combination of two or more materials selected from the group consisting of inorganic materials such as alumina and titania, and metals such as stainless steel, titanium, and aluminum is preferable.
  • the mesh sheet 40 is provided in the container body 10 so that the surface of the mesh sheet is substantially flat when the liquid is put into at least the internal space 13.
  • FIGS. 2-1 and 2-2 show a state in which a liquid (not shown) is put in the internal space 13 of the container 1 shown in FIGS. 1-1 to 1-3. Since the mesh sheet 40 can transmit the liquid, the liquid medium, the dissolved component, and the component having a size capable of transmitting the mesh sheet in the liquid input through the input port 20 are not limited to the first space 11. The components that pass through the mesh sheet 40 and move to the second space 12 and cannot pass through the mesh sheet 40 remain in the first space 11.
  • the pore size of the mesh sheet is the maximum inscribed in the contour of the inner circumference of the pore, which is specified by observing the pores penetrating from one surface of the mesh sheet to the other surface along the penetration direction. Means the average diameter of the inscribed circle. The average value is preferably calculated from, for example, a value obtained by observing 50 or more pores, preferably 100 or more pores. When the mesh sheet is woven so that the fibers form a network structure, the pore diameter is equal to the average opening of the mesh. The average opening can be calculated based on the number of fibers per unit length (for example, 1 inch) measured using, for example, a urnometer.
  • the opening rate of the mesh sheet refers to the ratio of the total area of the opening portions to the entire area when the mesh sheet is viewed in plan.
  • the inlet 21 is provided with a liquid inlet 20 into the first space 11 of the internal space 13, and the outlet 31 is provided with a liquid outlet 30 from the second space 12 of the internal space 13. Yes. Only one input port 20 and one discharge port 30 may be provided, or two or more of one or both of the input ports 20 and the discharge ports 30 may be provided as necessary.
  • a cell-containing sample such as a living tissue and an enzyme for separating cells into a cell suspension are input from the input port 20.
  • the enzyme reaction is carried out in 11.
  • an enzyme-treated solution obtained by subjecting a cell-containing sample such as a living tissue to an enzyme reaction treatment with an enzyme is introduced from the inlet 20 and accommodated in the first space 11. Is done.
  • a cell suspension is generated on the second space 12 side. The cell suspension is discharged from the discharge port 30.
  • the input unit 21 and the discharge unit 31 may be provided in any way.
  • the relative relationship between the container body 10 and the mesh sheet 40 is the configuration shown in FIGS.
  • throwing-in part 21 is between the peripheral part 150 of the 1st side wall 15, and the peripheral part 41 of the mesh sheet 40.
  • the first space 11 and the outside are arranged to communicate with each other through the insertion port 20, and the discharge portion 31 is disposed between the peripheral portion 160 of the second side wall 16 and the peripheral portion 41 of the mesh sheet 40. It arrange
  • the input portion 21 and the discharge portion 31 are made of a hollow cylindrical material having an arbitrary cross-sectional shape, for example, a resin tube, and the peripheral portion 150 of the first side wall 15 and the peripheral portion 41 of the mesh sheet 40. Or between the peripheral edge portion 160 of the second side wall 16 and the peripheral edge portion 41 of the mesh sheet 40.
  • the material constituting the input unit 21 and the discharge unit 31 include vinyl chloride, soft vinyl chloride, polyurethane, ethylene-vinyl acetate copolymer, polyolefin such as polyethylene and polypropylene, styrene-butadiene-styrene copolymer.
  • thermoplastic elastomers such as styrene-isoprene-styrene copolymers or hydrogenated products thereof, and mixtures of thermoplastic elastomers with softeners such as polyolefin and ethylene-ethyl acrylate.
  • the inlet 20 and outlet 30 are closed by at least a part of the inlet 21 and outlet 31 that communicate with each other by silicon rubber or the like that allows a sample to be introduced using an injection needle so that the internal space 13 can be closed. It is preferable that a structure such as a needleless port can be directly inserted.
  • the portion of the input portion 21 that communicates with the input port 20 has a plurality of ports for inputting the sample by branching in the middle, and the like so that the cell-containing sample and the enzyme can be input from separate ports. It may be.
  • the port may be provided with a filter as necessary.
  • the input unit 21 and the discharge unit 31 may be provided at any position of the container body 10 as long as the relative position with respect to the mesh sheet 40 is as described above. However, if the input part 21 and the discharge part 31 are provided in positions opposite to each other in the container body 10, from the input of the cell-containing sample and the enzyme or the input of the enzyme-treated solution of the cell-containing sample to the discharge of the cell suspension. This is preferable because the processing can be performed smoothly.
  • “providing at positions facing each other” means that, for example, as shown in FIG. 1-1, when the container body 10 has a quadrangular shape or a shape similar thereto, the insertion portion 21 is provided on one of the opposed sides, and the other It means that the discharge part 31 is provided in the side of
  • FIG. 2-3 shows the discharge part 31 of the CC line cutting part of the cell suspension preparation container 1 in a state where a liquid (not shown) is accommodated in the internal space 13 shown in FIG. FIG.
  • FIG. 4 is a schematic end view of the vicinity, showing a relationship of ⁇ (°) as a narrow angle formed by the flow direction F of the liquid discharged from the discharge port 30 and the normal line L of the surface along the mesh sheet 40. ing.
  • °
  • the mesh sheet 40 since 90- ⁇ is in the above range, positions on the mesh sheet 40 having different distances from the discharge port 30 along the direction F are included, and an undigested tissue mass It is difficult for the mesh sheet 40 to be clogged with impurities such as debris and debris, and the cell suspension can be taken out from the outlet 30 smoothly.
  • 90- ⁇ is preferably less than 50, more preferably 45 or less, further preferably 30 or less, and particularly preferably 5 or less. The smaller the value of 90- ⁇ , the higher the effect of the first embodiment.
  • the lower limit of 90-0 is not particularly limited, and may be 0.
  • the portion exposed to the internal space 13 of the mesh sheet 40 is preferably 50% or more, more preferably 60% or more, more preferably with respect to the area when the portion is viewed in plan. Is 70% or more, more preferably 80% or more, more preferably 90% or more, more preferably 95% or more, and more preferably 100% of the area so that the 90- ⁇ is in the above range. It is done. If the region in which the 90- ⁇ is in the above range in the mesh sheet 40 is in the above range, the above effect of the first embodiment is sufficiently exhibited.
  • the container body 10 includes a first side wall 15 and a second side wall 16 that face each other with the mesh sheet 40 therebetween, The first side wall 15 and the mesh sheet 40 surround the first space 11, The second side wall 16 and the mesh sheet 40 surround the second space 12, The insertion portion 21 is disposed between the peripheral portion 150 of the first side wall 15 and the peripheral portion 41 of the mesh sheet 40 so as to communicate the first space 21 and the outside via the input port 20.
  • the discharge part 31 is arrange
  • the first side wall 15, the second side wall 16, and the mesh sheet 40 are integrated at the peripheral edge portions 150, 160, and 41.
  • the two members constituting the first side wall 15 and the second side wall 16, the mesh sheet material, and the material for the input part and the discharge part are integrated. This makes it relatively easy to manufacture.
  • the first side wall 15, the second side wall 16, and the mesh sheet 40 are integrated as long as these three members cannot be separated and need to be directly coupled to each other. Instead, any one or more of these three members or other members may be combined.
  • the first side wall 15 and the second side wall 16 are not directly connected to each other and are connected and integrated via the mesh sheet 40 therebetween.
  • the first The side wall 15, the second side wall 16, and the mesh sheet 40 are an example “integrated at the peripheral edge”.
  • the angle ⁇ (°) of the mesh sheet 40 can be adjusted by the dimensions and relative distances of the input portion 21 and the discharge portion 31 in the container body 10, thereby
  • the cell suspension preparation container 1 having a 90- ⁇ value of less than 50 can be easily produced.
  • the input unit 21 and the discharge unit 31 are disposed at positions facing the container body 10, (i) the first side wall of the end 22 on the first space 11 side of the input unit 21. 15 and the width along the direction in which the second side wall 16 faces W1, and (ii) the first side wall 15 and the second side wall 16 of the end 32 on the second space 12 side of the discharge part 31 face each other.
  • the angle ⁇ (°) can be adjusted by the ratio (D / W) of D, which is the average value of D, W1, and W2. For example, if D / W is 12 or more, 15 or more, or 20 or more, the value of 90 ⁇ can be 5 or less. As D / W is larger, 90- ⁇ is smaller.
  • the upper limit of D / W is not particularly limited, but is usually 50 or less, 40 or less, or 30 or less.
  • the ratio of W1 and W2 is not particularly limited, but W1 / W2 is more preferably 0.2 to 5, and more preferably 0.5 to 2, from the viewpoint of facilitating the production of the cell suspension preparation container 1. 0.9 to 1.1 is more preferable, and 1 is particularly preferable. In this embodiment, it is preferable that the input part 21 and the discharge part 31 are arranged so that the input path by the input port 20 and the input path by the discharge port 30 are located on the same axis.
  • the present invention also relates to a method for preparing a cell suspension from a cell-containing sample such as a living tissue.
  • the method is (A) To the first space provided in the container body, the container main body containing the internal space capable of holding the liquid, the mesh sheet arranged to divide the internal space into the first space and the second space, A cell-containing sample and an enzyme through the input port in a container having an input unit in which the liquid input port is formed and a discharge unit provided in the container body and formed with a liquid discharge port from the second space.
  • an enzyme reaction is performed in the first space to generate an enzyme treatment solution and / or a cell-containing sample enzyme treatment solution is introduced through the inlet, and (b) the enzyme treatment solution is passed through the mesh sheet. At least a step of removing impurities, generating a cell suspension on the second space side, and discharging the generated cell suspension through a discharge port.
  • an enzyme used for enzyme treatment of a cell-containing sample an enzyme that can be used for separation of cells from a cell-containing sample such as a biological tissue such as collagenase, trypsin, dispase, collagenase, pepsin can be appropriately used.
  • the mesh sheet is permeable to liquids such as water, and is selected from the range described for the mesh sheet used in the embodiment of the cell suspension preparation container. be able to.
  • the pore size of the mesh sheet is, for example, in the range of 50 to 300 ⁇ m, preferably 50 ⁇ m or more, more preferably 95 ⁇ m or more, preferably 300 ⁇ m or less, more preferably 200 ⁇ m or less.
  • the container is preferably sterilized before use.
  • sterilization methods generally used for sterilization of medical devices such as ⁇ -ray sterilization, electron beam sterilization, EOG sterilization, and high-pressure steam sterilization can be suitably used.
  • the container for step (a) may be any container as long as it has the structure described above, but preparation of a cell suspension having a structure as shown in FIGS. 1-1 to 1-3. It is preferable to use a container for a cell because a cell suspension can be smoothly prepared without clogging or the like.
  • step (a) when a cell-containing sample and an enzyme are put through an inlet and an enzyme reaction is performed in the first space to generate an enzyme-treated solution, a cell-containing sample that is a raw material for the cell suspension;
  • the enzyme for separating the cells and preparing the cell suspension is put into the first space of the container through the inlet, where the enzyme reaction is carried out.
  • the reaction mixture containing the enzyme and the cell-containing sample formed at this time is preferably in a liquid state.
  • the enzyme and the cell-containing sample are first mixed in the presence of a liquid medium such as water as a dispersion medium. It is preferable to accommodate in a space.
  • the enzyme can be added as an aqueous enzyme solution as necessary.
  • step (a) Since the mesh sheet can permeate the liquid, in step (a), the liquid medium contained in the reaction mixture placed in the first space, the dissolved component, and a size that can permeate the mesh sheet.
  • the component moves not only in the first space but also in the second space, and the component having a size that cannot pass through the mesh sheet remains in the first space.
  • the enzyme reaction of the step (a) the component that cannot permeate the mesh sheet in the first space is enzyme-treated, and the target cell becomes an enzyme-treated solution dispersed in a liquid medium. By passing the enzyme-treated solution after the enzyme reaction through the mesh sheet, undigested tissue clumps and debris are removed, and a cell suspension is generated in the second space. To be discharged.
  • the step (a) is preferably carried out in a state where the inlet and outlet of the container are closed.
  • the inlet and outlet portions communicating with the inlet and outlet of the container are sealed in such a manner that a sample can be input, such as silicon rubber and a needleless port.
  • a sample can be input, such as silicon rubber and a needleless port.
  • Is a closed system and it is preferable that an enzymatic reaction can be performed without touching the outside air.
  • it can put on suitable reaction conditions by putting the container on a shaker or putting it in a thermostat.
  • placing the cell-containing sample and enzyme, or when carrying out the enzyme reaction placing the container so that the first space is vertically below the second space, This is preferable because clogging can be prevented.
  • the enzyme-treated enzyme is used to separate the cells and prepare the cell suspension of the cell-containing sample as a raw material of the cell suspension. Is performed in another container, and the enzyme treatment liquid produced in the other container is accommodated in the first space of the container through the inlet.
  • the enzyme treatment liquid accommodated in the first space includes a liquid medium such as water, a dissolved component, and a component (such as a target cell) having a size that can permeate the mesh sheet.
  • the enzyme-treated solution passes through the mesh sheet, thereby removing undigested tissue masses and debris and other contaminants, generating a cell suspension in the second space, and then the outlet.
  • the container When putting the enzyme treatment liquid, it is preferable to place the container so that the first space is located below the second space in the vertical direction because clogging of the mesh sheet can be prevented. Also in this case, it is preferable that the inlet of the container inlet and / or the outlet of the outlet are sealed in such a manner that a sample can be introduced, such as silicon rubber or a needleless port.
  • a closed system in which the discharge port is connected to a container for containing the cell suspension or a device for a further processing step by a closed channel. It is preferable from the viewpoint of suppressing contamination.
  • the narrow angle formed by the flow direction of the cell suspension discharged through the discharge port and the normal of the surface along the mesh sheet is ⁇ (°).
  • 90- ⁇ is less than 50, preferably 45 or less, more preferably 30 or less, and particularly preferably 5 or less, clogging of the mesh sheet is less likely to occur.
  • the value of 90- ⁇ based on the angle ⁇ (°) is less than 50, preferably 45 or less, more preferably 30 or less, and particularly preferably 5 It is preferable to have the following structure, more specifically, a structure as shown in FIGS. 1-1 to 1-3.
  • the flow rate at which the enzyme treatment liquid passes through the mesh sheet can be appropriately adjusted by applying a negative pressure from the discharge port, but may be a flow rate that is allowed to fall naturally due to gravity.
  • the flow rate through the mesh sheet should be in the range of 1 to 600 mL / min, particularly in the range of 10 to 500 mL / min, especially in the range of 20 to 350 mL / min. preferable.
  • step (b) may be performed after the step (a) is completed, or the step (a) and the step (b) may be performed in parallel.
  • the cell suspension preparation container 1 shown in FIGS. 1-1 to 1-3 is used.
  • FIG. 8 shows an example of a cell suspension preparation system suitable for storing the generated enzyme treatment liquid in the first space 11 of the cell suspension preparation container 1 through the inlet 20.
  • a cell suspension preparation system 800 shown in FIG. 8 contains a cell-containing sample and an enzyme, performs an enzyme treatment, and prepares an enzyme treatment liquid, and an enzyme treatment liquid prepared.
  • a general plastic tube can be used, and among them, a vinyl chloride tube can be preferably used from the viewpoint of safety and durability.
  • the enzyme processing container 810 includes an enzyme processing container main body 811, a sample input part 812 in which an input port for inputting a cell-containing sample is formed, an enzyme An enzyme input unit 813 formed with an input port for supplying an enzyme solution containing, and a filter sterilization filter 814 disposed on the upstream side of the enzyme input unit 813 for filter sterilizing the enzyme solution to be input.
  • the enzyme input part 813 and the enzyme processing container main body 811 are connected by a pipe 850 as necessary, and a clamp 854 for sealing the pipe 850 of this part as necessary is provided.
  • the container body 811 for enzyme treatment is preferably a flexible plastic container.
  • the inner surface is pear-finished because residual liquid can be reduced.
  • the cell-containing sample input through the sample input unit 812 and the enzyme solution input through the filter sterilization filter 814 and the enzyme input unit 813 are mixed in the enzyme treatment container body 811 to form a reaction mixture.
  • the reaction mixture is preferably in a liquid form, and for that purpose, a liquid medium such as water is appropriately included as a dispersion medium.
  • the enzyme can be added as an aqueous enzyme solution as necessary.
  • An enzyme reaction is performed in the enzyme processing container main body 811 to generate an enzyme processing solution for the cell-containing sample.
  • the enzyme treatment container 810 can be placed on a shaker or placed in a thermostatic bath, so that appropriate reaction conditions can be obtained.
  • the container body 811 for enzyme treatment and the cell suspension preparation container 1 are connected by a tube 850.
  • the enzyme treatment solution generated in the enzyme treatment container 810 passes through the tube 850 and enters the cell suspension preparation container from the input port 20 formed in the input part 21 of the cell suspension preparation container 1. 1 to the first space 11. This step corresponds to the above step (a).
  • the portion of the tube 850 that connects the enzyme treatment container 810 and the cell suspension preparation container 1 can be configured to be separable by a pair of luer locks 851 and 852.
  • One of the pair of luer locks 851 and 852 is a male luer lock and the other is a female luer lock, which can be connected in a liquid-tight manner.
  • a clamp 856 that can close the tube 850 may be disposed in the portion of the tube 850 between the enzyme treatment container 810 and the upstream luer lock 851 as necessary.
  • the cell suspension preparation system 800 is installed so that the enzyme treatment container 810 containing the enzyme treatment solution is located vertically above and the cell suspension preparation container 1 is located below vertically,
  • the enzyme treatment liquid may be moved from the enzyme treatment container 810 to the cell suspension preparation container 1, or by applying negative pressure from the discharge port 30 side of the cell suspension preparation container 1 to perform the enzyme treatment.
  • the liquid may be moved from the enzyme treatment container 810 to the cell suspension preparation container 1.
  • the enzyme treatment liquid stored in the first space 11 of the cell suspension preparation container 1 passes through the mesh sheet 40, impurities are removed, and the second A cell suspension is generated on the space 12 side, and the generated cell suspension is accommodated in the collection container 820 through the discharge port 30 formed in the discharge unit 31 and the pipe 850 connected to the discharge unit 31.
  • the discharge part 31 of the cell suspension preparation container 1 and the collection container 820 are connected by a tube 850, and a clamp 857 for sealing the tube 850 of this portion as necessary is provided.
  • the collection container 820 is preferably a flexible plastic container. Moreover, it is preferable that the inner surface is pear-finished because residual liquid can be reduced.
  • a pipe 850 is connected to the downstream side of the collection container 820, and the cell suspension collected in the collection container 820 is discharged through the pipe 850.
  • a luer lock 853 is provided at the downstream end of this portion of the tube 850 as necessary, and the luer lock 853 is attached to an apparatus for further processing of the cell suspension, for example, a cell suspension processing apparatus described later. Can be connected through.
  • the luer lock 853 may be either a female lock or a male luer lock depending on the luer lock provided in the further downstream device.
  • the cell suspension preparation system 800 is installed so that the cell suspension preparation container 1 is positioned above the vertical direction and the collection container 820 is positioned below the vertical direction.
  • the suspension preparation container 1 may be moved from the second space 12 to the collection container 820, or a negative pressure is applied from the tube 850 downstream of the collection container 820 to apply the cell suspension.
  • the cell suspension preparation container 1 may be moved from the second space 12 to the collection container 820.
  • the discharge port of the container may be connected to a separately prepared cell suspension processing apparatus, whereby the cell suspension obtained from the discharge port is washed and concentrated in a closed system to obtain a cell concentrate. You may do it.
  • the discharge port of the container and the cell suspension treatment apparatus are connected by a closed flow path, and the collection container 820 as described above may be interposed therebetween.
  • the washing of the cell suspension includes body fluids and enzymes contained in the cell suspension, including dilute solutions such as physiological saline, infusion, medium, distilled water, inorganic salts, saccharides, serum, and proteins. It means replacing with liquid, buffer, medium, plasma and the like.
  • the present invention provides: (A) A container main body that encloses an internal space capable of holding a liquid, a mesh sheet that is disposed so as to divide the internal space into a first space and a second space, and the container main body.
  • a cell-containing sample and an enzyme are placed through the inlet in a container provided with an inlet part formed with a liquid inlet and a discharge part provided in the container body and formed with a liquid outlet from the second space.
  • the present invention relates to a method for obtaining a cell concentrate from a living tissue. According to this method, a cell concentrate having a concentration that can be directly administered to a subject can be prepared directly from a living tissue in a closed system, and a high cell recovery rate can be realized.
  • FIG. 3 shows a schematic view of one embodiment of the apparatus (cell suspension treatment apparatus 900).
  • the cell suspension treatment apparatus (900) of the document includes a cell suspension storage container (903) having a solution inlet port (915), a circulation outlet port (916) and a circulation inlet port (917), a cell A container having a suspension inlet (918), a cell suspension outlet (919) and a filtrate outlet (920) is filled with a hollow fiber separation membrane, and the liquid is filtered from the cell suspension and concentrated.
  • a control means for stopping the liquid feed cell concentrate to 906) characterized in that it comprises a.
  • the outlet of the container of the present invention is for injecting a solution into the solution inlet port (915) of the cell suspension storage container (903).
  • the injection path (927) is connected to the cell suspension preparation container connection section (901). At this time, it is preferable that the discharge port of the container of the present invention and the cell suspension treatment apparatus are connected by a closed channel, and the collection container 820 as described above is interposed therebetween. Also good.
  • the cell suspension treatment apparatus (900) connected to the discharge port of the container in the present invention is a cell suspension. The liquid may be manually washed and concentrated.
  • a storage container (903) used in the cell suspension processing apparatus (900) stores a cell suspension for processing, and passes the cell suspension through a cell suspension processing device as described later.
  • the storage container has a solution inlet port, a circulation outlet port, and a circulation inlet port.
  • the solution inlet port refers to a port for supplying the cell suspension into the storage container.
  • the circulation inlet port refers to a port for passing the liquid from the storage container to the cell suspension treatment device, and the circulation outlet port refers to the flow of the cell concentrate concentrated by the cell suspension treatment device through the storage container.
  • These ports are preferably installed in the lower part of the storage container. By installing all these ports at the bottom, the cell suspension supplied through the solution inlet port and the solution for dilution are efficiently agitated with the liquid circulating in the storage container and the circulation circuit. Can be concentrated and diluted.
  • the number of solution inlet ports, circulation outlet ports, and circulation inlet ports may be one each, but may be increased to a plurality as necessary.
  • the solution inlet port can be used not only as a cell suspension but also as a port for a diluting solution or a priming solution.
  • an inlet port for a diluting solution or a priming solution May be provided.
  • a target port different from the above three types of ports may be provided.
  • a collection port for passing the cell concentrate through the collection container can be mentioned. By directly connecting the recovery port of the storage container and the recovery container, the cell concentrate in the storage container can be recovered quickly.
  • the material of the storage container is preferably one that does not affect the cells in the cell suspension or cell concentrate, and a flexible resin material is particularly preferable from the viewpoint of easy handling. Moreover, it is advantageous that the inner surface of the storage container is pear-finished because the remaining liquid when the suspension is discharged from the storage container can be reduced.
