WO2025183119A1 - Method for producing mesenchymal stem cells - Google Patents
Method for producing mesenchymal stem cellsInfo
- Publication number
- WO2025183119A1 WO2025183119A1 PCT/JP2025/006987 JP2025006987W WO2025183119A1 WO 2025183119 A1 WO2025183119 A1 WO 2025183119A1 JP 2025006987 W JP2025006987 W JP 2025006987W WO 2025183119 A1 WO2025183119 A1 WO 2025183119A1
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- stem cells
- mesenchymal stem
- culture
- stirring
- minutes
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K35/00—Medicinal preparations containing materials or reaction products thereof with undetermined constitution
- A61K35/12—Materials from mammals; Compositions comprising non-specified tissues or cells; Compositions comprising non-embryonic stem cells; Genetically modified cells
- A61K35/28—Bone marrow; Haematopoietic stem cells; Mesenchymal stem cells of any origin, e.g. adipose-derived stem cells
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P19/00—Drugs for skeletal disorders
- A61P19/02—Drugs for skeletal disorders for joint disorders, e.g. arthritis, arthrosis
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P19/00—Drugs for skeletal disorders
- A61P19/08—Drugs for skeletal disorders for bone diseases, e.g. rachitism, Paget's disease
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N15/00—Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
- C12N15/09—Recombinant DNA-technology
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
- C12N5/06—Animal cells or tissues; Human cells or tissues
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
- C12N5/10—Cells modified by introduction of foreign genetic material
Definitions
- the present invention relates to a method for producing mesenchymal stem cells, which comprises culturing mesenchymal stem cells in the presence of microcarriers, and which includes an agitated static culture step that includes a step of agitating the mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand still.
- mesenchymal stem cells are expected to be a useful cell source for cell therapy.
- Mesenchymal stem cells can be harvested from a variety of body tissues, and it has been reported that they can be isolated from bone marrow, synovium, periosteum, fat, muscle, dental pulp, placenta, umbilical cord, and other tissues.
- Patent Document 1 describes culturing adherent cells in a cell suspension containing the adherent cells, microcarriers, and a medium, and describes that the culturing may include intermittent stirring of the cell suspension.
- Patent Document 2 describes a method for harvesting cultured cells from a soluble substrate, which comprises separating the cultured cells from the substrate by digesting the soluble substrate by exposing it to a chelating agent, an enzyme, or both.
- mesenchymal stem cells are grown by intermittent stirring followed by continuous stirring in the step of adhering the mesenchymal stem cells to the soluble substrate.
- Patent Document 3 describes cell culture using microcarriers. Patent Document 3 also describes the attachment and proliferation of MSCs to microcarriers while continuously stirring them.
- Agitated culture technology has been used in the production of biopharmaceuticals using CHO cells (Chinese hamster ovary cells) and vaccines using Vero cells. However, in these cases, the cells themselves are not the final product, but rather the proteins secreted by the cells.
- agitated culture technology is used to produce cell therapy products using mesenchymal stem cells, where the cells themselves are the final product, a problem has been discovered in that microcarriers to which cells do not adhere are scattered, preventing full use of the microcarriers. This has also led to the problem of low cell recovery rates.
- the objective of the present invention is to provide a method for producing mesenchymal stem cells that can reduce empty microcarriers (microcarriers to which cells do not adhere), thereby increasing the number of cells recovered through culture.
- an agitation and static culture step which includes a step of agitating the mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand, is carried out for 48 hours or more, and the agitation and static culture step is carried out two or more times during the 48-hour or more culture period, and that starting 24 hours after the start of culture, the agitation and static culture step is carried out at least once every 48 hours, thereby reducing empty microcarriers and improving the number of recovered cells.
- the present invention was completed based on the above findings.
- a method for producing mesenchymal stem cells comprising culturing mesenchymal stem cells in the presence of microcarriers, the method comprising carrying out an agitation static culture step, for 48 hours or more, which step includes a step of agitating the mesenchymal stem cells and a step of allowing the mesenchymal stem cells to stand thereafter, and carrying out the agitation static culture step two or more times during the 48-hour or longer culture period, and carrying out the agitation static culture step one or more times every 48 hours starting 24 hours after the start of culture.
- ⁇ 2> The method for producing mesenchymal stem cells according to ⁇ 1>, wherein each of the two or more stirring and static culture steps is the same step, or the two or more stirring and static culture steps include a stirring and static culture step in which either one or more of the duration of the stirring step and the duration of the static culture step are different.
- ⁇ 3> The method for producing mesenchymal stem cells according to ⁇ 1> or ⁇ 2>, wherein the stirring and static culture step is carried out from the start of culture to the end of culture.
- ⁇ 4> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 3>, wherein the mesenchymal stem cells are derived from a human.
- ⁇ 5> The method for producing mesenchymal stem cells according to ⁇ 4>, wherein the mesenchymal stem cells are derived from induced pluripotent stem cells, bone marrow, fat, dental pulp, umbilical cord, placenta, or synovium.
- ⁇ 6> The method for producing mesenchymal stem cells according to ⁇ 5>, wherein the mesenchymal stem cells are derived from synovial membrane.
- ⁇ 7> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 6>, wherein the time for the step of leaving the mesenchymal stem cells stationary in the stirring static culture step is 1 minute or more and 2,400 minutes or less.
- ⁇ 8> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 7>, wherein the time for the step of leaving the mesenchymal stem cells standing in the stirring static culture step is 0.1 min/mL or more and 240.0 min/mL or less per volume of culture solution.
- ⁇ 9> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 8>, wherein the time for the step of stirring the mesenchymal stem cells in the stirring static culture step is 1 minute or more and 2000 minutes or less.
- ⁇ 10> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 9>, wherein the time for the step of stirring the mesenchymal stem cells in the stirring static culture step is 0.1 min/mL or more and 200.0 min/mL or less per volume of culture solution.
- ⁇ 11> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 10>, wherein the stirring and static culture step is carried out 1 to 48 times per 24 hours.
- ⁇ 12> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 11>, wherein the duration of each stirring and static culture step is 30 minutes to 1,440 minutes.
- ⁇ 13> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 12>, wherein the ratio of the time taken for the step of stirring the mesenchymal stem cells to the time taken for the step of allowing the mesenchymal stem cells to stand in the stirring static culture step is within the range of 1:0.005 to 1:700.
- ⁇ 14> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 13>, wherein the total time of the stirring step during the entire culture period is longer than the total time of the standing step.
- ⁇ 15> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 14>, wherein no microcarriers are added in the stirring static culture step.
- ⁇ 16> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 15>, wherein the stirring static culture is carried out for 48 hours or more after 24 hours from the start of the culture, and then the stirring culture is carried out continuously.
- ⁇ 17> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 16>, wherein the stirring static culture step is carried out 24 hours or more after the start of culture, and stirring culture is carried out continuously from at least two days before the end of culture.
- ⁇ 18> The method for producing mesenchymal stem cells according to any one of ⁇ 1> to ⁇ 17>, wherein the ratio of the time of the stirring static culture step to the time of the continuous stirring step is 1:0.3 to 1:5.5.
- the method for producing mesenchymal stem cells of the present invention promotes cell adhesion to empty carriers, thereby increasing the number of viable cells at the time of collection.
- the present invention relates to a method for producing mesenchymal stem cells, which comprises culturing mesenchymal stem cells in the presence of microcarriers, and which comprises carrying out an agitation-static culture step, which includes a step of agitating the mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand, for 48 hours or more, and which comprises carrying out the agitation-static culture step two or more times during the 48-hour or more culture period, and which comprises carrying out the agitation-static culture step one or more times every 48 hours starting 24 hours after the start of culture.
- empty microcarriers microcarriers to which cells do not adhere
- the present invention can ensure the differentiation ability of mesenchymal stem cells, mesenchymal stem cells are useful as therapeutic agents.
- cells for cell therapy can be easily produced in large quantities.
- the input microcarriers can be used efficiently, making it possible to culture using a minimum number of microcarriers and culturing at low cost.
- the method for producing mesenchymal stem cells according to the present invention can be used in industries that require large quantities of cells, such as allogeneic cell therapy products.
- Stem cells refer to immature cells that have the ability to self-renew and differentiate and proliferate, and include pluripotent stem cells, multipotent stem cells, unipotent stem cells, etc., depending on their differentiation potential.
- Stem cells are generally defined as undifferentiated cells that have the "self-renewal ability" to proliferate while maintaining an undifferentiated state, and the "pluripotency" to differentiate into all three germ layer lineages.
- Pluripotent stem cells refer to cells that have the ability to differentiate into all tissues and cells that make up a living organism.
- Multipotent stem cells refer to cells that have the ability to differentiate into multiple types of tissues and cells, but not all types.
- Unipotent stem cells refer to cells that have the ability to differentiate into specific tissues or cells.
- Mesenchymal stem cells broadly refer to a population of stem cells or their precursor cells that can differentiate into all or some of the mesenchymal cells, such as osteoblasts, chondroblasts, adipblasts, and muscle cells. Mesenchymal stem cells are also called stromal cells.
- the origin of the mesenchymal stem cells is not particularly limited, and may be cells from, for example, rodents such as rats, mice, hamsters, and guinea pigs; lagomorphs such as rabbits; ungulates such as pigs, cows, goats, and sheep; Carnivores such as dogs and cats; and primates such as humans, monkeys, rhesus monkeys, marmosets, orangutans, and chimpanzees. It is preferable that the mesenchymal stem cells are derived from humans.
- Mesenchymal stem cells are preferably derived from induced pluripotent stem cells, bone marrow, fat, dental pulp, umbilical cord, placenta, or synovial membrane. Mesenchymal stem cells are particularly preferably derived from synovial membrane.
- mesenchymal stem cells When used as a therapeutic agent, they may be autologous cells of the patient to be administered, or allogeneic cells.
- Mesenchymal stem cells can be identified by detecting molecules characteristic of mesenchymal stem cells, such as enzymes, receptors, and low-molecular-weight compounds.
- Molecules characteristic of mesenchymal stem cells include, but are not limited to, cell surface markers (positive markers), such as CD73, CD90, CD105, and CD166.
- Negative markers not expressed in mesenchymal stem cells include, but are not limited to, CD19, CD34, CD45, HLA-DR, CD11b, and CD14.
- CD stands for Clusters of Differentiation
- HLA-DR stands for Human Leukocyte Antigen-D-Related.
- synovial membrane-derived mesenchymal stem cells can be used as mesenchymal stem cells.
- Synovial membrane-derived mesenchymal stem cells also called synovial stem cells
- synovial membrane-derived mesenchymal stem cells are stem cells contained in the synovial membrane.
- Synovial membrane-derived mesenchymal stem cells can be detected, for example, by detecting CD90 positivity, CD45 negativity, and chondrogenic differentiation ability, but the detection method is not particularly limited.
- Synovium-derived mesenchymal stem cells can be obtained, for example, by a method comprising step A of treating synovial tissue with an enzyme, step B of washing the mixture after enzyme treatment and culturing the synovium-derived mesenchymal stem cells contained in the mixture in a culture medium, and step C of cryopreserving the cultured synovium-derived mesenchymal stem cells.
- Synovial tissue can be harvested during arthroscopic surgery and then treated with enzymes.
- the enzyme is not particularly limited as long as it contains a protease, but is preferably a mixed enzyme containing one or more types of collagenase and one or more types of neutral protease.
- a particularly preferred enzyme is Liberase (registered trademark).
- Liberase MNP-S manufactured by Roche
- the enzyme reaction can be carried out in an aqueous solution containing the enzyme.
- the enzymatic reaction can be carried out at a temperature of preferably 15°C to 40°C, more preferably 20°C to 40°C, and even more preferably 25°C to 40°C.
- the reaction time may be 10 minutes or more, preferably 30 minutes or more, more preferably 1 hour or more, even more preferably 1.5 hours or more, and may be 2 hours or more.
- the upper limit of the reaction time is not particularly limited, but may be 10 hours or less, 9 hours or less, 8 hours or less, 7 hours or less, 6 hours or less, 5 hours or less, or 4 hours or less.
- the enzyme-treated mixture contains synovium-derived mesenchymal stem cells.
- the enzyme-treated mixture is passed through a cell strainer and transferred to a centrifuge tube, and then centrifuged to recover synovium-derived mesenchymal stem cells.
- Step B Culturing the synovium-derived mesenchymal stem cells contained in the mixture after washing the mixture after enzyme treatment in a culture medium
- Washing can be performed by resuspending the synovium-derived mesenchymal stem cells recovered by the above-mentioned centrifugation in a medium and centrifuging again.
- the medium can be, but is not limited to, ⁇ -modified Eagle's minimum essential medium ( ⁇ MEM). Washing can be performed multiple times (two or more times) using the medium described above.
- the synovium-derived mesenchymal stem cells contained in the mixture after washing the mixture following enzyme treatment are cultured in a culture medium.
- substrates include, but are not limited to, flat plastic substrates such as flasks and culture plates, and three-dimensional substrates such as culture bags, microcarriers, or gels.
- the medium used for culturing can be prepared using a medium used for culturing ordinary animal cells as the basal medium.
- the medium may also contain an antibiotic or antifungal agent (e.g., amphotericin B, gentamicin, etc.).
- the cell culture conditions are not particularly limited, and ordinary cell culture conditions can be used. For example, culture at a temperature of 30 to 40°C and 3 to 7% CO2 can be used, but the conditions are not particularly limited. One example is culture at a temperature of 37°C and 5% CO2 .
- the synovium-derived mesenchymal stem cells cultured in step B are preferably separated from the substrate prior to step C.
- separation from the substrate can be achieved by allowing a cell detachment solution to act on the mesenchymal stem cells for 120 minutes or less.
- the cell detachment solution is a solution containing a trypsin-like enzyme and EDTA.
- a particularly preferred enzyme is TrypLE. Examples of TrypLE that can be used include TrypLE Select Enzyme (manufactured by ThermoFisher Scientific), TrypL Express (manufactured by Gibco), and TrypLE Select (manufactured by Gibco).
- the time for which the cell detachment solution is allowed to act on the mesenchymal stem cells is preferably 5 to 120 minutes, more preferably 5 to 60 minutes, and especially preferably 5 to 30 minutes.
- Step C of cryopreserving the cultured synovium-derived mesenchymal stem cells After cultivation, the synovium-derived mesenchymal stem cells can be cryopreserved.
- mesenchymal stem cells are cultured in the presence of microcarriers.
- microcarriers may or may not be added.
- Microcarriers are carriers that serve as scaffolds for cell growth in adherent cell culture. Microcarriers known as carriers for cell culture can be used. Microcarriers may be made of organic, inorganic, or composite materials of these. Microcarriers may be soluble or insoluble.
- organic materials include synthetic polymers such as polystyrene, polyester, polyurethane, polyethylene, polypropylene, polyvinyl alcohol, (meth)acrylic polymers, (meth)acrylamide polymers, silicone polymers, epoxy resins, and urethane resins; and natural polymers such as cellulose, dextran, collagen, polygalacturonic acid, polyalginic acid, and gelatin.
- synthetic polymers such as polystyrene, polyester, polyurethane, polyethylene, polypropylene, polyvinyl alcohol, (meth)acrylic polymers, (meth)acrylamide polymers, silicone polymers, epoxy resins, and urethane resins
- natural polymers such as cellulose, dextran, collagen, polygalacturonic acid, polyalginic acid, and gelatin.
- Inorganic materials include, for example, glass, ceramic, metal, alloy, and metal oxide.
- the microcarrier material preferably contains an organic material, and more preferably contains a natural polymer. From the viewpoint of operability, soluble microcarriers are preferable, but are not limited to this.
- microcarriers examples include, but are not limited to, SoloHill (registered trademark) Plastic microcarriers (Sartorius), CellBIND (Corning), SyntheMAX (Corning), Cytodex 1, and Cytodex 3 (Cytiva).
- cationic functional groups may be introduced onto the surface of the microcarrier.
- cationic functional groups include groups containing substituted or unsubstituted amino groups such as dimethylamino, diethylamino, and amino groups.
- a cell adhesive polymer may be disposed on the surface of the microcarrier.
- the cell adhesive polymer may be a polypeptide or polysaccharide that exhibits cell adhesive properties, such as collagen, gelatin, alginic acid, Matrigel® (BD Biosciences), hyaluronic acid, laminin, fibronectin, vitronectin, elastin, heparan sulfate, dextran, dextran sulfate, and chondroitin sulfate.
- the cell adhesive polymer may be a partial peptide or oligosaccharide that exhibits cell adhesive properties.
- hydrophilic functional groups may be generated by plasma treatment, corona treatment, or the like to hydrophilize the microcarrier surface. Examples of hydrophilic functional groups include groups containing hydroxyl, carbonyl, and carboxyl groups.
- Microcarrier shapes include, for example, spherical, flat, cylindrical, plate-like, and prismatic. Microcarriers may be porous microcarriers with internal pores, or microcarriers without internal pores.
- the average particle diameter (D50) of the microcarriers is, for example, 50 to 1,000 ⁇ m, preferably 100 to 500 ⁇ m, and more preferably 150 to 250 ⁇ m.
- the average particle diameter of the microcarriers is the value measured as the median diameter (D50) in physiological saline.
- the average particle diameter of the microcarriers can be measured using a laser diffraction/scattering particle size distribution measuring device.
- the concentration of microcarriers in the culture medium can be adjusted appropriately based on the shape, size, surface area, etc. of the microcarriers, but may be, for example, 0.1 to 100 mg/mL, 1 to 100 mg/mL, or 5 to 100 mg/mL.
- the mesenchymal stem cells can be seeded by adding the mesenchymal stem cells to a medium containing microcarriers.
- a microcarrier solution is added to a container such as a centrifuge tube and allowed to stand to allow the microcarriers to settle, after which the supernatant is removed and culture medium is added.
- the microcarriers are thoroughly suspended, and the resulting suspension is added to a culture vessel, to which culture medium is then added.
- Cell seeding can then be carried out by adding a cell suspension containing a predetermined number of cells in culture medium to the culture vessel.
- the method of the present invention comprises carrying out an agitation static culture step, which includes a step of agitating mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand, for 48 hours or more, and comprises carrying out the agitation static culture step two or more times during the 48-hour or more culture period, and carrying out the agitation static culture step at least once every 48 hours starting 24 hours after the start of culture.
- the agitation static culture step is a combination of an agitation step and a standing step, and this set may be repeated multiple times.
- the start of culture refers to the moment when cells and microcarriers coexist in the same liquid in the same container.
- the stirring step is a step in which mesenchymal stem cells are cultured while stirring the culture solution containing mesenchymal stem cells and microcarriers.
- the stirring speed can be set appropriately depending on the volume of the culture solution, but is a speed at which all of the microcarriers in the culture solution are suspended.
- the stirring speed is not particularly limited, but is generally 50 rpm or higher, preferably 100 rpm or higher, more preferably 150 rpm or higher, and may be 200 rpm or higher, or 300 rpm or higher. There is no particular upper limit to the stirring speed, but it is generally 1000 rpm or lower, preferably 700 rpm or lower. Note that the stirring speed in the stirring step may be less than 50 rpm (for example, 10 rpm or higher but less than 50 rpm) depending on the volume of the culture solution.
- the "standing step” refers to a step in which no stirring is performed, or a step in which weak stirring at less than 50 rpm is performed. Note that if the stirring speed in the stirring step is less than 50 rpm (for example, 10 rpm or more but less than 50 rpm), the weak stirring speed in the standing step will be slower than the stirring speed in the stirring step. If the stirring speed in the stirring step is less than 50 rpm, it is preferable that the weak stirring speed in the standing step be less than half the stirring speed in the stirring step.
