WO2016208753A1 - Filtration device and filtration method - Google Patents

Filtration device and filtration method Download PDF

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Publication number
WO2016208753A1
WO2016208753A1 PCT/JP2016/068917 JP2016068917W WO2016208753A1 WO 2016208753 A1 WO2016208753 A1 WO 2016208753A1 JP 2016068917 W JP2016068917 W JP 2016068917W WO 2016208753 A1 WO2016208753 A1 WO 2016208753A1
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WO
WIPO (PCT)
Prior art keywords
liquid
container
membrane
filtration device
filtration
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Application number
PCT/JP2016/068917
Other languages
French (fr)
Japanese (ja)
Inventor
近藤 孝志
萬壽 優
順子 渡邉
Original Assignee
株式会社村田製作所
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Application filed by 株式会社村田製作所 filed Critical 株式会社村田製作所
Priority to JP2017525464A priority Critical patent/JP6516007B2/en
Publication of WO2016208753A1 publication Critical patent/WO2016208753A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08Flat membrane modules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/02Devices for withdrawing samples
    • G01N1/10Devices for withdrawing samples in the liquid or fluent state

Definitions

  • the present invention relates to a filtration apparatus and a filtration method for filtering a biological substance in a liquid.
  • Patent Document 1 a cell trapping system for filtering biological substances in liquid has been disclosed (for example, see Patent Document 1).
  • the cell capture system disclosed in Patent Document 1 captures cells by passing a liquid containing cells as a biological substance from the upper side to the lower side in the vertical direction of the filter.
  • Patent Document 1 has a problem that clogging occurs due to deposition of a biological material on a filter, making it impossible to separate the biological material from a liquid.
  • the present invention solves the above-described problems, and an object of the present invention is to provide a filtration device and a filtration method capable of suppressing clogging due to a biological substance and separating the biological substance from a liquid.
  • the filtration device includes: A container having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid; A membrane part provided between the inlet and the outlet of the container part and having a plurality of through holes; With The biological substance is separated from the liquid by allowing the liquid to pass through the membrane portion in a horizontal direction.
  • the filtration method of one embodiment of the present invention includes: A method of filtering biological material from a liquid, A container part having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid, and provided between the inlet and the outlet of the container part, and having a plurality of through holes A step of preparing a filtration device comprising a membrane part, Separating the biological material by passing the liquid in a horizontal direction to the membrane part; including.
  • a filtration device and a filtration method capable of suppressing clogging due to a biological substance and separating the biological substance from a liquid.
  • FIG. 1 is a schematic configuration diagram of a filtration device according to a first embodiment of the present invention. Schematic which shows a part of film
  • the figure which shows the operation of the filtration device of the reference example The figure which shows the operation of the filtration device of the reference example
  • the figure which shows the operation of the filtration device of the reference example The figure which shows the operation of the filtration device of the reference example
  • Schematic block diagram of a filtration device of a modification of the first embodiment according to the present invention Schematic configuration diagram of a filtration device according to a second embodiment of the present invention
  • the filtration device includes: A container having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid; A membrane part provided between the inlet and the outlet of the container part and having a plurality of through holes; With The biological substance may be separated from the liquid by allowing the liquid to pass through the membrane portion in a horizontal direction.
  • the membrane part may be a metal thin film.
  • Such a configuration can suppress the deformation of the film portion even when a force is applied to the film portion.
  • At least a part of the membrane part may be provided obliquely with respect to the horizontal direction.
  • Such a configuration can further suppress clogging of the membrane part due to a biological substance.
  • the filtration device may include a suction unit that sucks the liquid from the introduction port of the container unit to the discharge port.
  • the biological substance can be separated from the liquid by sucking the liquid. Moreover, a biological substance can be separated from the liquid in a short time.
  • the filtration device includes a liquid container that holds the liquid, The inlet of the container portion is disposed in the liquid held in the liquid container, The liquid container may be provided with a vent for releasing pressure applied to the liquid.
  • the filtration device comprising a liquid container for holding the liquid,
  • the container portion is arranged such that the introduction port and the discharge port are positioned in a horizontal direction,
  • the inlet of the container portion is disposed in the liquid container;
  • the membrane portion may allow the liquid in the liquid container to pass in a direction opposite to the centrifugal force when a centrifugal force is applied.
  • the filtration method of one embodiment of the present invention includes: A method of filtering biological material from a liquid, A container part having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid, and provided between the inlet and the outlet of the container part, and having a plurality of through holes A step of preparing a filtration device comprising a membrane part, Separating the biological material by passing the liquid in a horizontal direction to the membrane part; May be included.
  • the liquid in the separation step, may be passed through the membrane part provided at least partially obliquely with respect to the horizontal direction.
  • Such a configuration can further suppress clogging of the membrane part due to a biological substance.
  • the separating step may include a step of sucking the liquid from the introduction port of the container part to the discharge port.
  • the biological substance can be separated from the liquid by sucking the liquid. Moreover, a biological substance can be separated from the liquid in a short time.
  • the separating step may include a step of releasing pressure applied to the liquid.
  • This configuration allows the pressure applied to the liquid to escape. Therefore, the clogging due to the deformation of the biological substance can be suppressed in the film part. In addition, damage to biological materials can be reduced.
  • the separating step includes Arranging the container part such that the inlet and the outlet of the container part are positioned in a horizontal direction; Disposing the inlet of the container in the liquid; A step of passing the liquid in a direction opposite to the centrifugal force in the membrane portion when a centrifugal force is applied to the liquid; May be included.
  • the liquid when a centrifugal force is applied to the membrane part, the liquid can be passed in the direction opposite to the centrifugal force, thereby further suppressing the occurrence of clogging due to the deposition of biological substances in the membrane part. Can do.
  • FIG. 1 is a schematic diagram of a filtration device 100A according to Embodiment 1 of the present invention.
  • the filtration device 100 ⁇ / b> A includes a container unit 10 that introduces a liquid 60 containing a biological substance 61, a membrane unit 20 that separates the biological substance 61 from the liquid 60, and a liquid container that holds the liquid 60. 30 and a suction part 40 for sucking the liquid 60.
  • the “biological substance” means a substance derived from a living organism such as a cell (eukaryotic organism), a bacterium (eubacteria), or a virus.
  • cells eukaryotes
  • examples of cells include eggs, sperm, induced pluripotent stem cells (iPS cells), ES cells, stem cells, mesenchymal stem cells, mononuclear cells, single cells, cell masses, suspension cells, and adhesions.
  • sex cells nerve cells, leukocytes, lymphocytes, cells for regenerative medicine, autologous cells, cancer cells, circulating cancer cells (CTC), HL-60, HELA, and fungi.
  • bacteria examples include gram positive bacteria, gram negative bacteria, Escherichia coli, and tuberculosis bacteria.
  • virus examples include DNA virus, RNA virus, rotavirus, (bird) influenza virus, yellow fever virus, dengue fever virus, encephalitis virus, hemorrhagic fever virus, and immunodeficiency virus.
  • filtration device 100A is particularly excellent in separating artificial pluripotent stem cells (iPS cells), ES cells, stem cells, and circulating cancer cells (CTC) in blood.
  • the biological substance may be a tissue in which cells are collected or an aggregated cell.
  • the container unit 10 has a cylindrical shape, and includes an introduction port 11 for introducing the liquid 60 at one end and a discharge port 12 for discharging the liquid 60 at the other end.
  • the container part 10 is arrange
  • a film part 20 is provided at the inlet 11 of the container part 10.
  • the introduction port 11 of the container unit 10 is inserted into an opening 32 provided on the side wall of the liquid container 30 and is disposed in the liquid 60 held in the liquid container 30.
