WO2019102593A1 - Cell culture device - Google Patents

Cell culture device Download PDF

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Publication number
WO2019102593A1
WO2019102593A1 PCT/JP2017/042251 JP2017042251W WO2019102593A1 WO 2019102593 A1 WO2019102593 A1 WO 2019102593A1 JP 2017042251 W JP2017042251 W JP 2017042251W WO 2019102593 A1 WO2019102593 A1 WO 2019102593A1
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WIPO (PCT)
Prior art keywords
culture
solution
unit
cell
tank
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PCT/JP2017/042251
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French (fr)
Japanese (ja)
Inventor
倫教 志田
浩介 石井
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株式会社Ihi
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Application filed by 株式会社Ihi filed Critical 株式会社Ihi
Priority to PCT/JP2017/042251 priority Critical patent/WO2019102593A1/en
Publication of WO2019102593A1 publication Critical patent/WO2019102593A1/en

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M1/00Apparatus for enzymology or microbiology
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M3/00Tissue, human, animal or plant cell, or virus culture apparatus

Definitions

  • the present disclosure relates to cell culture devices.
  • Patent Document 1 discloses a cell culture apparatus having a cell culture unit that performs three-dimensional culture, and a unit that sends various liquid chemicals, a culture solution, waste liquid, and the like.
  • This cell culture apparatus is an apparatus for culturing cells on a carrier suspended in a culture solution, and automatically performs operations such as medium replacement and passaging, which have conventionally been performed manually by workers.
  • a control unit is provided to control each unit in order to do so.
  • the present disclosure describes a cell culture device capable of efficiently performing cell culture of stem cells and the like and stably obtaining high-quality cultured cells.
  • a cell culture apparatus includes a culture vessel for performing three-dimensional culture of cells suspended in a culture solution, and a circulation for circulating the culture solution so that the culture solution forms an ascending flow in the culture vessel.
  • a culture unit including means, a cell distribution detection unit for detecting cell distribution in the culture tank, and a control unit for controlling the circulation rate of the culture fluid by the circulation means based on the cell distribution detected by the cell distribution detection unit And.
  • cell culture of stem cells and the like can be efficiently performed, and high quality cultured cells can be stably obtained.
  • a cell culture apparatus includes a culture vessel for performing three-dimensional culture of cells suspended in a culture solution, and a circulation for circulating the culture solution so that the culture solution forms an ascending flow in the culture vessel.
  • a culture unit including means, a cell distribution detection unit for detecting cell distribution in the culture tank, and a control unit for controlling the circulation rate of the culture fluid by the circulation means based on the cell distribution detected by the cell distribution detection unit And.
  • cells are suspended in a culture solution and cultured while being suspended in the culture solution by the balance between the upward flow by circulation means and dead weight.
  • the cell distribution detection unit can detect the balance between the upward flow by the circulating means and the weight of the cells by detecting the distribution of cells suspended in the culture solution in the culture tank.
  • the control unit can control the circulation rate of the culture solution by the circulation means to control the balance between the upward flow by the circulation means and the dead weight of the cells, and can appropriately maintain the cell distribution in the culture tank.
  • the cultured cells are excessively aggregated, and homogeneous culture is difficult. It could have been.
  • the cell distribution gradually changes due to a change in the size of a cell mass and the like in the culture process, it has been difficult to maintain the cell distribution at an appropriate position in the culture tank.
  • the cell distribution detection unit detects the cell distribution, and the control unit controls the circulation speed of the culture fluid based on the detection result. Also, even if the cell distribution changes due to changes in cell size etc during the culture process, the detection by the cell distribution detection unit and the control by the control unit regulate the balance between the upward flow by circulating means and the cell's own weight . For this reason, in the cell culture device according to the above aspect, it is possible to carry out homogeneous culture while appropriately maintaining the cell distribution.
  • the cell distribution detection unit includes turbidity measurement means for measuring the turbidity of the culture solution in the culture vessel at multiple points in the vertical direction.
  • the distribution of cells in the culture solution can be detected by the degree of turbidity measured at a plurality of measurement points.
  • the culture unit includes culture environment detection means for detecting the culture environment in the culture vessel, and culture environment adjustment means for adjusting the culture environment in the culture vessel.
  • culture environment detection means for detecting the culture environment in the culture tank by the culture environment detection means
  • culture environment adjustment means for adjusting the culture environment in the culture vessel.
  • the culture environment adjusting means may be controlled by the control unit, and the control unit may control the adjustment of the culture environment by the culture environment adjusting means based on the culture environment detected by the culture environment detecting means.
  • the cell culture apparatus recovers a culture fluid supply unit that supplies culture fluid to the culture unit, a washing solution supply unit that supplies the washing solution to the culture unit, and a waste liquid containing the culture fluid or the washing solution from the culture unit. And a waste liquid recovery unit.
  • operations such as culture medium exchange and passage in cell culture can be easily carried out by the operation of each unit.
  • control unit sends the culture solution from the culture solution supply unit to the culture unit, sends the washing solution from the wash solution supply unit to the culture unit, and discharges the waste solution from the culture unit to the waste solution recovery unit. Control each liquid transfer. In this case, operations such as culture medium exchange and passage in cell culture can be performed collectively by the control unit, and the operation can be automated.
  • the culture solution supply unit includes culture solution storage means for storing the culture solution at a predetermined temperature, and culture solution heating means for heating the culture solution to a temperature higher than or equal to a predetermined temperature.
  • the culture solution is stored at a temperature suitable for storage in the culture solution storage means, heated to a temperature suitable for culture in the culture solution heating means, and supplied to the culture tank.
  • the culture solution stored in the culture solution storage unit can be used by heating it by the culture solution heating unit, so that the culture solution can be replenished from outside the apparatus
  • the work procedure is simplified compared to the case of
  • the cell culture apparatus further comprises fluid volume detection means for detecting the fluid volume of the culture fluid in the culture vessel, and the control unit is based on the fluid volume detected by the fluid volume detection means. And controlling the transfer of the culture solution from the culture solution supply unit to the culture unit.
  • the liquid volume detection means detects the liquid volume in the culture tank, and the culture solution is supplied into the culture tank under the control of the control unit based on the detection result. Thereby, the supply amount of the culture solution is precisely controlled, and the adverse effect on the cultured cells due to the large amount of the supply amount of the culture solution can be avoided.
  • the cell culture apparatus further comprises an enzyme supply unit that supplies an enzyme solution containing an enzyme to the culture unit, and the control unit controls transfer of the enzyme solution from the enzyme supply unit to the culture unit. Do. In this case, the control unit can easily supply the required amount of enzyme solution to the culture unit at the required timing.
  • the enzyme supply unit comprises an enzyme storage means for storing the enzyme solution at a predetermined temperature.
  • the enzyme solution is thereby stored at a temperature suitable for storage.
  • the cell culture apparatus further comprises a dissolved oxygen amount detection means for detecting the amount of dissolved oxygen in the culture fluid circulating in the culture unit, and the culture unit supplies oxygen to the culture fluid.
  • the control unit further controls the supply amount of oxygen by the oxygen supply unit based on the dissolved oxygen amount detected by the dissolved oxygen amount detection unit. In this case, since the necessary amount of oxygen is supplied to the culture solution by the control of the control unit, it is possible to easily carry out cell culture maintaining a fixed amount of dissolved oxygen.
  • the cell culture apparatus further comprises pH detection means for detecting the pH of the culture solution in the culture vessel, and the control unit controls the culture solution based on the pH detected by the pH detection means. Determine the replacement time and notify the user or replace the culture solution.
  • the pH detection means detects a change in pH of the culture solution, and the control unit automatically determines the culture solution replacement time based on the detection result. Etc. are prevented.
  • the control unit may notify the user of the replacement time via an interface unit or the like. Further, the control unit may automatically exchange the culture solution after the determination of the replacement time by controlling the culture solution supply unit, the washing solution supply unit, and the waste solution supply unit described above.
  • the cell culture apparatus may further comprise an inhibitor supply unit that supplies Rho kinase inhibitor to the culture unit, and the control unit controls the concentration of Rho kinase inhibitor in the culture solution in the culture vessel.
  • the amount of Rho kinase inhibitor supplied by the inhibitor supply unit is controlled so as to achieve a predetermined concentration.
  • the control unit can easily supply the necessary amount of Rho kinase inhibitor to the culture unit at the necessary timing.
  • the inhibitor delivery unit comprises an inhibitor storage means for storing the Rho kinase inhibitor at a predetermined temperature. This causes the Rho kinase inhibitor to be stored at a temperature suitable for storage.
  • the cell culture apparatus further comprises a drug solution supply unit for supplying a drug solution to the culture unit, and the control unit controls the delivery of the drug solution from the drug solution supply unit to the culture unit.
  • the control unit can easily supply the necessary amount of drug solution to the culture unit at the required timing.
  • the chemical solution supply unit includes chemical solution storage means for storing the chemical solution at a predetermined temperature. Thereby, the drug solution is stored at a temperature suitable for storage.
  • the cell culture apparatus further includes: a cell collection unit for photographing that collects a part of cells from the culture unit; and a photographing unit that acquires a micrograph of the cells collected by the cell collection unit for photographing.
  • a cell collection unit for photographing that collects a part of cells from the culture unit
  • a photographing unit that acquires a micrograph of the cells collected by the cell collection unit for photographing.
  • control unit controls the collection of cells by the imaging cell collection unit and the acquisition of photomicrographs by the imaging unit.
  • control unit can easily (possibly automatically) acquire a micrograph at a desired timing.
  • the cell culture apparatus 1 includes a culture vessel 11 for performing three-dimensional culture of cells suspended in a culture solution F1, and a circulation pump 12 for circulating the culture solution F1 so that the culture solution F1 forms an upward flow in the culture vessel. And an oxygen supply tank 13 provided in the middle of circulation of the culture solution F1 and supplying oxygen to the culture solution F1.
  • a culture unit is constituted by the culture tank 11, the circulation pump 12, the oxygen supply tank 13, and a line (a pipe or a pipe) connecting these to each other.
  • the culture tank 11 and the oxygen supply tank 13 are connected by the first circulation line L1, and the culture fluid F1 extracted from the upper portion of the culture tank 11 is fed to the oxygen supply tank 13 via the first circulation line L1. Be liquid.
  • the oxygen supply tank 13 and the circulation pump 12 are connected by the second circulation line L2, and the culture fluid F1 supplied with oxygen as necessary in the oxygen supply tank 13 is connected via the second circulation line L2.
  • the fluid is sent to the circulation pump 12.
  • the circulation pump 12 and the culture tank 11 are connected by the third circulation line L3, and the culture fluid F1 sent from the circulation pump 12 is supplied to the lower part of the culture tank 11 through the third circulation line L3. Be done.
  • the culture fluid F1 supplied via the third circulation line L3 moves upward from the lower part to the upper part of the culture tank 11 and is transferred out of the culture tank 11 from the first circulation line L1. .
  • the cell culture apparatus 1 is provided with a turbidimeter 15 which measures the turbidity of the culture solution F1 in the culture tank 11 at a plurality of locations in the vertical direction.
  • the turbidimeter 15 detects the cell distribution in the culture solution F1 in the culture tank 11.
  • the cell distribution detection unit is not limited to this, and includes, for example, a camera for acquiring an image of the culture fluid F1 and the like. Good.
  • the cell culture device 1 is provided with a micro bubble pump 14 as an auxiliary means for assisting the supply of oxygen to the culture fluid F1 in the oxygen supply tank 13.
  • the micro bubble pump 14 is connected to the oxygen supply tank 13 via a fourth circulation line L4 branched from the second circulation line L2 and a fifth circulation line L5 connected to the first circulation line L1.
  • a portion of the culture fluid F1 passing through the second circulation line L2 is sent to the microbubble pump 14 via the fourth circulation line L4, and the microbubble pump 14 feeds the fifth circulation line L5 and the first circulation line L1. It is returned to the oxygen supply tank 13 via
  • the micro bubble pump 14 generates micro bubbles in the culture fluid F1 and promotes the dissolution of oxygen in the culture fluid F1.
  • the cell culture apparatus 1 is equipped with the dissolved oxygen meter 16 which detects the dissolved oxygen amount in the culture solution F1 in the culture tank 11. As shown in FIG.
  • the dissolved oxygen meter 16 may detect the amount of dissolved oxygen before starting the culture, may constantly detect the amount of dissolved oxygen during the culture, and may detect the amount of dissolved oxygen at predetermined intervals during the culture.
  • the cell culture apparatus 1 further includes a pH meter 17 that detects the pH of the culture solution F1 in the culture tank 11.
  • the pH meter 17 may detect the pH before the start of the culture, may constantly detect the pH during the culture, and may detect the pH at predetermined intervals during the culture. The result of detection of pH by a pH meter can be used as a criterion of the replacement time of the culture fluid F1.
  • the culture tank 11 is disposed in an incubator 21 for keeping the culture environment in the culture tank 11 constant.
  • the incubator 21 adjusts and maintains the inside to a predetermined culture environment (for example, a temperature of 35 to 38 ° C., a carbon dioxide concentration of 5%), and prevents the culture environment from being changed by the external environment.
  • the oxygen supply tank 13 is also disposed in the incubator in order to avoid the temperature change of the culture solution F1 with oxygen supply.
  • the cell culture apparatus 1 may be provided with a thermometer 22 for measuring the temperature in the culture tank 11 or the temperature of the culture fluid F1 in the culture tank 11. In this case, the inside of the culture tank 11 is a predetermined culture by the thermometer 22. It can be confirmed that the environment is adjusted and maintained.
  • the cell culture apparatus 1 may further include detection means for detecting a culture environment other than temperature.
  • the cell culture apparatus 1 connects the culture solution storage tank 31 for storing the culture solution F1, the culture solution heating tank 32 for heating the culture solution F1, the culture solution storage tank 31, and the culture solution heating tank 32.
  • a culture fluid delivery line L6 is further provided, and a culture fluid delivery pump 33 is provided in the culture fluid delivery line L6.