- Agitation can be achieved by placing a stirring bar, stirring blade, or stirring impeller in the culture solution (for example, a rotating shaft with stirring blades can be provided in the culture vessel) and rotating it.
- a stirring bar, stirring blade, or stirring impeller in the culture solution (for example, a rotating shaft with stirring blades can be provided in the culture vessel) and rotating it.
- the duration of the above-mentioned stirring and static culture process is 48 hours or more, but it may also be 3 days or more, 4 days or more, 5 days or more, 6 days or more, or 7 days or more.
- the above-mentioned stirring and static culture step is carried out two or more times during a culture period of 48 hours or more, but the above-mentioned stirring and static culture step may also be carried out seven or more times, 42 or more times, 84 or more times, or 336 or more times during a culture period of 48 hours or more.
- the stirring static culture step is carried out at least once every 48 hours after 24 hours from the start of culture, but the stirring static culture step may also be carried out at least twice, at least 12 times, at least 24 times, or at least 96 times every 48 hours.
- the two or more stirring and static culture steps may be the same step, or the two or more stirring and static culture steps may include stirring and static culture steps in which one or more of the stirring step time and the stationary step time are different.
- the two or more stirring and static culture steps are the same step.
- the stirring static culture step is carried out from the start of the culture to the end of the culture.
- the time for the step of allowing the mesenchymal stem cells to stand in the stirred static culture step is preferably 1 minute or more and 2,400 minutes or less, more preferably 1 minute or more and 2,000 minutes or less, even more preferably 1 minute or more and 1,900 minutes or less, even more preferably 1 minute or more and 1,600 minutes or less, even more preferably 1 minute or more and 1,500 minutes or less, 10 minutes or more and 1,500 minutes or less, 20 minutes or more and 1,500 minutes or less, 30 minutes or more and 1,500 minutes or less, 50 minutes or more and 1,500 minutes or less, or 60 minutes or more and 1,500 minutes or less, or 1 minute or more and 240 minutes or less, 1 minute or more and 120 minutes or less, or 15 minutes or more and 120 minutes or less.
- the time for the step of allowing the mesenchymal stem cells to stand in the stirred static culture step is preferably 0.1 min/mL or more and 240.0 min/mL or less, more preferably 0.1 min/mL or more and 200.0 min/mL or less, more preferably 0.1 min/mL or more and 100.0 min/mL or less, more preferably 0.1 min/mL or more and 50.0 min/mL or less, and may be 0.1 min/mL or more and 24.0 min/mL or less, 0.1 min/mL or more and 12.0 min/mL or less, or 1.5 min/mL or more and 12.0 min/mL or less, per volume of culture solution.
- the time for the process of stirring the mesenchymal stem cells in the stirring static culture process is preferably 1 minute or more and 2000 minutes or less, and may be 1 minute or more and 1000 minutes or less, 1 minute or more and 500 minutes or less, 1 minute or more and 100 minutes or less, 1 minute or more and 60 minutes or less, 1 minute or more and 50 minutes or less, 1 minute or more and 30 minutes or less, 1 minute or more and 20 minutes or less, 1 minute or more and 15 minutes or less, or 1 minute or more and 10 minutes or less, or may be 5 minutes or more and 2000 minutes or less, 5 minutes or more and 1500 minutes or less, 5 minutes or more and 1440 minutes or less.
- the time for the process of stirring the mesenchymal stem cells in the stirring static culture process is preferably 0.1 min/mL or more and 200.0 min/mL or less per volume of culture solution, and may be 0.1 min/mL or more and 150.0 min/mL or less, 0.1 min/mL or more and 144.0 min/mL or less, 0.5 min/mL or more and 200.0 min/mL or less, 0.5 min/mL or more and 150.0 min/mL or less, or 0.5 min/mL or more and 144.0 min/mL or less.
- the stirring and static culture process can be performed preferably 1 to 48 times per 24 hours, or may be performed 1 to 24 times, 1 to 12 times, 1 to 6 times, or 6 to 12 times.
- the duration of one stirring static culture step is preferably 30 to 1440 minutes, or 30 to 1000 minutes, 30 to 800 minutes, 30 to 600 minutes, 30 to 500 minutes, 30 to 400 minutes, 30 to 300 minutes, 30 to 240 minutes, 30 to 120 minutes, 50 to 1440 minutes, 50 to 1000 minutes, 50 to 800 minutes, 50 to 600 minutes, minutes, 50 to 500 minutes, 50 to 400 minutes, 50 to 300 minutes, 50 to 240 minutes, 50 to 120 minutes, 120 to 1440 minutes, 120 to 1000 minutes, 120 to 800 minutes, 120 to 600 minutes, 120 to 500 minutes, 120 to 400 minutes, 120 to 300 minutes, 120 to 240 minutes, or 240 to 1440 minutes.
- the ratio of the time between the step of stirring the mesenchymal stem cells and the step of allowing the mesenchymal stem cells to stand in the stirring static culture step may be within the range of 1:0.005 to 1:700, 1:0.005 to 1:600, 1:0.005 to 1:500, 1:0.005 to 1:400, 1:0.005 to 1:380, 1:0.005 to 1:320, 1:0.005 to 1:300, 1:0.005 to 1:10, 1:0.01 to 1:10, 1:0.05 to 1:10, 1:0.08 to 1:10, 1:0.1 to 1:00, 1:0.01 to 1:1 ...
- the ratio may be 1 to 1:5, 1:1 to 1:700, 1:1 to 1:600, 1:1 to 1:500, 1:1 to 1:400, 1:1 to 1:300, 1:2 to 1:700, 1:2 to 1:600, 1:2 to 1:500, 1:1 to 2:400, 1:2 to 1:300, 1:5 to 1:700, 1:5 to 1:600, 1:5 to 1:500, 1:5 to 1:400, 1:5 to 1:300, 1:10 to 1:700, 1:10 to 1:600, 1:10 to 1:500, 1:10 to 1:400, or 1:10 to 1:300.
- the total time for the stirring step during the entire culture period is longer than the total time for the standing step.
- stirring static culture may be carried out for 48 hours or more, and thereafter stirring culture may be carried out continuously.
- agitation static culture may be performed for 72 hours or more after 24 hours from the start of culture, followed by continuous agitation culture.
- agitation static culture may be performed for 96 hours or more after 24 hours from the start of culture, followed by continuous agitation culture, or agitation static culture may be performed for 120 hours or more after 24 hours from the start of culture, followed by continuous agitation culture, or agitation static culture may be performed for 144 hours or more after 24 hours from the start of culture, followed by continuous agitation culture.
- the stirring static culture process may be carried out 24 hours or more after the start of culture, and stirring culture may be carried out continuously from two days or more before the end of culture.
- the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 3 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 4 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 5 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 6 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 7 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 3 days
- the ratio of the time for the stirring static culture step to the time for the continuous stirring step may preferably be 1:0.3 to 1:5.5.
- the culture vessel used for culturing mesenchymal stem cells is not particularly limited as long as it is capable of culturing mesenchymal stem cells, and examples include flasks, tissue culture flasks, dishes, Petri dishes, tissue culture dishes, multi-dishes, microplates, microwell plates, multi-plates, multi-well plates, microslides, chamber slides, petri dishes, tubes, trays, culture bags, roller bottles, culture tanks, and bioreactors.
- the culture scale (volume of culture medium) is not particularly limited, but is generally 0.01 to 3000 L, preferably 0.01 to 500 L, more preferably 0.01 to 50 L, and even more preferably 0.01 to 10 L.
- a basal medium containing components necessary for the survival and proliferation of mesenchymal stem cells can be used.
- DMEM Denbecco Modified Eagle Medium
- RPMI medium GIBCO (registered trademark) RPMI1640 medium, etc.
- RoosterNourish medium, RoosterBio RoosterNourish medium, RoosterBio
- Culture conditions can be set appropriately.
- the culture temperature is not particularly limited, but can be about 30 to 40°C, preferably about 37°C.
- the CO2 concentration can be about 1 to 10%, preferably about 2 to 5%.
- the oxygen concentration can be 1 to 20%, preferably 1 to 10%.
- the positive rate of microcarriers can be increased, and the number of recovered viable cells can also be increased.
- the number of viable cells recovered can be determined as follows. After culturing, the bioreactor is recovered, a 100 ⁇ m cell strainer is placed in the centrifuge tube, and the entire contents of the bioreactor are filtered. The cells and microcarriers remaining on the cell strainer are washed twice with DPBS, and then the cells and microcarriers on the cell strainer are recovered using TrypLE Select Enzyme (Gibco) and returned to the bioreactor. The bioreactor is stirred at 300 rpm for 30 minutes at 37°C. The bioreactor is recovered, and the entire contents of the bioreactor are filtered into a centrifuge tube equipped with a 100 ⁇ m cell strainer.
- the bioreactor and the carriers on the cell strainer are washed together with Rooster Nourish medium.
- the centrifuge tube is centrifuged, the supernatant is removed, and then Rooster Nourish medium is added and suspended.
- the suspension is mixed with AO/PI Cell Viability Kit at a ratio of 9:1, and the number of cells is counted using LUNA (Logos Biosystems).
- the method of the present invention preferably produces mesenchymal stem cells for use as a therapeutic agent. That is, mesenchymal stem cells produced by the method of the present invention can be suitably used for medical purposes such as cell therapy.
- Mesenchymal stem cells produced by the method of the present invention can be used undifferentiated or after differentiation into osteocytes, chondrocytes, adipocytes, or the like, depending on the target disease.
- Target diseases include, for example, joint diseases, avascular necrosis of the lunate bone, avascular necrosis of the femoral head, osteochondritis dissecans, lumbar disc herniation, ischemic heart disease, epidermolysis bullosa, and the like.
- Joint diseases include, for example, meniscus injury, traumatic cartilage injury, osteochondritis dissecans, avascular necrosis of osteonecrosis, osteoarthritis (e.g., knee osteoarthritis), rheumatoid arthritis (e.g., rheumatoid arthritis), gout, reactive arthritis, psoriatic arthritis, juvenile arthritis, inflammatory arthritis, and articular cartilage defect.
- Mesenchymal stem cells can also be differentiated into adipocytes and then used for cosmetic surgery.
- the cells can be prepared into a formulation suitable for administration to an individual by, for example, mixing them with a pharmaceutically acceptable carrier using standard methods.
- a pharmaceutically acceptable carrier include isotonic distilled water for injection made with physiological saline, glucose, or other adjuvants (e.g., D-sorbitol, D-mannitol, sodium chloride, etc.).
- buffers e.g., phosphate buffer, sodium acetate buffer
- soothing agents e.g., benzalkonium chloride, procaine hydrochloride, etc.
- stabilizers e.g., human serum albumin, polyethylene glycol, etc.
- preservatives, antioxidants, etc. may also be added.
- Example 1 Production under one set of conditions: "119 minutes of stirring, 1 minute of static culture” in the stirring static culture process (1) Obtaining synovial stem cells Human clinical synovial tissue was placed on a dish and shredded with scissors. The shredded tissue was transferred to a centrifuge tube containing a mixed solution (1 mg/mL) of Liberase (Roche) and n-Liven PR (Sexton Biotechnologies) and subjected to enzyme treatment at 37°C for approximately 3 hours using a rotating mixer. After enzyme treatment, ⁇ MEM (prepared in-house, JP 2021-040551) was added to the tube, and the tissue was dispersed by pipetting.
- ⁇ MEM prepared in-house, JP 2021-040551
- the tissue was then passed through a 70 ⁇ m cell strainer placed in a 50 mL centrifuge tube and centrifuged. After removing the supernatant, the pellet was broken up, ⁇ MEM was added, and the mixture was centrifuged. This process was repeated once.
- the cells were suspended in ⁇ MEM, and the suspension was mixed with AO/PI Cell Viability Kit (Logos Biosystems) at a ratio of 9:1, and the number of cells was counted using LUNA (Logos Biosystems).
- the cells were seeded in a flask at a density of 1000 cells/ cm2 and cultured for 3 to 5 days in a culture medium (hereinafter referred to as ⁇ MEM medium) prepared by mixing ⁇ MEM with n-Liven PR, amphotericin B (ThemoFisher Scientific), and gentamicin (ThemoFisher Scientific). After that, the medium was changed to RoosterNourish TM -MSC-XF medium (hereinafter referred to as RoosterNourish medium, RoosterBio) and cultured until the cells reached 70 to 80% confluence. The supernatant was removed from the flask, and the cells were washed twice with DPBS (ThemoFisher Scientific).
- ⁇ MEM medium a culture medium prepared by mixing ⁇ MEM with n-Liven PR, amphotericin B (ThemoFisher Scientific), and gentamicin (ThemoFisher Scientific).
- ⁇ MEM medium a culture
- TrypLE Select Enzyme (ThemoFisher Scientific) was added and the mixture was left to stand at 37°C for 10 to 30 minutes. An equal volume of ⁇ MEM medium was added, and the cell suspension was transferred to a centrifuge tube and centrifuged. The supernatant was removed, and the cells were suspended in ⁇ MEM medium. After mixing with AO/PI Cell Viability Kit at a ratio of 9:1, the cells were counted using LUNA. The suspension containing the specified number of cells was transferred to a new centrifuge tube and centrifuged. The supernatant was removed, and the cells were frozen using a DMSO-containing cryopreservation solution (P0: passage 0).
- P0 DMSO-containing cryopreservation solution
- P0 frozen cells were thawed in a water bath, added to a centrifuge tube containing Rooster Nourish medium, and centrifuged. The supernatant was removed, and the cells were suspended in Rooster Nourish medium. After mixing with AO/PI Cell Viability Kit at a ratio of 9:1, the number of cells was counted using LUNA. The cells were seeded into flasks at a density of 1,000-3,000 cells/ cm2 and cultured until 70-80% confluent. The supernatant was removed from the flask, washed with DPBS, and then TrypLE Select Enzyme was added. The mixture was allowed to stand at 37°C for approximately 5 minutes.
- Rooster Nourish medium An equal volume of Rooster Nourish medium was added, and the cell suspension was transferred to a centrifuge tube and centrifuged. The supernatant was removed, and the cells were suspended in Rooster Nourish medium. After mixing with AO/PI Cell Viability Kit at a ratio of 9:1, the number of cells was counted using LUNA. The suspension containing the desired number of cells was transferred to a new centrifuge tube and centrifuged. The supernatant was removed and frozen using a DMSO-containing freezing medium (P1: passage 1).
- P1 DMSO-containing freezing medium
- Rooster Nourish medium was added to 50 mL centrifuge tubes so that 2 mL x the required number of tubes was added, and then 2 mL/tube was added to the Ambr15 bioreactor.
- the microcarrier concentration was 0.14 g/4 mL.
- the frozen cells (P1) from (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL). The same procedure was repeated twice on separate days.
- the medium exchange was performed at the same time as the static culture step of the stirring and static culture step, and the culture was allowed to stand for about 5 minutes, allowing the carriers and cells to settle, and 5 mL of culture supernatant was withdrawn. Then, Rooster Nourish medium was added at the same time as the stirring and static culture step.
- the Ambr15 bioreactor was recovered.
- a 100 ⁇ m cell strainer was placed in a 50 mL centrifuge tube, and the entire contents of the Ambr15 bioreactor were filtered.
- the cells and microcarriers remaining on the cell strainer were washed twice with DPBS, and then the cells and microcarriers on the cell strainer were recovered using TrypLE Select Enzyme (Gibco) and returned to the Ambr15 bioreactor.
- the Ambr15 bioreactor was placed in the Ambr15 and stirred at 300 rpm for 30 minutes at 37 °C.
- the Ambr15 bioreactor was recovered, and the entire contents of the Ambr15 bioreactor were filtered into a 50 mL centrifuge tube containing a 100 ⁇ m cell strainer.
- the Ambr15 bioreactor and the carrier on the cell strainer were washed together with Rooster Nourish medium.
- the 50 mL centrifuge tube was centrifuged, the supernatant was removed, and Rooster Nourish medium was added to suspend the cells.
- the suspension was mixed with AO/PI Cell Viability Kit at a ratio of 9:1, and the cell number was counted using LUNA (Logos Biosystems).
- the cells were frozen using CP-1 High Grade (Kyokuto Pharmaceutical Industries Co., Ltd.) as needed.
- Example 2 Production under the condition of "225 minutes of stirring and 15 minutes of static culture” as one set in the stirring and static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- the frozen cells (P1) in (1) were thawed and prepared in Rooster Nourish medium at 15 x 10 cells/mL for seeding at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
- Example 3 Production under the condition of "5 minutes of stirring and 25 minutes of static culture” as one set in the stirring and static culture process (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 1.
- Example 4 Production under the condition of "95 minutes of stirring and 25 minutes of static culture” as one set in the stirring and static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
- the frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm .
- 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL). The same procedure was repeated four times on different days.
- Example 5 Production under one set of conditions in the stirring and static culture process: "215 minutes of stirring, 25 minutes of static culture” (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 1.
- Example 6 Production under the condition of "1415 minutes of stirring and 25 minutes of static culture" as one set in the stirring and static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
- the frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm .
- 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL). The same procedure was repeated once on another day.
- Example 7 Production under conditions where one set of "60 minutes of stirring, 60 minutes of standing" was used in the static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
- the frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm .
- 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL). The same procedure was repeated once on another day.
- Example 8 Production under one set of conditions in the static culture process: "180 minutes of stirring, 60 minutes of static culture” (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
- the frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
- Example 9 Production under conditions where one set of "120 minutes of stirring, 120 minutes of standing" was used in the static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
- the frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
- Comparative Example 1 Production under the condition of "stirring only, no standing" (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 1.
- Example 10 Production under the conditions of "5 minutes of stirring and 1435 minutes of static culture” as one set in the stirring static culture process. (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
- Example 10 Seeding of synovial mesenchymal stem cells The amount to be used in Example 10 and Comparative Example 2 was prepared together.
- the microcarrier solution prepared in (2) was thoroughly suspended and then 280 mL was transferred to a 500 mL storage bottle. After allowing the microcarriers to settle for approximately 10 minutes, the supernatant DPBS was removed and 200 mL of Rooster Nourish medium (RoosterBio) was added. The microcarriers were thoroughly suspended and divided equally among four suspension cell culture flasks 225 (Sumitomo Bakelite). 32 mL of Rooster Nourish medium was added to the 500 mL storage bottle and divided equally among the four suspension cell culture flasks.
- the frozen cells (P1) in (1) were thawed and adjusted to 0.5 x 10 cells/2 mL with Rooster Nourish medium to seed at a density of 2 x 10 cells/ cm . 2 mL of this cell suspension was added to the previously prepared suspension cell culture flasks (microcarrier concentration per suspension cell culture flask: 7 g/60 mL).
- the 50 mL centrifuge tube 1 was collected, and the entire contents of the 50 mL centrifuge tube 1 were filtered into a new 50 mL centrifuge tube (2) equipped with a 100 ⁇ m cell strainer.
- the 50 mL centrifuge tube 1 and the carrier on the cell strainer were washed together with Rooster Nourish medium.
- the 50 mL centrifuge tube (2) was centrifuged, the supernatant was removed, and Rooster Nourish medium was added to suspend the cells.
- the suspension was filled into a dedicated cassette, and the cell number was counted using a NucleoCounter NC-202 (MSESS Techno Systems).
- the cells were frozen using CTS TM Synth-a-Freeze TM Medium (Gibco) as needed. When cultured under one set of conditions of "agitation for 5 minutes and standing for 1435 minutes," the number of viable cells recovered was 2.01 x 10 6 cells.
- the 2L container On the 9th day of culture, the 2L container was collected. The 2L container was left to stand for approximately 10 minutes to allow the carriers and cells to settle, after which the culture supernatant was removed and the cells + microcarriers were washed once with DPBS. The carriers and cells were allowed to settle, the DPBS was removed, a detachment agent was added, the cells were detached, and the cell number was counted (cell count 2).