  • the volume of the storage container can be used without any particular limitation. However, if it is too large, a large amount of diluent used for dilution is required, and therefore it is preferably 1000 mL or less. Further, the shape of the storage container, the structure of each port, the material, and the like may be appropriately determined depending on the type and volume of the cell suspension to be processed, and are not particularly limited.
  • a ventilation hole may be provided in the upper part of the storage container.
  • the atmosphere in the storage container can be exchanged with the atmosphere and the atmosphere can be exchanged. For example, when the liquid in the storage container is discharged, the storage container is decompressed and the storage container is crushed. There is an advantage to prevent.
  • This vent may be provided with an air filter (908), which can prevent unwanted components from entering the storage container from the outside.
  • the cell suspension treatment device (906) is an apparatus for filtering and concentrating liquid from the cell suspension, and is connected so that the cell suspension can be passed from the storage container.
  • a hollow fiber separation membrane is filled in a container having a cell suspension inlet, a cell suspension outlet, and a filtrate outlet.
  • the cell suspension introduction port is an inlet for introducing the cell suspension from the storage container into the cell suspension processor, and is connected to a circulation inlet port of the storage container.
  • the cell suspension outlet is an outlet for taking out the concentrated cell suspension (cell concentrate). By connecting the cell suspension outlet to the circulation outlet port of the storage container, the cell suspension can be circulated between the storage container and the cell suspension treatment device to perform concentration.
  • the filtrate outlet is an outlet for taking out the filtered liquid from the cell suspension.
  • the hollow fiber separation membrane used in the cell suspension treatment apparatus preferably has a cylindrical container filled with several tens to thousands of hollow fibers bundled.
  • the arrangement of the hollow fiber separation membrane may be linear, bent, or spiral, and the hollow fiber separation membrane is arranged at both ends of the hollow fiber separation membrane between the cell suspension inlet and the cell suspension outlet. If is held, the shape is not particularly limited.
  • a synthetic polymer material can be used for the hollow fiber separation membrane used in the cell suspension treatment device from the viewpoint of the safety and stability of the material.
  • polysulfone-based, polyolefin-based, or cellulose-based polymer materials can be preferably used.
  • the pore diameter of the hollow fiber separation membrane is not limited as long as cells do not leak to the outside, and is preferably as large as possible so that unnecessary components can be efficiently filtered. Specifically, those having an average pore diameter of 0.01 ⁇ m or more and 1.0 ⁇ m or less can be suitably used.
  • a hollow fiber having an inner diameter of 400 ⁇ m or more and 1000 ⁇ m or less is preferably used.
  • a hollow container is filled with a hollow fiber separation membrane, and the end of the hollow fiber is in close contact with the end of the tubular container with an adhesive or the like, and is opened at the end.
  • a header portion serving as a cell suspension inlet or a cell suspension outlet is provided at the end of the cylindrical container so that the cell suspension can flow into and out of the hollow fiber membrane.
  • the cylindrical container only needs to have one or more outlets for filtrate, and the filtrate filtered from the inside of the hollow fiber is discharged from the outlet for filtrate.
  • the cell suspension treatment device generally needs to have a structure in which a hollow fiber separation membrane is packed in a sealed container, but the cell suspension inlet and the cell suspension outlet are outlets for filtrate.
  • a structure separated from the wall material constituting the hollow fiber separation membrane various structures can be adopted.
  • a dialyzer used for hemodialysis can be exemplified as a similar structure.
  • a circuit is installed for the filtrate separated by the hollow fiber separation membrane to flow out. It is preferable to connect the circuit for the filtrate and the waste liquid container (904) because the concern that the filtrate leaks to the outside can be reduced.
  • the filtrate taken out from the outlet for filtrate can be collected by passing it through a waste liquid container or the like.
  • the waste liquid container can be used without particular limitation as long as it does not leak waste liquid.
  • a pump (914) for feeding the filtrate may or may not be installed between the filtrate outlet of the cell suspension treatment device and the waste container.
  • the filtrate can be discharged at a constant flow rate, so that the treatment time can be made constant and the filtration efficiency in the cell suspension treatment device can be increased. It becomes possible to control. That is, by driving the pump, the discharge of the filtrate from the cell suspension treatment device is promoted, and as a result, the concentration treatment in the cell suspension treatment device can be promoted.
  • rapid recovery can be achieved by stopping the pump.
  • the collected filtrate may be discarded as it is, or may be reused by performing reprocessing such as sterilization.
  • the cell suspension processor sends the cell concentrate in the cell suspension processor to a collection container.
  • a cell concentrate recovery port may be provided. This cell concentrate recovery port can be connected to a recovery container (905).
  • the circulation circuit (930) includes a communication pipe for introduction communicating with a circulation inlet port of the storage container and a cell suspension introduction port of the cell suspension treatment device, and a cell suspension of the cell suspension treatment device. It is a circuit comprising a lead-out port and a lead-out communicating tube that communicates with the circulation outlet port of the storage container. Through this circulation circuit, a cell concentrate can be produced by performing concentration while circulating the cell suspension between the storage container and the cell suspension treatment device.
  • a tube constituting the circulation circuit a general plastic tube can be suitably used. Vinyl chloride can be suitably used in terms of safety and durability.
  • the circulation circuit is preferably provided with a pump (913) from the viewpoint of facilitating control of circulation of the cell suspension or cell concentrate.
  • a pump There is no particular limitation on the number of pumps, but one is sufficient from the viewpoint of easy control.
  • the position of the pump it may be installed in either the introduction communication pipe or the extraction communication pipe, but if it is installed in the introduction communication pipe, the cell suspension introduction port of the cell suspension treatment device It is preferable because a solution having a high pressure can be introduced into the liquid and the liquid can be efficiently separated.
  • a branch (not shown) is provided between the pump (913) and the cell suspension inlet (918), an air chamber is provided at the branch, and the tip of the branch is connected to a pressure gauge. It is preferable.
  • a branching portion may be provided on either of the circulation circuits.
  • the branch portion By connecting the branch portion to the recovery container (905) by piping, the path from the branch portion to the recovery container is used as the final recovery path (931), and the cell suspension
  • the cell concentrate in the liquid processor and the circulation circuit can be quickly recovered in the recovery container.
  • the branching section be installed at a position as close as possible to the circulation outlet port because the amount of residual liquid remaining in the circulation circuit from the branching section to the outlet port can be reduced in the recovery step.
  • the recovery container (905) is a container for recovering the cell concentrate concentrated to a predetermined concentration.
  • the collection container is preferably a flexible plastic container. Moreover, if pear processing is given to the inner surface, there exists an advantage which can reduce the residual liquid after collect
  • the shape of the collection container is not particularly limited. For example, when the volume increases, the inner area of the container with which the collected cells come into contact increases, and the attached cells may remain in the container and lead to cell loss. Therefore, the capacity inside the container is preferably small.
  • the collection path (931) is a path for sending the cell concentrate in the storage container, the cell suspension treatment device, and the circulation circuit to the collection container.
  • a general plastic tube can be used as the tube constituting the recovery path, and among these, a vinyl chloride tube can be preferably used from the viewpoint of safety and durability.
  • Examples of the recovery path include the following three aspects. 1) When a branch portion is provided on the circulation circuit, a path connecting the branch portion and the recovery container is a recovery path. 2) When the recovery port of the storage container and the recovery container are connected, the connected path becomes the recovery path. 3) When the cell concentrate recovery port of the cell suspension treatment device and the recovery container are connected, this connected path becomes the recovery path.
  • any one of the above embodiments is preferable, and two or more may be used in combination.
  • the injection path (927) is a path for injecting the solution into the solution inlet port of the storage container.
  • a general plastic tube can be used, and among them, a vinyl chloride tube can be preferably used from the viewpoint of safety and durability.
  • a priming solution for priming may be included. Diluents include physiological saline, infusion, distilled water, buffer, culture medium, plasma and inorganic salts, saccharides, serum, liquids containing proteins, etc.
  • physiological saline and infusion are suitable.
  • the priming solution include physiological saline, infusion solution, distilled water, buffer solution, culture medium, plasma, inorganic salts, saccharides, serum, and liquids containing protein. It can be used suitably.
  • the same solution may be used for the diluent and the priming solution, or different solutions may be used.
  • a pump (912) for feeding a liquid is installed in the injection path.
  • the pump can stably feed liquid to the storage container.
  • the position where the pump is installed is a junction of circuits connected to the cell suspension preparation container connection part (901), the diluent container connection part (902), and the optionally provided priming liquid container connection part (926).
  • a solution inlet port are preferable because the number of pumps required for liquid feeding can be reduced.
  • a branch (not shown) is provided between the pump (912) and the clamp (921 or 922), an air chamber is provided at the branch, and the tip of the branch is connected to a pressure gauge. Is preferred.
  • the detection means is means for detecting the amount of the cell concentrate in the storage container or the communication pipe for introduction of the circulation circuit.
  • Examples of the means for detecting the liquid amount in the storage container include using a bubble sensor that directly detects the liquid level of the storage liquid in the storage container.
  • a tube is installed so as to be parallel to the vertical direction with respect to the storage container, and a circuit in which the storage container and the tube communicate with each other below is used.
  • the bubble sensor may be installed in this tube by adjusting it so that it is equal to the liquid level. With this means, the liquid level in the tube can be detected by the bubble sensor as the liquid level in the storage container.
  • a chamber having an inner diameter larger than that of the tube it is expected to reduce the occurrence of defects that are detected by the intrusion of bubbles in the tubes installed in parallel.
  • a bubble sensor (911) is provided in the introduction communication pipe (928) communicating with the circulation inlet port of the storage container. If it is this form, since the cell suspension can be concentrated more than the means for detecting the amount of liquid in the storage container, the amount of the concentrated suspension (cell concentrate) can be reduced, There is an advantage that the amount of unnecessary components in the suspension can be reduced. Further, the position of the bubble sensor to be installed in the introduction communication pipe is not particularly limited, but by installing it at a position close to the storage container, the length of the circuit connecting the storage container and the bubble sensor can be increased. Can be shortened.
  • the bubble sensor (910) may be installed in the injection path (927) connected to the solution inlet port of the storage container.
  • a solution such as a cell suspension, a diluent, a priming solution in the storage container.
  • the bubble sensor in the injection path, the entire amount of the target liquid can be processed without setting the pump driving time for each processing. There is an advantage that can be. Moreover, it can also be set as the process of adding a fixed quantity of solution from the drive time of a pump.
  • the process can be performed by setting the driving time of the pump.
  • This bubble sensor can be installed anywhere in the injection path, but it is more advantageous to install the bubble sensor as close to the storage container as possible to reduce the amount of liquid remaining in the injection path.
  • another bubble sensor (909) may be provided on the upper part of the storage container.
  • this bubble sensor it is possible to determine the presence or absence of a solution near the top in the storage container. That is, when a liquid exceeding the capacity of the storage container is supplied, the sensor can detect and notify the user as an alarm.
  • a commonly used pump or bubble sensor used in the cell suspension treatment apparatus (900) can be used. It is also possible to switch the flow path by providing a clamp at a desired position in the circuit.
  • These pumps, bubble sensors, and clamps are not particularly limited, and for example, those used in dialysis machines and the like may be used.
  • Cell-containing sample An example of a cell-containing sample used as a starting material in the method of the present invention or a cell-containing sample used for preparing an enzyme-treated solution is biological tissue.
  • the biological tissue is not particularly limited as long as it is collected from animal tissue, for example, fat, skin, blood vessel, cornea, oral cavity, kidney, liver, pancreas, heart, nerve, muscle, prostate, intestine, amniotic membrane, placenta, The thing derived from an umbilical cord etc. is mentioned.
  • the method of the present invention is particularly useful for removing stromal vascular fraction (SVF) cells from collected adipose tissue.
  • another example of the cell-containing sample is a cell culture prepared in vitro.
  • the cell suspension or cell concentrate obtained by the present invention is used for leukemia treatment, myocardial regeneration and blood vessel regeneration, stem cell exhaustion disease, bone disease, cartilage disease, ischemic disease, vascular disease, neurological disease, burn, chronic inflammation. It can be used for regenerative medicine such as heart disease, immune deficiency, coulomb disease, breast augmentation, wrinkle removal, cosmetic molding, tissue enlargement such as tissue depression.
  • the obtained cells can be seeded and cultured in a structural material such as a scaffold and used for treatment. Alternatively, the resulting cells may be stored frozen for future therapeutic uses.
  • the preparation of the cell suspension that has undergone the separation treatment can be carried out all in a closed system and in the same container.
  • the passage of the enzyme-treated solution through the mesh sheet smoothly proceeds inside the container, even an operator who does not have a special technique can easily prepare the cell suspension.
  • the cell suspension preparation container of the present invention does not have a particularly complicated structure, it provides a low-cost device capable of preparing a cell suspension in a short time without causing clogging of the mesh sheet. can do.
  • the present invention is very useful for collecting an SVF fraction from adipose tissue, which has conventionally been troublesome.
  • pore diameter represents the mesh opening, and is calculated based on the result of measurement with a luminometer.
  • Example 1 When the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is ⁇ (°), clogging occurs when 90- ⁇ is set to 45. 30 mL of the cell suspension was allowed to pass through until the occurrence of (stopping the flow of the liquid passing through the mesh sheet). Cell recovery was 95%.
  • Example 2 When the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is ⁇ (°), clogging occurs when 90- ⁇ is set to 30 32 mL of cell suspension could be passed before the occurrence of.
  • the cell recovery rate was 98%.
  • FIG. 4 shows the relationship between 90- ⁇ and the throughput of the cell suspension, where ⁇ (°) is the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet.
  • FIG. 5 is a graph showing the relationship between 90- ⁇ and the cell recovery rate. It was confirmed that by using a mesh sheet having a pore size of 95 ⁇ m and setting 90- ⁇ to less than 50, a high volume cell suspension can be treated and a high cell recovery rate can be achieved.
  • Test Using Cell Suspension Preparation Container A test was conducted using a cell suspension preparation container 1 having the structure shown in FIGS. 1-1 to 2-2.
  • the first side wall 15 and the second side wall 16 are made of a flexible resin sheet.
  • Three types of containers having different pore diameters of the incorporated polyester mesh sheet 40 were prepared.
  • the side wall of the container was manufactured using flexible polyvinyl chloride.
  • the outer diameter of the tube sandwiched between the container ends as the input part 21 and the discharge part 22 is 8 mm, and the container internal side end part 32 of the discharge part 31 from the container internal side end part 22 of the input part 21. The distance to was about 20 cm.
  • the membrane area of the mesh sheet was 208 cm 2 .
  • the cell suspension preparation containers are suspended so that the input part 21 is at the top, and 50 mL of the cell suspension derived from the same individual is allowed to flow through each container by natural dropping and is taken out from the discharge port 30. It was.
  • the cell concentration of each cell suspension was 1.4 ⁇ 10 6 cells / mL.
  • the mesh sheet in the container at the time of liquid flow has 90- ⁇ of about 1 when the narrow angle formed by the normal L of the surface along the mesh sheet and the liquid flow direction F (vertical direction) is ⁇ (°). Met.
  • Example 3 When a container having a mesh sheet with a pore size of 95 ⁇ m and an open area ratio of 46% was used, clogging did not occur during liquid flow, and the cell recovery rate was 95%.
  • Example 4 When a container having a mesh sheet with a pore size of 200 ⁇ m and an open area ratio of 61% was used, no clogging occurred during the flow of liquid, and the cell recovery rate was 100%.
  • Example 5 When a container having a mesh sheet with a pore size of 300 ⁇ m and an open area ratio of 65% was used, clogging did not occur during liquid flow, and the cell recovery rate was 100%.
  • FIG. 6 is a graph showing the relationship between the pore size of the mesh sheet and the cell recovery rate. It was confirmed that when the angle of the mesh sheet surface with respect to the liquid passing direction was set to the same angle, the cells could be collected at a high recovery rate at least when the pore diameter of the mesh sheet was 95 ⁇ m to 300 ⁇ m.
  • the cell suspension preparation container having the structure shown in FIGS. 1-1 and 2-2 and a cell concentration washing system were connected.
  • the cell suspension was prepared in a closed system, and the results were compared with the results when a cell suspension was prepared in an open system by a conventional method from a sample obtained from the same individual.
  • the cell concentration washing system (manufactured by Kaneka) is an example of “a cell suspension treatment apparatus capable of washing and concentrating a cell suspension in a closed system” disclosed in the present specification.
  • the container for cell suspension preparation used what the pore diameter of the mesh sheet
  • Example 6 A fat tissue sample and a 0.075% collagenase aqueous solution were prepared in a cell suspension preparation container 1, and 102 mL of a cell suspension having a cell concentration of 1.6 ⁇ 10 6 cells / mL was prepared in the container.
  • the enzyme reaction was performed while shaking the container with a shaker.
  • the enzyme reaction was performed with the inlet 20 and outlet 30 closed.
  • the solution in the container was separated into two layers, an oil layer and an aqueous layer.
  • the container was hung with the input part 21 facing upward, and the boundary between the two separated layers was clamped so that the components of the oil layer did not flow toward the discharge part 31.
  • the mesh sheet 40 in the container had 90- ⁇ of about 1 when the narrow angle formed by the normal L of the surface along the mesh sheet and the liquid flow direction F (vertical direction) was ⁇ (°). .
  • negative pressure is applied from the discharge port, the solution is discharged from the container at a rate of 300 mL / min from the discharge port, the cell suspension is transferred to the connected cell concentration washing system, and washing is performed. It was.
  • the cell recovery rate in the cell suspension obtained after washing was 83%.
  • Example 3 A cell suspension having a cell concentration of 1.6 ⁇ 10 6 cells / mL was prepared in a centrifuge tube using the same adipose tissue sample and 0.075% collagenase solution as in Example 6. As usual, 20 mL of the resulting cell suspension was opened by opening the centrifuge tube lid, the supernatant liquid was discharged, washing liquid was added, the lid was closed, and centrifugation was repeated and concentrated and washed. Was 68%.
  • FIG. 7 is a graph showing the results in Example 6 and Comparative Example 3.
  • a container capable of forming a closed system container for cell suspension preparation
  • an automated cell concentration washing system centrifugation is a common method. It was confirmed that the cells could be recovered at a higher cell recovery rate.
  • SYMBOLS 1 Cell suspension preparation container, 10 ... Container main body, 11 ... First space, 12 ... Second space, 13 ... Internal space, 15 ... First side wall, 16 ... Second side wall, 20 ... Input port, DESCRIPTION OF SYMBOLS 21 ... Input part, 22 ... End of 1st space side of input part, 30 ... Discharge port, 31 ... Discharge part, 32 ... End of 2nd space side of discharge part, 40 ... Mesh sheet, 41 ... Perimeter of mesh sheet , 150 ... first side wall peripheral part, trough 160 ... second side wall peripheral part, 901 ... cell suspension preparation container connection part, 902 ... dilution liquid bag connection part, 903 ...

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Abstract

The purpose of the present invention is to provide a method for simply preparing a cell suspension from a living tissue with a high cell recovery rate, and a container used in the method. Provided is a container for cell suspension preparation that is equipped with: a container body 10 that encloses an interior space 13 capable of holding a liquid; a mesh sheet 40 disposed so as to divide the interior space 13 into a first space 11 and a second space 12; an input unit 21 provided to the container body 10; and a discharge unit 31 provided to the container body 10. An input port 20 for pouring liquid into the first space 11 is formed in the input unit 21. A discharge port 30 for discharging liquid from the second space 12 is formed in the discharge unit 31. If the value of the narrow angle formed by the flow direction F of the liquid discharged from the discharge port 30 and a line L normal to the plane conforming to the mesh sheet 40 is taken as θ(º), 90-θ is less than 50. Also provided is a method for preparing a cell suspension from a cell-containing specimen using the container.

Description

細胞懸濁液調製用容器および細胞懸濁液の調製方法Cell suspension preparation container and cell suspension preparation method
 本発明は、採取した生体組織などの細胞含有試料の酵素処理液から夾雑物を除去して細胞懸濁液を調製する方法、およびその方法に用いるための細胞懸濁液調製用容器に関する。 The present invention relates to a method for preparing a cell suspension by removing impurities from an enzyme-treated solution of a cell-containing sample such as a collected biological tissue, and a cell suspension preparation container for use in the method.
 細胞医療の分野では、治療に用いる細胞を患者に投与する場合、細胞を含む組織を生体から採取したのち、一度生体外で分離操作や洗浄などを行い、さらに投与に適した濃度の細胞懸濁液に調製して投与することが一般的に行われている。分離操作の種類としては、例えば不織布を用いたフィルター分離や遠心分離が知られている。 In the field of cell medicine, when cells used for treatment are administered to a patient, the tissue containing the cells is collected from the living body, then once separated and washed in vitro, and a cell suspension at a concentration suitable for administration. It is a common practice to prepare and administer a solution. As a kind of separation operation, for example, filter separation using a non-woven fabric or centrifugation is known.
 例えば、特許文献1には、血液の入口と出口とを有する可撓性容器と該容器内部を入口側と出口側とに隔てるように配置したシート状の血液処理フィルター材を含む血液処理フィルターが開示されている。また、特許文献2には、1次側流入口と1次側流出口とをつなぐ、膜周辺部から膜中心部へ至る渦巻き形の1次側流路と、濾過膜を透過した濾液が2次側流出口に至る2次側流路が形成されている、血中低分子量物質濃度測定試料採取用のプレート型膜モジュールが開示されている。 For example, Patent Document 1 discloses a blood processing filter including a flexible container having an inlet and an outlet for blood and a sheet-like blood processing filter material arranged so that the inside of the container is separated from the inlet side and the outlet side. It is disclosed. Patent Document 2 discloses a spiral-shaped primary flow path connecting the primary side inlet and the primary side outlet and extending from the membrane periphery to the center of the membrane, and 2 filtrates permeated through the filtration membrane. A plate-type membrane module for collecting a low-molecular-weight substance concentration measurement sample in blood in which a secondary-side flow path leading to a secondary-side outlet is formed is disclosed.
 一方、特許文献3には、生体組織から穿刺針を用いて採取した組織片から特定の組織幹細胞を得る際に、閉鎖系において(1)細孔径200~300μmフィルターに通過させることで組織片から血球成分を除去する工程、(2)抗生物質を含有したリン酸緩衝液で洗浄する工程、(3)得られた組織片に酵素処理を施し細胞懸濁液とする工程、(4)比重の軽い細胞を浮かせることで目的の細胞と分離させる工程、(5)その目的の細胞の懸濁液を再び、細孔径250~300μmフィルターを通過させる工程、(6)さらに細孔径20~40μmフィルターに通過させる工程、(7)遠心分離、及びまたは400~500nmフィルターを通過させることで細胞懸濁液より目的の細胞を得る工程を行うことが開示されている。 On the other hand, in Patent Document 3, when specific tissue stem cells are obtained from a tissue piece collected from a living tissue using a puncture needle, (1) the pore size is passed through a filter of 200 to 300 μm in a closed system. A step of removing blood cell components, (2) a step of washing with a phosphate buffer containing an antibiotic, (3) a step of subjecting the obtained tissue piece to enzyme treatment to form a cell suspension, and (4) a specific gravity A step of separating light cells from the target cells by floating; (5) a step of passing the suspension of the target cells again through a filter having a pore size of 250 to 300 μm; and (6) a filter having a pore size of 20 to 40 μm. It is disclosed to perform a step of passing, (7) centrifugation and / or a step of obtaining a target cell from a cell suspension by passing through a 400-500 nm filter.