  • the culture solution F1 stored in the culture solution storage tank 31 is transferred to the culture solution heating tank 32 via the culture solution supply line L6 as necessary, and culture is performed in the culture solution heating tank 32. It is warmed to a suitable temperature.
  • the culture fluid F1 heated in the culture fluid heating tank 32 is fed from the culture fluid heating tank 32 via the heated culture fluid delivery line L7 connecting the culture fluid heating tank 32 and the culture tank 11. The liquid is sent to the culture tank 11.
  • the culture solution storage tank 31 and the culture solution delivery line L6 are connected via the aseptic connector 34. As a result, when the culture solution storage tank 31 is replaced, it is possible to easily maintain the aseptic condition after the culture solution delivery line L6.
  • the culture solution storage tank 31 is disposed in the refrigeration unit 35.
  • the refrigeration unit 35 maintains the culture solution storage tank 31 at a temperature (for example, 2 to 6 ° C.) suitable for storage of the culture solution F1.
  • the culture solution heating tank 32 is disposed in the incubator 21, and the incubator 21 heats the culture solution F1 in the culture solution heating tank 32 to a temperature (for example, 35 to 38 ° C.) suitable for culture.
  • the cell culture apparatus 1 further includes a cell recovery line L8 serving as a recovery path for recovering cells cultured in the culture tank 11.
  • the cell recovery line L8 is provided with a cell recovery pump 41.
  • a sterile connector 42 is provided at the outlet of the cell collection line L8, and can be aseptically connected to the cell collection vial 43.
  • the cultured cells can be recovered by circulating the cells from the inside of the culture tank 11 to the cell recovery line L8 by the operation of the cell recovery pump 41.
  • the cell culture apparatus 1 further includes a washing solution storage tank 51 for storing the washing solution F 2, and a washing solution sending pump 52 for sending the washing solution F 2 from the washing solution storage tank 51 to the culture tank 11.
  • the washing solution storage tank 51 is connected to the culture tank 11 through the washing solution feeding line L9, and the washing solution F2 stored in the washing solution storage tank 51 is fed by the washing solution feeding pump 52 as needed. Is sent to the culture tank 11 via the The washing solution feed line L9 is connected to the third circulation line L3 which is a circulation route of the culture unit, and the washing solution F2 is sent to the culture tank 11 via the washing solution feed line L9 and the third circulation line L3. After being optionally circulated in the circulation route of the culture unit, it is discharged from the culture unit as waste liquid.
  • the cleaning solution storage tank 51 and the cleaning solution supply line L9 are connected via the aseptic connector 53. Thus, when replacing the cleaning solution storage tank 51, the aseptic condition after the cleaning solution supply line L9 can be easily maintained.
  • the washing solution F2 is not particularly limited, and may be a known washing solution used for cell culture.
  • the washing solution F2 may be Phosphate Buffered Salin (PBS).
  • PBS Phosphate Buffered Salin
  • the washing solution F2 may be a basal medium or the like suitable for cells to be cultured.
  • DMEM, F-12, RPMI and the like are representative media.
  • the cell culture apparatus 1 further includes a waste liquid storage tank 61 for storing the waste liquid F3 collected from the culture unit.
  • the cell culture apparatus 1 also connects a first waste liquid line L10 connecting the culture tank 11 and the waste liquid storage tank 61 as a first waste liquid path, and connects an oxygen supply tank 13 and a waste liquid storage tank 61 as a second waste liquid path.
  • the second waste liquid line L11 is provided.
  • the first waste liquid line L10 is provided with a first waste liquid pump 62 for feeding the waste liquid discharged from the culture tank 11 to the waste liquid storage tank 61, and the second waste liquid line L11 is discharged from the oxygen supply tank 13
  • a second waste liquid pump 63 is provided to feed the waste liquid to the waste liquid storage tank 61.
  • the first waste liquid line L10 and the second waste liquid line L11 join together before reaching the waste liquid storage tank 61, and are connected to the waste liquid storage tank 61 via the aseptic connector 64.
  • the sterile connector 64 allows the waste liquid storage tank 61 to be replaced while easily maintaining the aseptic condition of the first waste liquid line L10 and the second waste liquid line L11.
  • the waste solution stored in the waste solution storage tank 61 may be a waste solution containing a culture solution or a washing solution, for example, a used culture solution at the time of culture medium replacement, a used culture solution discarded before cell recovery or passage. It may be a waste liquid or the like generated after the cleaning with the cleaning liquid.
  • the cell culture apparatus 1 further includes an enzyme solution storage tank 71 for storing an enzyme solution F4 containing an enzyme, and an enzyme solution delivery pump 72 for transferring the enzyme solution F4 from the enzyme solution storage tank 71 to the culture tank 11 There is.
  • the enzyme solution storage tank 71 is connected to the culture tank 11 via the enzyme solution feed line L12, and the enzyme solution F4 stored in the enzyme solution storage tank 71 is optionally sent by the enzyme solution feed pump 72.
  • the liquid is fed to the culture tank 11 via the enzyme liquid feed line L12.
  • the enzyme solution storage tank 71 and the enzyme solution delivery line L12 are connected via the aseptic connector 73, whereby when replacing the enzyme solution storage tank 71, the sterile condition after the enzyme solution delivery line L12 can be easily maintained. it can.
  • the enzyme solution storage tank 71 is disposed in the refrigeration unit 35, and is held together with the culture solution storage tank 31 under a predetermined temperature (for example, 2 to 6 ° C.).
  • a predetermined temperature for example, 2 to 6 ° C.
  • the enzyme solution storage tank 71 is maintained at a temperature different from that of the culture solution storage tank 31 in the refrigeration unit 35. It may well be arranged in another refrigeration unit different from the refrigeration unit 35.
  • the enzyme may be a known drug used for cell dispersion.
  • enzymes include Accutase, Trypsin-EDTA, Dispase, and Collagenase.
  • a drug having a function of cell dispersion may be used. Such agents include EDTA solution and the like.
  • the cell culture apparatus 1 further includes an inhibitor storage tank 81 for storing Rho kinase inhibitor, and an inhibitor delivery pump 82 for transferring Rho kinase inhibitor to the culture tank 11 from the inhibitor storage tank 81.
  • the inhibitor storage tank 81 is connected to the culture tank 11 via the inhibitor delivery line L13, and the Rho kinase inhibitor stored in the inhibitor storage tank 81 is an inhibitor delivery pump 82 as needed.
  • the liquid is fed to the culture tank 11 via the inhibitor delivery line L13.
  • the inhibitor storage tank 81 and the inhibitor delivery line L13 are connected via the aseptic connector 83, whereby when the inhibitor storage tank 81 is replaced, the sterility of the inhibitor delivery line L13 and thereafter can be easily maintained. it can.
  • the inhibitor storage tank 81 is disposed in the refrigeration unit 35, and is held together with the culture solution storage tank 31 under a predetermined temperature (for example, 2 to 6 ° C.).
  • a predetermined temperature for example, 2 to 6 ° C.
  • the inhibitor storage tank 81 is maintained at a temperature different from that of the culture fluid storage tank 31 in the refrigeration unit 35. It may be disposed in another refrigeration unit different from the refrigeration unit 35.
  • the cell culture apparatus 1 further includes a drug solution storage tank 91 for storing a drug solution, and a drug solution sending pump 92 for sending a drug solution from the drug solution storage tank 91 to the culture tank 11.
  • the chemical solution storage tank 91 is connected to the culture tank 11 via the chemical solution delivery line L14, and the chemical solution stored in the chemical solution storage tank 91 is transferred by the chemical solution delivery pump 92 as needed.
  • the liquid is sent to the culture tank 11 via
  • the drug solution storage tank 91 and the drug solution sending line L14 are connected via the aseptic connector 93, whereby when replacing the drug solution storage tank 91, it is possible to easily maintain the aseptic condition of the drug solution sending line L14 and thereafter.
  • the chemical solution storage tank 91 is disposed in the refrigeration unit 35, and is held together with the culture solution storage tank 31 under a predetermined temperature (for example, 2 to 6 ° C.).
  • a predetermined temperature for example, 2 to 6 ° C.
  • the drug solution storage tank 91 may be kept at a temperature different from that of the culture solution storage tank 31 in the refrigeration unit 35, It may be disposed in another refrigeration unit different from the unit 35.
  • the drug solution may be a known drug solution used for cell culture.
  • the drug solution may be an agent related to maintenance of undifferentiation such as cytokine, promotion of differentiation, activation, etc., and includes Activin, b-FGF, SCF, TGF-beta and the like.
  • the cell culture apparatus 1 further includes an imaging unit 101, and a liquid transfer line L15 for imaging which is branched from the cell collection line L8 and connected to the imaging unit 101.
  • the imaging liquid supply line L15 includes the imaging unit A photographing liquid-sending pump 102 is provided for feeding a measurement sample containing cells at 101. Further, a buffer tank 103 for storing a shooting buffer F5 is connected to the shooting unit 101.
  • the imaging unit 101 images the measurement sample fed by the imaging liquid feed pump 102, and obtains a micrograph of the cells contained in the measurement sample. The measurement sample after obtaining the microphotograph may be discarded from the imaging unit 101 as a waste liquid.
  • the measurement sample after obtaining the microphotograph may be sent to the cell collection line L8 via the imaging liquid supply line L15 and collected in the cell collection vial 43.
  • the imaging liquid transfer pump 102 may play a role of transporting the measurement sample from the imaging unit 101 to the cell recovery line L8.
  • the imaging unit 101 and the buffer tank 103 are disposed in the incubator 21 and maintained at a predetermined temperature (for example, 35 to 38 ° C.) in order to observe the cell state in the culture environment more accurately.
  • the cell culture apparatus 1 further includes a controller 111 as a control unit.
  • the controller 111 acquires information on the turbidity detected by the turbidity meter 15, controls the circulation pump 12 based on the information on the turbidity, and adjusts the circulation speed of the culture fluid F1.
  • the controller 111 acquires detection information (input value) relating to turbidity from the turbidity meter 15 (step S01).
  • the turbidity meter 15 measures the turbidity of the culture solution F1 in the culture tank 11 at a plurality of locations in the vertical direction, and the controller 111 receives information detected at each location.
  • the controller 111 converts the plurality of input values from the turbidity meter 15 into predetermined engineering values (step S02).
  • step S02 may be omitted.
  • the controller 111 compares the turbidity of the culture fluid F1 in the culture tank 11 in the vertical direction based on the plurality of acquired engineering values (step S03), and creates a turbidity distribution (step S04). Among the plurality of measurement positions by the wattmeter 15, the measurement position at which the turbidity is maximum is extracted (step S05). By these steps, the controller 111 obtains information of cell distribution in the culture solution F1 in the culture tank 11.
  • the controller 111 determines the circulation speed of the culture fluid F1 and controls the circulation pump 12 based on the information of the obtained cell distribution. Specifically, first, based on the relationship between the position where cells should be distributed in culture fluid F1 and the measurement position by turbidity meter 15, the circulating speed is increased by a predetermined amount for each measurement position. Setting to decrease the circulation speed by a predetermined decrease amount or to maintain the circulation speed. The controller 111 refers to this setting and determines whether or not the measurement position of the object (for example, the measurement position of the maximum turbidity extracted in step S05) is the speed increase setting (step S06).
  • step S06 determines that the speed increase setting is made (step S06: YES)
  • the controller 111 refers to the set increase amount to temporarily determine the increase amount of the circulation speed (step S07). If it is determined that the speed increase setting is not set (step S06: NO), the controller 111 determines whether the target measurement position is the speed decrease setting (step S08), and if it is determined that the speed decrease setting is Step S08: YES) With reference to the set descent amount, the descent amount of the circulating speed is temporarily determined (step S09).
  • the controller 111 uses the increase amount temporarily determined in step S07 or the decrease amount temporarily determined in step S08, and the initial circulation speed (the circulation speed before execution of the circulation speed control), a provisional value of the circulation speed after circulation ( The circulation speed before the execution + the increase amount, or the circulation speed before the execution ⁇ the decrease amount) is calculated (step S10). If it is determined in step S08 that the speed reduction setting is not set (step S08: NO), the initial circulation speed is calculated as a temporary value of the circulation speed after control.
  • the controller 111 determines whether the calculated temporary value exceeds the upper limit value of the circulation rate in the cell culture device 1 (step S11). If the controller 111 determines that the provisional value exceeds the upper limit (step S11: YES), it replaces the provisional value with the upper limit (step S12). When the controller 111 determines that the temporary value does not exceed the upper limit (step S11: NO), it then determines whether the temporary value is less than the lower limit (step S13). If the controller 111 determines that the temporary value is less than the lower limit value (step S13: YES), the temporary value is replaced with the lower limit value (step S14).
  • step S14 determines that the temporary value is not less than the lower limit (step S14: NO)
  • the temporary value is maintained.
  • the controller 111 determines the temporary value set through steps S11 to S14 as the circulation speed after control (step S15).
  • the controller 111 controls the circulation pump 12 based on the determined circulation speed (step S16).
  • the execution procedure of the circulation speed control by the controller 111 is not limited to the above, and the circulation pump 12 may be controlled based on the detection result by the turbidity meter 15. Moreover, the controller 111 may further acquire information measured from a meter other than the turbidity meter 15 and may further control a pump other than the circulation pump 12.
  • the controller 111 may acquire the detection result of the dissolved oxygen meter 16 and control the micro bubble pump 14 based on the acquired detection result.
  • the controller 111 reduces the amount of microbubbles generated by the microbubble pump 14 when the amount of dissolved oxygen detected by the dissolved oxygen meter 16 exceeds the predetermined value so that the predetermined value of the amount of dissolved oxygen is maintained. If the amount of dissolved oxygen detected by the total 16 is less than the specified value, the amount of microbubbles generated by the microbubble pump 14 may be increased.
  • the controller 111 may acquire the detection result of the pH meter 17, determine the replacement time of the culture fluid F1 based on the acquired detection result, and notify the user or exchange the culture fluid F1.