  • the discharge port 12 of the container unit 10 is connected to the suction unit 40 via the tube 41.
  • the container portion 10 is formed of a resin such as acrylic, epoxy, polystyrene, or polycarbonate, glass mainly composed of silicon oxide, or the like.
  • the container portion 10 may be formed of a thermoplastic resin such as polypropylene, polystyrene, or polycarbonate resin.
  • the material of the container part 10 is preferably a material capable of various sterilizations such as gamma ray irradiation, autoclave, ethylene oxide gas, and the like.
  • the container portion 10 has, for example, an outer diameter of 1 mm to 60 mm, an inner diameter of 0.5 mm to 50 mm, and a height of 5 mm to 300 mm within a range smaller than the outer shape.
  • the membrane unit 20 is a porous membrane that separates the biological material 61 from the liquid 60.
  • the film part 20 is a metal thin film having a plurality of through holes 21.
  • the film unit 20 is a circular metal mesh, and has a pair of main surfaces facing each other, and a structure having a plurality of through holes 21 penetrating both main surfaces.
  • the membrane unit 20 separates the biological material 61 from the liquid 60 by allowing the liquid 60 in the liquid container 30 to pass in the horizontal direction 80.
  • the main surface located on the liquid container 30 side is defined as a first main surface HS1
  • the main surface located on the discharge port 12 side is defined as a second main surface HS2.
  • the film part 20 is provided in the introduction port 11 of the container part 10. The film part 20 is disposed so that the first main surface HS1 and the second main surface HS2 are orthogonal to the horizontal direction.
  • first main surface HS1 and the second main surface HS2 of the film unit 20 are orthogonal to the direction in which the liquid 60 flows from the introduction port 11 to the discharge port 12 of the container unit 10 (arrow 80 shown in FIG. 1). Are arranged.
  • the plurality of through holes 21 are periodically arranged over the first main surface HS1 and the second main surface HS2 of the film part 20.
  • the film part 20 is made of nickel, for example.
  • the dimensions of the film part 20 are, for example, a diameter of 6 mm and a thickness of 1.2 ⁇ m.
  • the material of the film part 20 may be gold, silver, copper, platinum, iron, nickel, chromium, stainless steel, palladium, titanium, cobalt, and oxides or alloys thereof.
  • gold, nickel, stainless steel, and titanium are preferable.
  • the material of the film part 20 is nickel, the nickel surface may be plated with gold.
  • the material of the film part 20 is preferably a material capable of various sterilizations such as gamma ray irradiation, autoclave, ethylene oxide gas, and the like.
  • FIG. 2 shows a schematic configuration diagram of a part of the film part 20 which is a two-dimensional periodic structure.
  • the X, Y, and Z directions in FIG. 2 indicate the vertical direction, horizontal direction, and thickness direction of the structure, respectively.
  • FIG. 3 shows a view of a part of the film part 20 of FIG. 2 as viewed from the Z direction.
  • the film part 20 may be a plate-like structure (lattice-like structure) in which a plurality of through holes 21 are arranged in a matrix at regular intervals.
  • the film part 20 is a plate-like structure provided with a plurality of square through holes 21 when viewed from the Z direction which is the main surface side.
  • the plurality of through holes 21 are provided at equal intervals in two arrangement directions parallel to each side of the square, that is, in the X direction and the Y direction in FIG.
  • the through-hole 21 is not limited to a square, For example, a rectangle, a circle
  • the arrangement of the holes is not limited to the square lattice arrangement, and for example, if the arrangement is a square arrangement, a rectangular arrangement in which the intervals in the two arrangement directions are not equal may be used, and a triangular lattice arrangement or a quasi-periodic arrangement may be used.
  • the through hole 21 may be provided with a taper.
  • the shape and dimensions of the through-hole 21 of the membrane part 20 are appropriately designed according to the size and shape of the biological substance 61 to be filtered.
  • the liquid container 30 is a container that holds the liquid 60 containing the biological substance 61.
  • the upper wall of the liquid container 30 is provided with a vent 31 for releasing the pressure applied to the liquid 60.
  • the biological substance 61 is pressurized by a negative pressure.
  • the filtering device 100A since the liquid 60 can be opened to the outside by the vent 31, the pressure applied to the biological substance 61 in the liquid 60 can be released to the outside.
  • an opening 32 to which the inlet 11 of the container part 10 is attached is provided on the side wall of the liquid container 30.
  • the introduction port 11 of the container unit 10 is inserted into the opening 32 provided on the side wall of the liquid container 30 and is disposed in the liquid 60 held in the liquid container 30.
  • the suction unit 40 sucks the liquid 60 held in the liquid container 30 from the introduction port 11 of the container unit 10 to the discharge port 12.
  • the suction part 40 is connected to the discharge port 12 of the container part 10 via the tube 41.
  • the suction unit 40 is a syringe. As shown in FIG. 1, the suction part 40 sucks the liquid 60 held in the liquid container 30 by pulling the plunger of the syringe (arrow 81 shown in FIG. 1). Thereby, the liquid 60 in the liquid container 30 moves in the horizontal direction from the first main surface HS1 to the second main surface HS2 through the film unit 20 from the inlet 11 to the outlet 12 of the container 10 (FIG. 1). Arrow 80).
  • FIG. 4 is a flowchart of the filtration method according to the first embodiment.
  • a filtration device 100A is prepared. Specifically, the inlet 11 of the container unit 10 is inserted into the opening 32 of the liquid container 30. A suction part 40 is attached to the discharge port 12 of the container part 10 via a tube 41.
  • step ST12 the liquid 60 containing the biological substance 61 is introduced into the liquid container 30.
  • step ST ⁇ b> 13 the biological material 61 is separated from the liquid 60 by allowing the liquid 60 to pass through the membrane unit 20.
  • Step ST13 includes step ST14 of sucking the liquid 60 in the liquid container 30 by the suction unit 40.
  • step ST14 by pulling the plunger of the suction part 40 (arrow 81 shown in FIG. 1), the liquid 60 held in the liquid container 30 is sucked from the inlet 11 of the container 10 to the outlet 12 ( Arrow 80 shown in FIG.
  • the liquid 60 passes in the horizontal direction from the first main surface HS1 of the film part 20 to the second main surface HS2.
  • the biological substance 61 cannot pass through the through hole 21 and remains in the liquid container 30.
  • Step ST13 includes step ST15 for releasing the pressure applied to the liquid 60 held in the liquid container 30.
  • the suction pressure is applied to the liquid 60 in the liquid container 30 by the suction unit 40, the biological material 61 may be deformed. Therefore, the pressure applied to the biological substance 61 in the liquid 60 can be reduced by releasing the pressure applied to the liquid 60 from the vent 31 of the liquid container 30.
  • the biological material 61 is separated from the liquid 60 by steps ST11 to ST15.
  • the liquid 60 that has passed through the membrane unit 20 can also be recovered.
  • FIGS. 5A to 5C show the operation of the filtration device 100A.
  • 5A to 5C omit the suction part 40 and the tube 41 for the sake of simplicity.
  • the liquid 60 is introduced into the liquid container 30 to which the container unit 10 is attached.
  • the liquid 60 is sucked from the inlet 11 to the outlet 12 of the container 10 by the suction part 40 (arrow 80 shown in FIG. 5B).
  • the liquid 60 in the liquid container 30 passes in the horizontal direction from the first main surface HS1 of the film unit 20 to the second main surface HS2.
  • the biological substance 61 cannot be passed through the through hole 21 and is captured by the membrane part 20. Therefore, the biological material 61 starts to collect on the first main surface HS1 of the film unit 20.
  • the cake layer A1 is formed by further gathering the biological material 61 on the lower side in the vertical direction of the first main surface HS1 of the film unit 20.