特開2011-72816号公報JP 2011-72816 A 特開平10-99659号公報JP-A-10-99659 特開2005-287479号公報JP 2005-287479 A
 特許文献1および2に開示されているようなフィルターを用いた分離操作は、血液等の液体組織から、凝集物や白血球等の好ましくない成分を除去するために行われ、一部をフィルター内部に残すことを意図している。しかし、例えば脂肪組織の酵素処理物から未消化物などの夾雑物を除去する場合にフィルターを用いた分離操作を行うと、早期にフィルターの目詰まりが発生してしまう。そのため、十分な量の細胞を得るためには、広大な面積を有するフィルターを使用しなければならない。一方、遠心分離による分離操作では、装置が大型になりがちであり、コスト高に繋がり、さらに利用できる施設が限定されてしまう。また、細胞を洗浄する際には、遠心分離により細胞から分離した上清を取り除くが、その際に細胞は大気に接触し、汚染などが発生する危険がある。そもそも、遠心分離にかけられてペレット化した細胞は損傷を受け死んでしまうことが多い。 The separation operation using a filter as disclosed in Patent Documents 1 and 2 is performed to remove undesirable components such as aggregates and leukocytes from a liquid tissue such as blood, and a part of the separation operation is performed inside the filter. Intended to leave. However, for example, when a separation operation using a filter is performed to remove impurities such as undigested material from an enzyme-treated product of adipose tissue, the filter is clogged at an early stage. Therefore, in order to obtain a sufficient amount of cells, a filter having a large area must be used. On the other hand, in the separation operation by centrifugation, the apparatus tends to be large, leading to high costs and further limiting the facilities that can be used. In addition, when washing the cells, the supernatant separated from the cells by centrifugation is removed, but at that time, the cells come into contact with the air and there is a risk of contamination. In the first place, cells that have been pelleted by centrifugation are often damaged and die.
 一方、特許文献3では、閉鎖系で生体組織を酵素処理するために注射器様装置を用いることが記載されているが、閉鎖系を維持しながら生体組織に酵素を供給するための具体的な手段は開示されていない。注射器様装置の内部で閉鎖系を維持しながら生体組織に酵素を実際に供給するためには複雑な装置が必要であり、実現は容易ではないと考えられる。 On the other hand, Patent Document 3 describes the use of a syringe-like device for enzyme treatment of living tissue in a closed system, but specific means for supplying enzymes to living tissue while maintaining the closed system. Is not disclosed. In order to actually supply an enzyme to a living tissue while maintaining a closed system inside the syringe-like device, a complicated device is required and it is considered that the realization is not easy.
 そこで、本発明は、生体組織などの細胞含有試料から簡便にかつ高い細胞回収率で細胞懸濁液を調整するための方法、およびそれに用いる容器を提供することを目的とする。 Therefore, an object of the present invention is to provide a method for preparing a cell suspension easily from a cell-containing sample such as a living tissue with a high cell recovery rate, and a container used therefor.
 本発明者らは、上記のような問題に鑑み、生体組織などの細胞含有試料の酵素処理液から夾雑物を除去するためのメッシュシートを備えた、目詰まり等を生じさせずに細胞懸濁液を調製可能な構成を有する容器、およびそれを用いた細胞懸濁液の調製方法を見出した。前記酵素処理液は、前記容器の内部で前記細胞含有試料の酵素処理を実施して得てもよいし、前記容器外で調製してもよい。本発明の要旨は以下のとおりである。 In view of the above problems, the present inventors have provided a mesh sheet for removing impurities from an enzyme-treated solution of a cell-containing sample such as a living tissue, and suspended the cell without causing clogging or the like. The present inventors have found a container having a constitution capable of preparing a liquid and a method for preparing a cell suspension using the container. The enzyme treatment solution may be obtained by performing an enzyme treatment of the cell-containing sample inside the container, or may be prepared outside the container. The gist of the present invention is as follows.
(1)細胞懸濁液調製用容器であって、
 液体を保持可能な内部空間を内包する容器本体と、
 前記内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、
 前記容器本体に設けられ、前記第一空間への液体の投入口が形成された投入部と、
 前記容器本体に設けられ、前記第二空間からの液体の排出口が形成された排出部と、
を備え、
 前記排出口から排出される液体の流れの方向と、前記メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θが50未満である、前記容器。
(2)前記メッシュシートの細孔径が50~300μmである、(1)に記載の容器。
(3)前記容器本体が可撓性を有する、(1)または(2)に記載の容器。
(4)前記容器本体の少なくとも一部が透明または半透明の材料からなる、(1)~(3)のいずれかに記載の容器。
(5)前記メッシュシートの開孔率が40%以上である、(1)~(4)のいずれかに記載の容器。
(6)前記メッシュシートの前記内部空間に露出する部分のうち、該部分を平面視したときの面積に対して50%以上の面積の領域が、90-θが50未満となる領域である、(1)~(5)のいずれかに記載の容器。
(7)細胞懸濁液調製用容器であって、
 液体を保持可能な内部空間を内包する容器本体と、
 前記内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、
 前記容器本体に設けられ、前記第一空間への液体の投入口が形成された投入部と、
 前記容器本体に設けられ、前記第二空間からの液体の排出口が形成された排出部と、
を備え、
 前記容器本体が、前記メッシュシートを間に介して対向する第一側壁と第二側壁とを含み、
 前記第一側壁と前記メッシュシートとが前記第一空間を囲い、
 前記第二側壁と前記メッシュシートとが前記第二空間を囲い、
 前記投入部が、前記第一側壁の周縁部と前記メッシュシートの周縁部との間に、前記投入口を介して前記第一空間と外部とを連通するように配置されており、
 前記排出部が、前記第二側壁の周縁部と前記メッシュシートの周縁部との間に、前記排出口を介して前記第二空間と外部とを連通するように配置されており、
 前記第一側壁、前記第二側壁、及び、前記メッシュシートが周縁部において一体化されている、前記容器。
(8)前記投入部と、前記排出部とが、前記容器本体の対向する位置に配置されており、 前記投入部の、前記第一空間の側の端の、前記第一側壁と前記第二側壁とが対向する方向に沿った幅をW1、
 前記排出部の、前記第二空間の側の端の、前記第一側壁と前記第二側壁とが対向する方向に沿った幅をW2、
 W1とW2との平均値をW、
 前記投入部の、前記第一空間の側の端と、前記排出部の、前記第二空間の側の端との間の距離をD
としたとき、
 D/Wが12以上である、(7)に記載の容器。
(9)前記第一側壁及び前記第二側壁が可撓性を有する、(7)または(8)に記載の容器。
(10)細胞含有試料から細胞懸濁液を調製するための方法であって、
(a)液体を保持可能な内部空間を内包する容器本体と、
 前記内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、
 前記容器本体に設けられ、前記第一空間への液体の投入口が形成された投入部と、
 前記容器本体に設けられ、前記第二空間からの液体の排出口が形成された排出部と、
を備える容器において、前記投入口を通じて細胞含有試料と酵素を入れ、前記第一空間内で酵素反応を実施して酵素処理液を生成する、及び/又は、前記投入口を通じて細胞含有試料の酵素処理液を入れる工程、
(b)前記酵素処理液を前記メッシュシートに通して夾雑物を除去し、前記第二空間側に細胞懸濁液を生成し、生成された前記細胞懸濁液を、前記排出口を通じて排出する工程、を含む、前記方法。
(11)工程(b)において、前記排出口を通じて排出される前記細胞懸濁液の流れ方向と、前記メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θが50未満となるように、前記細胞懸濁液を排出する、(10)に記載の方法。
(12)前記容器が、(1)~(9)のいずれかに記載の容器である、(10)または(11)に記載の方法。
(13)前記細胞含有試料が、脂肪、皮膚、血管、角膜、口腔、腎臓、肝臓、膵臓、心臓、神経、筋肉、前立腺、腸、羊膜、胎盤および臍帯からなる群から選択される1以上に由来する、(10)~(12)のいずれかに記載の方法。
(14)前記投入口および/または前記排出口が、シリコンゴムおよび/またはニードルレスポートにより封鎖されている、(10)~(13)のいずれかに記載の方法。
(15)前記排出口が、細胞懸濁液を閉鎖系で洗浄および濃縮することができる細胞懸濁液処理装置に接続されており、
(c)前記排出口から排出された前記細胞懸濁液を、前記装置により閉鎖系で洗浄および濃縮し、細胞濃縮液を得る工程
をさらに含む、(10)~(14)のいずれかに記載の方法。
(1) A cell suspension preparation container,
A container body containing an internal space capable of holding liquid;
A mesh sheet arranged to divide the internal space into a first space and a second space;
A charging unit provided in the container body, and formed with a liquid charging port into the first space;
A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
With
The container in which 90-θ is less than 50, where θ (°) is a narrow angle formed between the flow direction of the liquid discharged from the discharge port and the normal line of the surface along the mesh sheet .
(2) The container according to (1), wherein the mesh sheet has a pore diameter of 50 to 300 μm.
(3) The container according to (1) or (2), wherein the container body has flexibility.
(4) The container according to any one of (1) to (3), wherein at least a part of the container body is made of a transparent or translucent material.
(5) The container according to any one of (1) to (4), wherein the mesh sheet has a porosity of 40% or more.
(6) Of the portion exposed to the internal space of the mesh sheet, a region having an area of 50% or more with respect to the area when the portion is viewed in plan is a region where 90-θ is less than 50. (1) A container according to any one of (5).
(7) A cell suspension preparation container,
A container body containing an internal space capable of holding liquid;
A mesh sheet arranged to divide the internal space into a first space and a second space;
A charging unit provided in the container body, and formed with a liquid charging port into the first space;
A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
With
The container body includes a first side wall and a second side wall facing each other with the mesh sheet interposed therebetween,
The first side wall and the mesh sheet surround the first space;
The second side wall and the mesh sheet surround the second space;
The insertion portion is disposed between the peripheral portion of the first side wall and the peripheral portion of the mesh sheet so as to communicate the first space and the outside via the input port,
The discharge part is arranged between the peripheral part of the second side wall and the peripheral part of the mesh sheet so as to communicate the second space and the outside through the discharge port,
The said container by which said 1st side wall, said 2nd side wall, and said mesh sheet are integrated in the peripheral part.
(8) The charging unit and the discharging unit are disposed at positions facing the container body, and the first side wall and the second of the end of the charging unit on the first space side The width along the direction facing the side wall is W1,
The width of the end of the discharge portion on the second space side along the direction in which the first side wall and the second side wall face each other is W2,
The average value of W1 and W2 is W,
The distance between the end of the input portion on the first space side and the end of the discharge portion on the second space side is D
When
The container according to (7), wherein D / W is 12 or more.
(9) The container according to (7) or (8), wherein the first side wall and the second side wall have flexibility.
(10) A method for preparing a cell suspension from a cell-containing sample,
(A) a container body containing an internal space capable of holding a liquid;
A mesh sheet arranged to divide the internal space into a first space and a second space;
A charging unit provided in the container body, and formed with a liquid charging port into the first space;
A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
A cell-containing sample and an enzyme are introduced through the inlet, and an enzyme treatment solution is generated by performing an enzyme reaction in the first space, and / or an enzyme treatment of the cell-containing sample is conducted through the inlet. The process of adding liquid,
(B) The enzyme treatment liquid is passed through the mesh sheet to remove impurities, a cell suspension is generated on the second space side, and the generated cell suspension is discharged through the discharge port. A process comprising the steps of:
(11) When the narrow angle formed by the flow direction of the cell suspension discharged through the discharge port and the normal of the surface along the mesh sheet is θ (°) in step (b) The method according to (10), wherein the cell suspension is discharged so that 90-θ is less than 50.
(12) The method according to (10) or (11), wherein the container is the container according to any one of (1) to (9).
(13) The cell-containing sample is one or more selected from the group consisting of fat, skin, blood vessel, cornea, oral cavity, kidney, liver, pancreas, heart, nerve, muscle, prostate, intestine, amniotic membrane, placenta and umbilical cord The method according to any one of (10) to (12), which is derived.
(14) The method according to any one of (10) to (13), wherein the input port and / or the discharge port are sealed with silicon rubber and / or a needleless port.
(15) the discharge port is connected to a cell suspension treatment apparatus capable of washing and concentrating the cell suspension in a closed system;
(C) The method according to any one of (10) to (14), further comprising a step of washing and concentrating the cell suspension discharged from the discharge port with the device in a closed system to obtain a cell concentrate. the method of.
 本明細書は本願の優先権の基礎となる日本国特許出願番号2016-082252号の開示内容を包含する。 This specification includes the disclosure of Japanese Patent Application No. 2016-082522, which is the basis of the priority of the present application.
 本発明の方法によれば、採取した生体組織などの細胞含有試料又は細胞含有試料の酵素処理液から遠心分離などの開放系の操作を経ずに閉鎖系で細胞懸濁液を調製することができる。また、本発明の細胞懸濁液調製用容器をその方法に用いることにより、メッシュの目詰まりなどを発生させずに、優れた処理量および細胞回収率で細胞懸濁液を調製することができる。 According to the method of the present invention, a cell suspension can be prepared in a closed system without an open system operation such as centrifugation from a cell-containing sample such as a collected biological tissue or an enzyme-treated solution of a cell-containing sample. it can. Further, by using the cell suspension preparation container of the present invention in the method, it is possible to prepare a cell suspension with an excellent throughput and cell recovery rate without causing clogging of the mesh. .
本発明の細胞懸濁液調製用容器1の一実施形態を示す斜視図である。It is a perspective view which shows one Embodiment of the container 1 for cell suspension preparation of this invention. 図1-1の細胞懸濁液調製用容器1のA-A線切断部断面図である。FIG. 1 is a cross-sectional view taken along line AA of the cell suspension preparation container 1 of FIG. 1-1. 図1-1の細胞懸濁液調製用容器1のB-B線切断部断面図である。FIG. 2 is a cross-sectional view taken along the line BB of the cell suspension preparation container 1 of FIG. 1-1. 図1-1に示した本発明の細胞懸濁液調製用容器1の内部空間13に液体を入れた状態を表す斜視図である。FIG. 1 is a perspective view showing a state in which a liquid is placed in the internal space 13 of the cell suspension preparation container 1 of the present invention shown in FIG. 1-1. 図2-1の細胞懸濁液調製用容器1のC-C線切断部断面図である。FIG. 2 is a cross-sectional view taken along the line CC of the cell suspension preparation container 1 of FIG. 2-1. 図2-1の細胞懸濁液調製用容器1のC-C線切断部の排出部31近傍部分の概略端面図である。FIG. 2 is a schematic end view of the vicinity of a discharge part 31 of a CC line cutting part of the cell suspension preparation container 1 of FIG. 2-1. 本発明の細胞懸濁液調製用容器に接続する細胞懸濁液処理装置の一実施形態の概略図である。It is the schematic of one Embodiment of the cell suspension processing apparatus connected to the container for cell suspension preparation of this invention. 細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θと細胞懸濁液の処理量の関係を示したグラフである。A graph showing the relationship between 90-θ and the amount of cell suspension treated, where θ (°) is the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet It is. 細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θと細胞回収率の関係を示したグラフである。10 is a graph showing the relationship between 90-θ and the cell recovery rate when the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is θ (°). メッシュシートの細孔径と細胞回収率の関係を示したグラフである。It is the graph which showed the relationship between the pore diameter of a mesh sheet | seat, and a cell recovery rate. 実施例6と比較例3における結果を示すグラフである。It is a graph which shows the result in Example 6 and Comparative Example 3. 図8は、細胞含有試料と酵素とを収容して酵素処理を行い、酵素処理液を調製するための酵素処理用容器810と、調製された酵素処理液を収容し細胞懸濁液を生成する本発明の一実施形態に係る細胞懸濁液調製用容器1と、生成された細胞懸濁液を回収する回収用容器820とを備える細胞懸濁液調製用システム800の構成を示す概略図である。FIG. 8 shows an enzyme treatment container 810 for preparing an enzyme treatment solution by containing a cell-containing sample and an enzyme, and a cell suspension containing the prepared enzyme treatment solution. 1 is a schematic diagram showing a configuration of a cell suspension preparation system 800 including a cell suspension preparation container 1 according to an embodiment of the present invention and a collection container 820 that collects the generated cell suspension. is there.
(細胞懸濁液調製用容器)
 図1-1~1-3は、本発明の細胞懸濁液調製用容器の一実施形態を示す概略図である。本実施形態の細胞懸濁液調製用容器1は、液体を保持可能な内部空間13を内包する容器本体10と、内部空間13を、第一空間11と第二空間12とに区切るように配置されたメッシュシート40と、容器本体10に設けられ、前記第一空間11への液体の投入口20が形成された投入部21と、容器本体10に設けられ、前記第二空間12からの液体の排出口30が形成された排出部31とを備える。図1-1~1-3では、本実施形態の細胞懸濁液調製用容器1の、内部空間13に内容物が収容されていないときの形状の一例を模式的に示す。図2-1および2-2には、本実施形態の細胞懸濁液調製用容器1の内部空間13に液体を満たしたときの形状の一例を示す。ただし図2-1および2-2では図示の簡素化のために液体の描写は省略している。また、細胞懸濁液調製用容器1の内部空間13に液体を満たすためには排出口30が封鎖されている必要があるが、封鎖するための手段の描写も省略している。
(Cell suspension preparation container)
FIGS. 1-1 to 1-3 are schematic views showing one embodiment of the cell suspension preparation container of the present invention. The cell suspension preparation container 1 of this embodiment is arranged so that a container body 10 containing an internal space 13 capable of holding a liquid and the internal space 13 are divided into a first space 11 and a second space 12. The mesh sheet 40, the container main body 10 and the charging section 21 provided with the liquid inlet 20 into the first space 11, and the container main body 10 and the liquid from the second space 12 are provided. The discharge part 31 in which the discharge port 30 of this was formed is provided. FIGS. 1-1 to 1-3 schematically show an example of the shape of the cell suspension preparation container 1 of the present embodiment when no contents are contained in the internal space 13. FIGS. 2-1 and 2-2 show an example of the shape when the liquid is filled in the internal space 13 of the cell suspension preparation container 1 of the present embodiment. However, in FIGS. 2-1 and 2-2, the depiction of the liquid is omitted for simplicity of illustration. Further, in order to fill the internal space 13 of the cell suspension preparation container 1 with a liquid, the discharge port 30 needs to be sealed, but depiction of means for sealing is also omitted.
(容器本体)
 液体を保持可能な内部空間13の外殻を構成する容器本体10は、内部にメッシュシート40を後述する態様で設けることができ、かつ内部に保持する細胞等に影響を与えるようなものでなければ、どのような材質のもので、どのように形成されていてもよい。容器本体10とメッシュシート40は、例えば、メッシュシート40を間に介して対向する第一側壁15と第二側壁16とを含み、第一側壁15とメッシュシート40とが第一空間11を囲い、第二側壁16とメッシュシート40とが第二空間12を囲うように構成することができる。図1-1~1-3は、その実施態様を表したものである。この実施態様では、第一側壁15と、第二側壁16と、メッシュシート40は、第一側壁周縁部150、第二側壁周縁部160およびメッシュシート周縁部41において一体化されている。
(Container body)
The container body 10 that constitutes the outer shell of the internal space 13 that can hold the liquid can be provided with a mesh sheet 40 in the manner described later, and should not affect the cells that are held inside. For example, any material can be used. The container body 10 and the mesh sheet 40 include, for example, a first side wall 15 and a second side wall 16 that face each other with the mesh sheet 40 therebetween, and the first side wall 15 and the mesh sheet 40 surround the first space 11. The second side wall 16 and the mesh sheet 40 can be configured to surround the second space 12. FIGS. 1-1 to 1-3 represent such embodiments. In this embodiment, the first side wall 15, the second side wall 16, and the mesh sheet 40 are integrated at the first side wall peripheral part 150, the second side wall peripheral part 160 and the mesh sheet peripheral part 41.
 容器本体10は、少なくとも一部を透明または半透明の材料からなるものとすると、内部の細胞懸濁液の様子を目視で観察できるため好ましい。また、少なくとも一部、好ましくは全体を可撓性を有するようにすると、必要に応じてクランピングにより内部の細胞懸濁液を物理的に分離させることができるため好ましい。容器本体10は内部空間13に露出する部分には接着剤を含んでいないことが好ましい。容器本体10が第一側壁15と第二側壁16とを含む場合、側壁の材質は、接着剤を用いずに熱融着により接着可能なものであると、製造工程の簡素化を図ることができ、かつ接着剤の細胞への影響を考慮しなくてもよいため好ましい。容器本体10の材料の具体例としては、塩化ビニル、軟質塩化ビニル、ポリウレタン、エチレン-酢酸ビニル共重合体、ポリエチレンやポリプロピレンのようなポリオレフィン、スチレン-ブタジエン-スチレン共重合体の水添物、およびスチレン-イソプレン-スチレン共重合体またはその水添物等の熱可塑性エラストマー、ならびに、熱可塑性エラストマーとポリオレフィン、およびエチレン-エチルアクリレート等の軟化剤との混合物等が挙げられる。容器本体10の内部空間13を画定する内面は、ナシジ加工されていると、細胞懸濁液の排出時に残液を少なくすることができるため好ましい。 It is preferable that at least a part of the container body 10 is made of a transparent or translucent material because the state of the cell suspension inside can be visually observed. In addition, it is preferable that at least a part, preferably the whole, be flexible because the internal cell suspension can be physically separated by clamping as necessary. It is preferable that the container main body 10 does not contain an adhesive at a portion exposed to the internal space 13. When the container main body 10 includes the first side wall 15 and the second side wall 16, the manufacturing process can be simplified if the material of the side wall can be bonded by thermal fusion without using an adhesive. This is preferable because it does not need to consider the influence of the adhesive on the cells. Specific examples of the material of the container body 10 include vinyl chloride, soft vinyl chloride, polyurethane, ethylene-vinyl acetate copolymer, polyolefin such as polyethylene and polypropylene, hydrogenated product of styrene-butadiene-styrene copolymer, and Examples thereof include thermoplastic elastomers such as styrene-isoprene-styrene copolymers or hydrogenated products thereof, and mixtures of thermoplastic elastomers with polyolefins and softeners such as ethylene-ethyl acrylate. It is preferable that the inner surface defining the internal space 13 of the container body 10 is pear-finished because residual liquid can be reduced when the cell suspension is discharged.
 容器本体10が可撓性を有する場合、内部空間13内に液体を収容したときに形状が変化することが通常である。図1-1~図1-3に示す細胞懸濁液調製用容器1の実施形態において第一壁部15及び第二壁部16が組み合わされた容器本体10が可撓性を有する場合、内部空間13内に液体を収容したとき、図2-1および2-2に図示するように、第一壁部15及び第二壁部16は中央部分が外方に向けに膨出して、内部空間13の容積が増す。容積が増した内部空間13内で後述する酵素処理、メッシュシート40を通じた夾雑物の除去等の各処理を行うことができる。 When the container body 10 has flexibility, it is normal that the shape changes when the liquid is accommodated in the internal space 13. In the embodiment of the cell suspension preparation container 1 shown in FIGS. 1-1 to 1-3, when the container body 10 in which the first wall portion 15 and the second wall portion 16 are combined has flexibility, When the liquid is accommodated in the space 13, as shown in FIGS. 2-1 and 2-2, the central portions of the first wall portion 15 and the second wall portion 16 bulge outwardly, The volume of 13 increases. Each treatment such as an enzyme treatment, which will be described later, and removal of impurities through the mesh sheet 40 can be performed in the internal space 13 whose volume has increased.