  • the controller 111 may control the culture solution delivery pump 33, the washing solution delivery pump 52, the first waste solution pump 62, and the second waste solution pump 63, respectively.
  • the controller 111 can control each pump according to its own judgment or a user's instruction, and can perform operations such as culture medium replacement and passage.
  • the cell culture apparatus 1 may further include a liquid volume detector (not shown) for detecting the liquid volume of the culture fluid F1 in the culture tank 11, and the controller 111 acquires the detection result of the liquid volume detector. Then, on the basis of the acquired detection result, the amount of culture solution delivered by the culture solution delivery pump 33 may be controlled.
  • the controller 111 can control the cell recovery pump 41.
  • the controller 111 automatically performs the cell recovery pump 41 (in addition, if necessary, the culture fluid delivery pump 33, the washing solution delivery pump 52, the first waste solution pump 62, And the second waste liquid pump 63) to automatically collect the cells.
  • the controller 111 may control the enzyme solution delivery pump 72, and in this case, the enzyme solution F4 can be delivered to the culture tank 11 based on the user's instruction or the previous setting.
  • the controller 111 may control the inhibitor delivery pump 82, and in this case, the Rho kinase inhibitor can be delivered to the culture tank 11 based on the user's instruction or the previous setting.
  • the controller 111 may control the chemical solution delivery pump 92, and in this case, the chemical solution can be delivered to the culture tank 11 based on the user's instruction or the previous setting.
  • the controller 111 may control the liquid supply pump 102 for imaging, and in this case, the measurement sample can be supplied to the imaging unit 101 based on a user's instruction or a prior setting.
  • the controller 111 may control the photographing of the microphotograph by the photographing unit 101, and in this case, the microphotograph of the cell can be automatically acquired based on the user's instruction or the prior setting.
  • cells are suspended in the culture fluid F1, and are cultured while being suspended in the culture fluid F1 due to the balance between the upward flow of the culture fluid F1 and its own weight.
  • the controller 111 controls the circulation speed of the culture fluid F1 by the circulation pump 12 to adjust the equilibrium state between the upward flow of the culture fluid F1 and the dead weight of the cells, and appropriately maintain the cell distribution in the culture tank 11 it can.
  • the turbidimeter 15 detects the turbidity of the culture fluid F1 in the culture tank 11, and the controller 111 controls the circulation speed in the above execution procedure.
  • the controller 111 can automatically adjust the equilibrium state between the upward flow of the culture fluid F1 and the weight of the cell. For this reason, in the cell culture apparatus 1, homogeneous distribution can be performed while maintaining the cell distribution appropriately.
  • the turbidimeter 15 measures the turbidity of the culture solution F1 in the culture tank 11 in multiple places of the perpendicular direction.
  • the turbidity of the culture solution F1 increases.
  • the cell distribution gradually moves downward in the vertical direction due to its own weight. According to the above-mentioned turbidimeter 15, it also becomes possible to monitor these culture conditions.
  • the dissolved oxygen amount of the culture solution F1 is detected by the dissolved oxygen meter 16, and the controller 111 can control the micro bubble pump 14 based on the detection result. For this reason, in the cell culture apparatus 1, cell culture which maintained a fixed amount of dissolved oxygen can be easily implemented by control of the controller 111.
  • the pH meter 17 detects the pH of the culture fluid F1, and the controller 111 determines the replacement time of the culture fluid F1 based on the detection result, and notifies the user or the culture fluid F1 is exchanged. Can do In such a cell culture apparatus 1, the controller 111 automatically determines the replacement time of the culture solution F1 and prevents the deterioration of the cultured cells due to the passing of the replacement time.
  • the controller 111 can control the culture solution delivery pump 33, the washing solution delivery pump 52, the first waste solution pump 62, and the second waste solution pump 63. For this reason, in the cell culture apparatus 1, operations such as replacement of the culture fluid F1 and passage can be performed automatically according to the determination of the controller 111 or the instruction of the user.
  • the controller 111 can control the enzyme solution delivery pump 72, the inhibitor delivery solution pump 82, and the chemical solution delivery pump 92. For this reason, in the cell culture apparatus 1, the enzyme solution, the Rho kinase inhibitor and the drug solution can be automatically supplied to the culture tank 11 at the amount and timing set in advance by the control of the controller 111.
  • the culture vessel 11 may have a frusto-conical shape in which the cross-sectional area in the horizontal direction increases from the bottom toward the top. As a result, a velocity gradient is provided to the upflow, and the correlation between the circulation velocity and the cell distribution becomes remarkable.
  • cell culture of stem cells and the like can be performed efficiently, and high quality cultured cells can be stably obtained.

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Abstract

A cell culture device which comprises: a culture unit comprising a culture tank for three-dimensionally culturing cells suspended in a culture solution and a circulation means for circulating the culture solution so that an upward flow of the culture solution is generated in the culture tank; a cell distribution detection unit detecting the cell distribution in the culture tank; and a control unit controlling the circulation speed of the culture solution by the circulation means depending on the cell distribution detected by the cell distribution detection unit.

Description

細胞培養装置Cell culture device
 本開示は、細胞培養装置に関する。 The present disclosure relates to cell culture devices.
 細胞培養装置として、例えば、特許文献1には、三次元培養を行う細胞培養ユニットと、各種の薬液、培養液、廃液等を送液するユニットとを有する細胞培養装置が開示されている。この細胞培養装置は、培養液中に懸濁した担体上で細胞を培養するための装置であり、従来は作業者の手作業で実施していた培地交換、継代等の作業を自動的に行うために、各ユニットを制御する制御ユニットが設けられている。 As a cell culture apparatus, for example, Patent Document 1 discloses a cell culture apparatus having a cell culture unit that performs three-dimensional culture, and a unit that sends various liquid chemicals, a culture solution, waste liquid, and the like. This cell culture apparatus is an apparatus for culturing cells on a carrier suspended in a culture solution, and automatically performs operations such as medium replacement and passaging, which have conventionally been performed manually by workers. A control unit is provided to control each unit in order to do so.
特開2015-136330号公報JP, 2015-136330, A
 近年、医療分野への応用が拡大したことで、細胞培養装置には、培養の効率化や、得られる培養細胞の高品質化及び均質化が求められている。 In recent years, as the application to the medical field has been expanded, in the cell culture apparatus, there are demands for more efficient culture and higher quality and homogenization of the obtained cultured cells.
 本開示は、幹細胞等の細胞培養を効率良く実施し、高品質な培養細胞を安定して得ることが可能な細胞培養装置を説明する。 The present disclosure describes a cell culture device capable of efficiently performing cell culture of stem cells and the like and stably obtaining high-quality cultured cells.
 本開示の一態様に係る細胞培養装置は、培養液中に懸濁した細胞の三次元培養を行う培養槽、及び、培養槽内で培養液が上昇流を成すように培養液を循環させる循環手段を含む培養ユニットと、培養槽内の細胞分布を検出する細胞分布検出ユニットと、細胞分布検出ユニットで検出された細胞分布に基づいて、循環手段による培養液の循環速度を制御する制御ユニットと、を備える。 A cell culture apparatus according to one aspect of the present disclosure includes a culture vessel for performing three-dimensional culture of cells suspended in a culture solution, and a circulation for circulating the culture solution so that the culture solution forms an ascending flow in the culture vessel. A culture unit including means, a cell distribution detection unit for detecting cell distribution in the culture tank, and a control unit for controlling the circulation rate of the culture fluid by the circulation means based on the cell distribution detected by the cell distribution detection unit And.
 本開示の一態様に係る細胞培養装置によれば、幹細胞等の細胞培養を効率良く実施し、高品質な培養細胞を安定して得ることができる。 According to the cell culture apparatus according to one aspect of the present disclosure, cell culture of stem cells and the like can be efficiently performed, and high quality cultured cells can be stably obtained.
本開示の一実施形態に係る細胞培養装置の概略構成を示す図である。It is a figure showing a schematic structure of a cell culture device concerning one embodiment of this indication. 図1の細胞培養装置における循環速度制御の実行手順を示すフローチャートである。It is a flowchart which shows the execution procedure of circulation rate control in the cell culture apparatus of FIG.
 本開示の一態様に係る細胞培養装置は、培養液中に懸濁した細胞の三次元培養を行う培養槽、及び、培養槽内で培養液が上昇流を成すように培養液を循環させる循環手段を含む培養ユニットと、培養槽内の細胞分布を検出する細胞分布検出ユニットと、細胞分布検出ユニットで検出された細胞分布に基づいて、循環手段による培養液の循環速度を制御する制御ユニットと、を備える。 A cell culture apparatus according to one aspect of the present disclosure includes a culture vessel for performing three-dimensional culture of cells suspended in a culture solution, and a circulation for circulating the culture solution so that the culture solution forms an ascending flow in the culture vessel. A culture unit including means, a cell distribution detection unit for detecting cell distribution in the culture tank, and a control unit for controlling the circulation rate of the culture fluid by the circulation means based on the cell distribution detected by the cell distribution detection unit And.
 この細胞培養装置では、細胞は培養液中に懸濁しており、循環手段による上昇流と自重との均衡によって培養液中に浮遊しながら培養される。細胞分布検出ユニットは、培養槽内の培養液中に浮遊する細胞の分布を検出することで、循環手段による上昇流と細胞の自重との均衡状態を検知することができる。制御ユニットは、循環手段による培養液の循環速度を制御することで、循環手段による上昇流と細胞の自重との均衡状態を調節し、培養槽内における細胞分布を適切に保持できる。 In this cell culture apparatus, cells are suspended in a culture solution and cultured while being suspended in the culture solution by the balance between the upward flow by circulation means and dead weight. The cell distribution detection unit can detect the balance between the upward flow by the circulating means and the weight of the cells by detecting the distribution of cells suspended in the culture solution in the culture tank. The control unit can control the circulation rate of the culture solution by the circulation means to control the balance between the upward flow by the circulation means and the dead weight of the cells, and can appropriately maintain the cell distribution in the culture tank.
 ここで、従来の細胞培養装置では、培養液中の細胞分布が培養槽内の適切な位置より下段又は上段に偏ることで、培養細胞が過度に集塊するなどして均質な培養が困難となる場合があった。また、培養過程で、細胞塊のサイズの変化等によって細胞分布が徐々に変化するため、培養槽内の適切な位置に細胞分布を保持することが難しかった。 Here, in the conventional cell culture apparatus, when the cell distribution in the culture solution is biased lower or upper than the appropriate position in the culture tank, the cultured cells are excessively aggregated, and homogeneous culture is difficult. It could have been. In addition, since the cell distribution gradually changes due to a change in the size of a cell mass and the like in the culture process, it has been difficult to maintain the cell distribution at an appropriate position in the culture tank.
 上記態様に係る細胞培養装置では、細胞分布検出ユニットが細胞分布を検出し、その検出結果に基づいて制御ユニットが培養液の循環速度を制御する。また、培養過程で細胞のサイズの変化等により細胞分布が変化しても、細胞分布検出ユニットによる検出及び制御ユニットによる制御によって、循環手段による上昇流と細胞の自重との均衡状態が調節される。このため、上記態様に係る細胞培養装置では、細胞分布を適切に維持して、均質な培養を実施することができる。 In the cell culture device according to the above aspect, the cell distribution detection unit detects the cell distribution, and the control unit controls the circulation speed of the culture fluid based on the detection result. Also, even if the cell distribution changes due to changes in cell size etc during the culture process, the detection by the cell distribution detection unit and the control by the control unit regulate the balance between the upward flow by circulating means and the cell's own weight . For this reason, in the cell culture device according to the above aspect, it is possible to carry out homogeneous culture while appropriately maintaining the cell distribution.
 いくつかの態様において、細胞分布検出ユニットは、培養槽内の培養液の濁度を鉛直方向の複数箇所で測定する濁度測定手段を含んでいる。この場合、複数の測定箇所で測定される濁度の高低によって、培養液中の細胞分布を検出できる。また、細胞分布の検出と併せて、培養開始時からの濁度変化を基に培養液中の細胞数の増加量を推測することもできる。 In some embodiments, the cell distribution detection unit includes turbidity measurement means for measuring the turbidity of the culture solution in the culture vessel at multiple points in the vertical direction. In this case, the distribution of cells in the culture solution can be detected by the degree of turbidity measured at a plurality of measurement points. In addition to the detection of cell distribution, it is also possible to estimate the amount of increase in the number of cells in the culture solution based on the change in turbidity from the start of culture.
 いくつかの態様において、培養ユニットは、培養槽内の培養環境を検出する培養環境検出手段と、培養槽内の培養環境を調整する培養環境調整手段と、を含んでいる。この場合、培養環境検出手段により培養槽内の培養環境を検出することで、所期の培養環境が維持されているか否かを容易に確認することができ、必要に応じて培養環境調整手段により培養槽内の培養環境を容易に調整できる。培養環境調整手段は、制御ユニットによって制御されていてよく、制御ユニットは、培養環境検出手段で検出された培養環境に基づいて、培養環境調整手段による培養環境の調整を制御していてよい。 In some embodiments, the culture unit includes culture environment detection means for detecting the culture environment in the culture vessel, and culture environment adjustment means for adjusting the culture environment in the culture vessel. In this case, by detecting the culture environment in the culture tank by the culture environment detection means, it is possible to easily confirm whether or not the desired culture environment is maintained, and the culture environment adjustment means as needed. The culture environment in the culture vessel can be easily adjusted. The culture environment adjusting means may be controlled by the control unit, and the control unit may control the adjustment of the culture environment by the culture environment adjusting means based on the culture environment detected by the culture environment detecting means.
 いくつかの態様において、細胞培養装置は、培養ユニットに培養液を供給する培養液供給ユニットと、培養ユニットに洗浄液を供給する洗浄液供給ユニットと、培養ユニットから培養液又は洗浄液を含む廃液を回収する廃液回収ユニットと、を更に備えていてよい。この場合、細胞培養における培養液交換、継代等の作業を、各ユニットの操作により容易に実施できる。 In some embodiments, the cell culture apparatus recovers a culture fluid supply unit that supplies culture fluid to the culture unit, a washing solution supply unit that supplies the washing solution to the culture unit, and a waste liquid containing the culture fluid or the washing solution from the culture unit. And a waste liquid recovery unit. In this case, operations such as culture medium exchange and passage in cell culture can be easily carried out by the operation of each unit.