- Comparative Example 2 Production under the condition of "stirring only, no standing" (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 10.
- Example 10 As in Example 10, on the 9th day of culture, the 2 L container was harvested. When the cells 1 and 2 were cultured together under "stirring only, no standing", the number of viable cells recovered was 4.21 x 10 8 cells.
- ⁇ Evaluation of cartilage differentiation> The frozen cells from Examples 4 and 6 were thawed in a water bath and transferred to a centrifuge tube containing a culture medium (non-differentiation medium) prepared by mixing ⁇ MEM with 20% FBS (ThemoFisher Scientific) and 1% Antibiotic-Antimycotic (x100) (ThemoFisher Scientific). After centrifugation, the cells were suspended in non-differentiation medium and mixed with AO/PI Cell Viability Kit at a ratio of 9:1. The cell number was counted using LUNA. The suspension was dispensed into two 1.5 mL centrifuge tubes at 2.5 x 10 cells each and centrifuged.
- a culture medium non-differentiation medium
- FBS ThemoFisher Scientific
- x100 Antibiotic-Antimycotic
- one 1.5 mL centrifuge tube was filled with 1 mL of chondrogenic differentiation medium (DMEM high glucose (ThemoFisher Scientific), 10 ng/mL TGF- ⁇ 3 (Fujifilm Wako Pure Chemical Industries), 3.92 ⁇ g/mL Dexamethasone (Fujifilm Wako Pure Chemical Industries), 50 ⁇ g/mL L-Asorbic Acid 2-Phosphate (Cayman Chemical), 40 ⁇ g/mL L-Proline (MP Biomedicals), 1 mmol/L Sodium Pyruvate (Invitrogen), 100-fold diluted ITS-X supplement (x100) (Fujifilm Wako Pure Chemical Industries), 500 ng/mL To one tube, 1 mL of a BMP-2 (R&D Systems) mixed solution was added, and 1 mL of non-differentiation medium was added to the other.
- DMEM high glucose ThemoFisher Scientific
- 10 ng/mL TGF- ⁇ 3
- spheroid was removed from the 1.5 mL centrifuge tube using a microspatula and transferred to a 1.5 mL tube containing DPBS. The spheroid was removed, placed on a dish, and weighed using an analytical balance (A&D). A microscope microruler (Kennis) was placed near the spheroid, and images were taken with a compact digital camera (OLYMPUS). The major axis was measured from the captured images.
- Example 4 95 minutes of stirring, 25 minutes of standing
- Example 6 1415 minutes of stirring, 25 minutes of standing
- the differentiated specimens were larger in both weight and major axis than the undifferentiated specimens, and had differentiated into a cartilage-like structure.
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Abstract
Description
本発明は、マイクロキャリアの存在下において間葉系幹細胞を培養することを含む、間葉系幹細胞の製造方法であって、間葉系幹細胞を攪拌させる工程と、その後に間葉系幹細胞を静置させる工程とを含む攪拌静置培養工程を含む方法に関する。 The present invention relates to a method for producing mesenchymal stem cells, which comprises culturing mesenchymal stem cells in the presence of microcarriers, and which includes an agitated static culture step that includes a step of agitating the mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand still.
近年、再生医療技術および細胞治療技術の進歩により、自家、同種または異種の細胞を用いた各種の細胞治療や研究用細胞製品開発が盛んに実施されている。中でも間葉系幹細胞(mesenchymal stem cell:MSC)は、有用な細胞治療の細胞源として期待されている。間葉系幹細胞は種々の体組織から採取が可能であり、骨髄、滑膜、骨膜、脂肪、筋肉、歯髄、胎盤、臍帯などから単離できることが報告されている。 In recent years, advances in regenerative medicine and cell therapy technologies have led to the active development of various cell therapies and research cell products using autologous, allogeneic, or xenogeneic cells. Among these, mesenchymal stem cells (MSCs) are expected to be a useful cell source for cell therapy. Mesenchymal stem cells can be harvested from a variety of body tissues, and it has been reported that they can be isolated from bone marrow, synovium, periosteum, fat, muscle, dental pulp, placenta, umbilical cord, and other tissues.
特許文献1には、接着細胞、マイクロキャリア、および培地を含有する細胞懸濁液中で、上記接着細胞を培養することが記載されており、培養は細胞懸濁液を間欠撹拌することを含んでいてもよいことが記載されている。 Patent Document 1 describes culturing adherent cells in a cell suspension containing the adherent cells, microcarriers, and a medium, and describes that the culturing may include intermittent stirring of the cell suspension.
特許文献2には、溶解性基質から培養細胞を採取する方法であって、溶解性基質を、キレート化剤、酵素またはその両方に曝露することによって消化することによって、上記基質から培養細胞を分離することを含む方法が記載されている。特許文献2においては、間葉系幹細胞を溶解性基質に接着させる工程において間欠攪拌した後に連続攪拌することによって、間葉系幹細胞を増殖させている。 Patent Document 2 describes a method for harvesting cultured cells from a soluble substrate, which comprises separating the cultured cells from the substrate by digesting the soluble substrate by exposing it to a chelating agent, an enzyme, or both. In Patent Document 2, mesenchymal stem cells are grown by intermittent stirring followed by continuous stirring in the step of adhering the mesenchymal stem cells to the soluble substrate.
特許文献3においては、マイクロキャリアを用いて細胞培養することが記載されている。特許文献3においては、MSCを連続攪拌しながらマイクロキャリアに接着させて増殖させることが記載されている。 Patent Document 3 describes cell culture using microcarriers. Patent Document 3 also describes the attachment and proliferation of MSCs to microcarriers while continuously stirring them.
攪拌培養技術は、CHO細胞(チャイニーズハムスター卵巣細胞)によるバイオ医薬品製造や、Vero細胞によるワクチン製造などで用いられてきた。しかし、これらは細胞自体が最終製品ではなく、細胞が分泌するタンパク質等が最終製品である。一方、細胞自体が最終製品となる間葉系幹細胞による細胞治療製品の製造において攪拌培養技術を用いた場合、細胞が接着しないマイクロキャリアが散在することで、マイクロキャリアが十分に活用できないという問題点が見出された。また、それにともない、細胞の回収率が低いという問題点が見出された。 Agitated culture technology has been used in the production of biopharmaceuticals using CHO cells (Chinese hamster ovary cells) and vaccines using Vero cells. However, in these cases, the cells themselves are not the final product, but rather the proteins secreted by the cells. On the other hand, when agitated culture technology is used to produce cell therapy products using mesenchymal stem cells, where the cells themselves are the final product, a problem has been discovered in that microcarriers to which cells do not adhere are scattered, preventing full use of the microcarriers. This has also led to the problem of low cell recovery rates.
本発明の課題は、空のマイクロキャリア(細胞が接着しないマイクロキャリア)を減らし、その結果として培養による回収細胞数を向上させることが可能な間葉系幹細胞の製造方法を提供することである。 The objective of the present invention is to provide a method for producing mesenchymal stem cells that can reduce empty microcarriers (microcarriers to which cells do not adhere), thereby increasing the number of cells recovered through culture.
本発明者は上記課題を解決するために鋭意検討した結果、マイクロキャリアの存在下において間葉系幹細胞を培養することを含む、間葉系幹細胞の製造方法において、間葉系幹細胞を攪拌させる工程と、その後に間葉系幹細胞を静置させる工程とを含む攪拌静置培養工程を48時間以上行い、48時間以上の培養期間中に上記攪拌静置培養工程を2回以上行うことを含み、培養開始後24時間以降に、48時間毎に1回以上の攪拌静置培養工程を行うことによって、空のマイクロキャリアを減らし、回収細胞数を向上させることができることを見出した。本発明は上記の知見に基づいて完成したものである。 As a result of extensive research by the present inventors to solve the above-mentioned problems, they have found that in a method for producing mesenchymal stem cells, which includes culturing mesenchymal stem cells in the presence of microcarriers, an agitation and static culture step, which includes a step of agitating the mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand, is carried out for 48 hours or more, and the agitation and static culture step is carried out two or more times during the 48-hour or more culture period, and that starting 24 hours after the start of culture, the agitation and static culture step is carried out at least once every 48 hours, thereby reducing empty microcarriers and improving the number of recovered cells. The present invention was completed based on the above findings.
即ち、本発明によれば、以下の発明が提供される。
<1> マイクロキャリアの存在下において間葉系幹細胞を培養することを含む、間葉系幹細胞の製造方法であって、間葉系幹細胞を攪拌させる工程と、その後に間葉系幹細胞を静置させる工程とを含む攪拌静置培養工程を、48時間以上行うことを含み、48時間以上の培養期間中に上記攪拌静置培養工程を2回以上行うことを含み、培養開始後24時間以降に、48時間毎に1回以上の攪拌静置培養工程を行うことを含む、方法。
<2> 上記2回以上の攪拌静置培養工程における各々の攪拌静置培養工程が同一の工程であるか、または上記2回以上の攪拌静置培養工程が、攪拌させる工程の時間と静置させる工程の時間のいずれか一以上が異なる攪拌静置培養工程を含む、<1>に記載の間葉系幹細胞の製造方法。
<3> 上記攪拌静置培養工程が、培養開始から培養終了まで行われる、<1>または<2>に記載の間葉系幹細胞の製造方法。
<4> 上記間葉系幹細胞が、ヒト由来である、<1>から<3>の何れか一に記載の間葉系幹細胞の製造方法。
<5> 上記間葉系幹細胞が、人工多能性幹細胞、骨髄、脂肪、歯髄、臍帯、胎盤または滑膜由来である、<4>に記載の間葉系幹細胞の製造方法。
<6> 上記間葉系幹細胞が滑膜由来である、<5>に記載の間葉系幹細胞の製造方法。
<7> 上記攪拌静置培養工程における間葉系幹細胞を静置させる工程の時間が1分以上2400分以下である、<1>から<6>の何れか一に記載の間葉系幹細胞の製造方法。
<8> 上記攪拌静置培養工程における間葉系幹細胞を静置させる工程の時間が、培養液量あたり0.1分/mL以上240.0分/mL以下である、<1>から<7>の何れか一に記載の間葉系幹細胞の製造方法。
<9> 上記攪拌静置培養工程における間葉系幹細胞を攪拌させる工程の時間が、1分以上2000分以下である、<1>から<8>の何れか一に記載の間葉系幹細胞の製造方法。
<10> 上記攪拌静置培養工程における間葉系幹細胞を攪拌させる工程の時間が、培養液量あたり0.1分/mL以上200.0分/mL以下である、<1>から<9>の何れか一に記載の間葉系幹細胞の製造方法。
<11> 上記攪拌静置培養工程を24時間当たり1回~48回行う、<1>から<10>の何れか一に記載の間葉系幹細胞の製造方法。
<12> 上記攪拌静置培養工程の1回の時間が、30分~1440分である、<1>から<11>の何れか一に記載の間葉系幹細胞の製造方法。
<13> 上記攪拌静置培養工程における間葉系幹細胞を攪拌させる工程と、間葉系幹細胞を静置させる工程との時間の比率が1:0.005~1:700の範囲内である、<1>から<12>の何れか一に記載の間葉系幹細胞の製造方法。
<14> 全培養期間における攪拌させる工程の時間の総和が静置させる工程の時間の総和よりも長い、<1>から<13>の何れか一に記載の間葉系幹細胞の製造方法。
<15> 上記攪拌静置培養工程においてマイクロキャリアを追加しない、<1>から<14>の何れか一に記載の間葉系幹細胞の製造方法。
<16> 培養開始後24時間以降に攪拌静置培養を48時間以上行い、その後連続的に攪拌培養を行う、<1>から<15>の何れか一に記載の間葉系幹細胞の製造方法。
<17> 培養開始後24時間以降に攪拌静置培養工程を行い、培養終了2日以上前から連続的に攪拌培養を行う、<1>から<16>の何れか一に記載の間葉系幹細胞の製造方法。
<18> 攪拌静置培養工程と、連続的に攪拌させる工程との時間の比率が、1:0.3~1:5.5である、<1>から<17>の何れか一に記載の間葉系幹細胞の製造方法。
<19> 間葉系幹細胞を静置させる工程(A)と、攪拌静置させる工程(B)と、連続的に攪拌させる工程(C)との時間の比率が、A=1のとき、B=2~6、C=2~11である、<1>から<18>の何れか一に記載の間葉系幹細胞の製造方法。
<20> 治療剤として使用するための間葉系幹細胞が製造される、<1>から<19>の何れか一に記載の方法。
That is, according to the present invention, the following inventions are provided.
<1> A method for producing mesenchymal stem cells, comprising culturing mesenchymal stem cells in the presence of microcarriers, the method comprising carrying out an agitation static culture step, for 48 hours or more, which step includes a step of agitating the mesenchymal stem cells and a step of allowing the mesenchymal stem cells to stand thereafter, and carrying out the agitation static culture step two or more times during the 48-hour or longer culture period, and carrying out the agitation static culture step one or more times every 48 hours starting 24 hours after the start of culture.
<2> The method for producing mesenchymal stem cells according to <1>, wherein each of the two or more stirring and static culture steps is the same step, or the two or more stirring and static culture steps include a stirring and static culture step in which either one or more of the duration of the stirring step and the duration of the static culture step are different.
<3> The method for producing mesenchymal stem cells according to <1> or <2>, wherein the stirring and static culture step is carried out from the start of culture to the end of culture.
<4> The method for producing mesenchymal stem cells according to any one of <1> to <3>, wherein the mesenchymal stem cells are derived from a human.
<5> The method for producing mesenchymal stem cells according to <4>, wherein the mesenchymal stem cells are derived from induced pluripotent stem cells, bone marrow, fat, dental pulp, umbilical cord, placenta, or synovium.
<6> The method for producing mesenchymal stem cells according to <5>, wherein the mesenchymal stem cells are derived from synovial membrane.
<7> The method for producing mesenchymal stem cells according to any one of <1> to <6>, wherein the time for the step of leaving the mesenchymal stem cells stationary in the stirring static culture step is 1 minute or more and 2,400 minutes or less.
<8> The method for producing mesenchymal stem cells according to any one of <1> to <7>, wherein the time for the step of leaving the mesenchymal stem cells standing in the stirring static culture step is 0.1 min/mL or more and 240.0 min/mL or less per volume of culture solution.
<9> The method for producing mesenchymal stem cells according to any one of <1> to <8>, wherein the time for the step of stirring the mesenchymal stem cells in the stirring static culture step is 1 minute or more and 2000 minutes or less.
<10> The method for producing mesenchymal stem cells according to any one of <1> to <9>, wherein the time for the step of stirring the mesenchymal stem cells in the stirring static culture step is 0.1 min/mL or more and 200.0 min/mL or less per volume of culture solution.
<11> The method for producing mesenchymal stem cells according to any one of <1> to <10>, wherein the stirring and static culture step is carried out 1 to 48 times per 24 hours.
<12> The method for producing mesenchymal stem cells according to any one of <1> to <11>, wherein the duration of each stirring and static culture step is 30 minutes to 1,440 minutes.
<13> The method for producing mesenchymal stem cells according to any one of <1> to <12>, wherein the ratio of the time taken for the step of stirring the mesenchymal stem cells to the time taken for the step of allowing the mesenchymal stem cells to stand in the stirring static culture step is within the range of 1:0.005 to 1:700.
<14> The method for producing mesenchymal stem cells according to any one of <1> to <13>, wherein the total time of the stirring step during the entire culture period is longer than the total time of the standing step.
<15> The method for producing mesenchymal stem cells according to any one of <1> to <14>, wherein no microcarriers are added in the stirring static culture step.
<16> The method for producing mesenchymal stem cells according to any one of <1> to <15>, wherein the stirring static culture is carried out for 48 hours or more after 24 hours from the start of the culture, and then the stirring culture is carried out continuously.
<17> The method for producing mesenchymal stem cells according to any one of <1> to <16>, wherein the stirring static culture step is carried out 24 hours or more after the start of culture, and stirring culture is carried out continuously from at least two days before the end of culture.
<18> The method for producing mesenchymal stem cells according to any one of <1> to <17>, wherein the ratio of the time of the stirring static culture step to the time of the continuous stirring step is 1:0.3 to 1:5.5.
<19> The method for producing mesenchymal stem cells according to any one of <1> to <18>, wherein the time ratios of the step (A) of leaving the mesenchymal stem cells to stand, the step (B) of stirring and leaving the mesenchymal stem cells to stand, and the step (C) of continuously stirring the mesenchymal stem cells are such that, when A=1, B=2 to 6, and C=2 to 11.
<20> The method according to any one of <1> to <19>, wherein mesenchymal stem cells are produced for use as a therapeutic agent.
本発明の間葉系幹細胞の製造方法によれば、空キャリアへの細胞の接着を促し、回収時の生細胞数を向上させることができる。 The method for producing mesenchymal stem cells of the present invention promotes cell adhesion to empty carriers, thereby increasing the number of viable cells at the time of collection.
以下において、本発明の内容について詳細に説明する。なお、本明細書において「~」とはその前後に記載される数値を下限値および上限値として含む意味で使用される。 The present invention will be described in detail below. Note that in this specification, the word "to" is used to mean that the numerical values before and after it are both upper and lower limits.
本発明は、マイクロキャリアの存在下において間葉系幹細胞を培養することを含む、間葉系幹細胞の製造方法であって、間葉系幹細胞を攪拌させる工程と、その後に間葉系幹細胞を静置させる工程とを含む攪拌静置培養工程を、48時間以上行うことを含み、48時間以上の培養期間中に上記攪拌静置培養工程を2回以上行うことを含み、培養開始後24時間以降に、48時間毎に1回以上の攪拌静置培養工程を行うことを含む、方法に関するものである。 The present invention relates to a method for producing mesenchymal stem cells, which comprises culturing mesenchymal stem cells in the presence of microcarriers, and which comprises carrying out an agitation-static culture step, which includes a step of agitating the mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand, for 48 hours or more, and which comprises carrying out the agitation-static culture step two or more times during the 48-hour or more culture period, and which comprises carrying out the agitation-static culture step one or more times every 48 hours starting 24 hours after the start of culture.
本発明によれば、空のマイクロキャリア(細胞が接着しないマイクロキャリア)を減らし、培養による回収細胞数を向上させることができる。さらに、本発明においては間葉系幹細胞の分化能を担保することができることから、間葉系幹細胞は治療剤として有用である。本発明によれば、細胞治療用の細胞を簡便に大量に製造することができる。また本発明によれば、投入したマイクロキャリアを効率的に使用できることで、最小限のマイクロキャリアでの培養が可能となり低コストでの培養が可能となる。本発明による間葉系幹細胞の製造方法は、他家細胞治療製品など大量の細胞が必要となる産業に利用可能である。 According to the present invention, empty microcarriers (microcarriers to which cells do not adhere) can be reduced, and the number of cells recovered from culture can be increased. Furthermore, since the present invention can ensure the differentiation ability of mesenchymal stem cells, mesenchymal stem cells are useful as therapeutic agents. According to the present invention, cells for cell therapy can be easily produced in large quantities. Furthermore, according to the present invention, the input microcarriers can be used efficiently, making it possible to culture using a minimum number of microcarriers and culturing at low cost. The method for producing mesenchymal stem cells according to the present invention can be used in industries that require large quantities of cells, such as allogeneic cell therapy products.