(メッシュシート)
 メッシュシート40は、内部空間13を第一空間11と第二空間12とに区切るように配置される。メッシュシートとしては、水等の液体を透過させることができ、好ましくは、必要な細胞を通過させることができるものを用いる。メッシュシート40は、細孔径が50~300μmの範囲であることが好ましい。細孔径がそのような範囲であれば、生体組織の酵素処理物に含まれる未消化の組織塊やデブリスなどの夾雑物を、メッシュの目詰まりを発生させずに除去し、必要な細胞のみを通過させることができる。この効果を一層発現させるためには細孔径は、好ましくは50μm以上、より好ましくは95μm以上であり、好ましくは300μm以下、より好ましくは200μm以下である。また、メッシュシート40は、開孔率が40%以上、特に45%以上であると、目詰まりが発生しづらく好ましい。
(Mesh sheet)
The mesh sheet 40 is disposed so as to divide the internal space 13 into a first space 11 and a second space 12. As the mesh sheet, one that can allow liquid such as water to pass therethrough, and preferably allows necessary cells to pass therethrough is used. The mesh sheet 40 preferably has a pore diameter in the range of 50 to 300 μm. If the pore size is in such a range, contaminants such as undigested tissue clumps and debris contained in the enzyme-treated product of living tissue are removed without causing clogging of the mesh, and only necessary cells are removed. Can be passed. In order to further manifest this effect, the pore diameter is preferably 50 μm or more, more preferably 95 μm or more, preferably 300 μm or less, more preferably 200 μm or less. The mesh sheet 40 preferably has a hole area ratio of 40% or more, particularly 45% or more because clogging is difficult to occur.
 なお、本明細書において「メッシュ」とは、面状に広がりを有し、一方の表面から他方の表面へと貫通する複数の細孔が二次元的に配置され網目構造が形成されている材料を意味する。メッシュの例としては、繊維が網目構造を形成するように織られてなるものや、厚さ方向に貫通した複数の細孔が形成されたメンブレン等が挙げられるがこれらには限らない。メッシュには、一般的に「スクリーン」と呼ばれるものも包含される。メッシュにより構成されたシートを「メッシュシート」と称する。本明細書において「メッシュ」は、前記網目構造を有さず且つ三次元細孔を有する材料(例えば、繊維状多孔性媒体やスポンジ状構造物であり、前記網目構造を有さず且つ三次元細孔を有する材料)とは異なる概念である。メッシュシート40の材質は、材料の安全性や安定性、入手容易性の観点から、合成樹脂材料、例えばナイロン、ポリエステル、レーヨン、ポリオレフィン、ポリスチレン、アクリル樹脂、ポリカーボネート、ポリアクリルアミド、ポリウレタン、塩化ビニル等の少なくとも1種より選択される合成高分子やヒドロキシアパタイト、ガラス、アルミナ、チタニア等の無機材料、ステンレス、チタン、アルミニウム等の金属が挙げられる。2種以上の材料を組み合わせる場合は、その組み合わせに特に限定はないが、ポリオレフィン、ポリスチレン、アクリル樹脂、ナイロン、ポリエステル、ポリカーボネート、ポリアクリルアミド、ポリウレタン、塩化ビニル等の合成高分子、ヒドロキシアパタイト、ガラス、アルミナ、チタニア等の無機材料、ステンレス、チタン、アルミニウム等の金属からなる群から選択される2種以上の材料の組み合わせが好ましい。メッシュシート40は、少なくとも内部空間13に液体を入れた際に、メッシュシート面がほぼ平坦となるよう容器本体10内に設けられている。図2-1および2-2に、図1-1~1-3に示した容器1の内部空間13に液体(図示せず)を入れた際の様子を示す。メッシュシート40は液体を透過することができるものであるため、投入口20を通じて投入された液体中の液状媒体、溶解成分及びメッシュシートを透過できる大きさの成分は、第一空間11だけでなく、メッシュシート40を透過して第二空間12にも移動し、メッシュシート40を透過できない大きさの成分は第一空間11に留まる。 In this specification, “mesh” refers to a material having a network structure in which a plurality of pores penetrating from one surface to the other surface are two-dimensionally arranged in a planar shape. Means. Examples of the mesh include, but are not limited to, one in which fibers are woven so as to form a network structure, and a membrane in which a plurality of pores penetrating in the thickness direction are formed. The mesh also includes what is generally called a “screen”. A sheet made of mesh is referred to as a “mesh sheet”. In this specification, the “mesh” is a material that does not have the network structure and has three-dimensional pores (for example, a fibrous porous medium or a sponge-like structure, does not have the network structure, and has a three-dimensional structure. This is a different concept from a material having pores. The material of the mesh sheet 40 is a synthetic resin material such as nylon, polyester, rayon, polyolefin, polystyrene, acrylic resin, polycarbonate, polyacrylamide, polyurethane, vinyl chloride, etc. from the viewpoint of material safety, stability, and availability. A synthetic polymer selected from at least one of the above, an inorganic material such as hydroxyapatite, glass, alumina, and titania, and a metal such as stainless steel, titanium, and aluminum. When two or more materials are combined, the combination is not particularly limited, but synthetic polymers such as polyolefin, polystyrene, acrylic resin, nylon, polyester, polycarbonate, polyacrylamide, polyurethane, vinyl chloride, hydroxyapatite, glass, A combination of two or more materials selected from the group consisting of inorganic materials such as alumina and titania, and metals such as stainless steel, titanium, and aluminum is preferable. The mesh sheet 40 is provided in the container body 10 so that the surface of the mesh sheet is substantially flat when the liquid is put into at least the internal space 13. FIGS. 2-1 and 2-2 show a state in which a liquid (not shown) is put in the internal space 13 of the container 1 shown in FIGS. 1-1 to 1-3. Since the mesh sheet 40 can transmit the liquid, the liquid medium, the dissolved component, and the component having a size capable of transmitting the mesh sheet in the liquid input through the input port 20 are not limited to the first space 11. The components that pass through the mesh sheet 40 and move to the second space 12 and cannot pass through the mesh sheet 40 remain in the first space 11.
 メッシュシートの細孔径とは、メッシュシートの一方の表面から他方の表面へと貫通する細孔を、貫通方向に沿って観察することにより特定される、細孔の内周の輪郭に内接する最大内接円の直径の平均値を意味する。平均値は、例えば細孔を50個以上、好ましくは100個以上観察して得られた値から算出することが好ましい。メッシュシートが、繊維が網目構造を形成するように織られてなるものである場合、細孔径はメッシュの平均目開きと等しい。平均目開きは、例えばルノメーターを用いて測定した単位長(例えば1インチ)あたりの繊維数に基づいて算出することができる。 The pore size of the mesh sheet is the maximum inscribed in the contour of the inner circumference of the pore, which is specified by observing the pores penetrating from one surface of the mesh sheet to the other surface along the penetration direction. Means the average diameter of the inscribed circle. The average value is preferably calculated from, for example, a value obtained by observing 50 or more pores, preferably 100 or more pores. When the mesh sheet is woven so that the fibers form a network structure, the pore diameter is equal to the average opening of the mesh. The average opening can be calculated based on the number of fibers per unit length (for example, 1 inch) measured using, for example, a urnometer.
 メッシュシートの開孔率は、メッシュシートを平面視したときの、全体の面積に対する、開孔部分を合計した面積の割合を指す。 The opening rate of the mesh sheet refers to the ratio of the total area of the opening portions to the entire area when the mesh sheet is viewed in plan.
(投入部および排出部)
 投入部21には、内部空間13の第一空間11への液体の投入口20が、排出部31には、内部空間13の第二空間12からの液体の排出口30が、それぞれ形成されている。投入口20および排出口30は、1つずつのみ設けられていてもよく、あるいは必要に応じて、投入口20および排出口30の一方又は両方が、2つ以上ずつ設けられていてもよい。細胞懸濁液調製用容器1の使用方法の一例では、投入口20からは、生体組織などの細胞含有試料と、細胞を分離し細胞懸濁液とするための酵素が投入され、第一空間11内において酵素反応が行われる。細胞懸濁液調製用容器1の使用方法の他の一例では、生体組織などの細胞含有試料を酵素により酵素反応処理した酵素処理液が、投入口20から投入され、第一空間11内に収容される。酵素反応後の酵素処理液または投入された酵素処理液がメッシュシート40を通過することにより、第二空間12側に細胞懸濁液が生成される。細胞懸濁液は、排出口30から排出される。
(Input section and discharge section)
The inlet 21 is provided with a liquid inlet 20 into the first space 11 of the internal space 13, and the outlet 31 is provided with a liquid outlet 30 from the second space 12 of the internal space 13. Yes. Only one input port 20 and one discharge port 30 may be provided, or two or more of one or both of the input ports 20 and the discharge ports 30 may be provided as necessary. In an example of a method for using the cell suspension preparation container 1, a cell-containing sample such as a living tissue and an enzyme for separating cells into a cell suspension are input from the input port 20. The enzyme reaction is carried out in 11. In another example of the method of using the cell suspension preparation container 1, an enzyme-treated solution obtained by subjecting a cell-containing sample such as a living tissue to an enzyme reaction treatment with an enzyme is introduced from the inlet 20 and accommodated in the first space 11. Is done. When the enzyme treatment liquid after the enzyme reaction or the charged enzyme treatment liquid passes through the mesh sheet 40, a cell suspension is generated on the second space 12 side. The cell suspension is discharged from the discharge port 30.
 投入部21と排出部31は、どのように設けてもよいが、例えば、容器本体10およびメッシュシート40の相対関係を前述したような図1-1~1-3に示した構成、すなわちメッシュシート40を間に介して対向する第一側壁15と第二側壁16とを含むようにする場合、投入部21は、第一側壁15の周縁部150とメッシュシート40の周縁部41との間に、投入口20を介して第一空間11と外部とを連通するように配置し、排出部31は、第二側壁16の周縁部160とメッシュシート40の周縁部41との間に、排出口30を介して第二空間12と外部とを連通するように配置する。より具体的には、投入部21および排出部31は、中空かつ任意の断面形状を有する筒状の材料、例えば樹脂製チューブを、第一側壁15の周縁部150とメッシュシート40の周縁部41との間に、あるいは第二側壁16の周縁部160とメッシュシート40の周縁部41との間に挟み込むことによって設けることができる。投入部21と排出部31を構成するための材料の具体例としては、塩化ビニル、軟質塩化ビニル、ポリウレタン、エチレン-酢酸ビニル共重合体、ポリエチレンやポリプロピレンのようなポリオレフィン、スチレン-ブタジエン-スチレン共重合体の水添物、およびスチレン-イソプレン-スチレン共重合体またはその水添物等の熱可塑性エラストマー、ならびに、熱可塑性エラストマーとポリオレフィン、エチレン-エチルアクリレート等の軟化剤との混合物等が挙げられる。 The input unit 21 and the discharge unit 31 may be provided in any way. For example, the relative relationship between the container body 10 and the mesh sheet 40 is the configuration shown in FIGS. When including the 1st side wall 15 and the 2nd side wall 16 which oppose through the sheet | seat 40 in between, the injection | throwing-in part 21 is between the peripheral part 150 of the 1st side wall 15, and the peripheral part 41 of the mesh sheet 40. In addition, the first space 11 and the outside are arranged to communicate with each other through the insertion port 20, and the discharge portion 31 is disposed between the peripheral portion 160 of the second side wall 16 and the peripheral portion 41 of the mesh sheet 40. It arrange | positions so that the 2nd space 12 and the exterior may be connected via the exit 30. FIG. More specifically, the input portion 21 and the discharge portion 31 are made of a hollow cylindrical material having an arbitrary cross-sectional shape, for example, a resin tube, and the peripheral portion 150 of the first side wall 15 and the peripheral portion 41 of the mesh sheet 40. Or between the peripheral edge portion 160 of the second side wall 16 and the peripheral edge portion 41 of the mesh sheet 40. Specific examples of the material constituting the input unit 21 and the discharge unit 31 include vinyl chloride, soft vinyl chloride, polyurethane, ethylene-vinyl acetate copolymer, polyolefin such as polyethylene and polypropylene, styrene-butadiene-styrene copolymer. Examples thereof include hydrogenated polymers, thermoplastic elastomers such as styrene-isoprene-styrene copolymers or hydrogenated products thereof, and mixtures of thermoplastic elastomers with softeners such as polyolefin and ethylene-ethyl acrylate. .
 投入口20と排出口30は、内部空間13を閉鎖系とできるよう、それぞれに連通する投入部21および排出部31の少なくとも一部が、注射針を用いて試料を投入できるシリコンゴムなどにより閉鎖されているか、あるいはニードルレスポートのようなシリンジを直接挿入できる構造が形成されていることが好ましい。また、例えば投入口20に連通する投入部21の部分は、途中で分岐する等によって試料を投入するためのポートを複数有しており、細胞含有試料と酵素とを別々のポートから投入できるようになっていてもよい。ポートには、必要に応じてフィルターなどを設けてもよい。 The inlet 20 and outlet 30 are closed by at least a part of the inlet 21 and outlet 31 that communicate with each other by silicon rubber or the like that allows a sample to be introduced using an injection needle so that the internal space 13 can be closed. It is preferable that a structure such as a needleless port can be directly inserted. In addition, for example, the portion of the input portion 21 that communicates with the input port 20 has a plurality of ports for inputting the sample by branching in the middle, and the like so that the cell-containing sample and the enzyme can be input from separate ports. It may be. The port may be provided with a filter as necessary.
 投入部21と排出部31は、メッシュシート40に対する相対的な位置が上記に説明したとおりであれば、容器本体10のいずれの位置に設けられていてもよい。しかしながら、容器本体10において投入部21と排出部31を互いに対向する位置に設けると、細胞含有試料と酵素の投入、または細胞含有試料の酵素処理液の投入、から細胞懸濁液の排出までの処理をスムーズに行うことができるため好ましい。なお、「互いに対向する位置に設ける」とは、例えば図1-1に示したように容器本体10が四角形またはそれに準じる形状をしている場合、対向する辺の一方に投入部21を、他方の辺に排出部31を設けることを意味する。 The input unit 21 and the discharge unit 31 may be provided at any position of the container body 10 as long as the relative position with respect to the mesh sheet 40 is as described above. However, if the input part 21 and the discharge part 31 are provided in positions opposite to each other in the container body 10, from the input of the cell-containing sample and the enzyme or the input of the enzyme-treated solution of the cell-containing sample to the discharge of the cell suspension. This is preferable because the processing can be performed smoothly. Note that “providing at positions facing each other” means that, for example, as shown in FIG. 1-1, when the container body 10 has a quadrangular shape or a shape similar thereto, the insertion portion 21 is provided on one of the opposed sides, and the other It means that the discharge part 31 is provided in the side of
(細胞懸濁液調製用容器の好適な第一実施形態)
 本発明の細胞懸濁液調製用容器1の特に好ましい第一の実施形態(以下「第一実施形態」という場合がある)では、メッシュシート40は、排出口30から排出される液体の流れ方向Fと、メッシュシート40に沿う面の法線Lとがなす狭角の角度をθ(°)としたとき、90-θが50未満となるよう設けられている。図2-3は、図2-2に示した、内部空間13内に液体(図示せず)を収容した状態での細胞懸濁液調製用容器1のC-C線切断部の排出部31近傍部分の概略端面図であり、排出口30から排出される液体の流れ方向Fと、メッシュシート40に沿う面の法線Lとがなす狭角の角度をθ(°)の関係が示されている。本第一実施形態では、90-θが上記範囲であることにより、メッシュシート40上に、排出口30からの前記方向Fに沿った距離が異なる位置が含まれることとなり、未消化の組織塊やデブリスなどの夾雑物によるメッシュシート40の目詰まりが発生しづらくなり、細胞懸濁液をスムーズに排出口30から取り出すことができる。この現象の機構は必ずしも明らかではないが、夾雑物が、メッシュシート40上の、排出口30からの前記方向Fに沿った距離が相対的に小さい位置に目詰まりしたときでも、メッシュシート40の、同距離が相対的により大きい位置においては目詰まりが少ないことによるものと推定される。90-θは50未満であることが好ましく、より好ましくは45以下、さらに好ましくは30以下、とりわけ好ましくは5以下である。90-θの値が小さいほど本第一実施形態の上記の効果は高い。90-0の下限値は特に限定されず、0であってもよい。
(Preferred first embodiment of container for cell suspension preparation)
In a particularly preferred first embodiment (hereinafter sometimes referred to as “first embodiment”) of the cell suspension preparation container 1 of the present invention, the mesh sheet 40 flows in the flow direction of the liquid discharged from the discharge port 30. When the narrow angle formed by F and the normal line L of the surface along the mesh sheet 40 is θ (°), 90−θ is set to be less than 50. FIG. 2-3 shows the discharge part 31 of the CC line cutting part of the cell suspension preparation container 1 in a state where a liquid (not shown) is accommodated in the internal space 13 shown in FIG. FIG. 4 is a schematic end view of the vicinity, showing a relationship of θ (°) as a narrow angle formed by the flow direction F of the liquid discharged from the discharge port 30 and the normal line L of the surface along the mesh sheet 40. ing. In the first embodiment, since 90-θ is in the above range, positions on the mesh sheet 40 having different distances from the discharge port 30 along the direction F are included, and an undigested tissue mass It is difficult for the mesh sheet 40 to be clogged with impurities such as debris and debris, and the cell suspension can be taken out from the outlet 30 smoothly. Although the mechanism of this phenomenon is not necessarily clear, even when the contaminants clog the mesh sheet 40 at a position where the distance along the direction F from the discharge port 30 is relatively small, the mesh sheet 40 It is estimated that the clogging is less at a position where the distance is relatively larger. 90-θ is preferably less than 50, more preferably 45 or less, further preferably 30 or less, and particularly preferably 5 or less. The smaller the value of 90-θ, the higher the effect of the first embodiment. The lower limit of 90-0 is not particularly limited, and may be 0.
 なお、本第一実施形態では、メッシュシート40の内部空間13に露出する部分のうち、該部分を平面視したときの面積に対して好ましくは50%以上、より好ましくは60%以上、より好ましくは70%以上、より好ましくは80%以上、より好ましくは90%以上、より好ましくは95%以上、より好ましくは100%の面積の領域が、前記90-θが上記の範囲となるように設けられる。メッシュシート40において前記90-θが上記の範囲となる領域が上記範囲であれば、本第一実施形態の上記の効果は十分に奏される。 In the first embodiment, the portion exposed to the internal space 13 of the mesh sheet 40 is preferably 50% or more, more preferably 60% or more, more preferably with respect to the area when the portion is viewed in plan. Is 70% or more, more preferably 80% or more, more preferably 90% or more, more preferably 95% or more, and more preferably 100% of the area so that the 90-θ is in the above range. It is done. If the region in which the 90-θ is in the above range in the mesh sheet 40 is in the above range, the above effect of the first embodiment is sufficiently exhibited.
(細胞懸濁液調製用容器の好適な第二実施形態)
 本発明の細胞懸濁液調製用容器1の特に好ましい第二の実施形態(以下「第二実施形態」という場合がある)では、上述の構造上の特徴のなかでも特に、
 容器本体10が、メッシュシート40を間に介して対向する第一側壁15と第二側壁16とを含み、
 第一側壁15とメッシュシート40とが第一空間11を囲い、
 第二側壁16とメッシュシート40とが第二空間12を囲い、
 投入部21が、第一側壁15の周縁部150とメッシュシート40の周縁部41との間に、投入口20を介して第一空間21と外部とを連通するように配置されており、
 排出部31が、第二側壁16の周縁部160とメッシュシート40の周縁部41との間に、排出口30を介して第二空間12と外部とを連通するように配置されており、
 第一側壁15、第二側壁16、及び、メッシュシート40が周縁部150、160、41において一体化されているという特徴を備える。
(Second preferred embodiment of container for cell suspension preparation)
In the particularly preferred second embodiment (hereinafter sometimes referred to as “second embodiment”) of the cell suspension preparation container 1 of the present invention, among the above structural features,
The container body 10 includes a first side wall 15 and a second side wall 16 that face each other with the mesh sheet 40 therebetween,
The first side wall 15 and the mesh sheet 40 surround the first space 11,
The second side wall 16 and the mesh sheet 40 surround the second space 12,
The insertion portion 21 is disposed between the peripheral portion 150 of the first side wall 15 and the peripheral portion 41 of the mesh sheet 40 so as to communicate the first space 21 and the outside via the input port 20.
The discharge part 31 is arrange | positioned so that the 2nd space 12 and the exterior may be connected via the discharge port 30 between the peripheral part 160 of the 2nd side wall 16, and the peripheral part 41 of the mesh sheet 40,
The first side wall 15, the second side wall 16, and the mesh sheet 40 are integrated at the peripheral edge portions 150, 160, and 41.
 本第二実施形態の細胞懸濁液調製用容器1は、第一側壁15および第二側壁16を構成する2枚の部材と、メッシュシート材料と、投入部および排出部用の材料を一体化するのみで、比較的容易に製造できる。 In the cell suspension preparation container 1 of the second embodiment, the two members constituting the first side wall 15 and the second side wall 16, the mesh sheet material, and the material for the input part and the discharge part are integrated. This makes it relatively easy to manufacture.
 なお、第一側壁15と、第二側壁16と、メッシュシート40とが一体化されているとは、これらの三部材が分離できない状態にあればよく、それぞれ相互に直接結合している必要はなく、これらの三部材のいずれか1つ以上又は他の部材を介して結合されていてもよい。例えば、周縁部において、第一側壁15と第二側壁16とが直接には結合されておらず、間にメッシュシート40を介して結合され一体化されている場合や、周縁部において、第一側壁15と第二側壁16とが直接には結合されておらず、その間に、投入部21(又は排出部31)とメッシュシート40とを介して結合され一体化されている場合も、第一側壁15と、第二側壁16と、メッシュシート40とが「周縁部において一体化されている」一例である。 The first side wall 15, the second side wall 16, and the mesh sheet 40 are integrated as long as these three members cannot be separated and need to be directly coupled to each other. Instead, any one or more of these three members or other members may be combined. For example, in the peripheral portion, the first side wall 15 and the second side wall 16 are not directly connected to each other and are connected and integrated via the mesh sheet 40 therebetween. Even when the side wall 15 and the second side wall 16 are not directly coupled to each other and are coupled and integrated via the input unit 21 (or the discharge unit 31) and the mesh sheet 40 therebetween, the first The side wall 15, the second side wall 16, and the mesh sheet 40 are an example “integrated at the peripheral edge”.