  • the region A2 on the upper side in the vertical direction of the first main surface HS1 of the film part 20 the collection and separation of the biological material 61 are repeated. For this reason, in the region A2, clogging due to the cake layer does not occur, and the liquid 60 can pass through the film part 20 (arrow 82 shown in FIG. 5C).
  • the upward direction in the vertical direction is defined as the upper side
  • the downward direction in the vertical direction is defined as the lower side.
  • the biological substance 61 in the liquid 60 is a vertical force due to the suction force in the horizontal direction (arrow 80 shown in FIGS. 5B and 5C) from the introduction port 11 to the discharge port 12 of the container unit 10 by the suction unit 40 and gravity.
  • the downward force works.
  • the biological material 61 collects in the film unit 20 on the upper side in the vertical direction.
  • the biological substance 61 separates from the film part 20 on the upper side in the vertical direction and collects on the lower side in the vertical direction.
  • the collection and separation of the biological material 61 are repeated by the balance between the suction force of the suction unit 40 and the vertically downward force due to gravity.
  • the biological substance 61 can be detached from the cake layer A1 by vibration of the filtration device 100A.
  • the biological material 61 may be separated from the cake layer A1 by vibration generated by shaking the filtering device 100A up and down and / or left and right.
  • the biological material 61 repeats the collection and the separation, so that clogging is unlikely to occur.
  • the biological material 61 is likely to move downward in the vertical direction. Therefore, in the region A2, the biological material 61 is less likely to accumulate and clogging is less likely to occur.
  • the filtering device 100 ⁇ / b> A As described above, in the filtering device 100 ⁇ / b> A, clogging due to the deposition of the biological substance 61 can be suppressed in the region A ⁇ b> 2 on the upper side in the vertical direction of the membrane unit 20, and the biological substance 61 can be continuously separated from the liquid 60. it can.
  • the filtration device of the reference example includes a container part 110 having an introduction port 111 for introducing the liquid 60 and a discharge port 112 for discharging the liquid 60, and a membrane part 120 having a plurality of through holes.
  • the container part 110 is arranged such that the axial direction of the container part 110 is the same as the vertical direction, that is, the gravity direction.
  • the introduction port 111 of the container unit 110 is located above the discharge port 112 in the vertical direction, and the film unit 120 is provided at the discharge port 112 of the container unit 110.
  • the liquid 60 is allowed to pass from the second main surface VS12 of the membrane unit 120 to the first main surface VS11 positioned on the lower side in the vertical direction than the second main surface VS12. That is, the filtering device 100A of the first embodiment allows the liquid 60 to pass through the membrane part 20 in the horizontal direction, whereas the filtering device of the reference example causes the liquid 60 to flow from the upper side to the lower side in the vertical direction. To pass. In the filtration device of the reference example, the liquid 60 is passed through the membrane part 120 by sucking the liquid 60 with a suction pump installed below.
  • the liquid 60 containing the biological substance 61 flows from the inlet 111 of the container 110 to the outlet 112 (arrow 80r shown in FIG. 6A). For this reason, the liquid 60 flowing in the container part 110 passes from the second principal surface VS12 of the film part 120 to the first principal surface VS11 located on the lower side in the vertical direction than the second principal surface VS12.
  • the biological substance 61 is captured by the membrane part 120. For this reason, the biological substance 61 is deposited on the entire second main surface VS112 of the film part 120.
  • the cake layer A3 is formed on the second main surface VS12 of the film part 120 due to the deposition of the biological material 61.
  • the thickness of the cake layer A3 gradually increases as the capture of the biological substance 61 by the membrane part 120 increases.
  • the filtration gradually shifts from the second main surface VS12 of the film part 120 to the upper layer A4 of the cake layer A3. That is, the separation of the biological substance 61 is not performed in the membrane part 120 but in the upper layer A4 of the cake layer A3.
  • the biological substance 61 captured by the membrane unit 120 is deposited on the entire second main surface VS12 of the membrane unit 120. For this reason, since the cake layer A3 gradually increases as the amount of the biological substance 61 captured by the membrane portion 120 increases, clogging occurs in the upper layer A4 of the cake layer A3. As a result, in the filtering device of the reference example, the filtration is stopped due to clogging due to the deposition of the biological substance 61 captured by the membrane part 120, and the biological substance 61 cannot be separated from the liquid 60.
  • the container part 10 is arranged so that the axial direction of the container part 10 is horizontal, and the liquid 60 is allowed to pass through the film part 20 in the horizontal direction.
  • the filtering device 100A it is possible to suppress the occurrence of clogging due to the deposition of the biological material 61 in the region A2 in the vertical direction above the first main surface HS1 of the film unit 20. Therefore, the filtering device 100A can continue to separate the biological material 61 from the liquid 60 by suppressing clogging as compared with the filtering device of the reference example.
  • the liquid 60 containing the biological substance 61 is passed in the horizontal direction from the first main surface HS1 of the membrane unit 20 to the second main surface HS2.
  • the biological substance 61 can be efficiently separated from the liquid 60 as compared with the filtering device of the reference example that allows the liquid 60 to pass through the membrane portion 120 from the upper side to the lower side in the vertical direction.
  • the filtering device 100A can suppress clogging of the membrane part 20 as compared with the filtering device of the reference example, it is possible to filter the liquid 60 having a higher concentration in a shorter period. Moreover, it can filter with high reproducibility compared with the filter apparatus of a reference example.
  • the filtering device 100A separates the biological material 61 and the liquid 60, but is not limited to this.
  • the filtration device 100A may filter a foreign substance having a size larger than that of the biological substance 61 contained in the liquid 60 by allowing the solution in the liquid 60 and the biological substance 61 to pass therethrough.
  • 100A of filtration apparatuses may filter and classify
  • the membrane unit 20 uses a metal thin film as a porous membrane. With such a configuration, it is possible to prevent the membrane portion 20 from being damaged by applying a force to the membrane portion 20. Further, even when the liquid 60 passes through the membrane part 20, since the through-hole 21 of the membrane part 20 is not easily deformed, the biological substance 61 is prevented from passing through the membrane part 20 due to the deformation of the through-hole 21. can do. Furthermore, damage to the film part 20 due to the liquid 60 can also be suppressed.
  • a vent 31 for releasing the pressure applied to the liquid 60 is provided on the upper wall of the liquid container 30.
  • the liquid 60 in the liquid container 30 can be opened to the outside. Therefore, the pressure applied to the liquid 60 can be released from the vent 31 and the pressure applied to the biological substance 61 in the liquid 60 can be reduced. As a result, it is possible to suppress the biological material 61 from being deformed, and to reduce clogging in the film unit 20.
  • the gas passing through the vent 31 is preferably sterilized. This is to prevent the mixing of biological materials other than the biological material 61 originally contained in the liquid 60.
  • the suction part 40 sucks the liquid 60 held in the liquid container 30, thereby allowing the liquid 60 to pass from the first main surface HS1 of the film part 20 to the second main surface HS2.
  • the liquid 60 in the liquid container 30 can be passed through the film unit 20 in the horizontal direction, and clogging of the film unit 20 can be suppressed.
  • the suction can be performed in a shorter time by sucking the liquid 60 by the suction unit 40.
  • the container part 10 demonstrated the structure arrange
  • the container part 10 may be arrange
  • the filtering device 100A may be arranged in an oblique direction to perform filtration.
  • the container part 10 demonstrated the structure which is a cylindrical body, it is not limited to this.
  • the container unit 10 may be configured to introduce the liquid 60 therein, pass through the film unit 20 and discharge the liquid 60, and may have a polygonal column shape such as a square column.