 いくつかの態様において、制御ユニットは、培養液供給ユニットから培養ユニットへの培養液の送液、洗浄液供給ユニットから培養ユニットへの洗浄液の送液、及び、培養ユニットから廃液回収ユニットへの廃液の送液をそれぞれ制御する。この場合、細胞培養における培養液交換、継代等の作業を制御ユニットによって一括して実施でき、作業の自動化を図ることができる。 In some embodiments, the control unit sends the culture solution from the culture solution supply unit to the culture unit, sends the washing solution from the wash solution supply unit to the culture unit, and discharges the waste solution from the culture unit to the waste solution recovery unit. Control each liquid transfer. In this case, operations such as culture medium exchange and passage in cell culture can be performed collectively by the control unit, and the operation can be automated.
 いくつかの態様において、培養液供給ユニットは、培養液を所定温度で保管する培養液保管手段と、培養液を所定温度以上の温度に加温する培養液加温手段と、を含む。培養液は、培養液保管手段において保管に適した温度で保管され、培養液加温手段において培養に適した温度に加温されて、培養槽に供給される。この場合、培養槽に培養液を供給する必要が生じた際に、培養液保管手段で保管された培養液を培養液加温手段で加温して使用できるため、装置外から培養液を補充する場合と比較して作業手順が簡略化される。 In some embodiments, the culture solution supply unit includes culture solution storage means for storing the culture solution at a predetermined temperature, and culture solution heating means for heating the culture solution to a temperature higher than or equal to a predetermined temperature. The culture solution is stored at a temperature suitable for storage in the culture solution storage means, heated to a temperature suitable for culture in the culture solution heating means, and supplied to the culture tank. In this case, when it becomes necessary to supply the culture solution to the culture tank, the culture solution stored in the culture solution storage unit can be used by heating it by the culture solution heating unit, so that the culture solution can be replenished from outside the apparatus The work procedure is simplified compared to the case of
 いくつかの態様において、細胞培養装置は、培養槽内の培養液の液量を検出する液量検出手段を更に備えており、制御ユニットは、液量検出手段で検出された液量に基づいて、培養液供給ユニットから培養ユニットへの培養液の送液を制御する。この場合、液量検出手段によって培養槽内の液量が検出され、その検出結果に基づいて、制御ユニットの制御により培養槽内に培養液が供給される。これにより、培養液の供給量が緻密に制御され、培養液の供給量の多寡による培養細胞への悪影響が避けられる。 In some embodiments, the cell culture apparatus further comprises fluid volume detection means for detecting the fluid volume of the culture fluid in the culture vessel, and the control unit is based on the fluid volume detected by the fluid volume detection means. And controlling the transfer of the culture solution from the culture solution supply unit to the culture unit. In this case, the liquid volume detection means detects the liquid volume in the culture tank, and the culture solution is supplied into the culture tank under the control of the control unit based on the detection result. Thereby, the supply amount of the culture solution is precisely controlled, and the adverse effect on the cultured cells due to the large amount of the supply amount of the culture solution can be avoided.
 いくつかの態様において、細胞培養装置は、培養ユニットに酵素を含む酵素液を供給する酵素供給ユニットを更に備えており、制御ユニットは、酵素供給ユニットから培養ユニットへの酵素液の送液を制御する。この場合、制御ユニットによる制御によって、必要なタイミングで必要量の酵素液を容易に培養ユニットへ供給することができる。 In some embodiments, the cell culture apparatus further comprises an enzyme supply unit that supplies an enzyme solution containing an enzyme to the culture unit, and the control unit controls transfer of the enzyme solution from the enzyme supply unit to the culture unit. Do. In this case, the control unit can easily supply the required amount of enzyme solution to the culture unit at the required timing.
 いくつかの態様において、酵素供給ユニットは、酵素液を所定温度で保管する酵素保管手段を含む。これにより、酵素液が保管に適した温度で保管される。 In some embodiments, the enzyme supply unit comprises an enzyme storage means for storing the enzyme solution at a predetermined temperature. The enzyme solution is thereby stored at a temperature suitable for storage.
 いくつかの態様において、細胞培養装置は、培養ユニット内で循環する培養液の溶存酸素量を検出する溶存酸素量検出手段を更に備えており、培養ユニットは、培養液に酸素を供給する酸素供給手段を更に含んでおり、制御ユニットは、溶存酸素量検出手段で検出された溶存酸素量に基づいて、酸素供給手段による酸素の供給量を制御する。この場合、制御ユニットの制御により、必要量の酸素が培養液に供給されるため、一定の溶存酸素量を維持した細胞培養を容易に実施することができる。 In some embodiments, the cell culture apparatus further comprises a dissolved oxygen amount detection means for detecting the amount of dissolved oxygen in the culture fluid circulating in the culture unit, and the culture unit supplies oxygen to the culture fluid. The control unit further controls the supply amount of oxygen by the oxygen supply unit based on the dissolved oxygen amount detected by the dissolved oxygen amount detection unit. In this case, since the necessary amount of oxygen is supplied to the culture solution by the control of the control unit, it is possible to easily carry out cell culture maintaining a fixed amount of dissolved oxygen.
 いくつかの態様において、細胞培養装置は、培養槽内の培養液のpHを検出するpH検出手段を更に備えており、制御ユニットは、pH検出手段で検出されたpHに基づいて、培養液の交換時期を判断し、ユーザへの通知又は培養液の交換を行う。この場合、培養液のpHの変化をpH検出手段が検出し、検出結果に基づいて自動的に制御ユニットが培養液の交換時期を判断することから、交換時期の徒過による培養細胞の品質低下等が防止される。制御ユニットは、インターフェースユニット等を介して交換時期をユーザに通知してよい。また、制御ユニットは、上述の培養液供給ユニット、洗浄液供給ユニット及び廃液供給ユニットの制御により、交換時期の判断後に自動的に培養液の交換を行ってもよい。 In some embodiments, the cell culture apparatus further comprises pH detection means for detecting the pH of the culture solution in the culture vessel, and the control unit controls the culture solution based on the pH detected by the pH detection means. Determine the replacement time and notify the user or replace the culture solution. In this case, the pH detection means detects a change in pH of the culture solution, and the control unit automatically determines the culture solution replacement time based on the detection result. Etc. are prevented. The control unit may notify the user of the replacement time via an interface unit or the like. Further, the control unit may automatically exchange the culture solution after the determination of the replacement time by controlling the culture solution supply unit, the washing solution supply unit, and the waste solution supply unit described above.
 いくつかの態様において、細胞培養装置は、培養ユニットにRhoキナーゼ阻害剤を供給する阻害剤供給ユニットを更に備えていてよく、制御ユニットは、培養槽内における培養液中のRhoキナーゼ阻害剤の濃度が所定の濃度となるように、阻害剤供給ユニットによるRhoキナーゼ阻害剤の供給量を制御する。この場合、制御ユニットによる制御によって、必要なタイミングで必要量のRhoキナーゼ阻害剤を容易に培養ユニットへ供給できる。 In some embodiments, the cell culture apparatus may further comprise an inhibitor supply unit that supplies Rho kinase inhibitor to the culture unit, and the control unit controls the concentration of Rho kinase inhibitor in the culture solution in the culture vessel. The amount of Rho kinase inhibitor supplied by the inhibitor supply unit is controlled so as to achieve a predetermined concentration. In this case, the control unit can easily supply the necessary amount of Rho kinase inhibitor to the culture unit at the necessary timing.
 いくつかの態様において、阻害剤供給ユニットは、Rhoキナーゼ阻害剤を所定温度で保管する阻害剤保管手段を含む。これにより、Rhoキナーゼ阻害剤が保管に適した温度で保管される。 In some embodiments, the inhibitor delivery unit comprises an inhibitor storage means for storing the Rho kinase inhibitor at a predetermined temperature. This causes the Rho kinase inhibitor to be stored at a temperature suitable for storage.
 いくつかの態様において、細胞培養装置は、培養ユニットに薬液を供給する薬液供給ユニットを更に備えており、制御ユニットは、薬液供給ユニットから培養ユニットへの薬液の送液を制御する。この場合、制御ユニットによる制御によって、必要なタイミングで必要量の薬液を容易に培養ユニットへ供給できる。 In some embodiments, the cell culture apparatus further comprises a drug solution supply unit for supplying a drug solution to the culture unit, and the control unit controls the delivery of the drug solution from the drug solution supply unit to the culture unit. In this case, the control unit can easily supply the necessary amount of drug solution to the culture unit at the required timing.
 いくつかの態様において、薬液供給ユニットは、薬液を所定温度で保管する薬液保管手段を含む。これにより、薬液が保管に適した温度で保管される。 In some embodiments, the chemical solution supply unit includes chemical solution storage means for storing the chemical solution at a predetermined temperature. Thereby, the drug solution is stored at a temperature suitable for storage.
 いくつかの態様において、細胞培養装置は、培養ユニットから細胞の一部を回収する撮影用細胞回収ユニットと、撮影用細胞回収ユニットにより回収された細胞の顕微鏡写真を取得する撮影ユニットと、を更に備えている。この場合、細胞培養装置内で培養終了後又は培養途中の細胞の顕微鏡写真を容易に取得できるため、培養した細胞の評価、培養条件の評価等をより正確に行うことができる。 In some embodiments, the cell culture apparatus further includes: a cell collection unit for photographing that collects a part of cells from the culture unit; and a photographing unit that acquires a micrograph of the cells collected by the cell collection unit for photographing. Have. In this case, since it is possible to easily obtain a microphotograph of cells after or during culture in the cell culture apparatus, it is possible to more accurately evaluate cultured cells, evaluate culture conditions, and the like.
 いくつかの態様において、制御ユニットは、撮影用細胞回収ユニットによる細胞の回収、及び、撮影ユニットによる顕微鏡写真の取得を制御する。この場合、制御ユニットによる制御によって、所望のタイミングでの顕微鏡写真を容易に(場合により、自動的に)取得できる。 In some embodiments, the control unit controls the collection of cells by the imaging cell collection unit and the acquisition of photomicrographs by the imaging unit. In this case, the control unit can easily (possibly automatically) acquire a micrograph at a desired timing.
 以下、本開示の実施形態について、図面を参照しながら説明する。なお、図面の説明において同一要素には同一符号を付し、重複する説明を省略する。 Hereinafter, embodiments of the present disclosure will be described with reference to the drawings. In the description of the drawings, the same elements will be denoted by the same reference symbols, without redundant description.
 図1を参照して、本開示の一実施形態に係る細胞培養装置1について説明する。細胞培養装置1は、培養液F1中に懸濁した細胞の三次元培養を行う培養槽11と、培養槽内で培養液F1が上昇流を成すように培養液F1を循環させる循環用ポンプ12と、培養液F1の循環途中に設けられ、培養液F1に酸素を供給する酸素供給槽13と、を備えている。細胞培養装置1では、培養槽11と、循環用ポンプ12と、酸素供給槽13と、これらを互いに接続するライン(配管又は管路)とにより、培養ユニットが構成されている。培養槽11と酸素供給槽13とは第一循環ラインL1により接続されており、培養槽11の上段部から抜き出された培養液F1が第一循環ラインL1を介して酸素供給槽13へ送液される。酸素供給槽13と循環用ポンプ12とは第二循環ラインL2により接続されており、酸素供給槽13内で必要に応じて酸素を供給された培養液F1が、第二循環ラインL2を介して循環用ポンプ12へ送液される。循環用ポンプ12と培養槽11とは第三循環ラインL3により接続されており、循環用ポンプ12から送液された培養液F1が第三循環ラインL3を介して培養槽11の下段部へ供給される。第三循環ラインL3を介して供給された培養液F1は、培養槽11の下段部から上段部へ上昇流を成して移動し、第一循環ラインL1から培養槽11外へ送液される。 A cell culture device 1 according to an embodiment of the present disclosure will be described with reference to FIG. The cell culture apparatus 1 includes a culture vessel 11 for performing three-dimensional culture of cells suspended in a culture solution F1, and a circulation pump 12 for circulating the culture solution F1 so that the culture solution F1 forms an upward flow in the culture vessel. And an oxygen supply tank 13 provided in the middle of circulation of the culture solution F1 and supplying oxygen to the culture solution F1. In the cell culture apparatus 1, a culture unit is constituted by the culture tank 11, the circulation pump 12, the oxygen supply tank 13, and a line (a pipe or a pipe) connecting these to each other. The culture tank 11 and the oxygen supply tank 13 are connected by the first circulation line L1, and the culture fluid F1 extracted from the upper portion of the culture tank 11 is fed to the oxygen supply tank 13 via the first circulation line L1. Be liquid. The oxygen supply tank 13 and the circulation pump 12 are connected by the second circulation line L2, and the culture fluid F1 supplied with oxygen as necessary in the oxygen supply tank 13 is connected via the second circulation line L2. The fluid is sent to the circulation pump 12. The circulation pump 12 and the culture tank 11 are connected by the third circulation line L3, and the culture fluid F1 sent from the circulation pump 12 is supplied to the lower part of the culture tank 11 through the third circulation line L3. Be done. The culture fluid F1 supplied via the third circulation line L3 moves upward from the lower part to the upper part of the culture tank 11 and is transferred out of the culture tank 11 from the first circulation line L1. .