 また、本第二実施形態によれば、メッシュシート40の前記角θ(°)は、容器本体10における投入部21および排出部31の寸法および相対的な距離により調節することができ、それにより90-θの値が50未満となる細胞懸濁液調製用容器1を容易に製造することができる。具体的には、投入部21と排出部31とが容器本体10の対向する位置に配置されている場合、(i)投入部21の、第一空間11の側の端22の、第一側壁15と第二側壁16とが対向する方向に沿った幅をW1とし、(ii)排出部31の、第二空間12の側の端32の、第一側壁15と第二側壁16とが対向する方向に沿った幅をW2とし、かつ(iii)投入部21の、第一空間11の側の端22と、排出部31の、第二空間12の側の端32との間の距離をDとした場合、DとW1とW2との平均値であるWとの比(D/W)により角θ(°)を調節することができる。例えば、D/Wを12以上、15以上、又は20以上とすると、90-θの値を5以下とすることができる。D/Wが大きいほど90-θは小さい値となる。D/Wの上限は特に限定されないが通常は50以下、40以下、又は30以下である。W1とW2との比は特に限定されないが、細胞懸濁液調製用容器1の製造を容易にする観点から、W1/W2は0.2~5がより好ましく、0.5~2がより好ましく、0.9~1.1がより好ましく、1が特に好ましい。この実施形態では、投入部21と排出部31とが、投入口20による投入経路と排出口30による投入経路とが同軸上に位置するように配置されていることが好ましい。 Further, according to the second embodiment, the angle θ (°) of the mesh sheet 40 can be adjusted by the dimensions and relative distances of the input portion 21 and the discharge portion 31 in the container body 10, thereby The cell suspension preparation container 1 having a 90-θ value of less than 50 can be easily produced. Specifically, when the input unit 21 and the discharge unit 31 are disposed at positions facing the container body 10, (i) the first side wall of the end 22 on the first space 11 side of the input unit 21. 15 and the width along the direction in which the second side wall 16 faces W1, and (ii) the first side wall 15 and the second side wall 16 of the end 32 on the second space 12 side of the discharge part 31 face each other. And (iii) the distance between the end 22 on the first space 11 side of the input portion 21 and the end 32 on the second space 12 side of the discharge portion 31. In the case of D, the angle θ (°) can be adjusted by the ratio (D / W) of D, which is the average value of D, W1, and W2. For example, if D / W is 12 or more, 15 or more, or 20 or more, the value of 90−θ can be 5 or less. As D / W is larger, 90-θ is smaller. The upper limit of D / W is not particularly limited, but is usually 50 or less, 40 or less, or 30 or less. The ratio of W1 and W2 is not particularly limited, but W1 / W2 is more preferably 0.2 to 5, and more preferably 0.5 to 2, from the viewpoint of facilitating the production of the cell suspension preparation container 1. 0.9 to 1.1 is more preferable, and 1 is particularly preferable. In this embodiment, it is preferable that the input part 21 and the discharge part 31 are arranged so that the input path by the input port 20 and the input path by the discharge port 30 are located on the same axis.
(細胞含有試料から細胞懸濁液を調製する方法)
 本発明は、別の側面において、生体組織などの細胞含有試料から細胞懸濁液を調製するための方法にも関する。当該方法は、
(a)液体を保持可能な内部空間を内包する容器本体と、内部空間を第一空間と第二空間とに区切るように配置されたメッシュシートと、容器本体に設けられた、第一空間への液体の投入口が形成された投入部と、容器本体に設けられた、第二空間からの液体の排出口が形成された排出部とを備える容器において、投入口を通じて細胞含有試料と酵素を入れ、第一空間内で酵素反応を実施して酵素処理液を生成する、及び/又は、投入口を通じて細胞含有試料の酵素処理液を入れる工程、および
(b)酵素処理液をメッシュシートに通して夾雑物を除去し、第二空間側に細胞懸濁液を生成し、生成された細胞懸濁液を、排出口を通じて排出する工程を少なくとも含む。
(Method for preparing cell suspension from cell-containing sample)
In another aspect, the present invention also relates to a method for preparing a cell suspension from a cell-containing sample such as a living tissue. The method is
(A) To the first space provided in the container body, the container main body containing the internal space capable of holding the liquid, the mesh sheet arranged to divide the internal space into the first space and the second space, A cell-containing sample and an enzyme through the input port in a container having an input unit in which the liquid input port is formed and a discharge unit provided in the container body and formed with a liquid discharge port from the second space. And an enzyme reaction is performed in the first space to generate an enzyme treatment solution and / or a cell-containing sample enzyme treatment solution is introduced through the inlet, and (b) the enzyme treatment solution is passed through the mesh sheet. At least a step of removing impurities, generating a cell suspension on the second space side, and discharging the generated cell suspension through a discharge port.
 細胞含有試料の酵素処理に用いる酵素は、コラゲナーゼ、トリプシン、ディスパーゼ、コラゲナーゼ、ペプシン等の、生体組織などの細胞含有試料からの細胞の分離に用いることができる酵素を適宜用いることができる。 As an enzyme used for enzyme treatment of a cell-containing sample, an enzyme that can be used for separation of cells from a cell-containing sample such as a biological tissue such as collagenase, trypsin, dispase, collagenase, pepsin can be appropriately used.
 工程(a)で用いる容器において、メッシュシートは、水等の液体を透過させることができるものであり、上記の細胞懸濁液調製用容器の実施形態において用いるメッシュシートに関して説明した範囲から選択することができる。工程(a)で用いる容器において、メッシュシートの細孔径は例えば50~300μmの範囲であり、好ましくは50μm以上、より好ましくは95μm以上であり、好ましくは300μm以下、より好ましくは200μm以下である。容器は、使用前に予め滅菌しておくことが好ましい。滅菌方法としては、γ線滅菌や電子線滅菌やEOG滅菌、高圧蒸気滅菌などの医療用具の滅菌に汎用されている滅菌方法を好適に用いることができる。工程(a)の容器としては、上述した構造を有するものであればどのようなものであってもよいが、図1-1~1-3に示したような構造を有する細胞懸濁液調製用容器を用いると、目詰まり等が生じずにスムーズに細胞懸濁液を調製できるため好ましい。 In the container used in step (a), the mesh sheet is permeable to liquids such as water, and is selected from the range described for the mesh sheet used in the embodiment of the cell suspension preparation container. be able to. In the container used in the step (a), the pore size of the mesh sheet is, for example, in the range of 50 to 300 μm, preferably 50 μm or more, more preferably 95 μm or more, preferably 300 μm or less, more preferably 200 μm or less. The container is preferably sterilized before use. As the sterilization method, sterilization methods generally used for sterilization of medical devices such as γ-ray sterilization, electron beam sterilization, EOG sterilization, and high-pressure steam sterilization can be suitably used. The container for step (a) may be any container as long as it has the structure described above, but preparation of a cell suspension having a structure as shown in FIGS. 1-1 to 1-3. It is preferable to use a container for a cell because a cell suspension can be smoothly prepared without clogging or the like.
 工程(a)において、投入口を通じて細胞含有試料と酵素を入れ、第一空間内で酵素反応を実施して酵素処理液を生成する場合、細胞懸濁液の原料となる細胞含有試料と、細胞を分離し細胞懸濁液を調製するための酵素は、投入口を通じて容器の第一空間に入れられ、そこで酵素反応が実施される。このとき形成される、酵素と細胞含有試料とを含む反応混合物は液体状であることが好ましく、そのためには適宜分散媒体として水等の液状媒体の存在下で酵素と細胞含有試料とを第一空間に収容することが好ましい。酵素は必要に応じて酵素水溶液として添加することができる。メッシュシートは液体を透過することができるものであるため、工程(a)では、第一空間に入れられた反応混合物に含まれる液状媒体、溶解した成分、及び、メッシュシートを透過できる大きさの成分は第一空間だけでなく第二空間にも移動し、メッシュシートを透過できない大きさの成分は第一空間に留まる。工程(a)の酵素反応では、第一空間においてメッシュシートを透過できない成分が酵素処理され、目的とする細胞が液状媒体中に分散した酵素処理液となる。酵素反応後の酵素処理液がメッシュシートを通過することにより、未消化の組織塊やデブリスなどの夾雑物が除去され、第二空間に細胞懸濁液が生成され、その後排出口を通じて容器の外に排出される。工程(a)は、前記容器の投入口及び排出口が閉鎖された状態で実施することが好ましい。このためには、容器の投入口および排出口に連通する投入部および排出口の部分は、シリコンゴムやニードルレスポートのような、試料を投入可能な態様で封鎖されており、それにより容器内は閉鎖系となっており、外気に触れることなく酵素反応が行えるようになっていることが好ましい。また、酵素反応を実施する際には、容器ごとシェーカーに載せたり恒温槽に入れたりすることにより、適切な反応条件下におくことができる。なお、細胞含有試料と酵素を入れる際、あるいは酵素反応を実施する際には、第一空間が、第二空間に対して鉛直方向で下側になるように容器を置くと、メッシュシートの目詰まりを防ぐことができるため好ましい。 In the step (a), when a cell-containing sample and an enzyme are put through an inlet and an enzyme reaction is performed in the first space to generate an enzyme-treated solution, a cell-containing sample that is a raw material for the cell suspension; The enzyme for separating the cells and preparing the cell suspension is put into the first space of the container through the inlet, where the enzyme reaction is carried out. The reaction mixture containing the enzyme and the cell-containing sample formed at this time is preferably in a liquid state. For this purpose, the enzyme and the cell-containing sample are first mixed in the presence of a liquid medium such as water as a dispersion medium. It is preferable to accommodate in a space. The enzyme can be added as an aqueous enzyme solution as necessary. Since the mesh sheet can permeate the liquid, in step (a), the liquid medium contained in the reaction mixture placed in the first space, the dissolved component, and a size that can permeate the mesh sheet. The component moves not only in the first space but also in the second space, and the component having a size that cannot pass through the mesh sheet remains in the first space. In the enzyme reaction of the step (a), the component that cannot permeate the mesh sheet in the first space is enzyme-treated, and the target cell becomes an enzyme-treated solution dispersed in a liquid medium. By passing the enzyme-treated solution after the enzyme reaction through the mesh sheet, undigested tissue clumps and debris are removed, and a cell suspension is generated in the second space. To be discharged. The step (a) is preferably carried out in a state where the inlet and outlet of the container are closed. For this purpose, the inlet and outlet portions communicating with the inlet and outlet of the container are sealed in such a manner that a sample can be input, such as silicon rubber and a needleless port. Is a closed system, and it is preferable that an enzymatic reaction can be performed without touching the outside air. Moreover, when implementing an enzyme reaction, it can put on suitable reaction conditions by putting the container on a shaker or putting it in a thermostat. When placing the cell-containing sample and enzyme, or when carrying out the enzyme reaction, placing the container so that the first space is vertically below the second space, This is preferable because clogging can be prevented.
 工程(a)において、投入口を通じて細胞含有試料の酵素処理液を入れる場合、細胞懸濁液の原料となる細胞含有試料の、細胞を分離し細胞懸濁液を調製するための酵素による酵素処理は、別の容器において行われ、該別の容器中で生成された酵素処理液が、投入口を通じて容器の第一空間に収容される。第一空間に収容された酵素処理液は、水等の液状媒体、溶解した成分、及び、メッシュシートを透過できる大きさの成分(目的とする細胞等)を含む。後述する工程(b)において、酵素処理液がメッシュシートを通過することにより、未消化の組織塊やデブリスなどの夾雑物が除去され、第二空間に細胞懸濁液が生成され、その後排出口を通じて容器の外に排出される。酵素処理液を入れる際には、第一空間が、第二空間に対して鉛直方向で下側になるように容器を置くと、メッシュシートの目詰まりを防ぐことができるため好ましい。この場合もまた、容器の投入部の投入口および/または排出部の排出口は、シリコンゴムやニードルレスポートのような、試料を投入可能な態様で封鎖されていることが好ましい。 In the step (a), when the enzyme-treated solution of the cell-containing sample is introduced through the inlet, the enzyme-treated enzyme is used to separate the cells and prepare the cell suspension of the cell-containing sample as a raw material of the cell suspension. Is performed in another container, and the enzyme treatment liquid produced in the other container is accommodated in the first space of the container through the inlet. The enzyme treatment liquid accommodated in the first space includes a liquid medium such as water, a dissolved component, and a component (such as a target cell) having a size that can permeate the mesh sheet. In the step (b) described later, the enzyme-treated solution passes through the mesh sheet, thereby removing undigested tissue masses and debris and other contaminants, generating a cell suspension in the second space, and then the outlet. Through the container. When putting the enzyme treatment liquid, it is preferable to place the container so that the first space is located below the second space in the vertical direction because clogging of the mesh sheet can be prevented. Also in this case, it is preferable that the inlet of the container inlet and / or the outlet of the outlet are sealed in such a manner that a sample can be introduced, such as silicon rubber or a needleless port.
 工程(b)において細胞懸濁液を排出する際も、排出口と、細胞懸濁液を収容するための容器又は更なる処理工程のための装置とを閉鎖した流路で接続した閉鎖系で行うことが、コンタミネーションを抑制する観点から好ましい。 When the cell suspension is discharged in the step (b), a closed system in which the discharge port is connected to a container for containing the cell suspension or a device for a further processing step by a closed channel. It is preferable from the viewpoint of suppressing contamination.
 工程(b)において細胞懸濁液を排出する際、排出口を通じて排出される細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θが50未満、好ましくは45以下、さらに好ましくは30以下、とりわけ好ましくは5以下となるようにすると、メッシュシートの目詰まりが発生しづらくなるため好ましい。また、容器は、排出口が最下部となる状態で保持すると、細胞懸濁液の排出がスムーズに進むため好ましい。従って、容器は排出口が最下部となるよう保持した状態で、上記の角θ(°)に基づく90-θの値が50未満、好ましくは45以下、さらに好ましくは30以下、とりわけ好ましくは5以下となる構造、より具体的には図1-1~1-3に示したような構造を有することが好ましい。酵素処理液がメッシュシートを通過する流速は、排出口から陰圧をかける等することによって適宜調節することもできるが、重力による自然落下にまかせた流速としてもよい。酵素処理液がメッシュシートをスムーズに通過するには、メッシュシートを通過する流速は1~600mL/分の範囲、特に10~500mL/分の範囲、とりわけ20~350mL/分の範囲とすることが好ましい。 When discharging the cell suspension in the step (b), the narrow angle formed by the flow direction of the cell suspension discharged through the discharge port and the normal of the surface along the mesh sheet is θ (°). When 90-θ is less than 50, preferably 45 or less, more preferably 30 or less, and particularly preferably 5 or less, clogging of the mesh sheet is less likely to occur. In addition, it is preferable to hold the container in a state where the discharge port is at the lowermost end, since the discharge of the cell suspension proceeds smoothly. Therefore, with the container held so that the discharge port is at the bottom, the value of 90-θ based on the angle θ (°) is less than 50, preferably 45 or less, more preferably 30 or less, and particularly preferably 5 It is preferable to have the following structure, more specifically, a structure as shown in FIGS. 1-1 to 1-3. The flow rate at which the enzyme treatment liquid passes through the mesh sheet can be appropriately adjusted by applying a negative pressure from the discharge port, but may be a flow rate that is allowed to fall naturally due to gravity. In order for the enzyme treatment solution to smoothly pass through the mesh sheet, the flow rate through the mesh sheet should be in the range of 1 to 600 mL / min, particularly in the range of 10 to 500 mL / min, especially in the range of 20 to 350 mL / min. preferable.
 本実施形態において、工程(a)を完結後に工程(b)を行ってもよいし、工程(a)と工程(b)とを並行して行ってもよい。 In this embodiment, the step (b) may be performed after the step (a) is completed, or the step (a) and the step (b) may be performed in parallel.
 工程(a)及び工程(b)を含む本発明の方法の一例では、図1-1~1-3に示す細胞懸濁液調製用容器1を用いて行う。 In an example of the method of the present invention including steps (a) and (b), the cell suspension preparation container 1 shown in FIGS. 1-1 to 1-3 is used.
 工程(a)において、細胞懸濁液の原料となる細胞含有試料の、細胞を分離し細胞懸濁液を調製するための酵素による酵素処理を、別の容器において行い、該別の容器中で生成された酵素処理液を、投入口20を通じて細胞懸濁液調製用容器1の第一空間11に収容する場合に好適な細胞懸濁液調製用システムの一例を図8に示す。 In the step (a), an enzyme treatment with an enzyme for separating the cells and preparing the cell suspension of the cell-containing sample that is the raw material of the cell suspension is performed in another container, FIG. 8 shows an example of a cell suspension preparation system suitable for storing the generated enzyme treatment liquid in the first space 11 of the cell suspension preparation container 1 through the inlet 20.
 図8に示す細胞懸濁液調製用システム800は、細胞含有試料と酵素とを収容して酵素処理を行い酵素処理液を調製するための酵素処理用容器810と、調製された酵素処理液を収容し細胞懸濁液を生成する本発明の一実施形態に係る細胞懸濁液調製用容器1と、生成された細胞懸濁液を回収する回収用容器820とを備え、酵素処理用容器810と細胞懸濁液調製用容器1とは管850で接続され、細胞懸濁液調製用容器1と回収用容器820とは管850で接続される。管850としては、一般的なプラスチック製のチューブを用いることができ、中でも、塩化ビニル製のチューブを安全性や耐久性の面から好適に用いることができる。 A cell suspension preparation system 800 shown in FIG. 8 contains a cell-containing sample and an enzyme, performs an enzyme treatment, and prepares an enzyme treatment liquid, and an enzyme treatment liquid prepared. A container for cell suspension preparation 1 according to an embodiment of the present invention that accommodates and generates a cell suspension, and a recovery container 820 for recovering the generated cell suspension, and a container for enzyme treatment 810 And the cell suspension preparation container 1 are connected by a pipe 850, and the cell suspension preparation container 1 and the collection container 820 are connected by a pipe 850. As the pipe 850, a general plastic tube can be used, and among them, a vinyl chloride tube can be preferably used from the viewpoint of safety and durability.
 図8に示す細胞懸濁液調製用システム800において、酵素処理用容器810は、酵素処理用容器本体811と、細胞含有試料を投入するための投入口が形成された試料投入部812と、酵素を含む酵素液を投入するための投入口が形成された酵素投入部813と、酵素投入部813の上流側に配置され、投入する酵素液を濾過滅菌するための濾過滅菌フィルター814とを備える。酵素投入部813と酵素処理用容器本体811とは、必要に応じて、管850により接続されており、この部分の管850を必要に応じて封鎖するためのクランプ854が間に設けられる。酵素処理用容器本体811は、可撓性のプラスチック容器であることが好ましい。また、その内面にナシジ加工が施されていれば残液を少なくできるため好ましい。試料投入部812を通じて投入された細胞含有試料と、濾過滅菌フィルター814及び酵素投入部813を通じて投入された酵素液とは、酵素処理用容器本体811内で混合されて反応混合物を形成する。反応混合物は液体状であることが好ましく、そのためには適宜分散媒体として水等の液状媒体を含む。酵素は必要に応じて酵素水溶液として添加することができる。酵素処理用容器本体811内で酵素反応が行われ、細胞含有試料の酵素処理液が生成される。酵素反応を実施する際には、酵素処理用容器810ごとシェーカーに載せたり恒温槽に入れたりすることにより、適切な反応条件下におくことができる。 In the cell suspension preparation system 800 shown in FIG. 8, the enzyme processing container 810 includes an enzyme processing container main body 811, a sample input part 812 in which an input port for inputting a cell-containing sample is formed, an enzyme An enzyme input unit 813 formed with an input port for supplying an enzyme solution containing, and a filter sterilization filter 814 disposed on the upstream side of the enzyme input unit 813 for filter sterilizing the enzyme solution to be input. The enzyme input part 813 and the enzyme processing container main body 811 are connected by a pipe 850 as necessary, and a clamp 854 for sealing the pipe 850 of this part as necessary is provided. The container body 811 for enzyme treatment is preferably a flexible plastic container. Moreover, it is preferable that the inner surface is pear-finished because residual liquid can be reduced. The cell-containing sample input through the sample input unit 812 and the enzyme solution input through the filter sterilization filter 814 and the enzyme input unit 813 are mixed in the enzyme treatment container body 811 to form a reaction mixture. The reaction mixture is preferably in a liquid form, and for that purpose, a liquid medium such as water is appropriately included as a dispersion medium. The enzyme can be added as an aqueous enzyme solution as necessary. An enzyme reaction is performed in the enzyme processing container main body 811 to generate an enzyme processing solution for the cell-containing sample. When carrying out the enzyme reaction, the enzyme treatment container 810 can be placed on a shaker or placed in a thermostatic bath, so that appropriate reaction conditions can be obtained.
 酵素処理用容器本体811と本発明の一実施形態に係る細胞懸濁液調製用容器1とは管850により接続されている。酵素処理用容器810内で生成された酵素処理液は、管850を経由して、細胞懸濁液調製用容器1の投入部21に形成された投入口20から、細胞懸濁液調製用容器1の第一空間11に供給される。この工程が、上記の工程(a)に相当する。酵素処理用容器810と細胞懸濁液調製用容器1とを接続する管850の部分は、一対のルアロック851、852により分離可能に構成することができる。一対のルアロック851、852の一方がオスルアロック、他方がメスルアロックであり、液密に接続することが可能である。酵素処理用容器810と上流側のルアロック851との間の管850の部分には、必要に応じて、管850を閉鎖することができるクランプ856を配置してもよい。酵素処理液を収容した酵素処理用容器810が鉛直方向上方に、細胞懸濁液調製用容器1が鉛直方向下方にそれぞれ位置するように細胞懸濁液調製用システム800を設置し、重力により、酵素処理液を、酵素処理用容器810から細胞懸濁液調製用容器1へ移動させてもよいし、細胞懸濁液調製用容器1の排出口30の側から陰圧をかけて、酵素処理液を、酵素処理用容器810から細胞懸濁液調製用容器1へ移動させてもよい。 The container body 811 for enzyme treatment and the cell suspension preparation container 1 according to one embodiment of the present invention are connected by a tube 850. The enzyme treatment solution generated in the enzyme treatment container 810 passes through the tube 850 and enters the cell suspension preparation container from the input port 20 formed in the input part 21 of the cell suspension preparation container 1. 1 to the first space 11. This step corresponds to the above step (a). The portion of the tube 850 that connects the enzyme treatment container 810 and the cell suspension preparation container 1 can be configured to be separable by a pair of luer locks 851 and 852. One of the pair of luer locks 851 and 852 is a male luer lock and the other is a female luer lock, which can be connected in a liquid-tight manner. A clamp 856 that can close the tube 850 may be disposed in the portion of the tube 850 between the enzyme treatment container 810 and the upstream luer lock 851 as necessary. The cell suspension preparation system 800 is installed so that the enzyme treatment container 810 containing the enzyme treatment solution is located vertically above and the cell suspension preparation container 1 is located below vertically, The enzyme treatment liquid may be moved from the enzyme treatment container 810 to the cell suspension preparation container 1, or by applying negative pressure from the discharge port 30 side of the cell suspension preparation container 1 to perform the enzyme treatment. The liquid may be moved from the enzyme treatment container 810 to the cell suspension preparation container 1.