<間葉系幹細胞>
幹細胞とは、自己複製能および分化増殖能を有する未熟な細胞をいい、分化能力に応じて、多能性幹細胞(pluripotent stem cell)、複能性幹細胞(multipotent stem cell)、単能性幹細胞(unipotent stem cell)等が含まれる。幹細胞は、一般に、未分化状態を保持したまま増殖できる「自己再生能」と、三胚葉系列すべてに分化できる「分化多能性」とを有する未分化細胞と定義されている。多能性幹細胞とは、生体を構成する全ての組織や細胞へ分化し得る能力を有する細胞を意味する。複能性幹細胞とは、全ての種類ではないが、複数種の組織や細胞へ分化し得る能力を有する細胞を意味する。単能性幹細胞とは、特定の組織や細胞へ分化し得る能力を有する細胞を意味する。
<Mesenchymal stem cells>
Stem cells refer to immature cells that have the ability to self-renew and differentiate and proliferate, and include pluripotent stem cells, multipotent stem cells, unipotent stem cells, etc., depending on their differentiation potential. Stem cells are generally defined as undifferentiated cells that have the "self-renewal ability" to proliferate while maintaining an undifferentiated state, and the "pluripotency" to differentiate into all three germ layer lineages. Pluripotent stem cells refer to cells that have the ability to differentiate into all tissues and cells that make up a living organism. Multipotent stem cells refer to cells that have the ability to differentiate into multiple types of tissues and cells, but not all types. Unipotent stem cells refer to cells that have the ability to differentiate into specific tissues or cells.
間葉系幹細胞とは、骨芽細胞、軟骨芽細胞、脂肪芽細胞および筋細胞等の間葉系の細胞の全てまたはそのうちの一部の細胞への分化が可能な幹細胞またはその前駆細胞の集団を広義に意味する。間葉系幹細胞は、間質細胞とも称する。 Mesenchymal stem cells broadly refer to a population of stem cells or their precursor cells that can differentiate into all or some of the mesenchymal cells, such as osteoblasts, chondroblasts, adipblasts, and muscle cells. Mesenchymal stem cells are also called stromal cells.
間葉系幹細胞の由来は特に限定されず、例えば、ラット、マウス、ハムスター、モルモット等のげっ歯類、ウサギ等のウサギ目、ブタ、ウシ、ヤギ、ヒツジ等の有蹄目、イヌ、ネコ等のネコ目、ヒト、サル、アカゲザル、マーモセット、オランウータン、チンパンジーなどの霊長類などの細胞であってもよい。 間葉系幹細胞は、ヒト由来であることが好ましい。 The origin of the mesenchymal stem cells is not particularly limited, and may be cells from, for example, rodents such as rats, mice, hamsters, and guinea pigs; lagomorphs such as rabbits; ungulates such as pigs, cows, goats, and sheep; Carnivores such as dogs and cats; and primates such as humans, monkeys, rhesus monkeys, marmosets, orangutans, and chimpanzees. It is preferable that the mesenchymal stem cells are derived from humans.
間葉系幹細胞は、好ましくは、人工多能性幹細胞、骨髄、脂肪、歯髄、臍帯、胎盤または滑膜由来である。間葉系幹細胞は、特に好ましくは滑膜由来である。 Mesenchymal stem cells are preferably derived from induced pluripotent stem cells, bone marrow, fat, dental pulp, umbilical cord, placenta, or synovial membrane. Mesenchymal stem cells are particularly preferably derived from synovial membrane.
間葉系幹細胞を治療剤として使用する場合には、投与する患者の自家細胞でもよいし、他家細胞でもよい。 When mesenchymal stem cells are used as a therapeutic agent, they may be autologous cells of the patient to be administered, or allogeneic cells.
間葉系幹細胞は、間葉系幹細胞に特徴的な分子、例えば酵素、レセプター、低分子化合物等を検出して確認することができる。間葉系幹細胞に特徴的な分子としては、細胞表面マーカー(ポジティブマーカー)であるCD73、CD90、CD105、CD166、等が挙げられるが、これらに限定されるものではない。また、間葉系幹細胞においては発現していないネガティブマーカーとしては、CD19、CD34、CD45、HLA-DR、CD11b、CD14等が挙げられるが、これらに限定されるものではない。なお、CDは、Clusters of differentiationの略であり、HLA-DRは、human leukocyte antigen-D-relatedの略である。これらのポジティブマーカーおよびネガティブマーカーを利用して、間葉系幹細胞であることを確認することができる。これらのマーカーの検出には免疫学的方法を利用できるが、各分子のmRNA量の定量により検出を実施してもよい。 Mesenchymal stem cells can be identified by detecting molecules characteristic of mesenchymal stem cells, such as enzymes, receptors, and low-molecular-weight compounds. Molecules characteristic of mesenchymal stem cells include, but are not limited to, cell surface markers (positive markers), such as CD73, CD90, CD105, and CD166. Negative markers not expressed in mesenchymal stem cells include, but are not limited to, CD19, CD34, CD45, HLA-DR, CD11b, and CD14. CD stands for Clusters of Differentiation, and HLA-DR stands for Human Leukocyte Antigen-D-Related. These positive and negative markers can be used to confirm that the cells are mesenchymal stem cells. Immunological methods can be used to detect these markers, but detection can also be performed by quantifying the amount of mRNA for each molecule.
本発明の一例においては、間葉系幹細胞として、滑膜由来間葉系幹細胞を使用することができる。滑膜由来間葉系幹細胞(滑膜幹細胞とも言う)とは、滑膜に含まれる幹細胞である。滑膜由来間葉系幹細胞は、例えば、CD90陽性、CD45陰性、軟骨分化能を検出することにより検出することができるが、検出方法は特に限定されない。 In one example of the present invention, synovial membrane-derived mesenchymal stem cells can be used as mesenchymal stem cells. Synovial membrane-derived mesenchymal stem cells (also called synovial stem cells) are stem cells contained in the synovial membrane. Synovial membrane-derived mesenchymal stem cells can be detected, for example, by detecting CD90 positivity, CD45 negativity, and chondrogenic differentiation ability, but the detection method is not particularly limited.
滑膜由来間葉系幹細胞は、例えば、滑膜組織を酵素で処理する工程Aと、酵素処理後の混合物を洗浄した後の混合物に含まれる滑膜由来間葉系幹細胞を培養培地にて培養する工程Bと、培養後の滑膜由来間葉系幹細胞を凍結保存する工程Cとを含む方法により得ることができる。 Synovium-derived mesenchymal stem cells can be obtained, for example, by a method comprising step A of treating synovial tissue with an enzyme, step B of washing the mixture after enzyme treatment and culturing the synovium-derived mesenchymal stem cells contained in the mixture in a culture medium, and step C of cryopreserving the cultured synovium-derived mesenchymal stem cells.
(滑膜組織を酵素で処理する工程A)
滑膜組織は、関節鏡視下手術にて採取することができる。採取した滑膜組織は酵素で処理する。
(Step A: Treating synovial tissue with enzyme)
Synovial tissue can be harvested during arthroscopic surgery and then treated with enzymes.
酵素としては、プロテアーゼを含む酵素であれば特に限定されないが、好ましくは、1種以上のコラゲナーゼと1種以上の中性プロテアーゼを含む混合酵素である。特に好ましい酵素は、リベラーゼ(登録商標)である。リベラーゼ(登録商標)としては、例えば、リベラーゼMNP-S(ロシュ製)を使用することができるが、これはコラゲナーゼクラスIとコラゲナーゼクラスIIと中性プロテアーゼ(サーモシリン)とを含む酵素である。酵素反応は、酵素を含む水溶液中で行うことができる。 The enzyme is not particularly limited as long as it contains a protease, but is preferably a mixed enzyme containing one or more types of collagenase and one or more types of neutral protease. A particularly preferred enzyme is Liberase (registered trademark). For example, Liberase MNP-S (manufactured by Roche) can be used as Liberase (registered trademark), which is an enzyme containing collagenase class I, collagenase class II, and a neutral protease (thermocillin). The enzyme reaction can be carried out in an aqueous solution containing the enzyme.
酵素反応は、好ましくは15℃から40℃、より好ましくは20℃から40℃、さらに好ましくは25℃から40℃の温度で行うことができる。
反応時間は、10分以上であればよく、好ましくは30分以上であり、より好ましくは1時間以上であり、さらに好ましくは1.5時間以上であり、2時間以上でもよい。反応時間の上限は特に限定されないが、10時間以内、9時間以内、8時間以内、7時間以内、6時間以内、5時間以内、または、4時間以内でもよい。
The enzymatic reaction can be carried out at a temperature of preferably 15°C to 40°C, more preferably 20°C to 40°C, and even more preferably 25°C to 40°C.
The reaction time may be 10 minutes or more, preferably 30 minutes or more, more preferably 1 hour or more, even more preferably 1.5 hours or more, and may be 2 hours or more. The upper limit of the reaction time is not particularly limited, but may be 10 hours or less, 9 hours or less, 8 hours or less, 7 hours or less, 6 hours or less, 5 hours or less, or 4 hours or less.
酵素処理された混合物には、滑膜由来間葉系幹細胞が含まれている。
酵素処理された混合物は、セルストレーナーを通して遠沈管に移し、遠心処理することにより滑膜由来間葉系幹細胞を回収することができる。
The enzyme-treated mixture contains synovium-derived mesenchymal stem cells.
The enzyme-treated mixture is passed through a cell strainer and transferred to a centrifuge tube, and then centrifuged to recover synovium-derived mesenchymal stem cells.
(酵素処理後の混合物を洗浄した後の混合物に含まれる滑膜由来間葉系幹細胞を培養培地にて培養する工程B)
上記の通り酵素処理した後の混合物は洗浄することが好ましい。
洗浄は、上記した遠心処理により回収した滑膜由来間葉系幹細胞を培地に再懸濁し、再度遠心することにより行うことができる。培地としては、α改変イーグル最小必須培地(αMEM)を用いることができるが、特に限定されない。洗浄は、上記のように培地を用いて複数回(2回以上)行ってもよい。
(Step B: Culturing the synovium-derived mesenchymal stem cells contained in the mixture after washing the mixture after enzyme treatment in a culture medium)
As described above, it is preferable to wash the mixture after the enzyme treatment.
Washing can be performed by resuspending the synovium-derived mesenchymal stem cells recovered by the above-mentioned centrifugation in a medium and centrifuging again. The medium can be, but is not limited to, α-modified Eagle's minimum essential medium (αMEM). Washing can be performed multiple times (two or more times) using the medium described above.
酵素処理後の混合物を洗浄した後の混合物に含まれる滑膜由来間葉系幹細胞は、培養培地にて培養する。基材としては、フラスコ、培養プレートなどの平面プラスチック基材、および培養バッグ、マイクロキャリアまたはゲルなどの立体基材などを挙げることができるが、特に限定されない。 The synovium-derived mesenchymal stem cells contained in the mixture after washing the mixture following enzyme treatment are cultured in a culture medium. Examples of substrates include, but are not limited to, flat plastic substrates such as flasks and culture plates, and three-dimensional substrates such as culture bags, microcarriers, or gels.
培養において使用する培地は、通常の動物細胞の培養に用いられる培地を基礎培地として調製することができる。通常の動物細胞の培養に用いられる培地としては、αMEM、DMEM(Dulbecco Modified Eagle Medium)、DMEMとF12の混合培地(DMEM:F12=1:1)、RPMI培地(GIBCO(登録商標)RPMI1640培地など)、DMEM/F12とRPMIの混合培地(DMEM/F12:RPMI=1:1)RoosterNourishTM-MSC-XFなどを挙げることができるが、特に限定されない。培地には、抗生物質または抗真菌剤(例えば、アムホテリシンB、ゲンタマイシンなど)を添加してもよい。 The medium used for culturing can be prepared using a medium used for culturing ordinary animal cells as the basal medium. Examples of media used for culturing ordinary animal cells include, but are not limited to, αMEM, DMEM (Dulbecco Modified Eagle Medium), a mixed medium of DMEM and F12 (DMEM:F12=1:1), RPMI medium (GIBCO (registered trademark) RPMI 1640 medium, etc.), a mixed medium of DMEM/F12 and RPMI (DMEM/F12:RPMI=1:1), RoosterNourish ™ -MSC-XF, etc. The medium may also contain an antibiotic or antifungal agent (e.g., amphotericin B, gentamicin, etc.).
細胞の培養条件は特に限定されず、通常の細胞培養の条件を採用できる。例えば、温度30~40℃、3~7%CO2での培養を挙げることができるが、特に限定されるものではない。一例としては、温度37℃、5%CO2での培養を挙げることができる。 The cell culture conditions are not particularly limited, and ordinary cell culture conditions can be used. For example, culture at a temperature of 30 to 40°C and 3 to 7% CO2 can be used, but the conditions are not particularly limited. One example is culture at a temperature of 37°C and 5% CO2 .
(滑膜由来間葉系幹細胞の基材からの分離)
工程Bの培養後の滑膜由来間葉系幹細胞は、工程Cに先立って、基材から分離することが好ましい。好ましくは、間葉系幹細胞に細胞剥離液を、120分以内の時間、作用させることにより基材からの分離を行うことができる。細胞剥離液としては、トリプシン様酵素とEDTAを含む溶液である。特に好ましい酵素はTrypLEである。TrypLEとしては、例えば、TrypLE Select Enzyme(ThemoFisher Scientific社製)、TrypL Express(Gibco社製)、TrypLE Select(Gibco社製)などを使用することができる。
(Isolation of synovial membrane-derived mesenchymal stem cells from a substrate)
The synovium-derived mesenchymal stem cells cultured in step B are preferably separated from the substrate prior to step C. Preferably, separation from the substrate can be achieved by allowing a cell detachment solution to act on the mesenchymal stem cells for 120 minutes or less. The cell detachment solution is a solution containing a trypsin-like enzyme and EDTA. A particularly preferred enzyme is TrypLE. Examples of TrypLE that can be used include TrypLE Select Enzyme (manufactured by ThermoFisher Scientific), TrypL Express (manufactured by Gibco), and TrypLE Select (manufactured by Gibco).
間葉系幹細胞に細胞剥離液を作用させる時間は、5分間~120分間であることが好ましく、5分間~60分間であることがさらに好ましく、5分間~30分間であることが特に好ましい。 The time for which the cell detachment solution is allowed to act on the mesenchymal stem cells is preferably 5 to 120 minutes, more preferably 5 to 60 minutes, and especially preferably 5 to 30 minutes.
(培養後の滑膜由来間葉系幹細胞を凍結保存する工程C)
培養後の滑膜由来間葉系幹細胞は凍結保存することができる。
(Step C of cryopreserving the cultured synovium-derived mesenchymal stem cells)
After cultivation, the synovium-derived mesenchymal stem cells can be cryopreserved.
<マイクロキャリア>
本発明においては、マイクロキャリアの存在下において間葉系幹細胞を培養する。
攪拌静置培養工程においては、マイクロキャリアを追加してもよく、またはマイクロキャリアを追加しなくてもよい。
<Microcarriers>
In the present invention, mesenchymal stem cells are cultured in the presence of microcarriers.
In the stirring static culture step, microcarriers may or may not be added.
マイクロキャリアは、接着細胞の培養において、細胞の増殖の足場となる担体である。細胞培養用の担体として知られているマイクロキャリアを使用することができる。マイクロキャリアの材質は、有機物、無機物、またはこれらの複合材料でもよい。マイクロキャリアは、溶解性でもよく、不溶解性でもよい。 Microcarriers are carriers that serve as scaffolds for cell growth in adherent cell culture. Microcarriers known as carriers for cell culture can be used. Microcarriers may be made of organic, inorganic, or composite materials of these. Microcarriers may be soluble or insoluble.
有機物としては、例えば、ポリスチレン、ポリエステル、ポリウレタン、ポリエチレン、ポリプロピレン、ポリビニルアルコール、(メタ)アクリル系ポリマー、(メタ)アクリルアミド系ポリマー、シリコーン系ポリマー、エポキシ樹脂、ウレタン樹脂等の合成高分子;セルロース、デキストラン、コラーゲン、ポリガラクツロン酸、ポリアルギン酸、ゼラチン等の天然高分子などが挙げられる。 Examples of organic materials include synthetic polymers such as polystyrene, polyester, polyurethane, polyethylene, polypropylene, polyvinyl alcohol, (meth)acrylic polymers, (meth)acrylamide polymers, silicone polymers, epoxy resins, and urethane resins; and natural polymers such as cellulose, dextran, collagen, polygalacturonic acid, polyalginic acid, and gelatin.
無機物としては、例えば、ガラス、セラミック、金属、合金、金属酸化物等が挙げられる。細胞適合性の観点から、マイクロキャリアの材質は、有機物を含むことが好ましく、天然高分子を含むことがより好ましい。操作性の観点から、溶解性のマイクロキャリアであることが好ましいが、これに限定されない。 Inorganic materials include, for example, glass, ceramic, metal, alloy, and metal oxide. From the viewpoint of cytocompatibility, the microcarrier material preferably contains an organic material, and more preferably contains a natural polymer. From the viewpoint of operability, soluble microcarriers are preferable, but are not limited to this.
マイクロキャリアの一例としては、SoloHill(登録商標)Plasticマイクロキャリア(Sartorius)、CellBIND(Corning),SyntheMAX(Corning),Cytodex1,Cytodex3(Cytiva)などを使用することができるが、特に限定されない。 Examples of microcarriers that can be used include, but are not limited to, SoloHill (registered trademark) Plastic microcarriers (Sartorius), CellBIND (Corning), SyntheMAX (Corning), Cytodex 1, and Cytodex 3 (Cytiva).
細胞の付着を促進する観点から、マイクロキャリアの表面には、カチオン性官能基が導入されていてもよい。カチオン性官能基として、ジメチルアミノ基、ジエチルアミノ基、アミノ基等の置換または非置換のアミノ基を含む基が挙げられる。また、細胞の付着を促進する観点から、マイクロキャリアの表面には、細胞接着性ポリマーが配置されていてもよい。細胞接着性ポリマーとしては、細胞接着性を示すポリペプチドまたは多糖であってもよく、コラーゲン、ゼラチン、アルギン酸、Matrigel(登録商標)(BD Bi osciences)、ヒアルロン酸、ラミニン、フィブロネクチン、ビトロネクチン、エラスチン、ヘパラン硫酸、デキストラン、デキストラン硫酸、コンドロイチン硫酸等が挙げられる。細胞接着性ポリマーは、細胞接着性を示す部分ペプチドまたはオリゴ糖であってもよい。また、細胞の付着を促進する観点から、プラズマ処理、コロナ処理などによって、親水性の官能基を生成し、マイクロキャリア表面を親水化してもよい。親水性の官能基としては、水酸基、カルボニル基、カルボキシル基を含む基が挙げられる。 To promote cell attachment, cationic functional groups may be introduced onto the surface of the microcarrier. Examples of cationic functional groups include groups containing substituted or unsubstituted amino groups such as dimethylamino, diethylamino, and amino groups. Furthermore, to promote cell attachment, a cell adhesive polymer may be disposed on the surface of the microcarrier. The cell adhesive polymer may be a polypeptide or polysaccharide that exhibits cell adhesive properties, such as collagen, gelatin, alginic acid, Matrigel® (BD Biosciences), hyaluronic acid, laminin, fibronectin, vitronectin, elastin, heparan sulfate, dextran, dextran sulfate, and chondroitin sulfate. The cell adhesive polymer may be a partial peptide or oligosaccharide that exhibits cell adhesive properties. Furthermore, to promote cell attachment, hydrophilic functional groups may be generated by plasma treatment, corona treatment, or the like to hydrophilize the microcarrier surface. Examples of hydrophilic functional groups include groups containing hydroxyl, carbonyl, and carboxyl groups.
マイクロキャリアの形状としては、例えば、球状、扁平状、円柱状、板状、角柱状等が挙げられる。マイクロキャリアは、内部に細孔を有する多孔質マイクロキャリアでも、内部に細孔を有しないマイクロキャリアでもよい。 Microcarrier shapes include, for example, spherical, flat, cylindrical, plate-like, and prismatic. Microcarriers may be porous microcarriers with internal pores, or microcarriers without internal pores.