 細胞培養装置1には、培養槽11内の培養液F1の濁度を鉛直方向の複数箇所で測定する濁度計15が設けられている。細胞培養装置1では、濁度計15によって、培養槽11内における培養液F1中の細胞分布が検出される。なお、細胞培養装置1は、細胞分布検出ユニットとして濁度計15を備えるが、細胞分布検出ユニットはこれに限定されず、例えば、培養液F1の画像を取得するカメラ等を備えるものであってよい。 The cell culture apparatus 1 is provided with a turbidimeter 15 which measures the turbidity of the culture solution F1 in the culture tank 11 at a plurality of locations in the vertical direction. In the cell culture apparatus 1, the turbidimeter 15 detects the cell distribution in the culture solution F1 in the culture tank 11. Although the cell culture apparatus 1 includes the turbidimeter 15 as a cell distribution detection unit, the cell distribution detection unit is not limited to this, and includes, for example, a camera for acquiring an image of the culture fluid F1 and the like. Good.
 細胞培養装置1には、酸素供給槽13における培養液F1への酸素の供給を補助する補助手段として、マイクロバブルポンプ14が設けられている。マイクロバブルポンプ14は、第二循環ラインL2から分岐する第四循環ラインL4と、第一循環ラインL1に接続する第五循環ラインL5とを介して酸素供給槽13と接続されている。第二循環ラインL2を通過する培養液F1の一部は、第四循環ラインL4を介してマイクロバブルポンプ14へ送液され、マイクロバブルポンプ14から第五循環ラインL5及び第一循環ラインL1を介して酸素供給槽13へ返送される。マイクロバブルポンプ14は、培養液F1にマイクロバブルを発生させ、培養液F1への酸素の溶解を促進する。また、細胞培養装置1は、培養槽11内の培養液F1における溶存酸素量を検出する溶存酸素計16を備えている。溶存酸素計16は、培養開始前に溶存酸素量を検出してよく、培養途中に常時溶存酸素量を検出してよく、培養途中に所定の間隔で溶存酸素量を検出してもよい。 The cell culture device 1 is provided with a micro bubble pump 14 as an auxiliary means for assisting the supply of oxygen to the culture fluid F1 in the oxygen supply tank 13. The micro bubble pump 14 is connected to the oxygen supply tank 13 via a fourth circulation line L4 branched from the second circulation line L2 and a fifth circulation line L5 connected to the first circulation line L1. A portion of the culture fluid F1 passing through the second circulation line L2 is sent to the microbubble pump 14 via the fourth circulation line L4, and the microbubble pump 14 feeds the fifth circulation line L5 and the first circulation line L1. It is returned to the oxygen supply tank 13 via The micro bubble pump 14 generates micro bubbles in the culture fluid F1 and promotes the dissolution of oxygen in the culture fluid F1. Moreover, the cell culture apparatus 1 is equipped with the dissolved oxygen meter 16 which detects the dissolved oxygen amount in the culture solution F1 in the culture tank 11. As shown in FIG. The dissolved oxygen meter 16 may detect the amount of dissolved oxygen before starting the culture, may constantly detect the amount of dissolved oxygen during the culture, and may detect the amount of dissolved oxygen at predetermined intervals during the culture.
 細胞培養装置1は、培養槽11内の培養液F1のpHを検出するpH計17を更に備えている。pH計17は、培養開始前にpHを検出してよく、培養途中に常時pHを検出してよく、培養途中に所定の間隔でpHを検出してもよい。pH計によるpHの検出結果は培養液F1の交換時期の判断基準になり得る。 The cell culture apparatus 1 further includes a pH meter 17 that detects the pH of the culture solution F1 in the culture tank 11. The pH meter 17 may detect the pH before the start of the culture, may constantly detect the pH during the culture, and may detect the pH at predetermined intervals during the culture. The result of detection of pH by a pH meter can be used as a criterion of the replacement time of the culture fluid F1.
 培養槽11は、培養槽11内の培養環境を一定に保持するためのインキュベータ21内に配置されている。インキュベータ21は、内部を所定の培養環境(例えば、温度35~38℃、二酸化炭素濃度5%)に調整及び維持しており、外的環境によって培養環境が変動することを防止している。細胞培養装置1では、酸素供給持の培養液F1の温度変化を避けるため、酸素供給槽13もインキュベータ内に配置されている。細胞培養装置1は、培養槽11内の温度又は培養槽11内の培養液F1の温度を測定する温度計22を備えていてよく、この場合、温度計22によって培養槽11内が所定の培養環境に調整され、維持されていることが確認できる。なお、細胞培養装置1は、温度計22の他に、温度以外の培養環境を検出する検出手段を更に備えていてもよい。 The culture tank 11 is disposed in an incubator 21 for keeping the culture environment in the culture tank 11 constant. The incubator 21 adjusts and maintains the inside to a predetermined culture environment (for example, a temperature of 35 to 38 ° C., a carbon dioxide concentration of 5%), and prevents the culture environment from being changed by the external environment. In the cell culture apparatus 1, the oxygen supply tank 13 is also disposed in the incubator in order to avoid the temperature change of the culture solution F1 with oxygen supply. The cell culture apparatus 1 may be provided with a thermometer 22 for measuring the temperature in the culture tank 11 or the temperature of the culture fluid F1 in the culture tank 11. In this case, the inside of the culture tank 11 is a predetermined culture by the thermometer 22. It can be confirmed that the environment is adjusted and maintained. In addition to the thermometer 22, the cell culture apparatus 1 may further include detection means for detecting a culture environment other than temperature.
 細胞培養装置1は、培養液F1を保管する培養液保管タンク31と、培養液F1を加温する培養液加温タンク32と、培養液保管タンク31と培養液加温タンク32とを接続する培養液送液ラインL6とを更に備えており、培養液送液ラインL6には培養液送液ポンプ33が設けられている。培養液保管タンク31中に保管されている培養液F1は、必要に応じて培養液送液ラインL6を介して培養液加温タンク32に送液され、培養液加温タンク32内で培養に適した温度に加温される。培養液加温タンク32で加温された培養液F1は、培養液加温タンク32と培養槽11とを接続する加温済み培養液送液ラインL7を介して、培養液加温タンク32から培養槽11へ送液される。培養液保管タンク31と培養液送液ラインL6とは、無菌コネクタ34を介して接続されている。これにより、培養液保管タンク31の交換に際して、培養液送液ラインL6以降の無菌状態を容易に維持できる。培養液保管タンク31は、冷蔵ユニット35内に配置されている。冷蔵ユニット35は、培養液保管タンク31を、培養液F1の保管に適した温度(例えば、2~6℃)下に保持している。培養液加温タンク32はインキュベータ21内に配置されており、インキュベータ21は、培養液加温タンク32内の培養液F1を培養に適した温度(例えば、35~38℃)に加温する。 The cell culture apparatus 1 connects the culture solution storage tank 31 for storing the culture solution F1, the culture solution heating tank 32 for heating the culture solution F1, the culture solution storage tank 31, and the culture solution heating tank 32. A culture fluid delivery line L6 is further provided, and a culture fluid delivery pump 33 is provided in the culture fluid delivery line L6. The culture solution F1 stored in the culture solution storage tank 31 is transferred to the culture solution heating tank 32 via the culture solution supply line L6 as necessary, and culture is performed in the culture solution heating tank 32. It is warmed to a suitable temperature. The culture fluid F1 heated in the culture fluid heating tank 32 is fed from the culture fluid heating tank 32 via the heated culture fluid delivery line L7 connecting the culture fluid heating tank 32 and the culture tank 11. The liquid is sent to the culture tank 11. The culture solution storage tank 31 and the culture solution delivery line L6 are connected via the aseptic connector 34. As a result, when the culture solution storage tank 31 is replaced, it is possible to easily maintain the aseptic condition after the culture solution delivery line L6. The culture solution storage tank 31 is disposed in the refrigeration unit 35. The refrigeration unit 35 maintains the culture solution storage tank 31 at a temperature (for example, 2 to 6 ° C.) suitable for storage of the culture solution F1. The culture solution heating tank 32 is disposed in the incubator 21, and the incubator 21 heats the culture solution F1 in the culture solution heating tank 32 to a temperature (for example, 35 to 38 ° C.) suitable for culture.
 細胞培養装置1は、培養槽11内から培養した細胞を回収する回収経路となる細胞回収ラインL8を更に備えており、細胞回収ラインL8には細胞回収ポンプ41が設けられている。細胞回収ラインL8の出口には無菌コネクタ42が設けられており、細胞回収バイアル43と無菌的に接続可能になっている。細胞培養装置1では、無菌コネクタ42に細胞回収バイアル43を接続後、細胞回収ポンプ41の作動によって培養槽11内から細胞回収ラインL8に細胞を流通させることで、培養した細胞を回収できる。 The cell culture apparatus 1 further includes a cell recovery line L8 serving as a recovery path for recovering cells cultured in the culture tank 11. The cell recovery line L8 is provided with a cell recovery pump 41. A sterile connector 42 is provided at the outlet of the cell collection line L8, and can be aseptically connected to the cell collection vial 43. In the cell culture apparatus 1, after the cell recovery vial 43 is connected to the sterile connector 42, the cultured cells can be recovered by circulating the cells from the inside of the culture tank 11 to the cell recovery line L8 by the operation of the cell recovery pump 41.
 細胞培養装置1は、洗浄液F2を保管する洗浄液保管タンク51と、洗浄液保管タンク51から洗浄液F2を培養槽11へ送液する洗浄液送液ポンプ52とを更に備えている。洗浄液保管タンク51は洗浄液送液ラインL9を介して培養槽11と接続されており、洗浄液保管タンク51に保管されている洗浄液F2は、必要に応じて洗浄液送液ポンプ52により洗浄液送液ラインL9を介して培養槽11へ送液される。洗浄液送液ラインL9は、培養ユニットの循環経路である第三循環ラインL3に接続されており、洗浄液F2は洗浄液送液ラインL9及び第三循環ラインL3を経由して培養槽11に送液され、場合により培養ユニットの循環経路に流通した後、廃液として培養ユニットから排出される。洗浄液保管タンク51と洗浄液送液ラインL9とは、無菌コネクタ53を介して接続されている。これにより、洗浄液保管タンク51の交換に際して、洗浄液送液ラインL9以降の無菌状態を容易に維持できる。 The cell culture apparatus 1 further includes a washing solution storage tank 51 for storing the washing solution F 2, and a washing solution sending pump 52 for sending the washing solution F 2 from the washing solution storage tank 51 to the culture tank 11. The washing solution storage tank 51 is connected to the culture tank 11 through the washing solution feeding line L9, and the washing solution F2 stored in the washing solution storage tank 51 is fed by the washing solution feeding pump 52 as needed. Is sent to the culture tank 11 via the The washing solution feed line L9 is connected to the third circulation line L3 which is a circulation route of the culture unit, and the washing solution F2 is sent to the culture tank 11 via the washing solution feed line L9 and the third circulation line L3. After being optionally circulated in the circulation route of the culture unit, it is discharged from the culture unit as waste liquid. The cleaning solution storage tank 51 and the cleaning solution supply line L9 are connected via the aseptic connector 53. Thus, when replacing the cleaning solution storage tank 51, the aseptic condition after the cleaning solution supply line L9 can be easily maintained.
 洗浄液F2は特に限定されず、細胞培養に使用される公知の洗浄液であってよい。例えば洗浄液F2は、Phosphate Buffered Salin(PBS)であってよい。また、洗浄液F2は、培養する細胞に適切な基礎培地等であってもよい。例えば、DMEM、F-12、RPMI等が代表的な培地である。 The washing solution F2 is not particularly limited, and may be a known washing solution used for cell culture. For example, the washing solution F2 may be Phosphate Buffered Salin (PBS). In addition, the washing solution F2 may be a basal medium or the like suitable for cells to be cultured. For example, DMEM, F-12, RPMI and the like are representative media.
 細胞培養装置1は、培養ユニットから回収された廃液F3を貯留する廃液貯留タンク61を更に備えている。また、細胞培養装置1は、第一廃液経路として培養槽11と廃液貯留タンク61とを接続する第一廃液ラインL10、また、第二廃液経路として酸素供給槽13と廃液貯留タンク61とを接続する第二廃液ラインL11をそれぞれ備えている。第一廃液ラインL10には、培養槽11から排出される廃液を廃液貯留タンク61に送液する第一廃液ポンプ62が設けられており、第二廃液ラインL11には、酸素供給槽13から排出される廃液を廃液貯留タンク61に送液する第二廃液ポンプ63が設けられている。第一廃液ラインL10及び第二廃液ラインL11は、廃液貯留タンク61に到達する前に合流し、無菌コネクタ64を介して廃液貯留タンク61と接続されている。無菌コネクタ64により、第一廃液ラインL10及び第二廃液ラインL11の無菌状態を容易に維持しつつ、廃液貯留タンク61を交換できる。廃液貯留タンク61に貯留される廃液は、培養液又は洗浄液を含む廃液であってよく、例えば、培養液交換時の使用済み培養液、細胞回収又は継代前に廃棄される使用済み培養液、洗浄液による洗浄後に生じた廃液等であってよい。 The cell culture apparatus 1 further includes a waste liquid storage tank 61 for storing the waste liquid F3 collected from the culture unit. The cell culture apparatus 1 also connects a first waste liquid line L10 connecting the culture tank 11 and the waste liquid storage tank 61 as a first waste liquid path, and connects an oxygen supply tank 13 and a waste liquid storage tank 61 as a second waste liquid path. The second waste liquid line L11 is provided. The first waste liquid line L10 is provided with a first waste liquid pump 62 for feeding the waste liquid discharged from the culture tank 11 to the waste liquid storage tank 61, and the second waste liquid line L11 is discharged from the oxygen supply tank 13 A second waste liquid pump 63 is provided to feed the waste liquid to the waste liquid storage tank 61. The first waste liquid line L10 and the second waste liquid line L11 join together before reaching the waste liquid storage tank 61, and are connected to the waste liquid storage tank 61 via the aseptic connector 64. The sterile connector 64 allows the waste liquid storage tank 61 to be replaced while easily maintaining the aseptic condition of the first waste liquid line L10 and the second waste liquid line L11. The waste solution stored in the waste solution storage tank 61 may be a waste solution containing a culture solution or a washing solution, for example, a used culture solution at the time of culture medium replacement, a used culture solution discarded before cell recovery or passage. It may be a waste liquid or the like generated after the cleaning with the cleaning liquid.