 図8に示す細胞懸濁液調製用システム800において、細胞懸濁液調製用容器1の第一空間11に収容された酵素処理液がメッシュシート40を通過すると、夾雑物が除去され、第二空間12側に細胞懸濁液が生成し、生成した細胞懸濁液は、排出部31に形成された排出口30および排出部31に接続された管850を介して回収用容器820に収容される。細胞懸濁液調製用容器1の排出部31と回収用容器820とは管850により接続されており、この部分の管850を必要に応じて封鎖するためのクランプ857が間に設けられる。回収用容器820は、可撓性のプラスチック容器であることが好ましい。また、その内面にナシジ加工が施されていれば残液を少なくできるため好ましい。回収用容器820の下流側には管850が接続されており、回収用容器820に回収された細胞懸濁液は、管850を介して排出される。この部分の管850の下流側末端には必要に応じてルアロック853が設けられており、細胞懸濁液の更なる処理のための機器、例えば、後述する細胞懸濁液処理装置にルアロック853を介して接続することができる。ルアロック853は、下流側の更なる装置が備えるルアロックに応じてメスルアロックでもオスルアロックでもよい。細胞懸濁液調製用容器1が鉛直方向上方に、回収用容器820が鉛直方向下方にそれぞれ位置するように細胞懸濁液調製用システム800を設置し、重力により、細胞懸濁液を、細胞懸濁液調製用容器1の第二空間12から回収用容器820へ移動させてもよいし、回収用容器820の下流側の管850の側から陰圧をかけて、細胞懸濁液を、細胞懸濁液調製用容器1の第二空間12から回収用容器820へ移動させてもよい。 In the cell suspension preparation system 800 shown in FIG. 8, when the enzyme treatment liquid stored in the first space 11 of the cell suspension preparation container 1 passes through the mesh sheet 40, impurities are removed, and the second A cell suspension is generated on the space 12 side, and the generated cell suspension is accommodated in the collection container 820 through the discharge port 30 formed in the discharge unit 31 and the pipe 850 connected to the discharge unit 31. The The discharge part 31 of the cell suspension preparation container 1 and the collection container 820 are connected by a tube 850, and a clamp 857 for sealing the tube 850 of this portion as necessary is provided. The collection container 820 is preferably a flexible plastic container. Moreover, it is preferable that the inner surface is pear-finished because residual liquid can be reduced. A pipe 850 is connected to the downstream side of the collection container 820, and the cell suspension collected in the collection container 820 is discharged through the pipe 850. A luer lock 853 is provided at the downstream end of this portion of the tube 850 as necessary, and the luer lock 853 is attached to an apparatus for further processing of the cell suspension, for example, a cell suspension processing apparatus described later. Can be connected through. The luer lock 853 may be either a female lock or a male luer lock depending on the luer lock provided in the further downstream device. The cell suspension preparation system 800 is installed so that the cell suspension preparation container 1 is positioned above the vertical direction and the collection container 820 is positioned below the vertical direction. The suspension preparation container 1 may be moved from the second space 12 to the collection container 820, or a negative pressure is applied from the tube 850 downstream of the collection container 820 to apply the cell suspension. The cell suspension preparation container 1 may be moved from the second space 12 to the collection container 820.
(細胞懸濁液処理装置との接続)
 容器の排出口は、別途用意された細胞懸濁液処理装置に接続されていてもよく、それにより排出口から得られた細胞懸濁液を閉鎖系で洗浄および濃縮して細胞濃縮液を得るようにしてもよい。このとき、容器の排出口と、細胞懸濁液処理装置との間は閉じた流路により接続されていることが好ましく、その間に上記のような回収用容器820が介在していてもよい。なお、細胞懸濁液の洗浄とは、細胞懸濁液中に含まれる体液や酵素等を、希釈液、例えば生理食塩水、輸液、培地、蒸留水、無機塩、糖類、血清、蛋白質を含む液体、緩衝液、培地、および血漿等に置換することを意味する。本発明は一実施形態において、
(a)液体を保持可能な内部空間を内包する容器本体と、内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、容器本体に設けられ、第一空間への液体の投入口が形成された投入部と、容器本体に設けられ、第二空間からの液体の排出口が形成された排出部とを備える容器において、投入口を通じて細胞含有試料と酵素を入れ、第一空間内で酵素反応を実施して酵素処理液を生成する、及び/又は、投入口を通じて細胞含有試料の酵素処理液を入れる工程、
(b)酵素処理液をメッシュシートに通して夾雑物を除去し、第二空間側に細胞懸濁液を生成し、生成された細胞懸濁液を、排出口を通じて排出する工程、および
(c)排出口から排出された前記細胞懸濁液を、細胞懸濁液を閉鎖系で洗浄および濃縮することができる細胞懸濁液処理装置により閉鎖系で洗浄および濃縮し、細胞濃縮液を得る工程を含む、生体組織から細胞濃縮液を得る方法に関する。当該方法によれば、対象に直接投与可能な濃度を有する細胞濃縮液を、全て閉鎖系で生体組織から直接調製することができ、高い細胞回収率が実現可能である。
(Connection with cell suspension treatment equipment)
The discharge port of the container may be connected to a separately prepared cell suspension processing apparatus, whereby the cell suspension obtained from the discharge port is washed and concentrated in a closed system to obtain a cell concentrate. You may do it. At this time, it is preferable that the discharge port of the container and the cell suspension treatment apparatus are connected by a closed flow path, and the collection container 820 as described above may be interposed therebetween. The washing of the cell suspension includes body fluids and enzymes contained in the cell suspension, including dilute solutions such as physiological saline, infusion, medium, distilled water, inorganic salts, saccharides, serum, and proteins. It means replacing with liquid, buffer, medium, plasma and the like. In one embodiment, the present invention provides:
(A) A container main body that encloses an internal space capable of holding a liquid, a mesh sheet that is disposed so as to divide the internal space into a first space and a second space, and the container main body. A cell-containing sample and an enzyme are placed through the inlet in a container provided with an inlet part formed with a liquid inlet and a discharge part provided in the container body and formed with a liquid outlet from the second space. Performing an enzyme reaction in the first space to generate an enzyme treatment solution, and / or adding an enzyme treatment solution of a cell-containing sample through an inlet,
(B) passing the enzyme treatment solution through a mesh sheet to remove impurities, generating a cell suspension on the second space side, and discharging the generated cell suspension through a discharge port; and (c) ) A step of washing and concentrating the cell suspension discharged from the discharge port in a closed system with a cell suspension treatment apparatus capable of washing and concentrating the cell suspension in a closed system to obtain a cell concentrate. The present invention relates to a method for obtaining a cell concentrate from a living tissue. According to this method, a cell concentrate having a concentration that can be directly administered to a subject can be prepared directly from a living tissue in a closed system, and a high cell recovery rate can be realized.
 細胞懸濁液処理装置としては、例えば特開2015-42167号に開示されている装置を利用することができる。図3にその装置の一実施形態(細胞懸濁液処理装置900)の概略図を示す。下記の説明において、カッコ内の数字は図3における対応箇所を示す。当該文献の細胞懸濁液処理装置(900)は、溶液入口ポート(915)、循環出口ポート(916)および循環入口ポート(917)を有する、細胞懸濁液の貯留容器(903)と、細胞懸濁液導入口(918)、細胞懸濁液導出口(919)および濾液用出口(920)を有する容器内に中空糸分離膜が充填されてなり、細胞懸濁液から液体を濾して濃縮を行うための細胞懸濁液処理器(906)と、前記貯留容器(903)の循環入口ポート(917)および前記細胞懸濁液処理器(906)の細胞懸濁液導入口(918)を連通する導入用連通管(928)ならびに前記細胞懸濁液処理器(906)の細胞懸濁液導出口(919)および前記貯留容器の循環出口ポート(916)を連通する導出用連通管(929)からなり、貯留容器(903)および細胞懸濁液処理器(906)の間で細胞懸濁液を循環させながら濃縮を行うための循環回路(930)と、濃縮された細胞濃縮液を回収する回収容器(905)と、前記貯留容器(903)内、前記細胞懸濁液処理器(906)内および前記循環回路(930)内の細胞濃縮液を前記回収容器(905)に送液するための回収路(931)と、前記貯留容器(903)の溶液入口ポート(915)に溶液を注入するための注入路(927)と、前記貯留容器(903)内または循環回路(930)の導入用連通管(928)内の細胞濃縮液の液量を検知するための検知手段(911)と、前記検知手段(911)で細胞濃縮液が所定の液量にまで濃縮されたことを検知して、前記貯留容器(903)から細胞懸濁液処理器(906)への細胞濃縮液の送液を停止させる制御手段と、を備えることを特徴とする。上記文献の装置を細胞懸濁液処理装置(900)として用いる場合、本発明の容器の排出口は、細胞懸濁液貯留容器(903)の溶液入口ポート(915)に溶液を注入するための注入路(927)と、細胞懸濁液調製用容器接続部(901)を経て接続される。このとき、本発明の容器の排出口と、細胞懸濁液処理装置との間は閉じた流路により接続されていることが好ましく、その間に上記のような回収用容器820が介在していてもよい。なお、上記文献の装置は細胞懸濁液の洗浄および濃縮を自動で実施することができるが、本発明で容器の排出口に接続された細胞懸濁液処理装置(900)は、細胞懸濁液の洗浄および濃縮を手動で行うものであってもよい。 As the cell suspension treatment apparatus, for example, an apparatus disclosed in Japanese Patent Application Laid-Open No. 2015-42167 can be used. FIG. 3 shows a schematic view of one embodiment of the apparatus (cell suspension treatment apparatus 900). In the following description, the numbers in parentheses indicate corresponding portions in FIG. The cell suspension treatment apparatus (900) of the document includes a cell suspension storage container (903) having a solution inlet port (915), a circulation outlet port (916) and a circulation inlet port (917), a cell A container having a suspension inlet (918), a cell suspension outlet (919) and a filtrate outlet (920) is filled with a hollow fiber separation membrane, and the liquid is filtered from the cell suspension and concentrated. A cell suspension treatment device (906), a circulation inlet port (917) of the storage container (903), and a cell suspension introduction port (918) of the cell suspension treatment device (906). An introductory communication pipe (928) and an outflow communication pipe (929) communicating with the cell suspension outlet (919) of the cell suspension processor (906) and the circulation outlet port (916) of the storage container. Storage capacity (903) and a cell suspension processor (906), a circulation circuit (930) for performing concentration while circulating the cell suspension, and a collection container (905) for collecting the concentrated cell concentrate And a collection path (931) for feeding the cell concentrate in the storage container (903), the cell suspension treatment unit (906), and the circulation circuit (930) to the collection container (905). ), An injection path (927) for injecting a solution into the solution inlet port (915) of the storage container (903), and a communication pipe (928) for introducing the storage container (903) or the circulation circuit (930). ) Detecting means (911) for detecting the amount of the cell concentrate in the inside, and detecting that the cell concentrate has been concentrated to a predetermined amount by the detecting means (911), (903) to cell suspension processor And a control means for stopping the liquid feed cell concentrate to 906), characterized in that it comprises a. When the apparatus of the above document is used as the cell suspension processing apparatus (900), the outlet of the container of the present invention is for injecting a solution into the solution inlet port (915) of the cell suspension storage container (903). The injection path (927) is connected to the cell suspension preparation container connection section (901). At this time, it is preferable that the discharge port of the container of the present invention and the cell suspension treatment apparatus are connected by a closed channel, and the collection container 820 as described above is interposed therebetween. Also good. Although the apparatus of the above document can automatically perform washing and concentration of the cell suspension, the cell suspension treatment apparatus (900) connected to the discharge port of the container in the present invention is a cell suspension. The liquid may be manually washed and concentrated.
(細胞懸濁液処理装置:貯留容器)
 細胞懸濁液処理装置(900)で用いる貯留容器(903)は、処理するための細胞懸濁液を貯留し、後述のように細胞懸濁液処理器に細胞懸濁液を通液して得られる細胞濃縮液を循環して貯留する容器である。貯留容器は、溶液入口ポート、循環出口ポートおよび循環入口ポートを有する。溶液入口ポートとは、細胞懸濁液を貯留容器内に供給するためのポートをいう。循環入口ポートとは、貯留容器から細胞懸濁液処理器に通液するためのポートをいい、循環出口ポートとは、細胞懸濁液処理器で濃縮された細胞濃縮液を貯留容器に通液するためのポートをいう。これらのポートは、貯留容器の下部に設置されていることが好ましい。下部にこれらポート全てを設置することにより、溶液入口ポートを通じて供給される細胞懸濁液や希釈のための溶液が貯留容器や循環回路内を循環する液体と効率よく撹拌されることによって、効率的に濃縮および希釈を行うことができる。
(Cell suspension treatment device: storage container)
A storage container (903) used in the cell suspension processing apparatus (900) stores a cell suspension for processing, and passes the cell suspension through a cell suspension processing device as described later. A container for circulating and storing the obtained cell concentrate. The storage container has a solution inlet port, a circulation outlet port, and a circulation inlet port. The solution inlet port refers to a port for supplying the cell suspension into the storage container. The circulation inlet port refers to a port for passing the liquid from the storage container to the cell suspension treatment device, and the circulation outlet port refers to the flow of the cell concentrate concentrated by the cell suspension treatment device through the storage container. The port to do. These ports are preferably installed in the lower part of the storage container. By installing all these ports at the bottom, the cell suspension supplied through the solution inlet port and the solution for dilution are efficiently agitated with the liquid circulating in the storage container and the circulation circuit. Can be concentrated and diluted.
 なお、溶液入口ポート、循環出口ポート、循環入口ポートの数としては、それぞれ1つあればよいが、必要に応じて複数に増やしてもよい。例えば、前記溶液入口ポートは、細胞懸濁液だけでなく、希釈液やプライミング液用のポートとしても使用できるが、細胞懸濁液用のポートのほかに、希釈液やプライミング液用の入口ポートを設けてもよい。また、前記の3種類のポートとは別の目的のポートを設けてもよい。例えば、細胞濃縮液を回収容器に通液するための回収用ポートが挙げられる。貯留容器の回収用ポートと回収容器とを直接接続することで、貯留容器内の細胞濃縮液を速やかに回収することが可能になる。 The number of solution inlet ports, circulation outlet ports, and circulation inlet ports may be one each, but may be increased to a plurality as necessary. For example, the solution inlet port can be used not only as a cell suspension but also as a port for a diluting solution or a priming solution. In addition to a port for a cell suspension, an inlet port for a diluting solution or a priming solution May be provided. In addition, a target port different from the above three types of ports may be provided. For example, a collection port for passing the cell concentrate through the collection container can be mentioned. By directly connecting the recovery port of the storage container and the recovery container, the cell concentrate in the storage container can be recovered quickly.
 前記貯留容器の材質については、細胞懸濁液または細胞濃縮液中の細胞に影響を与えないものであることが好ましく、取扱性がよいという観点から、可撓性の樹脂材料が特に好ましい。また、貯留容器の内面はナシジ加工されていることが、貯留容器内から懸濁液を排出する際の残液を少なくできる点などから利点がある。貯留容器の容積は、特に制限なく用いることができる。ただし、大きすぎると希釈に用いる希釈液量が多く必要になることから、1000mL以下であることが好ましい。また、貯留容器の形状、各ポートの構造、材質などについては処理する細胞懸濁液の種類、容積により適宜決定すればよく、特に限定はない。 The material of the storage container is preferably one that does not affect the cells in the cell suspension or cell concentrate, and a flexible resin material is particularly preferable from the viewpoint of easy handling. Moreover, it is advantageous that the inner surface of the storage container is pear-finished because the remaining liquid when the suspension is discharged from the storage container can be reduced. The volume of the storage container can be used without any particular limitation. However, if it is too large, a large amount of diluent used for dilution is required, and therefore it is preferably 1000 mL or less. Further, the shape of the storage container, the structure of each port, the material, and the like may be appropriately determined depending on the type and volume of the cell suspension to be processed, and are not particularly limited.
 また、貯留容器の上部には、通気口を備えていてもよい。この通気口を備えることで貯留容器内の気体と大気との交換が可能な大気開放系となり、例えば、貯留容器内の液体を排出する際に、貯留容器内が減圧して貯留容器がつぶれることを予防する利点がある。この通気口には、エアフィルタ(908)を設けてもよく、外部から貯留容器内に不要な成分が混入することを防ぐことができる。 In addition, a ventilation hole may be provided in the upper part of the storage container. By providing this vent, the atmosphere in the storage container can be exchanged with the atmosphere and the atmosphere can be exchanged. For example, when the liquid in the storage container is discharged, the storage container is decompressed and the storage container is crushed. There is an advantage to prevent. This vent may be provided with an air filter (908), which can prevent unwanted components from entering the storage container from the outside.
(細胞懸濁液処理装置:細胞懸濁液処理器)
 細胞懸濁液処理器(906)は、細胞懸濁液から液体を濾して濃縮を行うための装置であり、前記貯留容器から細胞懸濁液を通液できるように接続されている。細胞懸濁液処理器は、細胞懸濁液導入口、細胞懸濁液導出口および濾液用出口を有する容器内に中空糸分離膜が充填されている。前記細胞懸濁液導入口は、前記貯留容器から細胞懸濁液処理器内に細胞懸濁液を導入するための入口であり、貯留容器の循環入口ポートと接続されている。
(Cell suspension treatment device: Cell suspension treatment device)
The cell suspension treatment device (906) is an apparatus for filtering and concentrating liquid from the cell suspension, and is connected so that the cell suspension can be passed from the storage container. In the cell suspension treatment device, a hollow fiber separation membrane is filled in a container having a cell suspension inlet, a cell suspension outlet, and a filtrate outlet. The cell suspension introduction port is an inlet for introducing the cell suspension from the storage container into the cell suspension processor, and is connected to a circulation inlet port of the storage container.
 前記細胞懸濁液導出口は、濃縮処理された細胞懸濁液(細胞濃縮液)を取り出すための出口である。この細胞懸濁液導出口を前記貯留容器の循環出口ポートと接続することで、貯留容器と細胞懸濁液処理器との間で細胞懸濁液を循環させて濃縮を行うことができる。前記濾液用出口は、細胞懸濁液から濾過された液体を取り出すための出口である。 The cell suspension outlet is an outlet for taking out the concentrated cell suspension (cell concentrate). By connecting the cell suspension outlet to the circulation outlet port of the storage container, the cell suspension can be circulated between the storage container and the cell suspension treatment device to perform concentration. The filtrate outlet is an outlet for taking out the filtered liquid from the cell suspension.
 細胞懸濁液処理器に用いられている中空糸分離膜は、中空糸を数十から数千本程度束ねたものを筒状の容器内に充填していることが好ましい。中空糸分離膜の配置は、直線状になっていても、撓んでいても、らせん状になっていてもよく、細胞懸濁液入口と細胞懸濁液出口の間に中空糸分離膜の両端が保持されていれば特に形状は限定されない。 The hollow fiber separation membrane used in the cell suspension treatment apparatus preferably has a cylindrical container filled with several tens to thousands of hollow fibers bundled. The arrangement of the hollow fiber separation membrane may be linear, bent, or spiral, and the hollow fiber separation membrane is arranged at both ends of the hollow fiber separation membrane between the cell suspension inlet and the cell suspension outlet. If is held, the shape is not particularly limited.
 細胞懸濁液処理器に用いられている中空糸分離膜は、材料の安全性、安定性などの点から合成高分子材料を用いることができる。この中でも、ポリスルホン系、ポリオレフィン系またはセルロース系の高分子材料を好ましく用いることができる。また、中空糸分離膜の孔径は、細胞が外側に漏れ出てこなければよく、また、不要な成分を効率的に濾過できるためになるべく大きな孔径であるほうが好ましい。具体的には、平均孔径が0.01μm以上から1.0μm以下のものが好適に用いることができる。また、中空糸の内径は、400μm以上から1000μm以下であるものが好適に用いられる。 A synthetic polymer material can be used for the hollow fiber separation membrane used in the cell suspension treatment device from the viewpoint of the safety and stability of the material. Among these, polysulfone-based, polyolefin-based, or cellulose-based polymer materials can be preferably used. In addition, the pore diameter of the hollow fiber separation membrane is not limited as long as cells do not leak to the outside, and is preferably as large as possible so that unnecessary components can be efficiently filtered. Specifically, those having an average pore diameter of 0.01 μm or more and 1.0 μm or less can be suitably used. In addition, a hollow fiber having an inner diameter of 400 μm or more and 1000 μm or less is preferably used.
 前記細胞懸濁液導入口から供給された細胞懸濁液が中空糸分離膜の内側を通過すると、中空糸分離膜の外側に液体が濾過され、細胞濃縮液が作製される。細胞懸濁液処理器の構造としては、例えば、筒状容器に中空糸分離膜が充填され、中空糸端部が接着剤などで筒状容器端部と密着されており、端部で開口した中空糸膜に細胞懸濁液が流入および流出できるように、筒状容器の端部に細胞懸濁液導入口や細胞懸濁液導出口となるヘッダー部分が備え付けられていることが挙げられる。前記筒状容器には、濾液用出口が一つ以上備え付けられていればよく、中空糸の内側より濾過された濾液が濾液用出口より排出される構造となっている。細胞懸濁液処理器は、一般に、中空糸分離膜が密閉された容器の中に充填された構造である必要があるが、細胞懸濁液導入口および細胞懸濁液導出口が濾液用出口から中空糸分離膜を構成する壁材により隔てられている構造を備えていれば、各種構造をとることが可能である。例えば、血液透析などに用いられる透析器を類似の構造として例示することができる。 When the cell suspension supplied from the cell suspension inlet passes through the inside of the hollow fiber separation membrane, the liquid is filtered to the outside of the hollow fiber separation membrane to produce a cell concentrate. As a structure of the cell suspension treatment device, for example, a hollow container is filled with a hollow fiber separation membrane, and the end of the hollow fiber is in close contact with the end of the tubular container with an adhesive or the like, and is opened at the end. It is mentioned that a header portion serving as a cell suspension inlet or a cell suspension outlet is provided at the end of the cylindrical container so that the cell suspension can flow into and out of the hollow fiber membrane. The cylindrical container only needs to have one or more outlets for filtrate, and the filtrate filtered from the inside of the hollow fiber is discharged from the outlet for filtrate. The cell suspension treatment device generally needs to have a structure in which a hollow fiber separation membrane is packed in a sealed container, but the cell suspension inlet and the cell suspension outlet are outlets for filtrate. As long as it has a structure separated from the wall material constituting the hollow fiber separation membrane, various structures can be adopted. For example, a dialyzer used for hemodialysis can be exemplified as a similar structure.
 細胞懸濁液処理器の濾液用出口(920)には、中空糸分離膜により濾別された濾液が流れ出るための回路が設置されている。濾液用の回路と廃液容器(904)は連結する方が、濾液が外部に漏洩する懸念が低減でき好ましい。前記濾液用出口から取り出した濾液は、廃液容器などに通液して回収することができる。廃液容器は、廃液の漏洩がない容器であれば特に制限なく用いることができる。 At the filtrate outlet (920) of the cell suspension treatment device, a circuit is installed for the filtrate separated by the hollow fiber separation membrane to flow out. It is preferable to connect the circuit for the filtrate and the waste liquid container (904) because the concern that the filtrate leaks to the outside can be reduced. The filtrate taken out from the outlet for filtrate can be collected by passing it through a waste liquid container or the like. The waste liquid container can be used without particular limitation as long as it does not leak waste liquid.