  • the membrane unit 20 may be a porous membrane, and may be a membrane, a filter paper, a nonwoven fabric, or the like, for example.
  • membrane part 20 is provided in the inlet 11 of the container part 10, it is not limited to this.
  • the film part 20 is only required to allow the liquid 60 to pass in the horizontal direction from the first main surface HS1 to the second main surface HS2, and the position of the film part 20 is not limited.
  • the film part 20 may be provided between the inlet 11 and the outlet 12 of the container part 10.
  • the film part 20 may be provided in the discharge port 12.
  • a plurality of film parts 20 may be provided between the inlet 11 and the outlet 12 of the container part 10.
  • the first film part 20 may be provided at the inlet 11 of the container part 10, and the second film part 20 may be provided closer to the discharge port 12 than the first film part 20.
  • the recovery rate can be improved by configuring the multistage filtration device 100A using the plurality of membrane portions 20.
  • the size of the through hole of the first film unit 20 and the size of the through hole of the second film unit 20 to be different, cells having two different sizes can be filtered. Thereby, a cell can be classified.
  • the film part 20 demonstrated the example which passes a liquid in the horizontal direction 80 toward the discharge port 12 from the inlet 11 of the container part 10, it is not limited to this.
  • the “horizontal direction” may include not only a direction orthogonal to the vertical direction but also an oblique direction having a predetermined angle with respect to the vertical direction. That is, in the film part 20, the main direction through which the liquid 60 passes may be a horizontal direction, and the direction through which the liquid 60 passes may include an oblique direction with respect to the horizontal direction.
  • FIG. 7 shows a filtration device 100B according to a modification of the first embodiment.
  • the membrane unit 20 may be arranged in an oblique direction with a predetermined angle ⁇ with respect to the horizontal direction.
  • the film part 20 may be disposed to be inclined with respect to the vertical direction.
  • membrane part 20 may be arrange
  • the liquid container 30 is provided with the vent 31 on the upper wall of the liquid container 30, but the present invention is not limited to this.
  • the vent 31 may be formed by providing a hole in the side wall of the liquid container 30.
  • a ventilation filter may be provided instead of the ventilation port 31.
  • the liquid container 30 demonstrated the structure provided with the vent 31 which releases the pressure concerning a liquid, it is not limited to this.
  • the liquid container 30 may be in a state where the vent 31 is not provided and the liquid 60 is not opened to the outside.
  • the present invention is not limited thereto.
  • the liquid 60 may be passed in the horizontal direction from the first main surface HS ⁇ b> 1 to the second main surface HS ⁇ b> 2 of the film unit 20.
  • the liquid 60 may be passed in the horizontal direction from the first main surface HS1 to the second main surface HS2 of the membrane unit 20.
  • the suction unit 40 may be any device that can suck the liquid 60, and may be, for example, a pump.
  • the liquid container 30 and the suction unit 40 are not essential components, and these elements may be omitted or replaced with other elements.
  • FIG. 8 shows a schematic configuration of a filtration device 100C according to the second embodiment.
  • differences from the first embodiment will be mainly described.
  • the same or similar components as those in the first embodiment will be described with the same or similar reference numerals.
  • descriptions overlapping with those in the first embodiment are omitted.
  • the filtration device 100C of the second embodiment is liquid by applying a centrifugal force in the direction from the discharge port 12a of the container part 10a to the introduction port 11a as compared with the filtration device 100A of the first embodiment.
  • the difference is that the biological material 61 can be separated from 60.
  • the filtration device 100C does not include the suction unit 40.
  • the filtration device 100C is disposed between a container portion 10a having an introduction port 11a for introducing the liquid 60 containing the biological substance 61 and a discharge port 12a for discharging the liquid 60, and the introduction port 11a and the discharge port 12a.
  • a film part 20 a having a plurality of through holes 21 and a liquid container 30 a for holding the liquid 60 are provided.
  • the container part 10a is arrange
  • the inlet 11a of the container part 10a is arranged in the liquid 60 in the liquid container 30a.
  • the membrane part 20a allows the liquid 60 in the liquid container 30a to pass in the direction opposite to the centrifugal force.
  • the filtering device 100C applies the centrifugal force in the direction from the discharge port 12a of the container part 10a to the introduction port 11a, thereby causing the liquid 60 in the liquid container 30a to flow from the first main surface HS1 of the film part 20a to the second main surface HS1. It passes through the surface HS2 in the horizontal direction.
  • the container portion 10a is provided with a deaeration hole.
  • a lid 50 that covers the opening of the liquid container 30a is attached in a state where the container portion 10a is disposed in the liquid container 30a.
  • FIGS. 9A to 9F show the filtration operation in the filtration device 100C.
  • the container portion 10a is removed from the liquid container 30a, and the liquid 60 containing the biological substance 61 is introduced into the liquid container 30a.
  • the container portion 10a is mounted in a liquid container 30a holding the liquid 60.
  • the lid 50 is attached to the liquid container 30a in a state where the container portion 10a is held inside the liquid container 30a. That is, the inlet 11a of the container part 10a is disposed in the liquid 60 in the liquid container 30a.
  • the lid 50 is attached by, for example, screwing a female screw provided inside the lid 50 and a male screw provided on the outer wall of the liquid container 30a.
  • the filtration device 100C is set in the centrifuge.
  • the filtration device 100C is set in the centrifuge so that the axial direction of the container portion 10a is horizontal. That is, the container part 10a is arranged in the centrifuge so that the inlet 11a and the outlet 12a of the container part 10a are positioned in the horizontal direction.
  • membrane part 20a become the same.
  • the height of the liquid surface of the liquid 60 between the outer wall of the container portion 10a and the inner wall of the liquid container 30a and the height of the liquid surface of the liquid 60 that has passed through the film portion 20a are the liquid container 30a at each location. This means the height of the liquid 60 from the bottom surface.
  • the centrifuge is stopped and the lid 50 is removed from the liquid container 30a.
  • the liquid 60 that has passed through the membrane portion 20a is discharged.
  • the liquid 60 is discharged by turning the liquid container 30a upside down with the container portion 10a attached to the liquid container 30a.
  • the biological substance 61 accumulated at the bottom of the liquid container 30a cannot pass through the through hole 21 of the membrane part 20a. Therefore, the liquid 60 not containing the biological substance 61 is discharged from the discharge port 12a.
  • a lid 50 is attached to the liquid container 30a, and centrifugal force from the outlet 12a to the inlet 11a is applied to the filtration device 100C by a centrifuge (arrow 83 shown in FIG. 9E).
  • a centrifuge arrow 83 shown in FIG. 9E.
  • the liquid 60 between the outer wall of the container 10a and the inner wall of the liquid container 30a flows to the bottom of the liquid container 30a (the arrow shown in FIG. 9E), similar to the operation shown in FIG. 9C.
  • the liquid 60 that does not contain the biological substance 61 passes through the membrane part 20a (arrow 85 shown in FIG. 9E).
  • membrane part 20a become the same.
  • the centrifuge is stopped and the lid 50 is removed from the liquid container 30a. Thereafter, similarly to the operation shown in FIG. 9D, the liquid 60 that has passed through the film part 20a and accumulated inside the container part 10a is discharged from the discharge port 12a.
  • the filtering device 100C separates the biological substance 61 from the liquid 60 by using the centrifugal force by performing the operations shown in FIGS. 9A to 9F. Furthermore, the filtration device 100C can concentrate the biological material 61 by repeating the operations shown in FIGS. 9A to 9F. Further, in the filtering device 100C, after concentration, the biological material 61 can be washed by introducing washing water. Further, in the filtering device 100C, after separating the biological material 61, the liquid 60 can be replaced with another liquid by introducing a replacement liquid.