マイクロキャリアの平均粒子径(D50)は、細胞の増殖促進の観点から、例えば50~1,000μmであり、100~500μmであることが好ましく、150~250μmであることがより好ましい。マイクロキャリアの平均粒子径は、生理食塩水中のメジアン径(D50)として測定した値とする。マイクロキャリアの平均粒子径は、レーザー回折散乱式の粒子径分布測定装置により測定することができる。 From the perspective of promoting cell proliferation, the average particle diameter (D50) of the microcarriers is, for example, 50 to 1,000 μm, preferably 100 to 500 μm, and more preferably 150 to 250 μm. The average particle diameter of the microcarriers is the value measured as the median diameter (D50) in physiological saline. The average particle diameter of the microcarriers can be measured using a laser diffraction/scattering particle size distribution measuring device.
培地中のマイクロキャリアの濃度は、マイクロキャリアの形状、大きさ、表面積等に基づいて適宜調整することが可能であるが、例えば、0.1~100mg/mLでもよく、1~100mg/mLでもよく、または5~100mg/mLでもよい。 The concentration of microcarriers in the culture medium can be adjusted appropriately based on the shape, size, surface area, etc. of the microcarriers, but may be, for example, 0.1 to 100 mg/mL, 1 to 100 mg/mL, or 5 to 100 mg/mL.
<間葉系幹細胞の播種>
間葉系幹細胞の播種は、マイクロキャリアを含む培地に、間葉系幹細胞を添加することにより行うことができる。
<Mesenchymal stem cell seeding>
The mesenchymal stem cells can be seeded by adding the mesenchymal stem cells to a medium containing microcarriers.
例えば、遠沈管などの容器に、マイクロキャリア溶液を添加して静置させ、マイクロキャリアを沈降させたのち、上清を取り除き、培地を添加する。マイクロキャリアをよく懸濁し、得られた懸濁液を、培養容器に添加し、さらに培養容器に培地を添加する。次いで、所定の細胞数を培地中に含む細胞懸濁液を培養容器に添加することにより、細胞の播種を行うことができる。また、マイクロキャリア溶液を事前に準備することなく、マイクロキャリアを直接培地で懸濁し、その懸濁液を培養容器に添加した後に、細胞懸濁液を添加することもできる。 For example, a microcarrier solution is added to a container such as a centrifuge tube and allowed to stand to allow the microcarriers to settle, after which the supernatant is removed and culture medium is added. The microcarriers are thoroughly suspended, and the resulting suspension is added to a culture vessel, to which culture medium is then added. Cell seeding can then be carried out by adding a cell suspension containing a predetermined number of cells in culture medium to the culture vessel. Alternatively, it is possible to suspend the microcarriers directly in culture medium without preparing the microcarrier solution in advance, and then add the suspension to the culture vessel, followed by the cell suspension.
<攪拌静置培養工程>
本発明の方法は、間葉系幹細胞を攪拌させる工程と、その後に間葉系幹細胞を静置させる工程とを含む攪拌静置培養工程を、48時間以上行うことを含み、48時間以上の培養期間中に上記攪拌静置培養工程を2回以上行うことを含み、培養開始後24時間以降に、48時間毎に1回以上の攪拌静置培養工程を行う。攪拌静置培養工程としては、攪拌させる工程と静置させる工程との組み合わせを1セットとし、このセットを複数回繰り返せばよい。
<Agitated stationary culture process>
The method of the present invention comprises carrying out an agitation static culture step, which includes a step of agitating mesenchymal stem cells and a subsequent step of allowing the mesenchymal stem cells to stand, for 48 hours or more, and comprises carrying out the agitation static culture step two or more times during the 48-hour or more culture period, and carrying out the agitation static culture step at least once every 48 hours starting 24 hours after the start of culture. The agitation static culture step is a combination of an agitation step and a standing step, and this set may be repeated multiple times.
本発明においては、培養開始とは、細胞とマイクロキャリアが同一容器の同一液内に共存した瞬間を意味する。 In the present invention, the start of culture refers to the moment when cells and microcarriers coexist in the same liquid in the same container.
攪拌させる工程とは、間葉系幹細胞とマイクロキャリアとを含む培養液を攪拌しながら間葉系幹細胞の培養を行う工程である。攪拌速度は、培養液の容量に応じて適宜設定することができるが、培養液中の全てのマイクロキャリアが浮遊する速度である。攪拌速度は、特に限定されないが、一般的には50rpm以上であり、好ましくは100rpm以上であり、より好ましくは150rpm以上であり、200rpm以上、または300rpm以上でもよい。攪拌速度の上限は特に限定されないが、一般的には1000rpm以下であり、好ましくは700rpm以下である。なお、攪拌させる工程における攪拌速度は、培養液の容量によっては50rpm未満である場合(例えば、10rpm以上50rpm未満)も想定される。 The stirring step is a step in which mesenchymal stem cells are cultured while stirring the culture solution containing mesenchymal stem cells and microcarriers. The stirring speed can be set appropriately depending on the volume of the culture solution, but is a speed at which all of the microcarriers in the culture solution are suspended. The stirring speed is not particularly limited, but is generally 50 rpm or higher, preferably 100 rpm or higher, more preferably 150 rpm or higher, and may be 200 rpm or higher, or 300 rpm or higher. There is no particular upper limit to the stirring speed, but it is generally 1000 rpm or lower, preferably 700 rpm or lower. Note that the stirring speed in the stirring step may be less than 50 rpm (for example, 10 rpm or higher but less than 50 rpm) depending on the volume of the culture solution.
静置させる工程とは、攪拌を行わない工程、または50rpm未満の微弱攪拌を含む工程を意味する。なお、攪拌させる工程における攪拌速度が、50rpm未満である場合(例えば、10rpm以上50rpm未満)には、静置させる工程における微弱攪拌の攪拌速度は、攪拌させる工程における攪拌速度よりも小さい攪拌速度になる。攪拌させる工程における攪拌速度が、50rpm未満である場合、静置させる工程における微弱攪拌の攪拌速度が、攪拌させる工程における攪拌速度の1/2未満であることが好ましい。 The "standing step" refers to a step in which no stirring is performed, or a step in which weak stirring at less than 50 rpm is performed. Note that if the stirring speed in the stirring step is less than 50 rpm (for example, 10 rpm or more but less than 50 rpm), the weak stirring speed in the standing step will be slower than the stirring speed in the stirring step. If the stirring speed in the stirring step is less than 50 rpm, it is preferable that the weak stirring speed in the standing step be less than half the stirring speed in the stirring step.
攪拌は、撹拌子、攪拌羽根、または攪拌翼などを培養液中に設置し(例えば、培養容器に、攪拌翼などを有する回転軸を設けてもよい)、回転させることにより行うことができる。 Agitation can be achieved by placing a stirring bar, stirring blade, or stirring impeller in the culture solution (for example, a rotating shaft with stirring blades can be provided in the culture vessel) and rotating it.
本発明においては、上記の攪拌静置培養工程の時間は、48時間以上であるが、3日間以上、4日間以上、5日間以上、6日間以上、または7日間以上でもよい。 In the present invention, the duration of the above-mentioned stirring and static culture process is 48 hours or more, but it may also be 3 days or more, 4 days or more, 5 days or more, 6 days or more, or 7 days or more.
本発明においては、48時間以上の培養期間中に上記攪拌静置培養工程を2回以上行うことを含むが、48時間以上の培養期間中に上記攪拌静置培養工程を7回以上、42回以上、84回以上、または336回以上行ってもよい。
本発明においては、培養開始後24時間以降に、48時間毎に1回以上の攪拌静置培養工程を行うが、48時間毎に2回以上、12回以上、24回以上、または96回以上の攪拌静置培養工程を行ってもよい。
In the present invention, the above-mentioned stirring and static culture step is carried out two or more times during a culture period of 48 hours or more, but the above-mentioned stirring and static culture step may also be carried out seven or more times, 42 or more times, 84 or more times, or 336 or more times during a culture period of 48 hours or more.
In the present invention, the stirring static culture step is carried out at least once every 48 hours after 24 hours from the start of culture, but the stirring static culture step may also be carried out at least twice, at least 12 times, at least 24 times, or at least 96 times every 48 hours.
上記の2回以上の攪拌静置培養工程における各々の攪拌静置培養工程は同一の工程でもよいし、または上記の2回以上の攪拌静置培養工程は、攪拌させる工程の時間と静置させる工程の時間のいずれか一以上が異なる攪拌静置培養工程を含んでいてもよい。好ましくは、上記の2回以上の攪拌静置培養工程における各々の攪拌静置培養工程は同一の工程である。
好ましくは、攪拌静置培養工程は、培養開始から培養終了まで行われる。
The two or more stirring and static culture steps may be the same step, or the two or more stirring and static culture steps may include stirring and static culture steps in which one or more of the stirring step time and the stationary step time are different. Preferably, the two or more stirring and static culture steps are the same step.
Preferably, the stirring static culture step is carried out from the start of the culture to the end of the culture.
攪拌静置培養工程における間葉系幹細胞を静置させる工程の時間は、好ましくは1分以上2400分以下であり、より好ましくは1分以上2000分以下であり、さらに好ましくは1分以上1900分以下であり、さらに好ましくは1分以上1600分以下であり、さらに好ましくは1分以上1500分以下であり、、10分以上1500分以下、20分以上1500分以下、30分以上1500分以下、50分以上1500分以下、または60分以上1500分以下であってもよく、1分以上240分以下、1分以上120分以下、15分以上120分以下あってもよい。
攪拌静置培養工程における間葉系幹細胞を静置させる工程の時間は、培養液量あたり好ましくは0.1分/mL以上240.0分/mL以下であり、より好ましくは、0.1分/mL以上200.0分/mL以下であり、より好ましくは、0.1分/mL以上100.0分/mL以下であり、より好ましくは、0.1分/mL以上50.0分/mL以下であり、0.1分/mL以上24.0分/mL以下、0.1分/mL以上12.0分/mL以下、または、1.5分/mL以上12.0分/mL以下であってもよい。
The time for the step of allowing the mesenchymal stem cells to stand in the stirred static culture step is preferably 1 minute or more and 2,400 minutes or less, more preferably 1 minute or more and 2,000 minutes or less, even more preferably 1 minute or more and 1,900 minutes or less, even more preferably 1 minute or more and 1,600 minutes or less, even more preferably 1 minute or more and 1,500 minutes or less, 10 minutes or more and 1,500 minutes or less, 20 minutes or more and 1,500 minutes or less, 30 minutes or more and 1,500 minutes or less, 50 minutes or more and 1,500 minutes or less, or 60 minutes or more and 1,500 minutes or less, or 1 minute or more and 240 minutes or less, 1 minute or more and 120 minutes or less, or 15 minutes or more and 120 minutes or less.
The time for the step of allowing the mesenchymal stem cells to stand in the stirred static culture step is preferably 0.1 min/mL or more and 240.0 min/mL or less, more preferably 0.1 min/mL or more and 200.0 min/mL or less, more preferably 0.1 min/mL or more and 100.0 min/mL or less, more preferably 0.1 min/mL or more and 50.0 min/mL or less, and may be 0.1 min/mL or more and 24.0 min/mL or less, 0.1 min/mL or more and 12.0 min/mL or less, or 1.5 min/mL or more and 12.0 min/mL or less, per volume of culture solution.
攪拌静置培養工程における間葉系幹細胞を攪拌させる工程の時間は、好ましくは1分以上2000分以下であり、1分以上1000分以下、1分以上500分以下、1分以上100分以下、1分以上60分以下、1分以上50分以下、1分以上30分以下、1分以上20分以下、1分以上15分以下、または1分以上10分以下であってもよいし、5分以上2000分以5分以上1500分以下5分以上1440分以下であってもよい。
攪拌静置培養工程における間葉系幹細胞を攪拌させる工程の時間は、培養液量あたり好ましくは0.1分/mL以上200.0分/mL以下であり、0.1分/mL以上150.0分/mL以下、0.1分/mL以上144.0分/mL以下、0.5分/mL以上200.0分/mL以下、0.5分/mL以上150.0分/mL以下、または0.5分/mL以上144.0分/mL以下であってもよい。
The time for the process of stirring the mesenchymal stem cells in the stirring static culture process is preferably 1 minute or more and 2000 minutes or less, and may be 1 minute or more and 1000 minutes or less, 1 minute or more and 500 minutes or less, 1 minute or more and 100 minutes or less, 1 minute or more and 60 minutes or less, 1 minute or more and 50 minutes or less, 1 minute or more and 30 minutes or less, 1 minute or more and 20 minutes or less, 1 minute or more and 15 minutes or less, or 1 minute or more and 10 minutes or less, or may be 5 minutes or more and 2000 minutes or less, 5 minutes or more and 1500 minutes or less, 5 minutes or more and 1440 minutes or less.
The time for the process of stirring the mesenchymal stem cells in the stirring static culture process is preferably 0.1 min/mL or more and 200.0 min/mL or less per volume of culture solution, and may be 0.1 min/mL or more and 150.0 min/mL or less, 0.1 min/mL or more and 144.0 min/mL or less, 0.5 min/mL or more and 200.0 min/mL or less, 0.5 min/mL or more and 150.0 min/mL or less, or 0.5 min/mL or more and 144.0 min/mL or less.
攪拌静置培養工程を24時間当たり、好ましくは1回~48回行うことができ、1回~24回行ってもよく、1回~12回行ってもよく、1回~6回、または6回~12回行ってもよい。 The stirring and static culture process can be performed preferably 1 to 48 times per 24 hours, or may be performed 1 to 24 times, 1 to 12 times, 1 to 6 times, or 6 to 12 times.
攪拌静置培養工程の1回の時間は、好ましくは30分~1440分であり、あるいは30分~1000分、30分~800分、30分~600分、30分~500分、30分~400分、30分~300分、30分~240分、30分~120分、50分~1440分、50分~1000分、50分~800分、50分~600分、50分~500分、50分~400分、50分~300分、50分~240分、50分~120分、120分~1440分、120分~1000分、120分~800分、120分~600分、120分~500分、120分~400分、120分~300分、120分~240分、または240分~1440分でもよい。
攪拌静置培養工程における間葉系幹細胞を攪拌させる工程と、間葉系幹細胞を静置させる工程との時間の比率は、1:0.005~1:700の範囲内であってもよく、1:0.005~1:600、1:0.005~1:500、1:0.005~1:400、1:0.005~1:380、1:0.005~1:320、1:0.005~1:300、1:0.005~1:10、1;0.01~1:10、1:0.05~1:10、1:0.08~1:10、1:0.1~1:0、1:0.1~1:5、1:1~1:700、1:1~1:600、1:1~1:500、1:1~1:400、1:1~1:300、1:2~1:700、1:2~1:600、1:2~1:500、1:1~2:400、1:2~1:300、1:5~1:700、1:5~1:600、1:5~1:500、1:5~1:400、1:5~1:300、1:10~1:700、1:10~1:600、1:10~1:500、1:10~1:400、または1:10~1:300、であってもよい。
The duration of one stirring static culture step is preferably 30 to 1440 minutes, or 30 to 1000 minutes, 30 to 800 minutes, 30 to 600 minutes, 30 to 500 minutes, 30 to 400 minutes, 30 to 300 minutes, 30 to 240 minutes, 30 to 120 minutes, 50 to 1440 minutes, 50 to 1000 minutes, 50 to 800 minutes, 50 to 600 minutes, minutes, 50 to 500 minutes, 50 to 400 minutes, 50 to 300 minutes, 50 to 240 minutes, 50 to 120 minutes, 120 to 1440 minutes, 120 to 1000 minutes, 120 to 800 minutes, 120 to 600 minutes, 120 to 500 minutes, 120 to 400 minutes, 120 to 300 minutes, 120 to 240 minutes, or 240 to 1440 minutes.
The ratio of the time between the step of stirring the mesenchymal stem cells and the step of allowing the mesenchymal stem cells to stand in the stirring static culture step may be within the range of 1:0.005 to 1:700, 1:0.005 to 1:600, 1:0.005 to 1:500, 1:0.005 to 1:400, 1:0.005 to 1:380, 1:0.005 to 1:320, 1:0.005 to 1:300, 1:0.005 to 1:10, 1:0.01 to 1:10, 1:0.05 to 1:10, 1:0.08 to 1:10, 1:0.1 to 1:00, 1:0.01 to 1:1 ... The ratio may be 1 to 1:5, 1:1 to 1:700, 1:1 to 1:600, 1:1 to 1:500, 1:1 to 1:400, 1:1 to 1:300, 1:2 to 1:700, 1:2 to 1:600, 1:2 to 1:500, 1:1 to 2:400, 1:2 to 1:300, 1:5 to 1:700, 1:5 to 1:600, 1:5 to 1:500, 1:5 to 1:400, 1:5 to 1:300, 1:10 to 1:700, 1:10 to 1:600, 1:10 to 1:500, 1:10 to 1:400, or 1:10 to 1:300.
好ましくは、全培養期間における攪拌させる工程の時間の総和は、静置させる工程の時間の総和よりも長い。 Preferably, the total time for the stirring step during the entire culture period is longer than the total time for the standing step.
本発明の一例においては、培養開始後24時間以降に攪拌静置培養を48時間以上行い、その後連続的に攪拌培養を行ってもよい。
本発明の別の例においては、培養開始後24時間以降に攪拌静置培養を72時間以上行い、その後連続的に攪拌培養を行ってもよい。本発明のさらに別の例においては、培養開始後24時間以降に攪拌静置培養を96時間以上行い、その後連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養を120時間以上行い、その後連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養を144時間以上行い、その後連続的に攪拌培養を行ってもよい。
In one example of the present invention, 24 hours or more after the start of the culture, stirring static culture may be carried out for 48 hours or more, and thereafter stirring culture may be carried out continuously.
In another example of the present invention, agitation static culture may be performed for 72 hours or more after 24 hours from the start of culture, followed by continuous agitation culture. In yet another example of the present invention, agitation static culture may be performed for 96 hours or more after 24 hours from the start of culture, followed by continuous agitation culture, or agitation static culture may be performed for 120 hours or more after 24 hours from the start of culture, followed by continuous agitation culture, or agitation static culture may be performed for 144 hours or more after 24 hours from the start of culture, followed by continuous agitation culture.
本発明の一例においては、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了2日以上前から連続的に攪拌培養を行ってもよい。本発明の別の例においては、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了3日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了4日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了5日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了6日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了7日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了8日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了9日以上前から連続的に攪拌培養を行ってもよいし、培養開始後24時間以降に攪拌静置培養工程を行い、培養終了10日以上前から連続的に攪拌培養を行ってもよい。 In one example of the present invention, the stirring static culture process may be carried out 24 hours or more after the start of culture, and stirring culture may be carried out continuously from two days or more before the end of culture. In another example of the present invention, the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 3 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 4 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 5 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 6 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 7 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 8 days or more before the end of culture; the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 9 days or more before the end of culture; or the stirring and static culture step may be performed 24 hours or more after the start of culture and then continuous stirring culture may be performed from 10 days or more before the end of culture.
攪拌静置培養工程と、連続的に攪拌させる工程との時間の比率は、好ましくは、1:0.3~1:5.5であってもよい。
間葉系幹細胞を静置させる工程(A)と、攪拌静置させる工程(B)と、連続的に攪拌させる工程(C)との時間の比率は、好ましくは、A=1のとき、B=2~6、C=2~11であってもよい。
The ratio of the time for the stirring static culture step to the time for the continuous stirring step may preferably be 1:0.3 to 1:5.5.