 細胞懸濁液処理器の濾液用出口と廃液容器の間には、濾液を送液するためのポンプ(914)が設置されてもよいし、設置されていなくてもよい。例えば、前記濾液用出口と廃液容器とをつなぐ経路にポンプを備えることで、一定流量で濾過液を排出できることから、処理時間を一定にすることができ、細胞懸濁液処理器における濾過効率を制御することが可能になる。すなわち、ポンプを駆動させることで細胞懸濁液処理器からの濾液の排出が促進されることになり、結果として、細胞懸濁液処理器における濃縮処理を促進することができる。また、所定の濃度まで濃縮された細胞濃縮液を回収容器に通液して回収する際には、前記ポンプを停止しておくことで、速やかな回収が可能になる。また、回収された濾液は、そのまま廃棄してもよいし、殺菌処理などの再処理を施すことで、再利用してもよい。また、細胞懸濁液処理器には、前記細胞懸濁液導入口、細胞懸濁液導出口および濾液用出口のほかに、細胞懸濁液処理器内の細胞濃縮液を回収容器に送液するための細胞濃縮液回収口を設けてもよい。この細胞濃縮液回収口は回収容器(905)に接続することができる。 A pump (914) for feeding the filtrate may or may not be installed between the filtrate outlet of the cell suspension treatment device and the waste container. For example, by providing a pump in the path connecting the filtrate outlet and the waste liquid container, the filtrate can be discharged at a constant flow rate, so that the treatment time can be made constant and the filtration efficiency in the cell suspension treatment device can be increased. It becomes possible to control. That is, by driving the pump, the discharge of the filtrate from the cell suspension treatment device is promoted, and as a result, the concentration treatment in the cell suspension treatment device can be promoted. In addition, when the cell concentrate concentrated to a predetermined concentration is passed through the collection container and collected, rapid recovery can be achieved by stopping the pump. Moreover, the collected filtrate may be discarded as it is, or may be reused by performing reprocessing such as sterilization. In addition to the cell suspension inlet, the cell suspension outlet, and the filtrate outlet, the cell suspension processor sends the cell concentrate in the cell suspension processor to a collection container. For this purpose, a cell concentrate recovery port may be provided. This cell concentrate recovery port can be connected to a recovery container (905).
(細胞懸濁液処理装置:循環回路)
 循環回路(930)は、前記貯留容器の循環入口ポートおよび前記細胞懸濁液処理器の細胞懸濁液導入口を連通する導入用連通管と、前記細胞懸濁液処理器の細胞懸濁液導出口および前記貯留容器の循環出口ポートを連通する導出用連通管とからなる回路である。この循環回路を通じて、貯留容器および細胞懸濁液処理器の間で細胞懸濁液を循環させながら濃縮を行うことで細胞濃縮液を作製することができる。循環回路を構成する管としては、一般的なプラスチック製のチューブを好適に用いることができる。塩化ビニルが安全性や耐久性の面から好適に用いることができる。なお、前記循環回路には、細胞懸濁液または細胞濃縮液の循環の制御を行いやすくする観点から、ポンプ(913)が設置されていることが好ましい。ポンプの数については特に限定はないが、制御しやすい観点から、1つあればよい。ポンプの位置については、導入用連通管または導出用連通管のいずれかに設置していればよいが、導入用連通管に設置していれば細胞懸濁液処理器の細胞懸濁液導入口に圧力の高い溶液を導入でき、効率的に液体を分離することができ好ましい。ポンプ(913)と細胞懸濁液導入口(918)の間には分岐(図示せず)が設けられており、分岐部にはエアチャンバが設けられ、かつ分岐部先端が圧力計と接続されていることが好ましい。
(Cell suspension treatment equipment: Circulation circuit)
The circulation circuit (930) includes a communication pipe for introduction communicating with a circulation inlet port of the storage container and a cell suspension introduction port of the cell suspension treatment device, and a cell suspension of the cell suspension treatment device. It is a circuit comprising a lead-out port and a lead-out communicating tube that communicates with the circulation outlet port of the storage container. Through this circulation circuit, a cell concentrate can be produced by performing concentration while circulating the cell suspension between the storage container and the cell suspension treatment device. As a tube constituting the circulation circuit, a general plastic tube can be suitably used. Vinyl chloride can be suitably used in terms of safety and durability. The circulation circuit is preferably provided with a pump (913) from the viewpoint of facilitating control of circulation of the cell suspension or cell concentrate. There is no particular limitation on the number of pumps, but one is sufficient from the viewpoint of easy control. As for the position of the pump, it may be installed in either the introduction communication pipe or the extraction communication pipe, but if it is installed in the introduction communication pipe, the cell suspension introduction port of the cell suspension treatment device It is preferable because a solution having a high pressure can be introduced into the liquid and the liquid can be efficiently separated. A branch (not shown) is provided between the pump (913) and the cell suspension inlet (918), an air chamber is provided at the branch, and the tip of the branch is connected to a pressure gauge. It is preferable.
 前記循環回路上には、いずれかに分岐部を設けていてもよい。この分岐部に配管で回収容器(905)に連結するように構成しておくことで、この分岐部から回収容器までの経路を最終的な回収路(931)として、貯留容器内、細胞懸濁液処理器内および循環回路内にある細胞濃縮液を回収容器に速やかに回収することができる。分岐部は、好ましくは、循環出口ポートになるべく近い位置に設置したほうが、回収する工程で分岐部より出口ポートまでの循環回路内に残存する残液量を少なくできるので好ましい。 A branching portion may be provided on either of the circulation circuits. By connecting the branch portion to the recovery container (905) by piping, the path from the branch portion to the recovery container is used as the final recovery path (931), and the cell suspension The cell concentrate in the liquid processor and the circulation circuit can be quickly recovered in the recovery container. It is preferable that the branching section be installed at a position as close as possible to the circulation outlet port because the amount of residual liquid remaining in the circulation circuit from the branching section to the outlet port can be reduced in the recovery step.
(細胞懸濁液処理装置:回収容器)
 回収容器(905)は、所定の濃度にまで濃縮された細胞濃縮液を回収するための容器である。回収容器は、可撓性のプラスチック容器であることが好ましい。また、その内面にナシジ加工が施されていれば、細胞濃縮液を回収した後の残液を少なくできる利点がある。また、回収容器は針やシリンジなどが接続できる接続口を具備していてもよい。このような構成とすることで、回収容器に回収された細胞濃縮液を他の容器に移し替える場合などに好適に用いることができる。回収容器の形状としては、特に限定はない。例えば、容量が大きくなると回収された細胞が接触する容器の内面積が大きくなり、付着した細胞が容器内に残り細胞の損失につながることがあることから、容器内側の容量は小さい形状が好ましい。
(Cell suspension treatment device: collection container)
The recovery container (905) is a container for recovering the cell concentrate concentrated to a predetermined concentration. The collection container is preferably a flexible plastic container. Moreover, if pear processing is given to the inner surface, there exists an advantage which can reduce the residual liquid after collect | recovering cell concentrate. Further, the collection container may have a connection port to which a needle, a syringe, or the like can be connected. By adopting such a configuration, it can be suitably used when the cell concentrate recovered in the recovery container is transferred to another container. The shape of the collection container is not particularly limited. For example, when the volume increases, the inner area of the container with which the collected cells come into contact increases, and the attached cells may remain in the container and lead to cell loss. Therefore, the capacity inside the container is preferably small.
(細胞懸濁液処理装置:回収路)
 回収路(931)は、前記貯留容器内、前記細胞懸濁液処理器内および前記循環回路内の細胞濃縮液を前記回収容器に送液するための経路である。回収路を構成する管としては、一般的なプラスチック製のチューブを用いることができ、中でも、塩化ビニル製のチューブを安全性や耐久性の面から好適に用いることができる。
(Cell suspension treatment device: recovery path)
The collection path (931) is a path for sending the cell concentrate in the storage container, the cell suspension treatment device, and the circulation circuit to the collection container. A general plastic tube can be used as the tube constituting the recovery path, and among these, a vinyl chloride tube can be preferably used from the viewpoint of safety and durability.
 前記回収路としては、次の3つの態様が挙げられる。
1)前記循環回路上に分岐部を設けた場合には、この分岐部と回収容器とを連結する経路が回収路となる。
2)前記貯留容器の回収ポートと回収容器とを接続した場合には、この接続した経路が回収路となる。
3)細胞懸濁液処理器の細胞濃縮液回収口と回収容器とを接続した場合には、この接続した経路が回収路となる。
Examples of the recovery path include the following three aspects.
1) When a branch portion is provided on the circulation circuit, a path connecting the branch portion and the recovery container is a recovery path.
2) When the recovery port of the storage container and the recovery container are connected, the connected path becomes the recovery path.
3) When the cell concentrate recovery port of the cell suspension treatment device and the recovery container are connected, this connected path becomes the recovery path.
 回収路については、上記いずれかの態様であることが好ましく、2つ以上を併用することも可能である。 Regarding the recovery path, any one of the above embodiments is preferable, and two or more may be used in combination.
(細胞懸濁液処理装置:注入路)
 注入路(927)は、前記貯留容器の溶液入口ポートに溶液を注入するための経路である。注入路を構成する管としては、一般的なプラスチック製のチューブを用いることができ、中でも、塩化ビニル製のチューブを安全性や耐久性の面から好適に用いることができる。なお、溶液としては、細胞懸濁液に加えて、細胞懸濁液を濃縮して得られる細胞濃縮液を再度希釈するための希釈液や濃縮処理前に細胞懸濁液処理装置(900)全体をプライミングするためのプライミング液が含まれていてもよい。希釈液には生理食塩水、輸液、蒸留水、緩衝液、培地、血漿や無機塩、糖類、血清、蛋白質を含む液体等が挙げられ、特に安全性の観点から生理食塩水や輸液を好適に用いることができる。また、プライミング液にも生理食塩水、輸液、蒸留水、緩衝液、培地、血漿や無機塩、糖類、血清、蛋白質を含む液体等が挙げられ、特に安全性の観点から生理食塩水や輸液を好適に用いることができる。希釈液およびプライミング液には同一の溶液を使用してもよいし、異なる溶液を使用してもよい。異なる溶液を使用する場合は、貯留容器の溶液入口ポートに繋がる回路上にある分岐部分より分離し、各接続部に連結する回路を設置することができる。
(Cell suspension treatment device: injection path)
The injection path (927) is a path for injecting the solution into the solution inlet port of the storage container. As the pipe constituting the injection path, a general plastic tube can be used, and among them, a vinyl chloride tube can be preferably used from the viewpoint of safety and durability. As the solution, in addition to the cell suspension, the whole cell suspension treatment apparatus (900) before the concentration treatment or a dilution solution for diluting the cell concentrate obtained by concentrating the cell suspension again. A priming solution for priming may be included. Diluents include physiological saline, infusion, distilled water, buffer, culture medium, plasma and inorganic salts, saccharides, serum, liquids containing proteins, etc. Especially from the viewpoint of safety, physiological saline and infusion are suitable. Can be used. Examples of the priming solution include physiological saline, infusion solution, distilled water, buffer solution, culture medium, plasma, inorganic salts, saccharides, serum, and liquids containing protein. It can be used suitably. The same solution may be used for the diluent and the priming solution, or different solutions may be used. When using a different solution, it is possible to install a circuit that is separated from the branch portion on the circuit connected to the solution inlet port of the storage container and connected to each connection portion.
 前記注入路には、液体を送液するためのポンプ(912)が設置されることが好ましい。ポンプにより、安定して貯留容器に液体を送液することができる。また、ポンプを設置する位置は、細胞懸濁液調製用容器接続部(901)、希釈液容器接続部(902)および任意に設けられるプライミング液容器接続部(926)に連結する回路の合流箇所と溶液入口ポートとを連結する回路上にあることが、送液に必要なポンプの数を少なくすることができる点から好ましい。ポンプ(912)とクランプ(921または922)の間には分岐(図示せず)が設けられており、分岐部にはエアチャンバが設けられ、かつ分岐部先端が圧力計と接続されていることが好ましい。 It is preferable that a pump (912) for feeding a liquid is installed in the injection path. The pump can stably feed liquid to the storage container. In addition, the position where the pump is installed is a junction of circuits connected to the cell suspension preparation container connection part (901), the diluent container connection part (902), and the optionally provided priming liquid container connection part (926). And a solution inlet port are preferable because the number of pumps required for liquid feeding can be reduced. A branch (not shown) is provided between the pump (912) and the clamp (921 or 922), an air chamber is provided at the branch, and the tip of the branch is connected to a pressure gauge. Is preferred.
(細胞懸濁液処理装置:検知手段)
 検知手段は、前記貯留容器内または循環回路の導入用連通管内の細胞濃縮液の液量を検知するための手段である。前記貯留容器内の液量を検知する手段としては、貯留容器内の貯留液の液面を直接検知する気泡センサーを用いることが挙げられる。また、他の実施形態としては、例えば、貯留容器に対して上下方向に平行になるようにチューブを設置し、下方で貯留容器とチューブが連通した回路とし、チューブ内の液面が貯留容器内の液面と等しくなるように調整し、このチューブに気泡センサーを設置してもよい。この手段であれば、貯留容器内の液面として、チューブ内の液面を気泡センサーで検知することができる。また、貯留容器と平行に設置された前記チューブの下方にチャンバーを設置してもよい。特にチューブより内径が大きなチャンバーを設置することにより、平行に設置されたチューブに誤って気泡が浸入して検知される不具合の発生を低減することが期待される。
(Cell suspension treatment device: detection means)
The detection means is means for detecting the amount of the cell concentrate in the storage container or the communication pipe for introduction of the circulation circuit. Examples of the means for detecting the liquid amount in the storage container include using a bubble sensor that directly detects the liquid level of the storage liquid in the storage container. Further, as another embodiment, for example, a tube is installed so as to be parallel to the vertical direction with respect to the storage container, and a circuit in which the storage container and the tube communicate with each other below is used. The bubble sensor may be installed in this tube by adjusting it so that it is equal to the liquid level. With this means, the liquid level in the tube can be detected by the bubble sensor as the liquid level in the storage container. Moreover, you may install a chamber under the said tube installed in parallel with the storage container. In particular, by installing a chamber having an inner diameter larger than that of the tube, it is expected to reduce the occurrence of defects that are detected by the intrusion of bubbles in the tubes installed in parallel.
 前記導入用連通管内の細胞濃縮液の液量を検知する手段としては、貯留容器の循環入口ポートに連通する導入用連通管(928)に気泡センサー(911)を備えることが挙げられる。この形態であれば、前記貯留容器内の液量を検知する手段に比べて細胞懸濁液をより濃縮することができるため、濃縮された懸濁液(細胞濃縮液)の量を少なくでき、懸濁液中の不要成分の量を低下することができるといった利点がある。また、前記導入用連通管に設置する気泡センサーの位置としては、特に限定はないが、貯留容器に近接している位置に設置することで、貯留容器と気泡センサーとをつなぐ回路の長さを短くすることができる。 As a means for detecting the amount of the cell concentrate in the introduction communication pipe, a bubble sensor (911) is provided in the introduction communication pipe (928) communicating with the circulation inlet port of the storage container. If it is this form, since the cell suspension can be concentrated more than the means for detecting the amount of liquid in the storage container, the amount of the concentrated suspension (cell concentrate) can be reduced, There is an advantage that the amount of unnecessary components in the suspension can be reduced. Further, the position of the bubble sensor to be installed in the introduction communication pipe is not particularly limited, but by installing it at a position close to the storage container, the length of the circuit connecting the storage container and the bubble sensor can be increased. Can be shortened.
 また、細胞懸濁液処理装置(900)では、貯留容器の溶液入口ポートに繋がる注入路(927)に、気泡センサー(910)を設置してもよい。この気泡センサーにより気泡が検知された場合に貯留容器への細胞懸濁液、希釈液、プライミング液などの溶液の貯留を停止することができる。例えば、対象とする細胞懸濁液の処理量がわからなくても、前記気泡センサーを注入路に設置することで、処理毎にポンプの駆動時間を設定することなく対象の液体全量を処理することができる利点がある。また、ポンプの駆動時間から一定量の溶液を加える工程にすることもできる。例えば、細胞懸濁液の一部のみを処理する必要がある場合は、ポンプの駆動時間を設定することで処理を行うことができる。この気泡センサーは注入路のどこでも設置できるが、貯留容器になるべく近い位置に設置するほうが、注入路内への残液量を低減する点で有利である。 In the cell suspension treatment apparatus (900), the bubble sensor (910) may be installed in the injection path (927) connected to the solution inlet port of the storage container. When bubbles are detected by the bubble sensor, storage of a solution such as a cell suspension, a diluent, a priming solution in the storage container can be stopped. For example, even if the processing amount of the target cell suspension is not known, by installing the bubble sensor in the injection path, the entire amount of the target liquid can be processed without setting the pump driving time for each processing. There is an advantage that can be. Moreover, it can also be set as the process of adding a fixed quantity of solution from the drive time of a pump. For example, when it is necessary to process only a part of the cell suspension, the process can be performed by setting the driving time of the pump. This bubble sensor can be installed anywhere in the injection path, but it is more advantageous to install the bubble sensor as close to the storage container as possible to reduce the amount of liquid remaining in the injection path.
 また、前記貯留容器の上部に別の気泡センサー(909)を設けてもよい。この気泡センサーを設置することで、貯留容器内の上部付近の溶液の有無を判別することができる。即ち、貯留容器の容量を超える液体が供給された場合に、前記センサーが検知して、警報として使用者に知らせることができる。 Further, another bubble sensor (909) may be provided on the upper part of the storage container. By installing this bubble sensor, it is possible to determine the presence or absence of a solution near the top in the storage container. That is, when a liquid exceeding the capacity of the storage container is supplied, the sensor can detect and notify the user as an alarm.
 細胞懸濁液処理装置(900)に用いるポンプや気泡センサーは一般的に用いられているものを使用することができる。また、回路の所望の位置にクランプを設けて流路の切り替えを行うこともできる。これらのポンプ、気泡センサーおよびクランプとしては、特に限定はなく、例えば、透析装置などに用いられているものを用いてもよい。 A commonly used pump or bubble sensor used in the cell suspension treatment apparatus (900) can be used. It is also possible to switch the flow path by providing a clamp at a desired position in the circuit. These pumps, bubble sensors, and clamps are not particularly limited, and for example, those used in dialysis machines and the like may be used.
(細胞含有試料)
 本発明の方法で出発原料として用いる細胞含有試料又は酵素処理液の調製に用いる細胞含有試料の一例としては生体組織が挙げられる。生体組織は、動物組織より採取したものであれば特に限定されないが、例えば、脂肪、皮膚、血管、角膜、口腔、腎臓、肝臓、膵臓、心臓、神経、筋肉、前立腺、腸、羊膜、胎盤、臍帯などに由来するものが挙げられる。本発明の方法は、特に採取した脂肪組織から間質血管画分(SVF)細胞を取り出すのに有用である。また、細胞含有試料の他の例としては、in vitroで調製された細胞の培養物が挙げられる。
(Cell-containing sample)
An example of a cell-containing sample used as a starting material in the method of the present invention or a cell-containing sample used for preparing an enzyme-treated solution is biological tissue. The biological tissue is not particularly limited as long as it is collected from animal tissue, for example, fat, skin, blood vessel, cornea, oral cavity, kidney, liver, pancreas, heart, nerve, muscle, prostate, intestine, amniotic membrane, placenta, The thing derived from an umbilical cord etc. is mentioned. The method of the present invention is particularly useful for removing stromal vascular fraction (SVF) cells from collected adipose tissue. In addition, another example of the cell-containing sample is a cell culture prepared in vitro.
 本発明により得られた細胞懸濁液または細胞濃縮液は、白血病治療、心筋再生や血管再生、幹細胞疲弊疾患、骨疾患、軟骨疾患、虚血性疾患、血管系疾患、神経病、やけど、慢性炎症、心疾患、免疫不全、クーロン病等の疾患、豊胸、シワとり、美容成形、組織陥没症等の組織増大などの再生医療などに用いることが可能である。また、得られた細胞をスキャフォールド等の構造材料に播種して培養し、治療に用いることもできる。あるいは、得られた細胞を将来の治療用途のために凍結保存してもよい。 The cell suspension or cell concentrate obtained by the present invention is used for leukemia treatment, myocardial regeneration and blood vessel regeneration, stem cell exhaustion disease, bone disease, cartilage disease, ischemic disease, vascular disease, neurological disease, burn, chronic inflammation. It can be used for regenerative medicine such as heart disease, immune deficiency, coulomb disease, breast augmentation, wrinkle removal, cosmetic molding, tissue enlargement such as tissue depression. In addition, the obtained cells can be seeded and cultured in a structural material such as a scaffold and used for treatment. Alternatively, the resulting cells may be stored frozen for future therapeutic uses.
 本発明の方法によれば、従来法では開放系で複数ステップを経て実施されていた生体組織からの酵素処理および分離処理を経た細胞懸濁液の調製、或いは、生体組織の酵素処理液からの分離処理を経た細胞懸濁液の調製を、全て閉鎖系で、かつ同一容器内で実施することができる。また、容器内部での酵素処理液のメッシュシートの通過もスムーズに進むため、特別な技術を有しない操作者であっても、容易に細胞懸濁液の調製を実施できる。さらに、本発明の細胞懸濁液調製用容器は、特に複雑な構造を有しないため、メッシュシートの目詰まりを発生させずに短時間に細胞懸濁液を調製可能な器具を低コストで提供することができる。本発明は、従来手間がかかっていた脂肪組織からのSVF画分の採取に非常に有用である。 According to the method of the present invention, preparation of a cell suspension that has been subjected to enzyme treatment and separation treatment from a biological tissue, which has been performed in a conventional method through a plurality of steps in the conventional method, or from an enzyme treatment solution of biological tissue. The preparation of the cell suspension that has undergone the separation treatment can be carried out all in a closed system and in the same container. In addition, since the passage of the enzyme-treated solution through the mesh sheet smoothly proceeds inside the container, even an operator who does not have a special technique can easily prepare the cell suspension. Furthermore, since the cell suspension preparation container of the present invention does not have a particularly complicated structure, it provides a low-cost device capable of preparing a cell suspension in a short time without causing clogging of the mesh sheet. can do. The present invention is very useful for collecting an SVF fraction from adipose tissue, which has conventionally been troublesome.
 以下、実施例を用いて本発明をより詳細に説明するが、本発明はこれら実施例に限定されるものではない。以下の説明において「細孔径」はメッシュの目開きを表し、ルノメーターにより測定した結果に基づいて算出したものを使用している。 Hereinafter, the present invention will be described in more detail using examples, but the present invention is not limited to these examples. In the following description, “pore diameter” represents the mesh opening, and is calculated based on the result of measurement with a luminometer.
1.細胞懸濁液の調製
 ウサギまたはヒトの脂肪組織を用意し、0.075%コラゲナーゼ溶液を加えて37℃にて30分から1時間反応させて細胞懸濁液を調製した。
1. Preparation of cell suspension A rabbit or human adipose tissue was prepared, a 0.075% collagenase solution was added, and the mixture was reacted at 37 ° C for 30 minutes to 1 hour to prepare a cell suspension.
2.メッシュシート面の角度の検討
 同一個体由来の細胞懸濁液を用いて、以下の予備試験を行った。試験に用いた細胞懸濁液の細胞濃度は、いずれも1.0×10cells/mLとした。細孔径100μm、開孔率42%、膜面積が3.14cmであるナイロンメッシュシートを有する市販のセルストレーナーを遠沈管に取り付け、メッシュシート面の角度を変えることにより、通液方向(鉛直方向)とメッシュシート面の角度を調節した。所定の角度に設定したメッシュシートに、細胞懸濁液を自然落下にて通液させ、メッシュシート通過後の細胞懸濁液中に含まれる細胞数を、メッシュシート通過前の細胞懸濁液中に含まれる細胞数で除することにより細胞回収率を算出した。なお、細胞数は改良ノイバウエル血球計算盤(日本血液協会認定品)により測定した。
2. Examination of mesh sheet surface angle The following preliminary test was performed using a cell suspension derived from the same individual. The cell concentration of the cell suspension used for the test was 1.0 × 10 6 cells / mL. A commercially available cell strainer having a nylon mesh sheet with a pore size of 100 μm, a porosity of 42%, and a membrane area of 3.14 cm 2 is attached to the centrifuge tube, and the angle of the mesh sheet surface is changed to change the liquid flow direction (vertical direction ) And the mesh sheet surface were adjusted. The cell suspension is allowed to flow spontaneously through a mesh sheet set at a predetermined angle, and the number of cells contained in the cell suspension after passing through the mesh sheet is counted in the cell suspension before passing through the mesh sheet. The cell recovery rate was calculated by dividing by the number of cells contained in. The number of cells was measured with a modified Neubauer hemocytometer (Japanese blood association certified product).