 細胞培養装置1は、酵素を含む酵素液F4を保管する酵素液保管タンク71と、酵素液保管タンク71から酵素液F4を培養槽11へ送液する酵素液送液ポンプ72とを更に備えている。酵素液保管タンク71は酵素液送液ラインL12を介して培養槽11と接続されており、酵素液保管タンク71に保管されている酵素液F4は、必要に応じて酵素液送液ポンプ72により酵素液送液ラインL12を介して培養槽11へ送液される。酵素液保管タンク71と酵素液送液ラインL12とは無菌コネクタ73を介して接続されており、これにより酵素液保管タンク71の交換に際して、酵素液送液ラインL12以降の無菌状態を容易に維持できる。酵素液保管タンク71は、冷蔵ユニット35内に配置され、培養液保管タンク31と共に所定の温度(例えば、2~6℃)下に保持されている。なお、酵素液F4の保管に適する温度が培養液F1の保管に適する温度と異なる場合、酵素液保管タンク71は、冷蔵ユニット35内で培養液保管タンク31とは異なる温度下に保持されていてよく、冷蔵ユニット35とは異なる他の冷蔵ユニット内に配置されていてもよい。酵素は細胞分散に用いられる既知の薬液であってよい。たとえば酵素としてはAccutase、Trypsin-EDTA、Dispase、Collagenaseがあげられる。また、一態様では、酵素に代えて、細胞分散の機能のある薬剤を用いてもよい。このような薬剤としては、EDTA溶液等があげられる。 The cell culture apparatus 1 further includes an enzyme solution storage tank 71 for storing an enzyme solution F4 containing an enzyme, and an enzyme solution delivery pump 72 for transferring the enzyme solution F4 from the enzyme solution storage tank 71 to the culture tank 11 There is. The enzyme solution storage tank 71 is connected to the culture tank 11 via the enzyme solution feed line L12, and the enzyme solution F4 stored in the enzyme solution storage tank 71 is optionally sent by the enzyme solution feed pump 72. The liquid is fed to the culture tank 11 via the enzyme liquid feed line L12. The enzyme solution storage tank 71 and the enzyme solution delivery line L12 are connected via the aseptic connector 73, whereby when replacing the enzyme solution storage tank 71, the sterile condition after the enzyme solution delivery line L12 can be easily maintained. it can. The enzyme solution storage tank 71 is disposed in the refrigeration unit 35, and is held together with the culture solution storage tank 31 under a predetermined temperature (for example, 2 to 6 ° C.). When the temperature suitable for storing the enzyme solution F4 is different from the temperature suitable for storing the culture solution F1, the enzyme solution storage tank 71 is maintained at a temperature different from that of the culture solution storage tank 31 in the refrigeration unit 35. It may well be arranged in another refrigeration unit different from the refrigeration unit 35. The enzyme may be a known drug used for cell dispersion. For example, enzymes include Accutase, Trypsin-EDTA, Dispase, and Collagenase. In one aspect, instead of the enzyme, a drug having a function of cell dispersion may be used. Such agents include EDTA solution and the like.
 細胞培養装置1は、Rhoキナーゼ阻害剤を保管する阻害剤保管タンク81と、阻害剤保管タンク81からRhoキナーゼ阻害剤を培養槽11へ送液する阻害剤送液ポンプ82とを更に備えている。阻害剤保管タンク81は阻害剤送液ラインL13を介して培養槽11と接続されており、阻害剤保管タンク81に保管されているRhoキナーゼ阻害剤は、必要に応じて阻害剤送液ポンプ82により阻害剤送液ラインL13を介して培養槽11へ送液される。阻害剤保管タンク81と阻害剤送液ラインL13とは無菌コネクタ83を介して接続されており、これにより阻害剤保管タンク81の交換に際して、阻害剤送液ラインL13以降の無菌状態を容易に維持できる。阻害剤保管タンク81は、冷蔵ユニット35内に配置され、培養液保管タンク31と共に所定の温度(例えば2~6℃)下に保持されている。なお、Rhoキナーゼ阻害剤の保管に適する温度が培養液F1の保管に適する温度と異なる場合、阻害剤保管タンク81は、冷蔵ユニット35内で培養液保管タンク31とは異なる温度下に保持されていてよく、冷蔵ユニット35とは異なる他の冷蔵ユニット内に配置されていてもよい。 The cell culture apparatus 1 further includes an inhibitor storage tank 81 for storing Rho kinase inhibitor, and an inhibitor delivery pump 82 for transferring Rho kinase inhibitor to the culture tank 11 from the inhibitor storage tank 81. . The inhibitor storage tank 81 is connected to the culture tank 11 via the inhibitor delivery line L13, and the Rho kinase inhibitor stored in the inhibitor storage tank 81 is an inhibitor delivery pump 82 as needed. Thus, the liquid is fed to the culture tank 11 via the inhibitor delivery line L13. The inhibitor storage tank 81 and the inhibitor delivery line L13 are connected via the aseptic connector 83, whereby when the inhibitor storage tank 81 is replaced, the sterility of the inhibitor delivery line L13 and thereafter can be easily maintained. it can. The inhibitor storage tank 81 is disposed in the refrigeration unit 35, and is held together with the culture solution storage tank 31 under a predetermined temperature (for example, 2 to 6 ° C.). When the temperature suitable for storage of the Rho kinase inhibitor is different from the temperature suitable for storage of the culture fluid F1, the inhibitor storage tank 81 is maintained at a temperature different from that of the culture fluid storage tank 31 in the refrigeration unit 35. It may be disposed in another refrigeration unit different from the refrigeration unit 35.
 細胞培養装置1は、薬液を保管する薬液保管タンク91と、薬液保管タンク91から薬液を培養槽11へ送液する薬液送液ポンプ92とを更に備えている。薬液保管タンク91は薬液送液ラインL14を介して培養槽11と接続されており、薬液保管タンク91に保管されている薬液は、必要に応じて薬液送液ポンプ92により薬液送液ラインL14を介して培養槽11へ送液される。薬液保管タンク91と薬液送液ラインL14とは無菌コネクタ93を介して接続されており、これにより薬液保管タンク91の交換に際して、薬液送液ラインL14以降の無菌状態を容易に維持できる。薬液保管タンク91は、冷蔵ユニット35内に配置され、培養液保管タンク31と共に所定の温度(例えば2~6℃)下に保持されている。なお、薬液の保管に適する温度が培養液F1の保管に適する温度と異なる場合、薬液保管タンク91は、冷蔵ユニット35内で培養液保管タンク31とは異なる温度下に保持されていてよく、冷蔵ユニット35とは異なる他の冷蔵ユニット内に配置されていてもよい。薬液は、細胞培養に使用される公知の薬液であってよい。例えば薬液は、サイトカイン等の未分化の維持、分化の促進、活性化に係る薬剤等であってよく、Activin、b-FGF、SCF、TGF-beta等が挙げられる。 The cell culture apparatus 1 further includes a drug solution storage tank 91 for storing a drug solution, and a drug solution sending pump 92 for sending a drug solution from the drug solution storage tank 91 to the culture tank 11. The chemical solution storage tank 91 is connected to the culture tank 11 via the chemical solution delivery line L14, and the chemical solution stored in the chemical solution storage tank 91 is transferred by the chemical solution delivery pump 92 as needed. The liquid is sent to the culture tank 11 via The drug solution storage tank 91 and the drug solution sending line L14 are connected via the aseptic connector 93, whereby when replacing the drug solution storage tank 91, it is possible to easily maintain the aseptic condition of the drug solution sending line L14 and thereafter. The chemical solution storage tank 91 is disposed in the refrigeration unit 35, and is held together with the culture solution storage tank 31 under a predetermined temperature (for example, 2 to 6 ° C.). When the temperature suitable for storing the drug solution is different from the temperature suitable for storing the culture solution F1, the drug solution storage tank 91 may be kept at a temperature different from that of the culture solution storage tank 31 in the refrigeration unit 35, It may be disposed in another refrigeration unit different from the unit 35. The drug solution may be a known drug solution used for cell culture. For example, the drug solution may be an agent related to maintenance of undifferentiation such as cytokine, promotion of differentiation, activation, etc., and includes Activin, b-FGF, SCF, TGF-beta and the like.
 細胞培養装置1は、撮影ユニット101と、細胞回収ラインL8から分岐して撮影ユニット101に接続される撮影用送液ラインL15とを更に備えており、撮影用送液ラインL15には、撮影ユニット101に細胞を含有する測定サンプルを送液する撮影用送液ポンプ102が設けられている。また、撮影ユニット101には、撮影用バッファF5を保管するバッファタンク103が接続されている。撮影ユニット101は、撮影用送液ポンプ102により送液された測定サンプルを撮影し、測定サンプルに含まれる細胞の顕微鏡写真を取得する。顕微鏡写真取得後の測定サンプルは、撮影ユニット101から廃液として破棄されてよい。また、顕微鏡写真取得後の測定サンプルは、撮影用送液ラインL15を介して細胞回収ラインL8に送液され、細胞回収バイアル43に回収されてもよい。このとき、撮影用送液ポンプ102は、測定サンプルを撮影ユニット101から細胞回収ラインL8へ送液する役割を担っていてよい。撮影ユニット101及びバッファタンク103は、培養環境における細胞状態をより正確に観察するため、インキュベータ21内に配置され、所定の温度(例えば、35~38℃)下に保持されている。 The cell culture apparatus 1 further includes an imaging unit 101, and a liquid transfer line L15 for imaging which is branched from the cell collection line L8 and connected to the imaging unit 101. The imaging liquid supply line L15 includes the imaging unit A photographing liquid-sending pump 102 is provided for feeding a measurement sample containing cells at 101. Further, a buffer tank 103 for storing a shooting buffer F5 is connected to the shooting unit 101. The imaging unit 101 images the measurement sample fed by the imaging liquid feed pump 102, and obtains a micrograph of the cells contained in the measurement sample. The measurement sample after obtaining the microphotograph may be discarded from the imaging unit 101 as a waste liquid. In addition, the measurement sample after obtaining the microphotograph may be sent to the cell collection line L8 via the imaging liquid supply line L15 and collected in the cell collection vial 43. At this time, the imaging liquid transfer pump 102 may play a role of transporting the measurement sample from the imaging unit 101 to the cell recovery line L8. The imaging unit 101 and the buffer tank 103 are disposed in the incubator 21 and maintained at a predetermined temperature (for example, 35 to 38 ° C.) in order to observe the cell state in the culture environment more accurately.
 細胞培養装置1は、制御ユニットとしてのコントローラ111を更に備えている。コントローラ111は、濁度計15により検出される濁度の情報を取得し、当該濁度の情報に基づいて循環用ポンプ12を制御し、培養液F1の循環速度の調整を実施する。 The cell culture apparatus 1 further includes a controller 111 as a control unit. The controller 111 acquires information on the turbidity detected by the turbidity meter 15, controls the circulation pump 12 based on the information on the turbidity, and adjusts the circulation speed of the culture fluid F1.
 図2を参照して、コントローラ111による循環速度制御の実行手順について説明する。まず、コントローラ111は、濁度計15から濁度に係る検出情報(入力値)を取得する(ステップS01)。濁度計15は、培養槽11内の培養液F1の濁度を鉛直方向の複数箇所で測定しており、コントローラ111には、各箇所で検出された情報がそれぞれ入力される。次いで、コントローラ111は、濁度計15からの複数の入力値を、それぞれ所定の工学値に変換する(ステップS02)。なお、コントローラ111が、濁度計15の検出情報を工学値として取得する場合、ステップS02は省略されてよい。 An execution procedure of circulation speed control by the controller 111 will be described with reference to FIG. First, the controller 111 acquires detection information (input value) relating to turbidity from the turbidity meter 15 (step S01). The turbidity meter 15 measures the turbidity of the culture solution F1 in the culture tank 11 at a plurality of locations in the vertical direction, and the controller 111 receives information detected at each location. Next, the controller 111 converts the plurality of input values from the turbidity meter 15 into predetermined engineering values (step S02). In addition, when the controller 111 acquires the detection information of the turbidity meter 15 as an engineering value, step S02 may be omitted.
 次いで、コントローラ111は、取得した複数の工学値に基づいて、培養槽11内の培養液F1の鉛直方向の濁度を比較し(ステップS03)、濁度分布を作成し(ステップS04)、濁度計15による複数の測定位置のうち、濁度が最大となる測定位置を抽出する(ステップS05)。これらのステップにより、コントローラ111は、培養槽11内の培養液F1中における細胞分布の情報を得る。 Next, the controller 111 compares the turbidity of the culture fluid F1 in the culture tank 11 in the vertical direction based on the plurality of acquired engineering values (step S03), and creates a turbidity distribution (step S04). Among the plurality of measurement positions by the wattmeter 15, the measurement position at which the turbidity is maximum is extracted (step S05). By these steps, the controller 111 obtains information of cell distribution in the culture solution F1 in the culture tank 11.