The time ratio between the step (A) of leaving the mesenchymal stem cells to stand, the step (B) of stirring and leaving the mesenchymal stem cells to stand, and the step (C) of continuously stirring the mesenchymal stem cells may preferably be A=1, B=2 to 6, and C=2 to 11.
<間葉系幹細胞の培養の一般的条件>
間葉系幹細胞の培養に用いる培養容器は、間葉系幹細胞の培養が可能なものであれば特に限定されないが、フラスコ、組織培養用フラスコ、ディッシュ、ペトリデッシュ、組織培養用ディッシュ、マルチディッシュ、マイクロプレート、マイクロウエルプレート、マルチプレート、マルチウエルプレート、マイクロスライド、チャンバースライド、シャーレ、チューブ、トレイ、培養バック、ローラーボトル、培養槽およびバイオリアクターなどが挙げられる。
<General conditions for culturing mesenchymal stem cells>
The culture vessel used for culturing mesenchymal stem cells is not particularly limited as long as it is capable of culturing mesenchymal stem cells, and examples include flasks, tissue culture flasks, dishes, Petri dishes, tissue culture dishes, multi-dishes, microplates, microwell plates, multi-plates, multi-well plates, microslides, chamber slides, petri dishes, tubes, trays, culture bags, roller bottles, culture tanks, and bioreactors.
培養スケール(培養液の量)は特に限定されないが、一般的には0.01~3000Lであり、好ましくは0.01~500Lであり、より好ましくは0.01~50Lであり、さらに好ましくは0.01~10Lである。 The culture scale (volume of culture medium) is not particularly limited, but is generally 0.01 to 3000 L, preferably 0.01 to 500 L, more preferably 0.01 to 50 L, and even more preferably 0.01 to 10 L.
培地としては、間葉系幹細胞の生存および増殖に必要な成分(無機塩、炭水化物、ホルモン、必須アミノ酸、非必須アミノ酸、ビタミン、脂肪酸)を含む基本培地を使用することができる、例えば、αMEM、DMEM(Dulbecco Modified Eagle Medium)、DMEMとF12の混合培地(DMEM:F12=1:1)、RPMI培地(GIBCO(登録商標)RPMI1640培地など)、DMEM/F12とRPMIの混合培地(DMEM/F12:RPMI=1:1)、RoosterNourishTM-MSC-XF培地(以下RoosterNourish培地、RoosterBio)などを使用することができる。 As the culture medium, a basal medium containing components necessary for the survival and proliferation of mesenchymal stem cells (inorganic salts, carbohydrates, hormones, essential amino acids, non-essential amino acids, vitamins, fatty acids) can be used. For example, αMEM, DMEM (Dulbecco Modified Eagle Medium), a mixed medium of DMEM and F12 (DMEM:F12=1:1), RPMI medium (GIBCO (registered trademark) RPMI1640 medium, etc.), a mixed medium of DMEM/F12 and RPMI (DMEM/F12:RPMI=1:1), RoosterNourish ™ -MSC-XF medium (hereinafter referred to as RoosterNourish medium, RoosterBio), etc. can be used.
培養条件は、適宜設定できる。例えば、培養温度は、特に限定されるものではないが約30~40℃、好ましくは約37℃であり得る。CO2濃度は、約1~10%、好ましくは約2~5%であり得る。酸素濃度は、1~20%、好ましくは1~10%であり得る。 Culture conditions can be set appropriately. For example, the culture temperature is not particularly limited, but can be about 30 to 40°C, preferably about 37°C. The CO2 concentration can be about 1 to 10%, preferably about 2 to 5%. The oxygen concentration can be 1 to 20%, preferably 1 to 10%.
<マイクロキャリアの陽性率および回収生細胞数>
本発明の方法によれば、マイクロキャリアの陽性率を高くすることができ、また回収生細胞数を高くすることができる。
<Positive rate of microcarriers and number of recovered viable cells>
According to the method of the present invention, the positive rate of microcarriers can be increased, and the number of recovered viable cells can also be increased.
マイクロキャリアの陽性率は以下の通り測定することができる。細胞とマイクロキャリアを含む培養液をサンプリングし、Nucblue(ThemoFisher Scientific)を添加し、37℃で15~30分間インキュベートする。蛍光顕微鏡(KEYENCE)にて核染色を観察し、撮影する。ImageJにて撮影した画像を開き、Split Channelsで二値化する。この二値化した画像を元に、目視で細胞が接着している(核染色されている)マイクロキャリアと視野にある総マイクロキャリアの数をカウントする。下記の計算式にて陽性率を算出する。
陽性率=細胞が接着しているマイクロキャリア数/総マイクロキャリア数×100
The positivity rate of microcarriers can be measured as follows. A sample of the culture medium containing cells and microcarriers is taken, and Nucblue (ThemoFisher Scientific) is added and incubated at 37°C for 15 to 30 minutes. Nuclear staining is observed and photographed using a fluorescence microscope (KEYENCE). The image taken using ImageJ is opened and binarized using Split Channels. Based on this binarized image, the number of microcarriers to which cells are attached (nuclear stained) and the total number of microcarriers in the field of view are visually counted. The positivity rate is calculated using the following formula.
Positive rate = number of microcarriers with cells attached / total number of microcarriers × 100
回収生細胞数は以下の通り測定することができる。
培養後に、バイオリアクターを回収し、遠沈管に100μmセルストレーナーをセットし、バイオリアクターの内容物を全量ろ過する。セルストレーナー上に残った細胞とマイクロキャリアをDPBSで2回洗ったのち、TrypLE Select Enzyme(Gibco)でセルストレーナー上の細胞+マイクロキャリアを回収し、バイオリアクターに戻す。バイオリアクターを37℃下で300rpm、30分間攪拌する。バイオリアクターを回収し、100μmセルストレーナーをセットした遠沈管に、バイオリアクターの内容物を全量ろ過する。RoosterNourish培地で、バイオリアクターおよびセルストレーナー上のキャリアを共洗いする。遠沈管を遠心し、上清を除去したのち、RoosterNourish培地を加えて懸濁する。懸濁液をAO/PI Cell Viability Kit 9:1の割合で混ぜ、LUNA(Logos Biosystems)にて細胞数をカウントする。
The number of viable cells recovered can be determined as follows.
After culturing, the bioreactor is recovered, a 100 μm cell strainer is placed in the centrifuge tube, and the entire contents of the bioreactor are filtered. The cells and microcarriers remaining on the cell strainer are washed twice with DPBS, and then the cells and microcarriers on the cell strainer are recovered using TrypLE Select Enzyme (Gibco) and returned to the bioreactor. The bioreactor is stirred at 300 rpm for 30 minutes at 37°C. The bioreactor is recovered, and the entire contents of the bioreactor are filtered into a centrifuge tube equipped with a 100 μm cell strainer. The bioreactor and the carriers on the cell strainer are washed together with Rooster Nourish medium. The centrifuge tube is centrifuged, the supernatant is removed, and then Rooster Nourish medium is added and suspended. The suspension is mixed with AO/PI Cell Viability Kit at a ratio of 9:1, and the number of cells is counted using LUNA (Logos Biosystems).
<治療剤>
本発明の方法においては、好ましくは、治療剤として使用するための間葉系幹細胞が製造される。即ち、本発明の方法により製造した間葉系幹細胞は、細胞治療用などの医療用に好適に使用することができる。本発明の方法により製造した間葉系幹細胞は、対象疾患等に応じて、未分化のまま、または骨細胞、軟骨細胞もしくは脂肪細胞等へ分化させた後に、使用することができる。対象疾患としては、例えば、関節疾患、月状骨無腐性壊死、大腿骨頭無腐性壊死、難断性骨軟骨炎、腰椎椎間板ヘルニア、虚血性心疾患、表皮水疱症等が挙げられる。関節疾患としては、例えば、半月板損傷、外傷性軟骨損傷、離断性骨軟骨炎、無腐性骨壊死、変形性関節症(変形性膝関節症など)、関節リウマチ(慢性関節リウマチなど)、痛風、反応性関節炎、乾癖性関節炎、若年性関節炎、炎症性関節炎、関節軟骨欠損からなる群より選択される疾患が挙げられる。また、間葉系幹細胞は、脂肪細胞へ分化させた後、美容整形用に使用することも可能である。
<Therapeutic Agent>
The method of the present invention preferably produces mesenchymal stem cells for use as a therapeutic agent. That is, mesenchymal stem cells produced by the method of the present invention can be suitably used for medical purposes such as cell therapy. Mesenchymal stem cells produced by the method of the present invention can be used undifferentiated or after differentiation into osteocytes, chondrocytes, adipocytes, or the like, depending on the target disease. Target diseases include, for example, joint diseases, avascular necrosis of the lunate bone, avascular necrosis of the femoral head, osteochondritis dissecans, lumbar disc herniation, ischemic heart disease, epidermolysis bullosa, and the like. Joint diseases include, for example, meniscus injury, traumatic cartilage injury, osteochondritis dissecans, avascular necrosis of osteonecrosis, osteoarthritis (e.g., knee osteoarthritis), rheumatoid arthritis (e.g., rheumatoid arthritis), gout, reactive arthritis, psoriatic arthritis, juvenile arthritis, inflammatory arthritis, and articular cartilage defect. Mesenchymal stem cells can also be differentiated into adipocytes and then used for cosmetic surgery.
間葉系幹細胞を治療剤として使用する場合には、常法により、上記細胞を医薬的に許容される担体と混合するなどして、個体への投与に適した形態の製剤とすればよい。担体としては、例えば、生理食塩水、ブドウ糖やその他の補助薬(例えば、D-ソルビトール、D-マンニトール、塩化ナトリウム等)を加えて等張とした注射用蒸留水を挙げることができる。さらに、緩衝剤(例えば、リン酸塩緩衝液、酢酸ナトリウム緩衝液)、無痛化剤(例えば、塩化ベンザルコニウム、塩酸プロカインなど)、安定剤(例えば、ヒト血清アルブミン、ポリエチレングリコールなど)、保存剤、酸化防止剤等を配合してもよい。 When mesenchymal stem cells are used as a therapeutic agent, the cells can be prepared into a formulation suitable for administration to an individual by, for example, mixing them with a pharmaceutically acceptable carrier using standard methods. Examples of carriers include isotonic distilled water for injection made with physiological saline, glucose, or other adjuvants (e.g., D-sorbitol, D-mannitol, sodium chloride, etc.). Additionally, buffers (e.g., phosphate buffer, sodium acetate buffer), soothing agents (e.g., benzalkonium chloride, procaine hydrochloride, etc.), stabilizers (e.g., human serum albumin, polyethylene glycol, etc.), preservatives, antioxidants, etc. may also be added.
以下の実施例により本発明をさらに具体的に説明するが、本発明は実施例によって限定されるものではない。 The present invention will be explained in more detail using the following examples, but the present invention is not limited to these examples.
(材料と方法)
実施例1:攪拌静置培養工程において「攪拌119分、静置1分」を1セットとした条件での製造
(1)滑膜幹細胞の入手
ヒト臨床滑膜組織をディッシュの上に置き、ハサミで細切した。細切した組織を、リベラーゼ(Roche)とn-Liven PR(Sexton Biotechnologies)の混合溶液(1mg/mL)入りの遠沈管に移し、ローテーティングミキサーにて約3時間37℃で酵素処理を行った。酵素処理後のチューブにαMEM(自社調製、特開2021-040551)を添加しピペッティングにより組織を分散させ、50mL遠沈管にセットした70μmセルストレーナーに通し遠心した。上清を除去したのち、ペレットを崩し、αMEMを添加し遠心した。これを1回繰り返した。αMEMで細胞を懸濁し、懸濁液をAO/PI Cell Viability Kit(Logos Biosystems)9:1の割合で混ぜ、LUNA(Logos Biosystems)にて細胞数をカウントした。フラスコに1000cells/cm2の密度で播種し、αMEMにn-Liven PR、アムホテリシンB(ThemoFisher Scientific)、ゲンタマイシン(ThemoFisher Scientific)を混合した培養液(以下αMEM培地)にて3~5日間培養したのち、RoosterNourishTM-MSC-XF培地(以下RoosterNourish培地、RoosterBio)へ交換し、70~80%コンフルエントになるまで培養した。フラスコの上清を除去し、DPBS(ThemoFisher Scientific)で2回洗ったのち、TrypLE Select Enzyme(ThemoFisher Scientific)を添加し、37℃で10~30分間静置した。等量のαMEM培地を添加し、細胞懸濁を遠沈管に移し遠心した。上清を除去し、αMEM培地で懸濁したのち、AO/PI Cell Viability Kit 9:1の割合で混ぜ、LUNAにて細胞数をカウントした。所定の細胞数の懸濁液を新しい遠沈管に移し、遠心した。上清を除去し、DMSO入り凍結保存液を用いて凍結した(P0:継代0)。P0凍結細胞をウォーターバスにて融解し、RoosterNourish培地入りの遠沈管に添加し遠心した。上清を除去しRoosterNourish培地で懸濁したのち、AO/PI Cell Viability Kit 9:1の割合で混ぜ、LUNAにて細胞数をカウントした。1000~3000cells/cm2の密度でフラスコに播種し、70~80%コンフルエントになるまで培養した。フラスコの上清を除去し、DPBSで洗ったのち、TrypLE Select Enzymeを添加し、37℃で約5分間静置した。等量のRoosterNourish培地を添加し、細胞懸濁を遠沈管に移し遠心した。上清を除去し、RoosterNourish培地で懸濁したのち、AO/PI Cell Viability Kit 9:1の割合で混ぜ、LUNAにて細胞数をカウントした。所定の細胞数の懸濁液を新しい遠沈管に移し、遠心した。上清を除去し、DMSO入り凍結保存液を用いて凍結した(P1:継代1)。
Materials and Methods
Example 1: Production under one set of conditions: "119 minutes of stirring, 1 minute of static culture" in the stirring static culture process (1) Obtaining synovial stem cells Human clinical synovial tissue was placed on a dish and shredded with scissors. The shredded tissue was transferred to a centrifuge tube containing a mixed solution (1 mg/mL) of Liberase (Roche) and n-Liven PR (Sexton Biotechnologies) and subjected to enzyme treatment at 37°C for approximately 3 hours using a rotating mixer. After enzyme treatment, αMEM (prepared in-house, JP 2021-040551) was added to the tube, and the tissue was dispersed by pipetting. The tissue was then passed through a 70 μm cell strainer placed in a 50 mL centrifuge tube and centrifuged. After removing the supernatant, the pellet was broken up, αMEM was added, and the mixture was centrifuged. This process was repeated once. The cells were suspended in αMEM, and the suspension was mixed with AO/PI Cell Viability Kit (Logos Biosystems) at a ratio of 9:1, and the number of cells was counted using LUNA (Logos Biosystems). The cells were seeded in a flask at a density of 1000 cells/ cm2 and cultured for 3 to 5 days in a culture medium (hereinafter referred to as αMEM medium) prepared by mixing αMEM with n-Liven PR, amphotericin B (ThemoFisher Scientific), and gentamicin (ThemoFisher Scientific). After that, the medium was changed to RoosterNourish ™ -MSC-XF medium (hereinafter referred to as RoosterNourish medium, RoosterBio) and cultured until the cells reached 70 to 80% confluence. The supernatant was removed from the flask, and the cells were washed twice with DPBS (ThemoFisher Scientific). TrypLE Select Enzyme (ThemoFisher Scientific) was added and the mixture was left to stand at 37°C for 10 to 30 minutes. An equal volume of αMEM medium was added, and the cell suspension was transferred to a centrifuge tube and centrifuged. The supernatant was removed, and the cells were suspended in αMEM medium. After mixing with AO/PI Cell Viability Kit at a ratio of 9:1, the cells were counted using LUNA. The suspension containing the specified number of cells was transferred to a new centrifuge tube and centrifuged. The supernatant was removed, and the cells were frozen using a DMSO-containing cryopreservation solution (P0: passage 0). P0 frozen cells were thawed in a water bath, added to a centrifuge tube containing Rooster Nourish medium, and centrifuged. The supernatant was removed, and the cells were suspended in Rooster Nourish medium. After mixing with AO/PI Cell Viability Kit at a ratio of 9:1, the number of cells was counted using LUNA. The cells were seeded into flasks at a density of 1,000-3,000 cells/ cm² and cultured until 70-80% confluent. The supernatant was removed from the flask, washed with DPBS, and then TrypLE Select Enzyme was added. The mixture was allowed to stand at 37°C for approximately 5 minutes. An equal volume of Rooster Nourish medium was added, and the cell suspension was transferred to a centrifuge tube and centrifuged. The supernatant was removed, and the cells were suspended in Rooster Nourish medium. After mixing with AO/PI Cell Viability Kit at a ratio of 9:1, the number of cells was counted using LUNA. The suspension containing the desired number of cells was transferred to a new centrifuge tube and centrifuged. The supernatant was removed and frozen using a DMSO-containing freezing medium (P1: passage 1).
(2)マイクロキャリアの準備
SoloHill(登録商標)Plasticマイクロキャリア(Sartorius Cat.No.PIR-221-020)を0.1g/mLの濃度でDPBS(Gibco)に懸濁し、室温で保管した。
(2) Preparation of Microcarriers SoloHill (registered trademark) Plastic microcarriers (Sartorius Cat. No. PIR-221-020) were suspended in DPBS (Gibco) at a concentration of 0.1 g/mL and stored at room temperature.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。マイクロキャリアの濃度は0.14g/4mLである。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube and then transferred to 1.4 mL x the required number of tubes. After leaving to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed and 2 mL x the required number of tubes of Rooster Nourish medium (RoosterBio) was added. The microcarriers were thoroughly suspended and added to Ambr15 bioreactors (Sartorius) at 2 mL/tube. Rooster Nourish medium was added to 50 mL centrifuge tubes so that 2 mL x the required number of tubes was added, and then 2 mL/tube was added to the Ambr15 bioreactor. The microcarrier concentration was 0.14 g/4 mL.
(1)の凍結細胞(P1)を解凍し、3×103cells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調整した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。同様の操作を別日に2回繰り返した。 The frozen cells (P1) from (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL). The same procedure was repeated twice on separate days.
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「攪拌5分、静置25分」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌119分、静置1分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。また、マイクロキャリアの陽性率の評価のために行う培養4日目のサンプリング後に、Ambr15のプログラムにて培地交換を実施した。培地交換は、攪拌静置培養工程の静置培養工程を行うタイミングで行い、5分程度静置させ、キャリアと細胞を沈降させ、培養上清5mLを抜き取った。その後、攪拌培養工程を行うタイミングでRoosterNourish培地を添加した。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of stirring, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. The cycle of "119 minutes of stirring, 1 minute of standing" was then repeated for 7 days, and the culture was continued (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The stirring speed was 300 rpm. Furthermore, after sampling on the fourth day of culture to evaluate the microcarrier positivity rate, medium exchange was performed using the Ambr15 program. The medium exchange was performed at the same time as the static culture step of the stirring and static culture step, and the culture was allowed to stand for about 5 minutes, allowing the carriers and cells to settle, and 5 mL of culture supernatant was withdrawn. Then, Rooster Nourish medium was added at the same time as the stirring and static culture step.