  • the liquid 60 when a centrifugal force is applied, the liquid 60 is passed in the direction opposite to the direction in which the centrifugal force is applied in the membrane portion 20a. Specifically, when a centrifugal force is applied to the filtration device 100C, the height of the liquid surface between the outer wall of the container portion 10a and the inner wall of the liquid container 30a and the liquid 60 that has passed through the membrane portion 20a. The liquid 60 is allowed to pass through the film part 20a in the horizontal direction by utilizing the difference in height from the liquid level. With such a configuration, the biological substance 61 can be separated from the liquid 60 without clogging the membrane part 20 a with the biological substance 61. Further, in the filtration device 100C, the biological substance 61 can be easily concentrated by repeatedly performing filtration by centrifugation.
  • the liquid 60 that has passed through the membrane portion 20a when the liquid 60 that has passed through the membrane portion 20a is taken out, for example, the liquid 60 can be easily discharged by turning the filtering device 100C upside down.
  • the filtering device 100C pipetting by the operator is unnecessary, and the liquid 60 can be discharged without requiring a special skill from the operator.
  • the recovery rate of the biological material 61 is not reduced by pipetting.
  • the liquid 60 may be discharged by suction or the like.
  • the biological substance 61 can be easily washed by introducing washing water and performing centrifugation. Further, in the filtering device 100C, after the biological material 61 is separated, the liquid can be easily replaced by introducing the replacement liquid.
  • the filtration device 100C can be set with the axial direction of the container portion 10a being the same as the direction in which the centrifugal force is applied when it is attached to the centrifuge. For this reason, the centrifugal force is easily transmitted to the biological material 61, and the biological material 61 is easily separated from the liquid 60.
  • a centrifuge tube generally used for centrifugation is set obliquely with respect to the direction in which centrifugal force is applied when it is attached to a centrifuge.
  • the centrifuge tube if the axial direction of the centrifuge tube is set in the same direction as the centrifugal force, the separated biological material 61 is mixed with the liquid 60 again after centrifugation. For this reason, the centrifuge tube is disposed obliquely with respect to the direction in which the centrifugal force is applied in order to maintain the state where the centrifuged biological substance 61 is collected at the bottom of the centrifuge tube.
  • the centrifuge tube is disposed obliquely with respect to the direction in which the centrifugal force is applied, the centrifugal force is hardly transmitted to the biological material 61.
  • the axial direction of the container portion 10a can be set in the centrifuge so as to be the same as the direction in which the centrifugal force is applied, so that the centrifugal force is easily transmitted to the biological material 61. Therefore, the filtration device 100C can perform centrifugal separation under a rotation condition with a smaller number of rotations or a shorter time than a centrifuge tube by efficiently transmitting a centrifugal force to the biological material 61.
  • the filtering device 100C is set in the centrifuge so that the axial direction of the container portion 10a is the same as the direction in which the centrifugal force is applied has been described, but is not limited thereto.
  • the filtration device 100C may be set in the centrifuge so that the axial direction of the container portion 10a is inclined with respect to the direction in which the centrifugal force is applied.
  • FIG. 10 shows a schematic configuration of the filtration device 100D of the third embodiment.
  • FIG. 11 shows the filtration device 1 The figure which saw 00D from the top is shown. In order to simplify the description, the lid 10bb is omitted in FIG. A black arrow shown in FIG. 11 indicates the rotation direction of the filtration device 100D.
  • differences from the first embodiment will be mainly described.
  • the same or similar components as those in the first embodiment will be described with the same or similar reference numerals.
  • descriptions overlapping with those in the first embodiment are omitted.
  • the filtering device 100D of the third embodiment rotates the container portion 10b around the central axis CL of the container portion 10b as compared with the filtering device 100A of the first embodiment.
  • the difference is that the biological material 61 can be separated from the liquid 60 by the generated centrifugal force.
  • the filtration device 100D does not include the liquid container 30 and the suction unit 40.
  • the filtration device 100 ⁇ / b> D includes a container portion 10 b for introducing a liquid 60 containing a biological substance 61 and a membrane portion 20 b having a plurality of through holes 21.
  • the container part 10b includes a container body 10ba having an introduction port 11b for introducing the liquid 60, a lid part 10bb having a discharge port 12b for discharging the liquid 60, and a decompression port 70 for decompressing the inside of the container body 10ba.
  • the filtration device 100D forms a double cylinder structure by the container body 10ba and the membrane part 20b.
  • the inner cylinder is formed by a cylindrical film portion 20b
  • the outer cylinder is formed by a side wall of the container body 10ba.
  • a space for introducing the liquid 60 is formed between the membrane portion 20b and the side wall of the container body 10ba.
  • the bottom of the container body 10ba is inclined vertically downward toward the center of the container body 10ba.
  • the film part 20b is arranged between the inlet 11b and the outlet 12b of the container part 10b, and is arranged at a certain distance from the side wall of the container main body 10ba.
  • the filtration device 100D applies a centrifugal force from the central axis CL to the side wall of the container part 10b by rotating around the central axis CL of the container part 10b.
  • a centrifugal force is applied to the filtration device 100D, the liquid 60 in the container body 10ba moves in a direction opposite to the direction in which the centrifugal force is applied, and is horizontal from the first main surface HS1 to the second main surface HS2 of the film part 20a. Pass in the direction.
  • FIGS. 12A to 12C show the filtration operation in the filtration device 100D.
  • the lid portion 10bb is removed from the container body 10ba, and the liquid 60 containing the biological substance 61 is introduced into the container body 10ba from the introduction port 11b (arrow 86 shown in FIG. 12A).
  • a sealing lid 10bc is attached to the container body 10ba to seal the liquid 60 in the container body 10ba. Thereafter, the container portion 10b is rotated around the central axis CL of the container portion 10b (arrow 87 shown in FIG. 12B).
  • the rotation condition of the container part 10b may be set to a lower rotation than, for example, a condition for rotating a general centrifuge tube used for centrifugation.
  • the centrifugal force from the central axis CL to the side wall of the container body 10ba is loaded by rotating the container part 10b, the biological substance 61 gathers on the side wall of the container body 10ba. Therefore, the liquid located on the first main surface HS1 of the film part 20b is in a state where the concentration of the biological substance 61 is low.
  • the lid portion 10bc for sealing is removed and the lid portion 10bb is attached.
  • the inside of the container part 10b is made into a pressure-reduced state by reducing the pressure inside the container part 10b from the decompression port 70 provided in the upper part of the cover part 10bb.
  • the liquid 60 moves toward the central axis CL that is the rotation center of the container body 10ba. Therefore, the liquid 60 passes through the first main surface HS1 to the second main surface HS2 of the film part 20b in the horizontal direction and collects at the center of the bottom of the container body 10ba.
  • the liquid 60 collected at the center of the bottom of the container body 10ba is discharged to the outside by being sucked from the discharge port 12b (arrow 88 shown in FIG. 12C).
  • the biological material 61 is collected on the side wall of the container body 10ba by applying a centrifugal force, and the liquid 60 is moved in the direction opposite to the centrifugal force by reducing the pressure inside the container body 10ba. ing. Thereby, the liquid 60 and the biological material 61 are separated by collecting the liquid 60 in the center of the container body 10ba and discharging the liquid 60. Further, the filtration device 100D can perform the replacement, cleaning, and concentration processing of the liquid 60 by repeating the operations shown in FIGS. 12A to 12C.