 コントローラ111は、得られた細胞分布の情報に基づいて培養液F1の循環速度の決定及び循環用ポンプ12の制御を行う。具体的には、まず、事前に、培養液F1中で細胞が分布すべき位置と濁度計15による測定位置との関係を基に、各測定位置に対して、循環速度を所定の上昇量で上昇させる、循環速度を所定の下降量で下降させる、又は、循環速度を保持する旨の設定を行っておく。コントローラ111は、この設定を参照して、対象の測定位置(例えば、ステップS05で抽出された濁度最大の測定位置)が速度上昇設定であるか否かを判断する(ステップS06)。コントローラ111は、速度上昇設定であると判断すると(ステップS06:YES)、設定された上昇量を参照して循環速度の上昇量を仮決定する(ステップS07)。また、速度上昇設定でないと判断すると(ステップS06:NO)、コントローラ111は、対象の測定位置が速度下降設定であるか否かを判断し(ステップS08)、速度下降設定であると判断すると(ステップS08:YES)、設定された下降量を参照して循環速度の下降量を仮決定する(ステップS09)。コントローラ111は、ステップS07で仮決定した上昇量又はステップS08で仮決定した下降量と、初期の循環速度(循環速度制御の実行前の循環速度)とから、循環後の循環速度の仮値(実行前の循環速度+上昇量、又は、実行前の循環速度-下降量)を算出する(ステップS10)。なお、ステップS08で速度降下設定でもないと判断した場合(ステップS08:NO)は、初期の循環速度を制御後の循環速度の仮値として算出する。 The controller 111 determines the circulation speed of the culture fluid F1 and controls the circulation pump 12 based on the information of the obtained cell distribution. Specifically, first, based on the relationship between the position where cells should be distributed in culture fluid F1 and the measurement position by turbidity meter 15, the circulating speed is increased by a predetermined amount for each measurement position. Setting to decrease the circulation speed by a predetermined decrease amount or to maintain the circulation speed. The controller 111 refers to this setting and determines whether or not the measurement position of the object (for example, the measurement position of the maximum turbidity extracted in step S05) is the speed increase setting (step S06). When the controller 111 determines that the speed increase setting is made (step S06: YES), the controller 111 refers to the set increase amount to temporarily determine the increase amount of the circulation speed (step S07). If it is determined that the speed increase setting is not set (step S06: NO), the controller 111 determines whether the target measurement position is the speed decrease setting (step S08), and if it is determined that the speed decrease setting is Step S08: YES) With reference to the set descent amount, the descent amount of the circulating speed is temporarily determined (step S09). The controller 111 uses the increase amount temporarily determined in step S07 or the decrease amount temporarily determined in step S08, and the initial circulation speed (the circulation speed before execution of the circulation speed control), a provisional value of the circulation speed after circulation ( The circulation speed before the execution + the increase amount, or the circulation speed before the execution−the decrease amount) is calculated (step S10). If it is determined in step S08 that the speed reduction setting is not set (step S08: NO), the initial circulation speed is calculated as a temporary value of the circulation speed after control.
 次いで、コントローラ111は、算出された仮値が細胞培養装置1における循環速度の上限値を超えるか否かを判断する(ステップS11)。コントローラ111は、仮値が上限値を超えると判断すると(ステップS11:YES)、仮値を上限値に置き換える(ステップS12)。また、コントローラ111は、仮値が上限値を超えないと判断すると(ステップS11:NO)、次いで仮値が下限値未満であるか否かを判断する(ステップS13)。コントローラ111は、仮値が下限値未満であると判断すると(ステップS13:YES)、仮値を下限値に置き換える(ステップS14)。また、コントローラ111は、仮値が下限値未満でないと判断すると(ステップS14:NO)、仮値が維持される。そしてコントローラ111は、ステップS11~S14を経て設定された仮値を、制御後の循環速度として決定する(ステップS15)。コントローラ111は、決定された循環速度に基づいて循環用ポンプ12を制御する(ステップS16)。 Next, the controller 111 determines whether the calculated temporary value exceeds the upper limit value of the circulation rate in the cell culture device 1 (step S11). If the controller 111 determines that the provisional value exceeds the upper limit (step S11: YES), it replaces the provisional value with the upper limit (step S12). When the controller 111 determines that the temporary value does not exceed the upper limit (step S11: NO), it then determines whether the temporary value is less than the lower limit (step S13). If the controller 111 determines that the temporary value is less than the lower limit value (step S13: YES), the temporary value is replaced with the lower limit value (step S14). In addition, when the controller 111 determines that the temporary value is not less than the lower limit (step S14: NO), the temporary value is maintained. Then, the controller 111 determines the temporary value set through steps S11 to S14 as the circulation speed after control (step S15). The controller 111 controls the circulation pump 12 based on the determined circulation speed (step S16).
 なお、コントローラ111による循環速度制御の実行手順は上記に限定されず、濁度計15による検出結果に基づいて循環用ポンプ12が制御されていればよい。また、コントローラ111は、濁度計15以外の計器から測定される情報を更に取得してよく、循環用ポンプ12以外のポンプを更に制御してもよい。 The execution procedure of the circulation speed control by the controller 111 is not limited to the above, and the circulation pump 12 may be controlled based on the detection result by the turbidity meter 15. Moreover, the controller 111 may further acquire information measured from a meter other than the turbidity meter 15 and may further control a pump other than the circulation pump 12.
 コントローラ111は、溶存酸素計16の検出結果を取得して、取得した検出結果に基づいてマイクロバブルポンプ14を制御してよい。コントローラ111は、溶存酸素量の既定値が維持されるように、溶存酸素計16により検出された溶存酸素量が既定値を超える場合はマイクロバブルポンプ14によるマイクロバブル発生量を減少させ、溶存酸素計16により検出された溶存酸素量が規定値未満である場合はマイクロバブルポンプ14によるマイクロバブル発生量を増加させてよい。 The controller 111 may acquire the detection result of the dissolved oxygen meter 16 and control the micro bubble pump 14 based on the acquired detection result. The controller 111 reduces the amount of microbubbles generated by the microbubble pump 14 when the amount of dissolved oxygen detected by the dissolved oxygen meter 16 exceeds the predetermined value so that the predetermined value of the amount of dissolved oxygen is maintained. If the amount of dissolved oxygen detected by the total 16 is less than the specified value, the amount of microbubbles generated by the microbubble pump 14 may be increased.
 コントローラ111は、pH計17の検出結果を取得して、取得した検出結果に基づいて培養液F1の交換時期を判断し、ユーザへの通知又は培養液F1の交換を行ってよい。また、コントローラ111は、培養液送液ポンプ33、洗浄液送液ポンプ52、第一廃液ポンプ62、及び第二廃液ポンプ63をそれぞれ制御してよい。この場合、コントローラ111は、自身の判断又はユーザの指示によって、各ポンプの制御を行い、培養液の交換、継代等の作業を実行できる。また、細胞培養装置1は、培養槽11内の培養液F1の液量を検出する液量検出計(図示しない)を更に備えていてよく、コントローラ111は、液量検出計の検出結果を取得して、取得した検出結果に基づいて培養液送液ポンプ33による培養液の送液量を制御してよい。 The controller 111 may acquire the detection result of the pH meter 17, determine the replacement time of the culture fluid F1 based on the acquired detection result, and notify the user or exchange the culture fluid F1. In addition, the controller 111 may control the culture solution delivery pump 33, the washing solution delivery pump 52, the first waste solution pump 62, and the second waste solution pump 63, respectively. In this case, the controller 111 can control each pump according to its own judgment or a user's instruction, and can perform operations such as culture medium replacement and passage. In addition, the cell culture apparatus 1 may further include a liquid volume detector (not shown) for detecting the liquid volume of the culture fluid F1 in the culture tank 11, and the controller 111 acquires the detection result of the liquid volume detector. Then, on the basis of the acquired detection result, the amount of culture solution delivered by the culture solution delivery pump 33 may be controlled.
 コントローラ111は、細胞回収ポンプ41を制御できる。この場合、例えば、コントローラ111は、事前に設定された培養時間経過後に自動で細胞回収ポンプ41(更に、必要に応じて培養液送液ポンプ33、洗浄液送液ポンプ52、第一廃液ポンプ62、及び第二廃液ポンプ63)を制御して、細胞を自動回収できる。 The controller 111 can control the cell recovery pump 41. In this case, for example, the controller 111 automatically performs the cell recovery pump 41 (in addition, if necessary, the culture fluid delivery pump 33, the washing solution delivery pump 52, the first waste solution pump 62, And the second waste liquid pump 63) to automatically collect the cells.
 コントローラ111は、酵素液送液ポンプ72を制御してよく、この場合、ユーザの指示又は事前の設定に基づいて酵素液F4を培養槽11に送液できる。また、コントローラ111は、阻害剤送液ポンプ82を制御してよく、この場合、ユーザの指示又は事前の設定に基づいてRhoキナーゼ阻害剤を培養槽11に送液できる。また、コントローラ111は、薬液送液ポンプ92を制御してよく、この場合、ユーザの指示又は事前の設定に基づいて薬液を培養槽11に送液できる。また、コントローラ111は、撮影用送液ポンプ102を制御していよく、この場合、ユーザの指示又は事前の設定に基づいて撮影ユニット101に測定サンプルを送液できる。さらに、コントローラ111は撮影ユニット101による顕微鏡写真の撮影を制御してよく、この場合、ユーザの指示又は事前の設定に基づいて自動的に細胞の顕微鏡写真を取得できる。 The controller 111 may control the enzyme solution delivery pump 72, and in this case, the enzyme solution F4 can be delivered to the culture tank 11 based on the user's instruction or the previous setting. In addition, the controller 111 may control the inhibitor delivery pump 82, and in this case, the Rho kinase inhibitor can be delivered to the culture tank 11 based on the user's instruction or the previous setting. In addition, the controller 111 may control the chemical solution delivery pump 92, and in this case, the chemical solution can be delivered to the culture tank 11 based on the user's instruction or the previous setting. Further, the controller 111 may control the liquid supply pump 102 for imaging, and in this case, the measurement sample can be supplied to the imaging unit 101 based on a user's instruction or a prior setting. Furthermore, the controller 111 may control the photographing of the microphotograph by the photographing unit 101, and in this case, the microphotograph of the cell can be automatically acquired based on the user's instruction or the prior setting.
 このような細胞培養装置1では、細胞は培養液F1中に懸濁しており、培養液F1の上昇流と自重との均衡によって培養液F1中に浮遊しながら培養される。コントローラ111は、循環用ポンプ12による培養液F1の循環速度を制御することで、培養液F1の上昇流と細胞の自重との均衡状態を調節し、培養槽11内における細胞分布を適切に保持できる。 In such a cell culture apparatus 1, cells are suspended in the culture fluid F1, and are cultured while being suspended in the culture fluid F1 due to the balance between the upward flow of the culture fluid F1 and its own weight. The controller 111 controls the circulation speed of the culture fluid F1 by the circulation pump 12 to adjust the equilibrium state between the upward flow of the culture fluid F1 and the dead weight of the cells, and appropriately maintain the cell distribution in the culture tank 11 it can.
 また、細胞培養装置1では、濁度計15が培養槽11内の培養液F1の濁度を検出し、コントローラ111が上記実行手順で循環速度を制御する。これにより、培養過程で細胞のサイズの変化等により細胞分布が変化しても、コントローラ111の制御によって培養液F1の上昇流と細胞の自重との均衡状態を自動的に調節できる。このため、細胞培養装置1では、細胞分布を適切に維持して、均質な培養を実施できる。 Further, in the cell culture apparatus 1, the turbidimeter 15 detects the turbidity of the culture fluid F1 in the culture tank 11, and the controller 111 controls the circulation speed in the above execution procedure. Thereby, even if the cell distribution changes due to a change in cell size or the like in the culture process, the controller 111 can automatically adjust the equilibrium state between the upward flow of the culture fluid F1 and the weight of the cell. For this reason, in the cell culture apparatus 1, homogeneous distribution can be performed while maintaining the cell distribution appropriately.
 また、細胞培養装置1では、濁度計15が培養槽11内の培養液F1の濁度を鉛直方向の複数箇所で測定している。ここで、培養槽11内で培養される細胞数が増加すると、培養液F1の濁度が増加する。また、培養される細胞のサイズ(又は細胞塊のサイズ)が大きくなると、自重により細胞分布が徐々に鉛直方向下側に移動する。上記の濁度計15によれば、これらの培養状態をモニターすることも可能となる。 Moreover, in the cell culture apparatus 1, the turbidimeter 15 measures the turbidity of the culture solution F1 in the culture tank 11 in multiple places of the perpendicular direction. Here, when the number of cells cultured in the culture tank 11 increases, the turbidity of the culture solution F1 increases. In addition, as the size of the cells to be cultured (or the size of the cell mass) increases, the cell distribution gradually moves downward in the vertical direction due to its own weight. According to the above-mentioned turbidimeter 15, it also becomes possible to monitor these culture conditions.
 また、細胞培養装置1では、溶存酸素計16により培養液F1の溶存酸素量が検出され、コントローラ111はその検出結果に基づいてマイクロバブルポンプ14を制御できる。このため、細胞培養装置1では、コントローラ111の制御により、一定の溶存酸素量を維持した細胞培養を容易に実施することができる。 Further, in the cell culture apparatus 1, the dissolved oxygen amount of the culture solution F1 is detected by the dissolved oxygen meter 16, and the controller 111 can control the micro bubble pump 14 based on the detection result. For this reason, in the cell culture apparatus 1, cell culture which maintained a fixed amount of dissolved oxygen can be easily implemented by control of the controller 111.
 また、細胞培養装置1では、pH計17により培養液F1のpHが検出され、コントローラ111はその検出結果に基づいて培養液F1の交換時期を判断し、ユーザへの通知又は培養液F1の交換を実行できる。このような細胞培養装置1では、コントローラ111によって自動的に培養液F1の交換時期が判断され、交換時期の徒過による培養細胞の品質低下等が防止される。 In the cell culture apparatus 1, the pH meter 17 detects the pH of the culture fluid F1, and the controller 111 determines the replacement time of the culture fluid F1 based on the detection result, and notifies the user or the culture fluid F1 is exchanged. Can do In such a cell culture apparatus 1, the controller 111 automatically determines the replacement time of the culture solution F1 and prevents the deterioration of the cultured cells due to the passing of the replacement time.
 また、細胞培養装置1では、コントローラ111が培養液送液ポンプ33、洗浄液送液ポンプ52、第一廃液ポンプ62、及び第二廃液ポンプ63をそれぞれ制御できる。このため、細胞培養装置1では、コントローラ111の判断又はユーザの指示に応じて、培養液F1の交換、継代等の作業を自動的に実施できる。 Further, in the cell culture apparatus 1, the controller 111 can control the culture solution delivery pump 33, the washing solution delivery pump 52, the first waste solution pump 62, and the second waste solution pump 63. For this reason, in the cell culture apparatus 1, operations such as replacement of the culture fluid F1 and passage can be performed automatically according to the determination of the controller 111 or the instruction of the user.