 (実施例1)細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θを45に設定したところ、目詰まりの発生(メッシュシートを通過する液の流れの停止)までに30mLの細胞懸濁液を通液させることができた。細胞回収率は95%であった。 Example 1 When the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is θ (°), clogging occurs when 90-θ is set to 45. 30 mL of the cell suspension was allowed to pass through until the occurrence of (stopping the flow of the liquid passing through the mesh sheet). Cell recovery was 95%.
 (実施例2)細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θを30に設定したところ、目詰まりの発生までに32mLの細胞懸濁液を通液させることができた。細胞回収率は98%であった。 (Example 2) When the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is θ (°), clogging occurs when 90-θ is set to 30 32 mL of cell suspension could be passed before the occurrence of. The cell recovery rate was 98%.
 (比較例1)細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θを50に設定したところ、目詰まりの発生までに27mLの細胞懸濁液を通液させることができた。細胞回収率は90%であった。 (Comparative Example 1) When the angle of the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is θ (°), clogging occurs when 90-θ is set to 50 27 mL of cell suspension could be passed through before the occurrence of. The cell recovery rate was 90%.
 (比較例2)細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θを90に設定したところ、目詰まりの発生までに26mLの細胞懸濁液を通液させることができた。細胞回収率は88%であった。 (Comparative Example 2) When the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet is θ (°), clogging occurs when 90-θ is set to 90. 26 mL of cell suspension could be passed before the occurrence of. The cell recovery rate was 88%.
 図4は、細胞懸濁液の流れ方向と、メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θと細胞懸濁液の処理量の関係を示したグラフであり、図5は、90-θと細胞回収率の関係を示したグラフである。細孔径95μmのメッシュシートを使用し、90-θを50未満にすることで、高容量の細胞懸濁液を処理でき、かつ高い細胞回収率を達成可能なことが確認された。 FIG. 4 shows the relationship between 90-θ and the throughput of the cell suspension, where θ (°) is the narrow angle formed by the flow direction of the cell suspension and the normal of the surface along the mesh sheet. FIG. 5 is a graph showing the relationship between 90-θ and the cell recovery rate. It was confirmed that by using a mesh sheet having a pore size of 95 μm and setting 90-θ to less than 50, a high volume cell suspension can be treated and a high cell recovery rate can be achieved.
3.細胞懸濁液調製用容器を用いた試験
 図1-1~2-2に示した構造を有する細胞懸濁液調製用容器1を用いて試験を行った。試験に用いた細胞懸濁液調製用容器では、第一側壁15及び第二側壁16が可撓性を有する樹脂シートにより構成されている。組み込まれたポリエステル製のメッシュシート40の細孔径が異なる三種類の容器を用意した。容器の側壁は、可撓性のポリ塩化ビニルを用いて製造した。いずれの容器も、投入部21および排出部22として容器端部に挟み込まれたチューブの外径は8mmであり、投入部21の容器内部側端部22から排出部31の容器内部側端部32までの距離は約20cmであった。このため本明細書で規定した前記D/Wの値は約25であった。メッシュシートの膜面積は208cmであった。細胞懸濁液調製用容器を投入部21が上となるように吊るし、それぞれの容器に、同一個体由来の細胞懸濁液50mLを投入口20から自然落下により通液させ、排出口30から取り出した。細胞懸濁液の細胞濃度は、いずれも1.4×10cells/mLとした。通液時の容器中のメッシュシートは、メッシュシートに沿う面の法線Lと通液方向F(鉛直方向)が成す狭角の角度をθ(°)としたとき、90-θが約1であった。
3. Test Using Cell Suspension Preparation Container A test was conducted using a cell suspension preparation container 1 having the structure shown in FIGS. 1-1 to 2-2. In the cell suspension preparation container used for the test, the first side wall 15 and the second side wall 16 are made of a flexible resin sheet. Three types of containers having different pore diameters of the incorporated polyester mesh sheet 40 were prepared. The side wall of the container was manufactured using flexible polyvinyl chloride. In any of the containers, the outer diameter of the tube sandwiched between the container ends as the input part 21 and the discharge part 22 is 8 mm, and the container internal side end part 32 of the discharge part 31 from the container internal side end part 22 of the input part 21. The distance to was about 20 cm. For this reason, the value of D / W defined in this specification was about 25. The membrane area of the mesh sheet was 208 cm 2 . The cell suspension preparation containers are suspended so that the input part 21 is at the top, and 50 mL of the cell suspension derived from the same individual is allowed to flow through each container by natural dropping and is taken out from the discharge port 30. It was. The cell concentration of each cell suspension was 1.4 × 10 6 cells / mL. The mesh sheet in the container at the time of liquid flow has 90-θ of about 1 when the narrow angle formed by the normal L of the surface along the mesh sheet and the liquid flow direction F (vertical direction) is θ (°). Met.
 (実施例3)メッシュシートの細孔径が95μm、開孔率が46%の容器を用いたところ、通液中に目詰まりは発生せず、細胞回収率は95%であった。 (Example 3) When a container having a mesh sheet with a pore size of 95 μm and an open area ratio of 46% was used, clogging did not occur during liquid flow, and the cell recovery rate was 95%.
 (実施例4)メッシュシートの細孔径が200μm、開孔率が61%の容器を用いたところ、通液中に目詰まりは発生せず、細胞回収率は100%であった。 (Example 4) When a container having a mesh sheet with a pore size of 200 μm and an open area ratio of 61% was used, no clogging occurred during the flow of liquid, and the cell recovery rate was 100%.
 (実施例5)メッシュシートの細孔径が300μm、開孔率が65%の容器を用いたところ、通液中に目詰まりは発生せず、細胞回収率は100%であった。 (Example 5) When a container having a mesh sheet with a pore size of 300 μm and an open area ratio of 65% was used, clogging did not occur during liquid flow, and the cell recovery rate was 100%.
 図6は、メッシュシートの細孔径と細胞回収率の関係を示したグラフである。通液方向に対するメッシュシート面の角度を同一角度に揃えた場合、少なくともメッシュシートの細孔径が95μm~300μmの範囲において、高い回収率で細胞を回収できることが確認された。 FIG. 6 is a graph showing the relationship between the pore size of the mesh sheet and the cell recovery rate. It was confirmed that when the angle of the mesh sheet surface with respect to the liquid passing direction was set to the same angle, the cells could be collected at a high recovery rate at least when the pore diameter of the mesh sheet was 95 μm to 300 μm.
4.細胞懸濁液調製用容器と細胞濃縮洗浄システムを用いた試験
 図1-1~2-2に示した構造を有する細胞懸濁液調製用容器と細胞濃縮洗浄システム(カネカ製)を接続して閉鎖系で細胞懸濁液を調製し、同一個体から得た試料から従来法により開放系で細胞懸濁液を調製した場合の結果と比較した。細胞濃縮洗浄システム(カネカ製)は、本明細書に開示する「細胞懸濁液を閉鎖系で洗浄および濃縮することができる細胞懸濁液処理装置」の一例である。なお、細胞懸濁液調製用容器は、実施例3で用いたメッシュシートの細孔径が95μmであるものを用いた。
4). Test using a cell suspension preparation container and a cell concentration washing system The cell suspension preparation container having the structure shown in FIGS. 1-1 and 2-2 and a cell concentration washing system (manufactured by Kaneka) were connected. The cell suspension was prepared in a closed system, and the results were compared with the results when a cell suspension was prepared in an open system by a conventional method from a sample obtained from the same individual. The cell concentration washing system (manufactured by Kaneka) is an example of “a cell suspension treatment apparatus capable of washing and concentrating a cell suspension in a closed system” disclosed in the present specification. In addition, the container for cell suspension preparation used what the pore diameter of the mesh sheet | seat used in Example 3 is 95 micrometers.
 (実施例6)細胞懸濁液調製用容器1に、脂肪組織サンプルと0.075%コラゲナーゼ水溶液を、容器内に細胞濃度1.6×10cells/mLの細胞懸濁液が102mL調製される量で注入し、容器をシェーカーで振盪させながら酵素反応を行った。酵素反応は投入口20及び排出口30を閉鎖した状態で行った。酵素反応後、容器内の溶液は油層と水層の2層に分離していた。容器を投入部21が上になるように吊るし、分離した2層の境界をクランプで挟み、油層の成分が排出部31方向に流れないようにした。容器中のメッシュシート40は、メッシュシートに沿う面の法線Lと通液方向F(鉛直方向)が成す狭角の角度をθ(°)としたとき、90-θが約1であった。その状態のまま、排出口から陰圧をかけて、排出口から300mL/分の速度で容器から溶液を排出させて、接続された細胞濃縮洗浄システムに細胞懸濁液を移送し、洗浄を行った。洗浄後に得られた細胞懸濁液における細胞回収率は83%であった。 (Example 6) A fat tissue sample and a 0.075% collagenase aqueous solution were prepared in a cell suspension preparation container 1, and 102 mL of a cell suspension having a cell concentration of 1.6 × 10 6 cells / mL was prepared in the container. The enzyme reaction was performed while shaking the container with a shaker. The enzyme reaction was performed with the inlet 20 and outlet 30 closed. After the enzyme reaction, the solution in the container was separated into two layers, an oil layer and an aqueous layer. The container was hung with the input part 21 facing upward, and the boundary between the two separated layers was clamped so that the components of the oil layer did not flow toward the discharge part 31. The mesh sheet 40 in the container had 90-θ of about 1 when the narrow angle formed by the normal L of the surface along the mesh sheet and the liquid flow direction F (vertical direction) was θ (°). . In that state, negative pressure is applied from the discharge port, the solution is discharged from the container at a rate of 300 mL / min from the discharge port, the cell suspension is transferred to the connected cell concentration washing system, and washing is performed. It was. The cell recovery rate in the cell suspension obtained after washing was 83%.
 (比較例3)実施例6と同じ脂肪組織サンプルと0.075%コラゲナーゼ溶液を用いて遠心管内で細胞濃度1.6×10cells/mLの細胞懸濁液を調製した。得られた細胞懸濁液20mLを従来どおり、遠心管の蓋を開放して上清液を排出し、洗浄液を加え、蓋を閉じて遠心分離する操作を繰り返して濃縮洗浄したところ、細胞回収率は68%であった。 (Comparative Example 3) A cell suspension having a cell concentration of 1.6 × 10 6 cells / mL was prepared in a centrifuge tube using the same adipose tissue sample and 0.075% collagenase solution as in Example 6. As usual, 20 mL of the resulting cell suspension was opened by opening the centrifuge tube lid, the supernatant liquid was discharged, washing liquid was added, the lid was closed, and centrifugation was repeated and concentrated and washed. Was 68%.
 図7は、実施例6と比較例3における結果を示すグラフである。実施例6と比較例3の結果を比較することにより、閉鎖系を形成できる容器(細胞懸濁液調製用容器)と自動化細胞濃縮洗浄システムを利用することで、一般的な方法である遠心処理よりも高い細胞回収率で細胞を回収できることが確認された。 FIG. 7 is a graph showing the results in Example 6 and Comparative Example 3. By comparing the results of Example 6 and Comparative Example 3, by using a container capable of forming a closed system (container for cell suspension preparation) and an automated cell concentration washing system, centrifugation is a common method. It was confirmed that the cells could be recovered at a higher cell recovery rate.
1…細胞懸濁液調製用容器、10…容器本体、11…第一空間、12…第二空間、13…内部空間、15…第一側壁、16…第二の側壁、20…投入口、21…投入部、22…投入部の第一空間側の端、30…排出口、31…排出部、32…排出部の第二空間側の端、40…メッシュシート、41…メッシュシート周縁部、150…第一側壁周縁部、 160…第二側壁周縁部、901…細胞懸濁液調製用容器接続部、902…希釈液バッグ接続部、903…貯留容器、904…廃液容器、905…回収容器、906…細胞懸濁液処理器、908…エアフィルタ、909…気泡センサー、910…気泡センサー、911…気泡センサー、912~14…ポンプ、915…溶液入口ポート、916…循環出口ポート、917…循環入口ポート、918…細胞懸濁液導入口、919…細胞懸濁液導出口、920…濾液用出口、921~25…クランプ、926…プライミング液バッグ接続部、927…注入路、928…導入用連通管、929…導出用連通管、930…循環回路、931…回収路 DESCRIPTION OF SYMBOLS 1 ... Cell suspension preparation container, 10 ... Container main body, 11 ... First space, 12 ... Second space, 13 ... Internal space, 15 ... First side wall, 16 ... Second side wall, 20 ... Input port, DESCRIPTION OF SYMBOLS 21 ... Input part, 22 ... End of 1st space side of input part, 30 ... Discharge port, 31 ... Discharge part, 32 ... End of 2nd space side of discharge part, 40 ... Mesh sheet, 41 ... Perimeter of mesh sheet , 150 ... first side wall peripheral part, trough 160 ... second side wall peripheral part, 901 ... cell suspension preparation container connection part, 902 ... dilution liquid bag connection part, 903 ... storage container, 904 ... waste liquid container, 905 ... collection Container, 906 ... Cell suspension treatment device, 908 ... Air filter, 909 ... Bubble sensor, 910 ... Bubble sensor, 911 ... Bubble sensor, 912-14 ... Pump, 915 ... Solution inlet port, 916 ... Circulation outlet port, 917 ... circulation inlet port, 18 ... Cell suspension inlet, 919 ... Cell suspension outlet, 920 ... Filtrate outlet, 921-25 ... Clamp, 926 ... Priming solution bag connection, 927 ... Injection path, 928 ... Inlet communication tube, 929... Communication pipe for derivation, 930... Circulation circuit, 931.
 本明細書で引用した全ての刊行物、特許および特許出願はそのまま引用により本明細書に組み入れられるものとする。 All publications, patents and patent applications cited in this specification are incorporated herein by reference in their entirety.

Claims (15)

  1.  細胞懸濁液調製用容器であって、
     液体を保持可能な内部空間を内包する容器本体と、
     前記内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、
     前記容器本体に設けられ、前記第一空間への液体の投入口が形成された投入部と、
     前記容器本体に設けられ、前記第二空間からの液体の排出口が形成された排出部と、
    を備え、
     前記排出口から排出される液体の流れの方向と、前記メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θが50未満である、前記容器。
    A cell suspension preparation container,
    A container body containing an internal space capable of holding liquid;
    A mesh sheet arranged to divide the internal space into a first space and a second space;
    A charging unit provided in the container body, and formed with a liquid charging port into the first space;
    A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
    With
    The container in which 90-θ is less than 50, where θ (°) is a narrow angle formed between the flow direction of the liquid discharged from the discharge port and the normal line of the surface along the mesh sheet .
  2.  前記メッシュシートの細孔径が50~300μmである、請求項1に記載の容器。 The container according to claim 1, wherein the pore size of the mesh sheet is 50 to 300 µm.
  3.  前記容器本体が可撓性を有する、請求項1または2に記載の容器。 The container according to claim 1 or 2, wherein the container body has flexibility.
  4.  前記容器本体の少なくとも一部が透明または半透明の材料からなる、請求項1~3のいずれか1項に記載の容器。 The container according to any one of claims 1 to 3, wherein at least a part of the container body is made of a transparent or translucent material.
  5.  前記メッシュシートの開孔率が40%以上である、請求項1~4のいずれか1項に記載の容器。 The container according to any one of claims 1 to 4, wherein the mesh sheet has a porosity of 40% or more.
  6.  前記メッシュシートの前記内部空間に露出する部分のうち、該部分を平面視したときの面積に対して50%以上の面積の領域が、90-θが50未満となる領域である、請求項1~5のいずれか1項に記載の容器。 2. A region having an area of 50% or more with respect to an area of the mesh sheet exposed to the internal space when viewed in plan is a region where 90−θ is less than 50. The container according to any one of 1 to 5.
  7.  細胞懸濁液調製用容器であって、
     液体を保持可能な内部空間を内包する容器本体と、
     前記内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、
     前記容器本体に設けられ、前記第一空間への液体の投入口が形成された投入部と、
     前記容器本体に設けられ、前記第二空間からの液体の排出口が形成された排出部と、
    を備え、
     前記容器本体が、前記メッシュシートを間に介して対向する第一側壁と第二側壁とを含み、
     前記第一側壁と前記メッシュシートとが前記第一空間を囲い、
     前記第二側壁と前記メッシュシートとが前記第二空間を囲い、
     前記投入部が、前記第一側壁の周縁部と前記メッシュシートの周縁部との間に、前記投入口を介して前記第一空間と外部とを連通するように配置されており、
     前記排出部が、前記第二側壁の周縁部と前記メッシュシートの周縁部との間に、前記排出口を介して前記第二空間と外部とを連通するように配置されており、
     前記第一側壁、前記第二側壁、及び、前記メッシュシートが周縁部において一体化されている、前記容器。
    A cell suspension preparation container,
    A container body containing an internal space capable of holding liquid;
    A mesh sheet arranged to divide the internal space into a first space and a second space;
    A charging unit provided in the container body, and formed with a liquid charging port into the first space;
    A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
    With
    The container body includes a first side wall and a second side wall facing each other with the mesh sheet interposed therebetween,
    The first side wall and the mesh sheet surround the first space;
    The second side wall and the mesh sheet surround the second space;
    The insertion portion is disposed between the peripheral portion of the first side wall and the peripheral portion of the mesh sheet so as to communicate the first space and the outside via the input port,
    The discharge part is arranged between the peripheral part of the second side wall and the peripheral part of the mesh sheet so as to communicate the second space and the outside through the discharge port,
    The said container by which said 1st side wall, said 2nd side wall, and said mesh sheet are integrated in the peripheral part.
  8.  前記投入部と、前記排出部とが、前記容器本体の対向する位置に配置されており、
     前記投入部の、前記第一空間の側の端の、前記第一側壁と前記第二側壁とが対向する方向に沿った幅をW1、
     前記排出部の、前記第二空間の側の端の、前記第一側壁と前記第二側壁とが対向する方向に沿った幅をW2、
     W1とW2との平均値をW、
     前記投入部の、前記第一空間の側の端と、前記排出部の、前記第二空間の側の端との間の距離をD
    としたとき、
     D/Wが12以上である、請求項7に記載の容器。
    The input part and the discharge part are arranged at opposing positions of the container body,
    W1 is the width along the direction in which the first side wall and the second side wall face each other at the end of the first space on the first space side,
    The width of the end of the discharge portion on the second space side along the direction in which the first side wall and the second side wall face each other is W2,
    The average value of W1 and W2 is W,
    The distance between the end of the input portion on the first space side and the end of the discharge portion on the second space side is D
    When
    The container of Claim 7 whose D / W is 12 or more.
  9.  前記第一側壁及び前記第二側壁が可撓性を有する、請求項7または8に記載の容器。 The container according to claim 7 or 8, wherein the first side wall and the second side wall have flexibility.
  10.  細胞含有試料から細胞懸濁液を調製するための方法であって、
    (a)液体を保持可能な内部空間を内包する容器本体と、
     前記内部空間を、第一空間と第二空間とに区切るように配置されたメッシュシートと、
     前記容器本体に設けられ、前記第一空間への液体の投入口が形成された投入部と、
     前記容器本体に設けられ、前記第二空間からの液体の排出口が形成された排出部と、
    を備える容器において、前記投入口を通じて細胞含有試料と酵素を入れ、前記第一空間内で酵素反応を実施して酵素処理液を生成する、及び/又は、前記投入口を通じて細胞含有試料の酵素処理液を入れる工程、
    (b)前記酵素処理液を前記メッシュシートに通して夾雑物を除去し、前記第二空間側に細胞懸濁液を生成し、生成された前記細胞懸濁液を、前記排出口を通じて排出する工程、を含む、前記方法。
    A method for preparing a cell suspension from a cell-containing sample comprising:
    (A) a container body containing an internal space capable of holding a liquid;
    A mesh sheet arranged to divide the internal space into a first space and a second space;
    A charging unit provided in the container body, and formed with a liquid charging port into the first space;
    A discharge part provided in the container body, and formed with a discharge port for liquid from the second space;
    A cell-containing sample and an enzyme are introduced through the inlet, and an enzyme treatment solution is generated by performing an enzyme reaction in the first space, and / or an enzyme treatment of the cell-containing sample is conducted through the inlet. Adding liquid,
    (B) The enzyme treatment liquid is passed through the mesh sheet to remove impurities, a cell suspension is generated on the second space side, and the generated cell suspension is discharged through the discharge port. A process comprising the steps of:
  11.  工程(b)において、前記排出口を通じて排出される前記細胞懸濁液の流れ方向と、前記メッシュシートに沿う面の法線とが成す狭角の角度をθ(°)としたとき、90-θが50未満となるように、前記細胞懸濁液を排出する、請求項10に記載の方法。 In step (b), when the narrow angle formed by the flow direction of the cell suspension discharged through the discharge port and the normal of the surface along the mesh sheet is θ (°), 90− The method according to claim 10, wherein the cell suspension is discharged so that θ is less than 50.
  12.  前記容器が、請求項1~9のいずれか1項に記載の容器である、請求項10または11に記載の方法。 The method according to claim 10 or 11, wherein the container is the container according to any one of claims 1 to 9.
  13.  前記細胞含有試料が、脂肪、皮膚、血管、角膜、口腔、腎臓、肝臓、膵臓、心臓、神経、筋肉、前立腺、腸、羊膜、胎盤および臍帯からなる群から選択される1以上に由来する、請求項10~12のいずれか1項に記載の方法。 The cell-containing sample is derived from one or more selected from the group consisting of fat, skin, blood vessels, cornea, oral cavity, kidney, liver, pancreas, heart, nerve, muscle, prostate, intestine, amniotic membrane, placenta and umbilical cord; The method according to any one of claims 10 to 12.
  14.  前記投入口および/または前記排出口が、シリコンゴムおよび/またはニードルレスポートにより封鎖されている、請求項10~13のいずれか1項に記載の方法。 The method according to any one of claims 10 to 13, wherein the input port and / or the discharge port are sealed with silicon rubber and / or a needleless port.
  15.  前記排出口が、細胞懸濁液を閉鎖系で洗浄および濃縮することができる細胞懸濁液処理装置に接続されており、
    (c)前記排出口から排出された前記細胞懸濁液を、前記装置により閉鎖系で洗浄および濃縮し、細胞濃縮液を得る工程
    をさらに含む、請求項10~14のいずれか1項に記載の方法。
    The outlet is connected to a cell suspension treatment device capable of washing and concentrating the cell suspension in a closed system;
    The cell suspension according to any one of claims 10 to 14, further comprising a step (c) of washing and concentrating the cell suspension discharged from the discharge port in a closed system by the device to obtain a cell concentrate. the method of.
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JPH09510916A (en) * 1994-03-31 1997-11-04 イ ノ テ Biological fluid filtration device and use thereof
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JPH09510916A (en) * 1994-03-31 1997-11-04 イ ノ テ Biological fluid filtration device and use thereof
JP2009038998A (en) * 2007-08-07 2009-02-26 Olympus Corp Cell-separating device
JP2013541958A (en) * 2010-10-25 2013-11-21 サイトゲン カンパニー リミテッド Cell collection device

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