  • the biological substance 61 can be separated from the liquid 60 by the centrifugal force from the central axis CL generated by rotating the container part 10b around the central axis CL of the container part 10b to the side wall of the container body 10ba. It has a configuration. With such a configuration, the filtration device 100D can collect the biological material 61 on the side wall of the container body 10ba by centrifugal force. Further, the liquid 60 having a low concentration of the biological substance 61 located on the first main surface HS1 of the film part 20b is moved in the direction opposite to the direction in which the centrifugal force is applied, thereby moving the first main part of the film part 20b. The liquid 60 can be passed in the horizontal direction from the surface HS1 to the second main surface HS2. As a result, clogging due to the biological material 61 can be suppressed in the film part 20b.
  • the biological material 61 collects on the side wall of the container body 10ba by the centrifugal action, the biological material 61 is unlikely to be deposited on the first main surface HS1 of the film part 20b. Therefore, the dimension of the through-hole 21 of the film part 20b can be made larger than the dimension of the through-hole of the filter used for filtration of Patent Document 1. As a result, in the filtering device 100D, it is possible to perform filtration under conditions superior to the extraction of the liquid 60.
  • the liquid 60 not containing the biological substance 61 can be extracted from the through-hole 21 of the membrane part 20b by reducing the pressure inside the container part 10b from the pressure reducing port 70. .
  • the filtering device 100D since the container portion 10b generates a centrifugal force by rotating around the central axis CL, the number of rotations can be reduced compared to a device that performs centrifugation using a centrifuge tube, Centrifugation time can be shortened. As a result, the number of organism-derived substances 61 that die due to centrifugation can be reduced.
  • the filtering device 100D when the liquid 60 that has passed through the membrane portion 20b is taken out, for example, the liquid 60 can be easily discharged by suction from the discharge port 12b. Thus, in the filtration device 100D, pipetting by the operator is unnecessary, and the liquid 60 can be discharged without requiring a special skill from the operator. As a result, in the filtration device 100D, the recovery rate of the biological material 61 is not reduced by pipetting.
  • the sealing lid 10bc is used when rotating the container 10b.
  • the present invention is not limited to this.
  • the lid portion 10bb having the discharge port 12b may be used even when the container portion 10b is rotated. With such a configuration, the rotation of the container portion 10b and the discharge of the liquid 60 can be performed simultaneously.
  • the film part 20b was demonstrated as a metal thin film which has the some cylindrical through-hole 21, it is not limited to this.
  • the film part 20 b may be a metallic thin film having at least a part of the through hole 21.
  • the shape of the film part 20b may be a polygonal cylindrical shape.
  • FIG. 13 shows a schematic configuration of a filtration device 100E according to a modification.
  • the filtration device 100E may be provided with a discharge port 12c near the center of the bottom of the container body 10ba. With such a configuration, the liquid 60 can be discharged without sucking the liquid 60 (arrow 89 shown in FIG. 13).
  • Embodiment 3 the configuration in which the decompression port 70 is provided in the lid portion 10bb of the container portion 10b has been described, but the configuration is not limited thereto.
  • the decompression port 70 is provided to facilitate passage of the liquid 60 in the horizontal direction from the first main surface HS1 of the film part 20b to the second main surface HS2, and is not an essential configuration.
  • the present invention relates to a filtration device and a filtration method, and is excellent in terms of filtering a high concentration liquid and filtering in a short time. For example, it is useful in the fields of chemical analysis, charge / pharmaceuticals, clinical examination, public health management, environmental measurement, and the like.

Abstract

Provided are a filtration device and filtration method which make it possible to suppress clogging caused by a biological substance, and separate the biological substance from a liquid. This filtration device is equipped with: a container having an introduction port through which a liquid containing a biological substance is introduced, and a discharge port through which the liquid is discharged; and a membrane having a plurality of through-holes and provided between the introduction port of the container and the discharge port thereof. The biological substance is separated from the liquid as a result of the passage of the liquid through the membrane in the horizontal direction.

Description

濾過装置及び濾過方法Filtration apparatus and filtration method
 本発明は、液体中の生物由来物質を濾過する濾過装置及び濾過方法に関する。 The present invention relates to a filtration apparatus and a filtration method for filtering a biological substance in a liquid.
 近年、液体中の生物由来物質を濾過する細胞捕捉システムが開示されている(例えば、特許文献1参照。)。特許文献1に開示された細胞捕捉システムは、生物由来物質として細胞を含む液体をフィルターの鉛直方向上側から下側に向かって通過させることによって細胞を捕捉している。 Recently, a cell trapping system for filtering biological substances in liquid has been disclosed (for example, see Patent Document 1). The cell capture system disclosed in Patent Document 1 captures cells by passing a liquid containing cells as a biological substance from the upper side to the lower side in the vertical direction of the filter.
国際公開第2015/019889号International Publication No. 2015/019889
 特許文献1の細胞捕捉システムにおいては、フィルター上に生物由来物質が堆積することによって目詰まりが生じ、液体から生物由来物質を分離することができなくなるという課題を有する。 The cell trapping system of Patent Document 1 has a problem that clogging occurs due to deposition of a biological material on a filter, making it impossible to separate the biological material from a liquid.
 本発明は、上記の課題を解決するものであり、生物由来物質による目詰まりを抑制し、液体から生物由来物質を分離することができる濾過装置及び濾過方法を提供することを目的とする。 The present invention solves the above-described problems, and an object of the present invention is to provide a filtration device and a filtration method capable of suppressing clogging due to a biological substance and separating the biological substance from a liquid.
 本発明の一態様の濾過装置は、
 生物由来物質を含む液体を導入する導入口と前記液体を排出する排出口とを有する容器部と、
 前記容器部の前記導入口と前記排出口との間に設けられ、複数の貫通孔を有する膜部と、
を備え、
 前記膜部へ水平方向に前記液体を通過させることによって、前記生物由来物質を前記液体から分離する。
The filtration device according to one embodiment of the present invention includes:
A container having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid;
A membrane part provided between the inlet and the outlet of the container part and having a plurality of through holes;
With
The biological substance is separated from the liquid by allowing the liquid to pass through the membrane portion in a horizontal direction.
 本発明の一態様の濾過方法は、
 液体から生物由来物質を濾過する方法であって、
 生物由来物質を含む液体を導入する導入口と前記液体を排出する排出口とを備える容器部と、前記容器部の前記導入口と前記排出口との間に設けられ、複数の貫通孔を有する膜部と、を備えた濾過装置を準備する工程、
 前記膜部へ水平方向に前記液体を通過させることによって、前記生物由来物質を分離する工程、
を含む。
The filtration method of one embodiment of the present invention includes:
A method of filtering biological material from a liquid,
A container part having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid, and provided between the inlet and the outlet of the container part, and having a plurality of through holes A step of preparing a filtration device comprising a membrane part,
Separating the biological material by passing the liquid in a horizontal direction to the membrane part;
including.
 本発明によれば、生物由来物質による目詰まりを抑制し、液体から生物由来物質を分離することができる濾過装置及び濾過方法を提供することができる。 According to the present invention, it is possible to provide a filtration device and a filtration method capable of suppressing clogging due to a biological substance and separating the biological substance from a liquid.