(4-2)マイクロキャリアの陽性率の評価
培養4日目の細胞とマイクロキャリアを含む培養液をAmbr15のプログラムにて100μLサンプリングした。これにDPBSを400μL添加したのち、Nucblue(ThemoFisher Scientific)を1滴垂らし、37℃で15~30分間インキュベートした。蛍光顕微鏡(KEYENCE)にて核染色を観察し、撮影した。ImageJにて撮影した画像を開き、Split Channelsで二値化した。この二値化した画像を元に、目視で細胞が接着している(核染色されている)マイクロキャリアと視野にある総マイクロキャリアの数をカウントした。
下記の計算式にて陽性率を算出した。
陽性率=細胞が接着しているマイクロキャリア数/総マイクロキャリア数×100
「攪拌119分、静置1分」を1セットとした条件で培養したときの陽性率は、36%(3回の試験の平均値)であった。
(4-2) Evaluation of Microcarrier Positivity Rate 100 μL of culture medium containing cells and microcarriers on day 4 of culture was sampled using the Ambr15 program. 400 μL of DPBS was added, and then one drop of Nucblue (ThemoFisher Scientific) was added and incubated at 37 °C for 15 to 30 minutes. Nuclear staining was observed and photographed using a fluorescence microscope (KEYENCE). The images taken with ImageJ were opened and binarized using Split Channels. Based on this binarized image, the number of microcarriers to which cells had adhered (nuclear stained) and the total number of microcarriers in the field of view were visually counted.
The positive rate was calculated using the following formula.
Positive rate = number of microcarriers with cells attached / total number of microcarriers × 100
The positive rate when cultured under one set of conditions of "119 minutes of stirring and 1 minute of standing" was 36% (average value of three tests).
(4-3)回収生細胞数の評価
7日間培養したのち、Ambr15バイオリアクターを回収した。50mL遠沈管に100μmセルストレーナーをセットし、Ambr15バイオリアクターの内容物を全量ろ過した。セルストレーナー上に残った細胞+マイクロキャリアをDPBSで2回洗ったのち、TrypLE Select Enzyme(Gibco)でセルストレーナー上の細胞+マイクロキャリアを回収し、Ambr15バイオリアクターに戻した。Ambr15バイオリアクターをAmbr15にセットし、37℃下で300rpm、30分間攪拌した。Ambr15バイオリアクターを回収し、100μmセルストレーナーをセットした50mL遠沈管に、Ambr15バイオリアクターの内容物を全量ろ過した。RoosterNourish培地で、Ambr15バイオリアクターおよびセルストレーナー上のキャリアを共洗いした。50mL遠沈管を遠心し、上清を除去したのち、RoosterNourish培地を加えて懸濁した。懸濁液をAO/PI Cell Viability Kit 9:1の割合で混ぜ、LUNA(Logos Biosystems)にて細胞数をカウントした。細胞は、必要に応じてCP-1 High Grade(極東製薬工業株式会社)用いて凍結した。
(4-3) Evaluation of the number of recovered viable cells After 7 days of culture, the Ambr15 bioreactor was recovered. A 100 μm cell strainer was placed in a 50 mL centrifuge tube, and the entire contents of the Ambr15 bioreactor were filtered. The cells and microcarriers remaining on the cell strainer were washed twice with DPBS, and then the cells and microcarriers on the cell strainer were recovered using TrypLE Select Enzyme (Gibco) and returned to the Ambr15 bioreactor. The Ambr15 bioreactor was placed in the Ambr15 and stirred at 300 rpm for 30 minutes at 37 °C. The Ambr15 bioreactor was recovered, and the entire contents of the Ambr15 bioreactor were filtered into a 50 mL centrifuge tube containing a 100 μm cell strainer. The Ambr15 bioreactor and the carrier on the cell strainer were washed together with Rooster Nourish medium. The 50 mL centrifuge tube was centrifuged, the supernatant was removed, and Rooster Nourish medium was added to suspend the cells. The suspension was mixed with AO/PI Cell Viability Kit at a ratio of 9:1, and the cell number was counted using LUNA (Logos Biosystems). The cells were frozen using CP-1 High Grade (Kyokuto Pharmaceutical Industries Co., Ltd.) as needed.
「攪拌119分、静置1分」を1セットとした条件で培養したときの回収生細胞数は、1.27×106cells(2回の試験の平均値)であった。 When cultured under one set of conditions of "agitation for 119 minutes and standing for 1 minute," the number of viable cells recovered was 1.27 x 10 6 cells (average value of two tests).
(4-4)総合評価
(4-2)陽性率および(4-3)回収生細胞数の評価を組み合わせ総合的な評価を行った。評価基準は下記の通りである。
(4-4) Overall Evaluation A comprehensive evaluation was performed by combining the evaluations of (4-2) Positive Rate and (4-3) Number of Recovered Viable Cells. The evaluation criteria are as follows:
「攪拌119分、静置1分」を1セットとした条件で培養したときの総合評価は「D」であった。 When cultured under one set of conditions, "119 minutes of agitation, 1 minute of standing," the overall rating was "D."
実施例2:攪拌静置培養工程において「攪拌225分、静置15分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は、実施例1と同様に行った。
Example 2: Production under the condition of "225 minutes of stirring and 15 minutes of static culture" as one set in the stirring and static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube, and then 1.4 mL of the required number of tubes was transferred. After leaving the tubes to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed, and 2 mL of Rooster Nourish medium (RoosterBio) was added in the required number of tubes. The microcarriers were thoroughly suspended, and added to Ambr15 bioreactors (Sartorius) in 2 mL/tube quantities. Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
(1)の凍結細胞(P1)を解凍し、3×103cells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調製した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。 The frozen cells (P1) in (1) were thawed and prepared in Rooster Nourish medium at 15 x 10 cells/mL for seeding at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌225分、静置15分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of agitation, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. The cycle of "225 minutes of agitation, 15 minutes of standing" was then repeated for seven days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌225分、静置15分」を1セットとした条件で培養したときの陽性率は、80%であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "225 minutes of stirring and 15 minutes of standing" was 80%.
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌225分、静置15分」を1セットとした条件で培養したときの回収生細胞数は、0.937×106cellsであった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "225 minutes of stirring and 15 minutes of standing," the number of viable cells recovered was 0.937 x 10 6 cells.
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌225分、静置15分」を1セットとした条件で培養したときの総合評価は「C」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
The overall evaluation when the culture was performed under one set of conditions of "225 minutes of stirring and 15 minutes of standing" was "C."
実施例3:攪拌静置培養工程において「攪拌5分、静置25分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、(2)マイクロキャリアの準備、および(3)滑膜間葉系幹細胞の播種は、実施例1と同様に行った。
Example 3: Production under the condition of "5 minutes of stirring and 25 minutes of static culture" as one set in the stirring and static culture process (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 1.
(4)培養および評価
(4-1)
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌5分、静置25分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1)
The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of stirring, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. The cycle of "5 minutes of stirring, 25 minutes of standing" was then repeated for seven days for cultivation (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The stirring speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌5分、静置25分」を1セットとした条件で培養したときの陽性率は、44%(3回の試験の平均値)であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "5 minutes of stirring and 25 minutes of standing" was 44% (average value of three tests).
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌5分、静置25分」を1セットとした条件で培養したときの回収生細胞数は、1.01×106cells(2回の試験の平均値)であった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "5 minutes of stirring and 25 minutes of standing," the number of viable cells recovered was 1.01 x 10 6 cells (average of two tests).
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌5分、静置25分」を1セットとした条件で培養したときの総合評価は「B」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "5 minutes of stirring and 25 minutes of standing," the overall evaluation was "B."
実施例4:攪拌静置培養工程において「攪拌95分、静置25分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は、実施例1と同様に行った。
Example 4: Production under the condition of "95 minutes of stirring and 25 minutes of static culture" as one set in the stirring and static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。
(1)の凍結細胞(P1)を解凍し、3×103cells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調整した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。
同様の操作を別日に4回繰り返した。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube, and then 1.4 mL of the required number of tubes was transferred. After leaving the tubes to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed, and 2 mL of Rooster Nourish medium (RoosterBio) was added in the required number of tubes. The microcarriers were thoroughly suspended, and added to Ambr15 bioreactors (Sartorius) in 2 mL/tube quantities. Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
The frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
The same procedure was repeated four times on different days.
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌95分、静置25分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of stirring, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. Subsequently, a cycle of "95 minutes of stirring, 25 minutes of standing" was repeated for seven days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The stirring speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌95分、静置25分」を1セットとした条件で培養したときの陽性率は、78%(5回の試験の平均値)であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "95 minutes of stirring and 25 minutes of standing" was 78% (average value of five tests).
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌95分、静置25分」を1セットとした条件で培養したときの回収生細胞数は、1.70×106cells(4回の試験の平均値)であった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "95 minutes of stirring and 25 minutes of standing," the number of viable cells recovered was 1.70 x 10 6 cells (average value of four tests).
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌95分、静置25分」を1セットとした条件で培養したときの総合評価は「A」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "95 minutes of stirring and 25 minutes of standing," the overall evaluation was "A."
実施例5:攪拌静置培養工程において「攪拌215分、静置25分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、(2)マイクロキャリアの準備、および(3)滑膜間葉系幹細胞の播種は、実施例1と同様に行った。
Example 5: Production under one set of conditions in the stirring and static culture process: "215 minutes of stirring, 25 minutes of static culture" (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 1.
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌215分、静置25分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of agitation, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. The cycle of "215 minutes of agitation, 25 minutes of standing" was then repeated for 7 days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌215分、静置25分」を1セットとした条件で培養したときの陽性率は、86%(3回の試験の平均値)であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "215 minutes of stirring and 25 minutes of standing" was 86% (average value of three tests).
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌215分、静置25分」を1セットとした条件で培養したときの回収生細胞数は、1.75×106cells(3回の試験の平均値)であった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "215 minutes of stirring and 25 minutes of standing," the number of viable cells recovered was 1.75 x 10 6 cells (average value of three tests).
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌215分、静置25分」を1セットとした条件で培養したときの総合評価は「A」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
The overall evaluation when the culture was performed under one set of conditions of "215 minutes of stirring and 25 minutes of standing" was "A."
実施例6:攪拌静置培養工程において「攪拌1415分、静置25分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は、実施例1と同様に行った。
Example 6: Production under the condition of "1415 minutes of stirring and 25 minutes of static culture" as one set in the stirring and static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。
(1)の凍結細胞(P1)を解凍し、3×103cells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調整した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。
同様の操作を別日に1回繰り返した。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube, and then 1.4 mL of the required number of tubes was transferred. After leaving the tubes to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed, and 2 mL of Rooster Nourish medium (RoosterBio) was added in the required number of tubes. The microcarriers were thoroughly suspended, and added to Ambr15 bioreactors (Sartorius) in 2 mL/tube quantities. Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
The frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
The same procedure was repeated once on another day.
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌1415分、静置25分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of agitation, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. The cycle of "1415 minutes of agitation, 25 minutes of standing" was then repeated for seven days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌1415分、静置25分」を1セットとした条件で培養したときの陽性率は、83%(2回の試験の平均値)であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "1415 minutes of stirring and 25 minutes of standing" was 83% (average value of two tests).
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌1415分、静置25分」を1セットとした条件で培養したときの回収生細胞数は、1.95×106cells(2回の試験の平均値)であった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "1415 minutes of stirring and 25 minutes of standing," the number of viable cells recovered was 1.95 x 10 6 cells (average of two tests).
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌1415分、静置25分」を1セットとした条件で培養したときの総合評価は「A」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
The overall evaluation when the culture was performed under one set of conditions of "1415 minutes of stirring and 25 minutes of standing" was "A."
実施例7:静置培養工程において「攪拌60分、静置60分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は、実施例1と同様に行った。
Example 7: Production under conditions where one set of "60 minutes of stirring, 60 minutes of standing" was used in the static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。
(1)の凍結細胞(P1)を解凍し、3×103 ells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調整した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。
同様の操作を別日に1回繰り返した。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube, and then 1.4 mL of the required number of tubes was transferred. After leaving the tubes to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed, and 2 mL of Rooster Nourish medium (RoosterBio) was added in the required number of tubes. The microcarriers were thoroughly suspended, and added to Ambr15 bioreactors (Sartorius) in 2 mL/tube quantities. Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
The frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
The same procedure was repeated once on another day.
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌60分、静置60分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of agitation, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. Subsequently, a cycle of "60 minutes of agitation, 60 minutes of standing" was repeated for seven days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌60分、静置60分」を1セットとした条件で培養したときの陽性率は、89%(2回の試験の平均値)であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "60 minutes of stirring and 60 minutes of standing" was 89% (average of two tests).
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌60分、静置60分」を1セットとした条件で培養したときの回収生細胞数は、1.33×106cells(2回の試験の平均値)であった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "agitation for 60 minutes and standing for 60 minutes," the number of viable cells recovered was 1.33 x 10 6 cells (average of two tests).
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌60分、静置60分」を1セットとした条件で培養したときの総合評価は「B」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
When the culture was performed under one set of conditions, "agitation for 60 minutes, standing for 60 minutes," the overall evaluation was "B."
実施例8:静置培養工程において「攪拌180分、静置60分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は、実施例1と同様に行った。
Example 8: Production under one set of conditions in the static culture process: "180 minutes of stirring, 60 minutes of static culture" (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。
(1)の凍結細胞(P1)を解凍し、3×103cells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調整した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube, and then 1.4 mL of the required number of tubes was transferred. After leaving the tubes to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed, and 2 mL of Rooster Nourish medium (RoosterBio) was added in the required number of tubes. The microcarriers were thoroughly suspended, and added to Ambr15 bioreactors (Sartorius) in 2 mL/tube quantities. Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
The frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌180分、静置60分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of agitation, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. Subsequently, a cycle of "180 minutes of agitation, 60 minutes of standing" was repeated for seven days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌180分、静置60分」を1セットとした条件で培養したときの陽性率は、84%であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "180 minutes of stirring and 60 minutes of standing" was 84%.
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌180分、静置60分」を1セットとした条件で培養したときの回収生細胞数は、1.22×106cellsであった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "180 minutes of stirring and 60 minutes of standing," the number of viable cells recovered was 1.22 x 10 6 cells.
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌180分、静置60分」を1セットとした条件で培養したときの総合評価は「B」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
The overall evaluation when the culture was performed under one set of conditions of "180 minutes of stirring and 60 minutes of standing" was "B."
実施例9:静置培養工程において「攪拌120分、静置120分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は、実施例1と同様に行った。
Example 9: Production under conditions where one set of "120 minutes of stirring, 120 minutes of standing" was used in the static culture process (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
50mL遠沈管に、(2)で準備したマイクロキャリア溶液をよく懸濁したのち1.4mL×必要数分移した。5分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)2mL×必要数分を添加した。マイクロキャリアをよく懸濁し、Ambr15バイオリアクター(Sartorius)に、2mL/本ずつ添加した。50mL遠沈管にRoosterNourish培地を2mL×必要数分になるように添加し、Ambr15バイオリアクターに、2mL/本ずつ添加した。
(1)の凍結細胞(P1)を解凍し、3×103cells/cm2の密度で播種するため、RoosterNourish培地で15×104cells/mLに調整した。この細胞懸濁液を1mLずつ先に準備したAmbr15バイオリアクターに添加した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/5mL)。
(3) Seeding of synovial mesenchymal stem cells The microcarrier solution prepared in (2) was thoroughly suspended in a 50 mL centrifuge tube, and then 1.4 mL of the required number of tubes was transferred. After leaving the tubes to stand for about 5 minutes to allow the microcarriers to settle, the supernatant DPBS was removed, and 2 mL of Rooster Nourish medium (RoosterBio) was added in the required number of tubes. The microcarriers were thoroughly suspended, and added to Ambr15 bioreactors (Sartorius) in 2 mL/tube quantities. Rooster Nourish medium was added to 50 mL centrifuge tubes in an amount of 2 mL of the required number of tubes, and then added to Ambr15 bioreactors in 2 mL/tube quantities.
The frozen cells (P1) in (1) were thawed and adjusted to 15 x 10 cells/mL with Rooster Nourish medium to seed at a density of 3 x 10 cells/ cm . 1 mL of this cell suspension was added to the previously prepared Ambr15 bioreactors (microcarrier concentration per Ambr15 bioreactor: 0.14 g/5 mL).
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌120分、静置120分」のセットを7日間繰り返し行い、培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and a cycle of "5 minutes of agitation, 25 minutes of standing" was repeated six times, followed by the addition of 5 mL of Rooster Nourish medium. Subsequently, a cycle of "120 minutes of agitation, 120 minutes of standing" was repeated for 7 days, and the culture was carried out (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌120分、静置120分」を1セットとした条件で培養したときの陽性率は、91%であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured under one set of conditions of "120 minutes of stirring and 120 minutes of standing" was 91%.
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌120分、静置120分」を1セットとした条件で培養したときの回収生細胞数は、1.11×106cellsであった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
When cultured under one set of conditions of "120 minutes of stirring and 120 minutes of standing," the number of viable cells recovered was 1.11 x 10 6 cells.
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌120分、静置120分」を1セットとした条件で培養したときの総合評価は「B」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
When the culture was performed under one set of conditions, "120 minutes of stirring and 120 minutes of standing," the overall evaluation was "B."
比較例1:「攪拌のみ、静置なし」とした条件での製造
(1)滑膜幹細胞の入手、(2)マイクロキャリアの準備、および(3)滑膜間葉系幹細胞の播種は、実施例1と同様に行った。
Comparative Example 1: Production under the condition of "stirring only, no standing" (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 1.
(4)培養および評価
(4-1)培養
(3)で播種したAmbr15バイオリアクターをAmbr15にセットし、「5分攪拌、25分静置」のセットを6回繰り返したのち、RoosterNourish培地を5mL添加した。その後、「攪拌のみ、静置なし」という条件、すなわち静置攪拌培養を行わない条件にて7日間培養した(Ambr15バイオリアクター1つあたりのマイクロキャリア濃度0.14g/10mL)。攪拌速度は300rpmとした。また、マイクロキャリアの陽性率の評価のために行う培養4日目のサンプリング後に、Ambr15のプログラムにて培地交換を実施した。培地交換は、5分程度静置させ、キャリアと細胞を沈降させ、培養上清5mLを抜き取った。その後、攪拌を再開するタイミングでRoosterNourish培地を添加した。
(4) Cultivation and Evaluation (4-1) Cultivation The Ambr15 bioreactor seeded in (3) was set in the Ambr15, and the "5 minutes of agitation, 25 minutes of standing" cycle was repeated six times, after which 5 mL of Rooster Nourish medium was added. The cells were then cultured for 7 days under "stirring only, no standing," i.e., without static agitation culture (microcarrier concentration per Ambr15 bioreactor: 0.14 g/10 mL). The agitation speed was 300 rpm. Furthermore, after sampling on the fourth day of culture to evaluate the microcarrier positivity rate, medium exchange was performed using the Ambr15 program. The medium exchange was performed by standing for approximately 5 minutes, allowing the carriers and cells to settle, and 5 mL of culture supernatant was withdrawn. Then, Rooster Nourish medium was added when agitation was resumed.
(4-2)マイクロキャリアの陽性率の評価
実施例1と同様に評価を行った。
「攪拌のみ、静置なし」で培養したときの陽性率は、24%(3回の試験の平均値)であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 1.
The positive rate when cultured with "agitation only, no standing" was 24% (average of three tests).
(4-3)回収生細胞数の評価
実施例1と同様に評価を行った。
「攪拌のみ、静置なし」で培養したときの回収生細胞数は、0.976×106cells(2回の試験の平均値)であった。
(4-3) Evaluation of the Number of Recovered Viable Cells Evaluation was carried out in the same manner as in Example 1.
The number of viable cells recovered when the culture was performed with "stirring only, without standing" was 0.976 x 10 6 cells (average value of two tests).
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌のみ、静置なし」で培養したときの総合評価は「E」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
The overall evaluation when the culture was performed with "stirring only, without standing" was "E".
実施例10:攪拌静置培養工程において「攪拌5分、静置1435分」を1セットとした条件での製造
(1)滑膜幹細胞の入手、および(2)マイクロキャリアの準備は実施例1と同様に行った。
Example 10: Production under the conditions of "5 minutes of stirring and 1435 minutes of static culture" as one set in the stirring static culture process. (1) Obtaining synovial stem cells and (2) preparing microcarriers were carried out in the same manner as in Example 1.