 また、細胞培養装置1では、コントローラ111が酵素液送液ポンプ72、阻害剤送液ポンプ82、及び薬液送液ポンプ92をそれぞれ制御できる。このため、細胞培養装置1では、コントローラ111の制御によって、事前に設定された量及びタイミングで酵素液、Rhoキナーゼ阻害剤及び薬液を培養槽11に自動で供給できる。 Further, in the cell culture apparatus 1, the controller 111 can control the enzyme solution delivery pump 72, the inhibitor delivery solution pump 82, and the chemical solution delivery pump 92. For this reason, in the cell culture apparatus 1, the enzyme solution, the Rho kinase inhibitor and the drug solution can be automatically supplied to the culture tank 11 at the amount and timing set in advance by the control of the controller 111.
 以上、本開示の一実施形態について説明したが、本開示は上記実施形態に限られない。例えば、培養槽11は、水平方向の断面積が底部から上方へ向かうに従い大きくなる円錐台状を有していてよい。これにより、上昇流に速度勾配が設けられ、循環速度と細胞分布との相関が顕著となる。 As mentioned above, although one embodiment of this indication was described, this indication is not limited to the above-mentioned embodiment. For example, the culture vessel 11 may have a frusto-conical shape in which the cross-sectional area in the horizontal direction increases from the bottom toward the top. As a result, a velocity gradient is provided to the upflow, and the correlation between the circulation velocity and the cell distribution becomes remarkable.
 本開示の細胞培養装置によれば、幹細胞等の細胞培養を効率良く実施し、高品質な培養細胞を安定して得ることができる。 According to the cell culture apparatus of the present disclosure, cell culture of stem cells and the like can be performed efficiently, and high quality cultured cells can be stably obtained.
1 細胞培養装置
11 培養槽
12 循環用ポンプ
13 酸素供給槽
14 マイクロバブルポンプ
15 濁度計
16 溶存酸素計
17 pH計
21 インキュベータ
22 温度計
31 培養液保管タンク
32 培養液加温タンク
33 培養液送液ポンプ
34 無菌コネクタ
35 冷蔵ユニット
41 細胞回収ポンプ
42 無菌コネクタ
43 細胞回収バイアル
51 洗浄液保管タンク
52 洗浄液送液ポンプ
53 無菌コネクタ
61 廃液貯留タンク
62 第一廃液ポンプ
63 第二廃液ポンプ
64 無菌コネクタ
71 酵素液保管タンク
72 酵素液送液ポンプ
73 無菌コネクタ
81 阻害剤保管タンク
82 阻害剤送液ポンプ
83 無菌コネクタ
91 薬液保管タンク
92 薬液送液ポンプ
93 無菌コネクタ
101 撮影ユニット
102 撮影用送液ポンプ
103 バッファタンク
111 コントローラ
F1 培養液
F2 洗浄液
F3 廃液
F4 酵素液
F5 撮影用バッファ
L1 第一循環ライン
L2 第二循環ライン
L3 第三循環ライン
L4 第四循環ライン
L5 第五循環ライン
L6 培養液送液ライン
L7 加温済み培養液送液ライン
L8 細胞回収ライン
L9 洗浄液送液ライン
L10 第一廃液ライン
L11 第二廃液ライン
L12 酵素液送液ライン
L13 阻害剤送液ライン
L14 薬液送液ライン
L15 撮影用送液ライン
DESCRIPTION OF SYMBOLS 1 cell culture apparatus 11 culture tank 12 pump for circulation 13 oxygen supply tank 14 micro bubble pump 15 turbidity meter 16 dissolved oxygen meter 17 pH meter 21 incubator 22 thermometer 31 culture solution storage tank 32 culture solution heating tank 33 culture solution delivery Liquid pump 34 Aseptic connector 35 Refrigeration unit 41 Cell collection pump 42 Aseptic connector 43 Cell collection vial 51 Washing liquid storage tank 52 Washing liquid feeding pump 53 Aseptic connector 61 Waste liquid storage tank 62 First waste liquid pump 63 Second waste liquid pump 64 Aseptic connector 71 Enzyme Liquid storage tank 72 Enzyme liquid supply pump 73 Aseptic connector 81 Inhibitor storage tank 82 Inhibitor liquid supply pump 83 Aseptic connector 91 Chemical liquid storage tank 92 Chemical liquid supply pump 93 Aseptic connector 101 Imaging unit 102 Imaging liquid delivery pump 103 Buffer tank 111 Controller F1 Culture solution F2 Washing solution F3 Waste solution F4 Enzyme solution F5 Imaging buffer L1 First circulation line L2 Second circulation line L3 Third circulation line L4 Fourth circulation line L5 Fifth circulation line L6 Culture solution delivery line L7 Warmed Culture solution delivery line L8 Cell recovery line L9 Washing solution delivery line L10 First waste liquid line L11 Second waste solution line L12 Enzyme solution delivery line L13 Inhibitor delivery line L14 Chemical solution delivery line L15 Imaging solution delivery line

Claims (17)

  1.  培養液中に懸濁した細胞の三次元培養を行う培養槽、及び、前記培養槽内で前記培養液が上昇流を成すように前記培養液を循環させる循環手段を含む培養ユニットと、
     前記培養槽内の細胞分布を検出する細胞分布検出ユニットと、
     前記細胞分布検出ユニットで検出された細胞分布に基づいて、前記循環手段による前記培養液の循環速度を制御する制御ユニットと、
    を備える、細胞培養装置。
    A culture vessel for performing three-dimensional culture of cells suspended in a culture solution, and a culture unit including circulation means for circulating the culture solution so that the culture solution forms an ascending flow in the culture vessel;
    A cell distribution detection unit for detecting cell distribution in the culture vessel;
    A control unit that controls the circulation speed of the culture fluid by the circulation unit based on the cell distribution detected by the cell distribution detection unit;
    A cell culture apparatus comprising:
  2.  前記細胞分布検出ユニットは、前記培養槽内の前記培養液の濁度を鉛直方向の複数箇所で測定する濁度測定手段を含む、請求項1に記載の細胞培養装置。 The cell culture device according to claim 1, wherein the cell distribution detection unit includes turbidity measurement means for measuring the turbidity of the culture solution in the culture tank at a plurality of locations in the vertical direction.
  3.  前記培養ユニットが、前記培養槽内の培養環境を検出する培養環境検出手段と、前記培養槽内の培養環境を調整する培養環境調整手段と、を含む、請求項1又は2に記載の細胞培養装置。 The cell culture according to claim 1 or 2, wherein the culture unit includes culture environment detection means for detecting a culture environment in the culture tank, and culture environment adjustment means for adjusting a culture environment in the culture tank. apparatus.
  4.  前記培養ユニットに前記培養液を供給する培養液供給ユニットと、
     前記培養ユニットに洗浄液を供給する洗浄液供給ユニットと、
     前記培養ユニットから前記培養液又は前記洗浄液を含む廃液を回収する廃液回収ユニットと、
    を更に備える、請求項1~3のいずれか一項に記載の細胞培養装置。
    A culture solution supply unit for supplying the culture solution to the culture unit;
    A cleaning solution supply unit for supplying a cleaning solution to the culture unit;
    A waste liquid recovery unit for collecting waste liquid containing the culture fluid or the washing liquid from the culture unit;
    The cell culture device according to any one of claims 1 to 3, further comprising
  5.  前記制御ユニットが、前記培養液供給ユニットから前記培養ユニットへの前記培養液の送液、前記洗浄液供給ユニットから前記培養ユニットへの前記洗浄液の送液、及び、前記培養ユニットから前記廃液回収ユニットへの前記廃液の送液をそれぞれ制御する、請求項4に記載の細胞培養装置。 The control unit sends the culture solution from the culture solution supply unit to the culture unit, sends the washing solution from the wash solution supply unit to the culture unit, and sends the culture solution from the culture unit to the waste solution recovery unit The cell culture apparatus according to claim 4, wherein each liquid feed of the waste liquid is controlled.
  6.  前記培養液供給ユニットが、前記培養液を所定温度で保管する培養液保管手段と、前記培養液を前記所定温度以上の温度に加温する培養液加温手段と、を含む、請求項4又は5に記載の細胞培養装置。 5. The culture solution storage unit according to claim 4, wherein the culture solution supply unit includes culture solution storage means for storing the culture solution at a predetermined temperature, and culture solution heating means for heating the culture solution to a temperature higher than the predetermined temperature. The cell culture apparatus as described in 5.
  7.  前記培養槽内の前記培養液の液量を検出する液量検出手段を更に備え、
     前記制御ユニットが、前記液量検出手段で検出された液量に基づいて、前記培養液供給ユニットから前記培養ユニットへの前記培養液の送液を制御する、請求項4~6のいずれか一項に記載の細胞培養装置。
    The apparatus further comprises a liquid amount detecting means for detecting the liquid amount of the culture solution in the culture tank,
    The control unit controls transfer of the culture solution from the culture solution supply unit to the culture unit based on the liquid volume detected by the liquid volume detection means. The cell culture apparatus as described in a term.
  8.  前記培養ユニットに酵素を含む酵素液を供給する酵素供給ユニットを更に備え、
     前記制御ユニットが、前記酵素供給ユニットから前記培養ユニットへの前記酵素液の送液を制御する、請求項1~7のいずれか一項に記載の細胞培養装置。
    It further comprises an enzyme supply unit for supplying an enzyme solution containing an enzyme to the culture unit,
    The cell culture device according to any one of claims 1 to 7, wherein the control unit controls the transfer of the enzyme solution from the enzyme supply unit to the culture unit.
  9.  前記酵素供給ユニットが、前記酵素液を所定温度で保管する酵素保管手段を含む、請求項8に記載の細胞培養装置。 The cell culture device according to claim 8, wherein the enzyme supply unit includes an enzyme storage unit that stores the enzyme solution at a predetermined temperature.
  10.  前記培養ユニット内で循環する前記培養液の溶存酸素量を検出する溶存酸素量検出手段を更に備え、
     前記培養ユニットが、前記培養液に酸素を供給する酸素供給手段を更に含み、
     前記制御ユニットが、前記溶存酸素量検出手段で検出された溶存酸素量に基づいて、前記酸素供給手段による酸素の供給量を制御する、請求項1~9のいずれか一項に記載の細胞培養装置。
    It further comprises a dissolved oxygen amount detection means for detecting the dissolved oxygen amount of the culture fluid circulating in the culture unit,
    The culture unit further includes an oxygen supply means for supplying oxygen to the culture solution;
    The cell culture according to any one of claims 1 to 9, wherein the control unit controls the supply amount of oxygen by the oxygen supply unit based on the dissolved oxygen amount detected by the dissolved oxygen amount detection unit. apparatus.
  11.  前記培養槽内の前記培養液のpHを検出するpH検出手段を更に備え、
     前記制御ユニットが、前記pH検出手段で検出されたpHに基づいて、前記培養液の交換時期を判断し、ユーザへの通知又は前記培養液の交換を行う、請求項1~10のいずれか一項に記載の細胞培養装置。
    The apparatus further comprises pH detection means for detecting the pH of the culture solution in the culture vessel,
    The control unit determines the replacement time of the culture solution based on the pH detected by the pH detection means, and notifies the user or exchanges the culture solution. The cell culture apparatus as described in a term.
  12.  前記培養ユニットにRhoキナーゼ阻害剤を供給する阻害剤供給ユニットを更に備え、
     前記制御ユニットが、前記培養槽内における前記培養液中の前記Rhoキナーゼ阻害剤の濃度が所定の濃度となるように、前記阻害剤供給ユニットによる前記Rhoキナーゼ阻害剤の供給量を制御する、請求項1~11のいずれか一項に記載の細胞培養装置。
    It further comprises an inhibitor supply unit for supplying Rho kinase inhibitor to the culture unit,
    The control unit controls the supply amount of the Rho kinase inhibitor by the inhibitor supply unit such that the concentration of the Rho kinase inhibitor in the culture solution in the culture tank becomes a predetermined concentration. Item 12. The cell culture device according to any one of items 1 to 11.
  13.  前記阻害剤供給ユニットが、前記Rhoキナーゼ阻害剤を所定温度で保管する阻害剤保管手段を含む、請求項12に記載の細胞培養装置。 The cell culture device according to claim 12, wherein the inhibitor supply unit comprises an inhibitor storage means for storing the Rho kinase inhibitor at a predetermined temperature.
  14.  前記培養ユニットに薬液を供給する薬液供給ユニットを更に備え、
     前記制御ユニットが、前記薬液供給ユニットから前記培養ユニットへの前記薬液の送液を制御する、請求項1~13のいずれか一項に記載の細胞培養装置。
    It further comprises a chemical solution supply unit for supplying a chemical solution to the culture unit,
    The cell culture device according to any one of claims 1 to 13, wherein the control unit controls the transfer of the drug solution from the drug solution supply unit to the culture unit.
  15.  前記薬液供給ユニットが、前記薬液を所定温度で保管する薬液保管手段を含む、請求項14に記載の細胞培養装置。 The cell culture device according to claim 14, wherein the drug solution supply unit includes a drug solution storage unit for storing the drug solution at a predetermined temperature.
  16.  前記培養ユニットから前記細胞の一部を回収する撮影用細胞回収ユニットと、
     前記撮影用細胞回収ユニットにより回収された前記細胞の顕微鏡写真を取得する撮影ユニットと、
    を更に備える、請求項1~15のいずれか一項に記載の細胞培養装置。
    A photographing cell collection unit for collecting a part of the cells from the culture unit;
    An imaging unit for acquiring a micrograph of the cells recovered by the imaging cell recovery unit;
    The cell culture device according to any one of claims 1 to 15, further comprising
  17.  前記制御ユニットが、前記撮影用細胞回収ユニットによる前記細胞の回収、及び、前記撮影ユニットによる前記顕微鏡写真の取得を制御する、請求項16に記載の細胞培養装置。 The cell culture device according to claim 16, wherein the control unit controls recovery of the cells by the imaging cell recovery unit and acquisition of the photomicrograph by the imaging unit.
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