本発明に係る実施の形態1の濾過装置の概略構成図1 is a schematic configuration diagram of a filtration device according to a first embodiment of the present invention. 本発明に係る実施の形態1における膜部の一部を示す概略図Schematic which shows a part of film | membrane part in Embodiment 1 which concerns on this invention. 図2の膜部の一部を厚み方向から見た概略図Schematic of a part of the film part of FIG. 2 as seen from the thickness direction 本発明に係る実施の形態1の濾過方法を示すフローチャートThe flowchart which shows the filtration method of Embodiment 1 which concerns on this invention. 本発明に係る実施の形態1の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 1 which concerns on this invention. 本発明に係る実施の形態1の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 1 which concerns on this invention. 本発明に係る実施の形態1の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 1 which concerns on this invention. 参考例の濾過装置の動作を示す図The figure which shows the operation of the filtration device of the reference example 参考例の濾過装置の動作を示す図The figure which shows the operation of the filtration device of the reference example 参考例の濾過装置の動作を示す図The figure which shows the operation of the filtration device of the reference example 参考例の濾過装置の動作を示す図The figure which shows the operation of the filtration device of the reference example 本発明に係る実施の形態1の変形例の濾過装置の概略構成図Schematic block diagram of a filtration device of a modification of the first embodiment according to the present invention 本発明に係る実施の形態2の濾過装置の概略構成図Schematic configuration diagram of a filtration device according to a second embodiment of the present invention 本発明に係る実施の形態2の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 2 which concerns on this invention. 本発明に係る実施の形態2の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 2 which concerns on this invention. 本発明に係る実施の形態2の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 2 which concerns on this invention. 本発明に係る実施の形態2の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 2 which concerns on this invention. 本発明に係る実施の形態2の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 2 which concerns on this invention. 本発明に係る実施の形態2の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 2 which concerns on this invention. 本発明に係る実施の形態3の濾過装置の概略構成図Schematic configuration diagram of a filtration device according to a third embodiment of the present invention 本発明に係る実施の形態3の濾過装置を上から見た図The figure which looked at the filtration apparatus of Embodiment 3 concerning the present invention from the top 本発明に係る実施の形態3の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 3 which concerns on this invention. 本発明に係る実施の形態3の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 3 which concerns on this invention. 本発明に係る実施の形態3の濾過装置の動作を示す図The figure which shows operation | movement of the filtration apparatus of Embodiment 3 which concerns on this invention. 本発明に係る実施の形態3の変形例の濾過装置の概略構成図Schematic configuration diagram of a filtration device of a modification of the third embodiment according to the present invention
 本発明の一態様の濾過装置は、
 生物由来物質を含む液体を導入する導入口と前記液体を排出する排出口とを有する容器部と、
 前記容器部の前記導入口と前記排出口との間に設けられ、複数の貫通孔を有する膜部と、
を備え、
 前記膜部へ水平方向に前記液体を通過させることによって、前記生物由来物質を前記液体から分離してもよい。
The filtration device according to one embodiment of the present invention includes:
A container having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid;
A membrane part provided between the inlet and the outlet of the container part and having a plurality of through holes;
With
The biological substance may be separated from the liquid by allowing the liquid to pass through the membrane portion in a horizontal direction.
 このような構成により、生物由来物質の堆積による膜部の目詰まりを抑制し、液体から生物由来物質を分離することができる。 With such a configuration, the clogging of the film part due to the deposition of the biological material can be suppressed, and the biological material can be separated from the liquid.
 前記濾過装置において、前記膜部は、金属製薄膜であってもよい。 In the filtration device, the membrane part may be a metal thin film.
 このような構成により、膜部に力が加えられても、膜部が変形するのを抑制することができる。 Such a configuration can suppress the deformation of the film portion even when a force is applied to the film portion.
 前記濾過装置において、前記膜部の少なくとも一部は、水平方向に対して斜めに設けられてもよい。 In the filtration device, at least a part of the membrane part may be provided obliquely with respect to the horizontal direction.
 このような構成により、生物由来物質による膜部の目詰まりを更に抑制することができる。 Such a configuration can further suppress clogging of the membrane part due to a biological substance.
 前記濾過装置においては、前記容器部の前記導入口から前記排出口へ前記液体を吸引する吸引部を備えてもよい。 The filtration device may include a suction unit that sucks the liquid from the introduction port of the container unit to the discharge port.
 このような構成により、液体を吸引することで、液体から生物由来物質を分離することができる。また、短時間で液体から生物由来物質を分離することができる。 With such a configuration, the biological substance can be separated from the liquid by sucking the liquid. Moreover, a biological substance can be separated from the liquid in a short time.
 前記濾過装置においては、前記液体を保持する液体容器を備え、
 前記容器部の前記導入口は、前記液体容器内に保持された前記液体内に配置され、
 前記液体容器には、前記液体にかかる圧力を逃がす通気口が設けられてもよい。
The filtration device includes a liquid container that holds the liquid,
The inlet of the container portion is disposed in the liquid held in the liquid container,
The liquid container may be provided with a vent for releasing pressure applied to the liquid.
 このような構成により、液体容器内に保持された液体にかかる圧力を通気口から逃がすことによって、液体中の生物由来物質にかかる圧力を低減することができて、生物由来物質の損傷を低減できる。その結果、膜部において生物由来物質の変形による目詰まりを抑制することができる。 With such a configuration, by releasing the pressure applied to the liquid held in the liquid container from the vent, the pressure applied to the biological substance in the liquid can be reduced, and damage to the biological substance can be reduced. . As a result, clogging due to the deformation of the biological substance can be suppressed in the film part.
 前記濾過装置において、前記液体を保持する液体容器を備え、
 前記容器部は、前記導入口と前記排出口とが水平方向に位置するように配置され、
 前記容器部の前記導入口は、前記液体容器内に配置され、
 前記膜部は、遠心力を負荷したときにおいて、前記遠心力とは逆の方向に前記液体容器内の前記液体を通過させてもよい。
In the filtration device, comprising a liquid container for holding the liquid,
The container portion is arranged such that the introduction port and the discharge port are positioned in a horizontal direction,
The inlet of the container portion is disposed in the liquid container;
The membrane portion may allow the liquid in the liquid container to pass in a direction opposite to the centrifugal force when a centrifugal force is applied.
 このような構成により、膜部において遠心力によって液体を水平方向に通過させることができるため、膜部において生物由来物質の堆積による目詰まりを抑制することができる。 With such a configuration, since the liquid can be passed in the horizontal direction by centrifugal force in the membrane portion, clogging due to the deposition of biological substances in the membrane portion can be suppressed.
 本発明の一態様の濾過方法は、
 液体から生物由来物質を濾過する方法であって、
 生物由来物質を含む液体を導入する導入口と前記液体を排出する排出口とを備える容器部と、前記容器部の前記導入口と前記排出口との間に設けられ、複数の貫通孔を有する膜部と、を備えた濾過装置を準備する工程、
 前記膜部へ水平方向に前記液体を通過させることによって、前記生物由来物質を分離する工程、
を含んでもよい。
The filtration method of one embodiment of the present invention includes:
A method of filtering biological material from a liquid,
A container part having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid, and provided between the inlet and the outlet of the container part, and having a plurality of through holes A step of preparing a filtration device comprising a membrane part,
Separating the biological material by passing the liquid in a horizontal direction to the membrane part;
May be included.
 このような構成により、生物由来物質の堆積による膜部の目詰まりを抑制し、液体から生物由来物質を分離することができる。 With such a configuration, the clogging of the film part due to the deposition of the biological material can be suppressed, and the biological material can be separated from the liquid.
 前記濾過方法において、前記分離する工程は、水平方向に対して少なくとも一部が斜めに設けられた前記膜部に前記液体を通過させてもよい。 In the filtration method, in the separation step, the liquid may be passed through the membrane part provided at least partially obliquely with respect to the horizontal direction.
 このような構成により、生物由来物質による膜部の目詰まりを更に抑制することができる。 Such a configuration can further suppress clogging of the membrane part due to a biological substance.
 前記濾過方法において、前記分離する工程は、前記容器部の前記導入口から前記排出口へ前記液体を吸引する工程を含んでもよい。 In the filtration method, the separating step may include a step of sucking the liquid from the introduction port of the container part to the discharge port.