(3)滑膜間葉系幹細胞の播種
実施例10と比較例2に使用する分をまとめて調製した。
500mLストレージボトルに、(2)で準備したマイクロキャリア溶液をよく懸濁したのち280mL移した。10分程度静置させ、マイクロキャリアを沈降させたのち、上清のDPBSを取り除き、RoosterNourish培地(RoosterBio)200mLを添加した。マイクロキャリアをよく懸濁し、浮遊細胞培養フラスコ225(住友ベークライト)4枚に等分した。500mLストレージボトルにRoosterNourish培地を32mL添加し、先の浮遊細胞培養フラスコ4枚に等分した。
(1)の凍結細胞(P1)を解凍し、2×103cells/cm2の密度で播種するため、RoosterNourish培地で0.5×107cells/2mLに調整した。この細胞懸濁液を2mLずつ先に準備した浮遊細胞培養フラスコに添加した(浮遊細胞培養フラスコ1枚あたりのマイクロキャリア濃度7g/60mL)。
(3) Seeding of synovial mesenchymal stem cells The amount to be used in Example 10 and Comparative Example 2 was prepared together.
The microcarrier solution prepared in (2) was thoroughly suspended and then 280 mL was transferred to a 500 mL storage bottle. After allowing the microcarriers to settle for approximately 10 minutes, the supernatant DPBS was removed and 200 mL of Rooster Nourish medium (RoosterBio) was added. The microcarriers were thoroughly suspended and divided equally among four suspension cell culture flasks 225 (Sumitomo Bakelite). 32 mL of Rooster Nourish medium was added to the 500 mL storage bottle and divided equally among the four suspension cell culture flasks.
The frozen cells (P1) in (1) were thawed and adjusted to 0.5 x 10 cells/2 mL with Rooster Nourish medium to seed at a density of 2 x 10 cells/ cm . 2 mL of this cell suspension was added to the previously prepared suspension cell culture flasks (microcarrier concentration per suspension cell culture flask: 7 g/60 mL).
(4)培養および評価
(4-1)培養
(3)で播種した浮遊細胞培養フラスコをインキュベーターに静置し、約24時間静置培養した。その後、あらかじめRoosterNourish培地800mLを入れ3時間程度平衡化(37℃、5%CO2(上面通気)、120rpm)をおこなったUniVessel SU 2L容器(Sartorius Stedim)中に、浮遊細胞培養フラスコで培養した細胞とキャリアの懸濁液を2枚分移液した。2枚の浮遊細胞培養フラスコをRoosterNourish培地で共洗いし、その溶液を2L容器に添加し、最終的に1Lまで培地が入った状態にした(2L容器あたりのマイクロキャリア濃度14g/1L)。これをBiostat B(Sartorius Stedim)にセットし、「攪拌5分、静置1435分」のセットを3日間繰り返し行い、3日目の静置培養開始から120分後攪拌のみの培養に切り換え、その後6日間培養した。攪拌速度は120rpmとした。2日目の静置培養開始から60分後にマイクロキャリア14gを追加した(2L容器あたりのマイクロキャリア濃度28g/1L)。マイクロキャリア14gを追加した直後に120rpmで2分ほど攪拌し、マイクロキャリアを混ぜた。培地交換は培養4日目および7日目に実施し、10分程度静置させ、キャリアと細胞を沈降させ、培養上清700mLを抜き取った。その後、RoosterNourish培地を700mL添加したのち攪拌を再開した。
(4) Cultivation and Evaluation (4-1) Cultivation The suspension cell culture flasks seeded in (3) were placed in an incubator and cultured for approximately 24 hours. Subsequently, two suspensions of cells and carriers cultured in the suspension cell culture flasks were transferred into UniVessel SU 2L containers (Sartorius Stedim) that had previously been equilibrated with 800 mL of Rooster Nourish medium for approximately 3 hours (37°C, 5% CO 2 (aeration from above), 120 rpm). The two suspension cell culture flasks were washed together with Rooster Nourish medium, and the solution was added to the 2L container, ultimately filling it to 1L with medium (microcarrier concentration of 14 g/1L per 2L container). This was set in a Biostat B (Sartorius Stedim) and the "5 minutes of stirring, 1435 minutes of static" setting was repeated for three days. On the third day, 120 minutes after the start of static culture, the culture was switched to stirring only, and culture was continued for six days. The stirring speed was 120 rpm. On the second day, 60 minutes after the start of static culture, 14 g of microcarriers were added (microcarrier concentration 28 g/1 L per 2 L container). Immediately after adding the 14 g of microcarriers, the microcarriers were mixed by stirring at 120 rpm for approximately 2 minutes. Medium changes were performed on the fourth and seventh days of culture. The medium was left to stand for approximately 10 minutes, the carriers and cells were allowed to settle, and 700 mL of culture supernatant was removed. Then, 700 mL of Rooster Nourish medium was added, and stirring was resumed.
(4-2)マイクロキャリアの陽性率の評価
培養4日目の細胞とマイクロキャリアを含む培養液を、2L容器のサンプルポートからシリンジを用いて10mLサンプリングした。これを100μL程度分取し、DPBSを400μL添加したのち、Nucblue(ThemoFisher Scientific)を1滴垂らし、37℃で15~30分間インキュベートした。以降は実施例1と同様に評価を行った。
「攪拌5分、静置1435分」を1セットとした条件で培養したときの陽性率は、80%であった。
(4-2) Evaluation of the positive rate of microcarriers On the fourth day of culture, 10 mL of the culture medium containing cells and microcarriers was sampled from the sample port of a 2 L container using a syringe. Approximately 100 μL of this was taken, and 400 μL of DPBS was added. One drop of Nucblue (ThermoFisher Scientific) was then added, and the mixture was incubated at 37°C for 15 to 30 minutes. Thereafter, evaluation was carried out in the same manner as in Example 1.
The positive rate was 80% when cultured under one set of conditions: "5 minutes of stirring, 1435 minutes of standing."
(4-3)回収生細胞数の評価
7日間培養したのち、細胞とマイクロキャリアを含む培養液10mLを、2L容器のサンプルポートからシリンジを用いて回収した。50mL遠沈管に100μmセルストレーナーをセットし、サンプリング溶液を全量ろ過した。セルストレーナー上に残った細胞+マイクロキャリアをDPBSで1回洗ったのち、TrypLE Select Enzyme(Gibco)でセルストレーナー上の細胞+マイクロキャリアを新しい50mL遠沈管1に回収した。50mL遠沈管1を半回転ローテーターにセットし、37℃下で30分間振とうした。50mL遠沈管1を回収し、100μmセルストレーナーをセットした新しい50mL遠沈管(2)に、50mL遠沈管1の内容物を全量ろ過した。RoosterNourish培地で、50mL遠沈管1およびセルストレーナー上のキャリアを共洗いした。50mL遠沈管(2)を遠心し、上清を除去したのち、RoosterNourish培地を加えて懸濁した。懸濁液を専用のカセットに充填し、NucleoCounter NC-202(エムセステクノシステムズ)にて細胞数をカウントした。細胞は、必要に応じてCTSTM Synth-a-FreezeTM Medium(Gibco)用いて凍結した。
「攪拌5分、静置1435分」を1セットとした条件で培養したときの回収生細胞数は、2.01×106cellsであった。
(4-3) Evaluation of the number of recovered viable cells After 7 days of culture, 10 mL of culture medium containing cells and microcarriers was collected from the sample port of a 2 L container using a syringe. A 100 μm cell strainer was placed on a 50 mL centrifuge tube, and the entire volume of the sampling solution was filtered. The cells and microcarriers remaining on the cell strainer were washed once with DPBS, and then the cells and microcarriers on the cell strainer were collected into a new 50 mL centrifuge tube 1 using TrypLE Select Enzyme (Gibco). The 50 mL centrifuge tube 1 was placed on a half-turn rotator and shaken at 37 °C for 30 minutes. The 50 mL centrifuge tube 1 was collected, and the entire contents of the 50 mL centrifuge tube 1 were filtered into a new 50 mL centrifuge tube (2) equipped with a 100 μm cell strainer. The 50 mL centrifuge tube 1 and the carrier on the cell strainer were washed together with Rooster Nourish medium. The 50 mL centrifuge tube (2) was centrifuged, the supernatant was removed, and Rooster Nourish medium was added to suspend the cells. The suspension was filled into a dedicated cassette, and the cell number was counted using a NucleoCounter NC-202 (MSESS Techno Systems). The cells were frozen using CTS ™ Synth-a-Freeze ™ Medium (Gibco) as needed.
When cultured under one set of conditions of "agitation for 5 minutes and standing for 1435 minutes," the number of viable cells recovered was 2.01 x 10 6 cells.
培養9日目には、2L容器を回収した。2L容器を10分程度静置させ、キャリアと細胞を沈降させたのち、培養上清を抜き取ったのち、細胞+マイクロキャリアをDPBSで1回洗った。キャリアと細胞を沈降させDPBSを抜き取り、剥離剤を添加し、細胞を剥離したのち、細胞数をカウントした(細胞数2)。 On the 9th day of culture, the 2L container was collected. The 2L container was left to stand for approximately 10 minutes to allow the carriers and cells to settle, after which the culture supernatant was removed and the cells + microcarriers were washed once with DPBS. The carriers and cells were allowed to settle, the DPBS was removed, a detachment agent was added, the cells were detached, and the cell number was counted (cell count 2).
上記の細胞数1と細胞数2を合わせた「攪拌5分、静置1435分」を1セットとした条件で培養したときの回収生細胞数は、5.65×108cellsであった。 When the above cell number 1 and cell number 2 were cultured under one set of conditions of "agitation for 5 minutes, standing for 1435 minutes", the number of viable cells recovered was 5.65 x 10 8 cells.
(4-4)総合評価
実施例1と同様に行った。
「攪拌5分、静置1435分」を1セットとした条件で培養したときの総合的評価は「A」であった。
(4-4) Overall Evaluation The overall evaluation was carried out in the same manner as in Example 1.
The overall evaluation when cultured under one set of conditions of "5 minutes of stirring and 1435 minutes of standing" was "A."
比較例2:「攪拌のみ、静置なし」とした条件での製造
(1)滑膜幹細胞の入手、(2)マイクロキャリアの準備、および(3)滑膜間葉系幹細胞の播種は、実施例10と同様に行った。
Comparative Example 2: Production under the condition of "stirring only, no standing" (1) Obtaining synovial stem cells, (2) preparing microcarriers, and (3) seeding synovial mesenchymal stem cells were carried out in the same manner as in Example 10.
(4)培養および評価
(4-1)培養
(3)で播種した浮遊細胞培養フラスコをインキュベーターに静置し、約24時間静置培養した。その後、あらかじめRoosterNourish培地800mLを入れ3時間程度平衡化(37℃、5%CO2(上面通気)、120rpm)をおこなったUniVessel SU 2L容器(Sartorius Stedim)中に、浮遊細胞培養フラスコで培養した細胞とキャリアの懸濁液を2枚分移液した。2枚の浮遊細胞培養フラスコをRoosterNourish培地で共洗いし、その溶液を2L容器に添加し、最終的に1Lまで培地が入った状態にした(2L容器あたりのマイクロキャリア濃度14g/1L)。これをBiostat B(Sartorius Stedim)にセットし、「攪拌のみ、静置なし」という条件、すなわち静置攪拌培養を行わない条件にて9日間培養した。攪拌速度は120rpmとした。2日目の培養途中にマイクロキャリア14gを追加した(2L容器あたりのマイクロキャリア濃度28g/1L)。マイクロキャリア14gの追加は、攪拌を停止後、2L容器を安全キャビネット内へ移して実施した。マイクロキャリア追加後は直ちにBiostat Bへセットし、攪拌を再開した。培地交換は培養4日目および7日目に実施し、10分程度静置させ、キャリアと細胞を沈降させ、培養上清700mLを抜き取った。その後、RoosterNourish培地を700mL添加したのち攪拌を再開した。
(4) Cultivation and Evaluation (4-1) Cultivation The suspension cell culture flasks seeded in (3) were placed in an incubator and cultured for approximately 24 hours. Subsequently, two suspensions of cells and carriers cultured in the suspension cell culture flasks were transferred into UniVessel SU 2L containers (Sartorius Stedim) that had previously been equilibrated with 800 mL of Rooster Nourish medium for approximately 3 hours (37°C, 5% CO 2 (aeration from above), 120 rpm). The two suspension cell culture flasks were washed together with Rooster Nourish medium, and the solution was added to the 2L container, ultimately filling it to 1L with medium (microcarrier concentration of 14 g/1L per 2L container). This was placed in a Biostat B (Sartorius Stedim) and cultured for 9 days under "agitation only, no standing" conditions, i.e., without static agitation culture. The agitation speed was 120 rpm. 14 g of microcarriers were added during the second day of culture (microcarrier concentration 28 g/1 L per 2 L container). The 14 g of microcarriers was added by stopping agitation and moving the 2 L container into a safety cabinet. After the microcarrier addition, the container was immediately placed in the Biostat B and agitation was resumed. The medium was replaced on the fourth and seventh days of culture. The container was left to stand for approximately 10 minutes, the carriers and cells were allowed to settle, and 700 mL of culture supernatant was removed. Then, 700 mL of Rooster Nourish medium was added, and agitation was resumed.
(4-2)マイクロキャリアの陽性率の評価
実施例10と同様に評価を行った。
「攪拌のみ、静置なし」で培養したときの陽性率は、24%であった。
(4-2) Evaluation of Positive Rate of Microcarriers Evaluation was carried out in the same manner as in Example 10.
The positive rate when cultured with "agitation only, no standing" was 24%.
(4-3)回収生細胞数の評価
実施例10と同様に評価を行った。
「攪拌のみ、静置なし」で培養したときの回収生細胞数は、1.61×106cellsであった。
(4-3) Evaluation of the number of recovered viable cells Evaluation was carried out in the same manner as in Example 10.
The number of viable cells recovered when the culture was performed with "stirring only, without standing" was 1.61 x 10 6 cells.
実施例10と同様に培養9日目には、2L容器を回収した。
細胞数1と細胞数2を合わせた「攪拌のみ、静置なし」で培養したときの回収生細胞数は、4.21×108cellsであった。
As in Example 10, on the 9th day of culture, the 2 L container was harvested.
When the cells 1 and 2 were cultured together under "stirring only, no standing", the number of viable cells recovered was 4.21 x 10 8 cells.
(4-4)総合評価
実施例1と同様に評価を行った。
「攪拌のみ、静置なし」で培養したときの総合評価は「E」であった。
(4-4) Overall Evaluation Evaluation was carried out in the same manner as in Example 1.
The overall evaluation when the culture was performed with "stirring only, without standing" was "E".
上記した実施例1~10および比較例1と2の結果のまとめを以下の表に示す。 The results of Examples 1 to 10 and Comparative Examples 1 and 2 described above are summarized in the table below.
<軟骨分化の評価>
実施例4および6の凍結細胞をウォーターバスにて融解し、αMEMに20%FBS(ThemoFisher Scientific)および1%Antibiotic-Antimycotic(x100)(ThemoFisher Scientific)を混合した培養液(非分化培地)入りの遠沈管に移した。遠心後、非分化培地で懸濁し、AO/PI Cell Viability Kit 9:1の割合で混ぜ、LUNAにて細胞数をカウントした。懸濁液を、2.5×105cells/1.5mL遠沈管×2本に分注し、遠心した。上清を除去したのち、一方の1.5mL遠沈管に1mLの軟骨分化培地(DMEM high glucose(ThemoFisher Scientific)、10ng/mL TGF-β3(富士フイルム和光純薬)、3.92μg/mL Dexamethason(富士フイルム和光純薬)、50μg/mL L-Asorbic Acis 2-Phosphate(Cayman Chemical)、40μg/mL L-プロリン(MP Biomedicals)、1mmol/L Sodium Pyruvate(Invitrogen)、100倍希釈ITS-Xサプリメント(x100)(富士フイルム和光純薬)、500ng/mL BMP-2(R&D Systems)混合溶液)を添加し、もう一方に非分化培地を1mL添加した。遠心し、細胞を沈降させたのち培養を開始した。培養2日目および7日目に培地交換を行い、14日目に評価した。ミクロスパーテルを用いて各スフェロイドを1.5mL遠沈管から取り出し、DPBS入りの1.5mLチューブに移した。スフェロイドを取り出し、ディッシュ上に置き、分析天秤(エー・アンド・デイ)にて重量を測定した。また、顕微鏡用マイクロルーラー(ケニス)をスフェロイド付近に設置し、コンパクトデジタルカメラ(OLYMPUS)にて撮影した。撮影画像から長径を測定した。
<Evaluation of cartilage differentiation>
The frozen cells from Examples 4 and 6 were thawed in a water bath and transferred to a centrifuge tube containing a culture medium (non-differentiation medium) prepared by mixing αMEM with 20% FBS (ThemoFisher Scientific) and 1% Antibiotic-Antimycotic (x100) (ThemoFisher Scientific). After centrifugation, the cells were suspended in non-differentiation medium and mixed with AO/PI Cell Viability Kit at a ratio of 9:1. The cell number was counted using LUNA. The suspension was dispensed into two 1.5 mL centrifuge tubes at 2.5 x 10 cells each and centrifuged. After removing the supernatant, one 1.5 mL centrifuge tube was filled with 1 mL of chondrogenic differentiation medium (DMEM high glucose (ThemoFisher Scientific), 10 ng/mL TGF-β3 (Fujifilm Wako Pure Chemical Industries), 3.92 μg/mL Dexamethasone (Fujifilm Wako Pure Chemical Industries), 50 μg/mL L-Asorbic Acid 2-Phosphate (Cayman Chemical), 40 μg/mL L-Proline (MP Biomedicals), 1 mmol/L Sodium Pyruvate (Invitrogen), 100-fold diluted ITS-X supplement (x100) (Fujifilm Wako Pure Chemical Industries), 500 ng/mL To one tube, 1 mL of a BMP-2 (R&D Systems) mixed solution was added, and 1 mL of non-differentiation medium was added to the other. After centrifugation to settle the cells, culture was initiated. Culture medium was replaced on days 2 and 7 of culture, and evaluation was performed on day 14. Each spheroid was removed from the 1.5 mL centrifuge tube using a microspatula and transferred to a 1.5 mL tube containing DPBS. The spheroid was removed, placed on a dish, and weighed using an analytical balance (A&D). A microscope microruler (Kennis) was placed near the spheroid, and images were taken with a compact digital camera (OLYMPUS). The major axis was measured from the captured images.
重量および長径の測定結果を下記表に示す。実施例4(攪拌95分、静置25分)、実施例6(攪拌1415分、静置25分)ともに、非分化検体と比較し、分化検体は重量、長径ともに大きく、軟骨様に分化した。 The results of measuring weight and major axis are shown in the table below. In both Example 4 (95 minutes of stirring, 25 minutes of standing) and Example 6 (1415 minutes of stirring, 25 minutes of standing), the differentiated specimens were larger in both weight and major axis than the undifferentiated specimens, and had differentiated into a cartilage-like structure.
上記の結果から、静置攪拌培養を行うことで、静置攪拌培養を行わない条件である「攪拌のみ、静置なし」と比較し、陽性率が上昇し、回収生細胞数が向上することが示された。また、静置攪拌培養を行うことで、培養した細胞は軟骨への分化能を有することが示された。 The above results show that static agitation culture increases the positive rate and the number of recovered viable cells compared to the "agitation only, no standing" condition, which does not involve static agitation culture. It was also shown that static agitation culture allows the cultured cells to differentiate into cartilage.
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