 このような構成により、液体を吸引することによって、液体から生物由来物質を分離することができる。また、短時間で液体から生物由来物質を分離することができる。 With such a configuration, the biological substance can be separated from the liquid by sucking the liquid. Moreover, a biological substance can be separated from the liquid in a short time.
 前記濾過方法において、前記分離する工程は、前記液体にかかる圧力を逃がす工程を含んでもよい。 In the filtration method, the separating step may include a step of releasing pressure applied to the liquid.
 このような構成により、液体にかかる圧力を逃がすことができる。そのため、膜部において生物由来物質の変形による目詰まりを抑制することができる。また、生物由来物質の損傷を低減できる。 This configuration allows the pressure applied to the liquid to escape. Therefore, the clogging due to the deformation of the biological substance can be suppressed in the film part. In addition, damage to biological materials can be reduced.
 前記濾過方法において、前記分離する工程は、
 前記容器部の前記導入口と前記排出口とが水平方向に位置するように前記容器部を配置する工程、
 前記液体内に前記容器部の前記導入口を配置する工程、
 前記液体に遠心力を負荷したとき、前記膜部において前記遠心力とは逆の方向に前記液体を通過させる工程、
を含んでもよい。
In the filtration method, the separating step includes
Arranging the container part such that the inlet and the outlet of the container part are positioned in a horizontal direction;
Disposing the inlet of the container in the liquid;
A step of passing the liquid in a direction opposite to the centrifugal force in the membrane portion when a centrifugal force is applied to the liquid;
May be included.
 このような構成により、膜部において遠心力を負荷したときに遠心力と逆の方向に液体を通過させることができるため、膜部において生物由来物質の堆積による目詰まりの発生を更に抑制することができる。 With such a configuration, when a centrifugal force is applied to the membrane part, the liquid can be passed in the direction opposite to the centrifugal force, thereby further suppressing the occurrence of clogging due to the deposition of biological substances in the membrane part. Can do.
 以下、本発明に係る実施の形態について、添付の図面を参照しながら説明する。また、各図においては、説明を容易なものとするため、各要素を誇張して示している。 Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. In each drawing, each element is exaggerated for easy explanation.
(実施の形態1)
[全体構成]
 図1は、本発明に係る実施の形態1の濾過装置100Aの概略図を示す。図1に示すように、濾過装置100Aは、生物由来物質61を含む液体60を導入する容器部10と、液体60から生物由来物質61を分離する膜部20と、液体60を保持する液体容器30と、液体60を吸引する吸引部40を備える。
(Embodiment 1)
[overall structure]
FIG. 1 is a schematic diagram of a filtration device 100A according to Embodiment 1 of the present invention. As shown in FIG. 1, the filtration device 100 </ b> A includes a container unit 10 that introduces a liquid 60 containing a biological substance 61, a membrane unit 20 that separates the biological substance 61 from the liquid 60, and a liquid container that holds the liquid 60. 30 and a suction part 40 for sucking the liquid 60.
 なお、本明細書において、「生物由来物質」とは、細胞(真核生物)、細菌(真性細菌)、ウィルス等の生物に由来する物質を意味する。細胞(真核生物)としては、例えば、卵、精子、人工多能性幹細胞(iPS細胞)、ES細胞、幹細胞、間葉系幹細胞、単核球細胞、単細胞、細胞塊、浮遊性細胞、接着性細胞、神経細胞、白血球、リンパ球、再生医療用細胞、自己細胞、がん細胞、血中循環がん細胞(CTC)、HL-60、HELA、菌類を含む。細菌(真性細菌)としては、例えば、グラム陽性菌、グラム陰性菌、大腸菌、結核菌を含む。ウィルスとしては、例えば、DNAウィルス、RNAウィルス、ロタウィルス、(鳥)インフルエンザウィルス、黄熱病ウィルス、デング熱病ウィルス、脳炎ウィルス、出血熱ウィルス、免疫不全ウィルスを含む。実施の形態1においては、濾過装置100Aは、特に、人工多能性幹細胞(iPS細胞)、ES細胞、幹細胞、血中循環がん細胞(CTC)、を液体中から分離するのに優れる。また、生物由来物質としては、細胞が集まった組織や、凝集した細胞であってもよい。 In the present specification, the “biological substance” means a substance derived from a living organism such as a cell (eukaryotic organism), a bacterium (eubacteria), or a virus. Examples of cells (eukaryotes) include eggs, sperm, induced pluripotent stem cells (iPS cells), ES cells, stem cells, mesenchymal stem cells, mononuclear cells, single cells, cell masses, suspension cells, and adhesions. Includes sex cells, nerve cells, leukocytes, lymphocytes, cells for regenerative medicine, autologous cells, cancer cells, circulating cancer cells (CTC), HL-60, HELA, and fungi. Examples of bacteria (true bacteria) include gram positive bacteria, gram negative bacteria, Escherichia coli, and tuberculosis bacteria. Examples of the virus include DNA virus, RNA virus, rotavirus, (bird) influenza virus, yellow fever virus, dengue fever virus, encephalitis virus, hemorrhagic fever virus, and immunodeficiency virus. In Embodiment 1, filtration device 100A is particularly excellent in separating artificial pluripotent stem cells (iPS cells), ES cells, stem cells, and circulating cancer cells (CTC) in blood. In addition, the biological substance may be a tissue in which cells are collected or an aggregated cell.
<容器部>
 容器部10は、筒状体の形状を有しており、一端に液体60を導入する導入口11と他端に液体60を排出する排出口12を備える。図1に示すように、容器部10は、容器部10の軸方向が水平方向、即ち重力方向(鉛直方向)に直交する方向となるように配置されている。容器部10の導入口11には、膜部20が設けられている。容器部10の導入口11は、液体容器30の側壁に設けられた開口32に挿入され、液体容器30に保持された液体60内に配置されている。容器部10の排出口12は、チューブ41を介して吸引部40に接続されている。
<Container part>
The container unit 10 has a cylindrical shape, and includes an introduction port 11 for introducing the liquid 60 at one end and a discharge port 12 for discharging the liquid 60 at the other end. As shown in FIG. 1, the container part 10 is arrange | positioned so that the axial direction of the container part 10 may turn into the direction orthogonal to a horizontal direction, ie, a gravity direction (vertical direction). A film part 20 is provided at the inlet 11 of the container part 10. The introduction port 11 of the container unit 10 is inserted into an opening 32 provided on the side wall of the liquid container 30 and is disposed in the liquid 60 held in the liquid container 30. The discharge port 12 of the container unit 10 is connected to the suction unit 40 via the tube 41.
 容器部10は、アクリル、エポキシ、ポリスチレン、ポリカーボネートなどの樹脂や、酸化ケイ素を主成分とするガラス等で形成されている。容器部10は、ポリプロピレン、ポリスチレン、ポリカーボネート樹脂等の熱可塑性樹脂で形成されてもよい。容器部10の材料は、ガンマ線照射、オートクレーブ、エチレンオキサイドガス、など各種滅菌が可能な材料であることが好ましい。容器部10は、例えば、外径1mm以上60mm以下、内径は外形より小さい範囲で0.5mm以上50mm以下、高さ5mm以上300mm以下である。 The container portion 10 is formed of a resin such as acrylic, epoxy, polystyrene, or polycarbonate, glass mainly composed of silicon oxide, or the like. The container portion 10 may be formed of a thermoplastic resin such as polypropylene, polystyrene, or polycarbonate resin. The material of the container part 10 is preferably a material capable of various sterilizations such as gamma ray irradiation, autoclave, ethylene oxide gas, and the like. The container portion 10 has, for example, an outer diameter of 1 mm to 60 mm, an inner diameter of 0.5 mm to 50 mm, and a height of 5 mm to 300 mm within a range smaller than the outer shape.
<膜部>
 膜部20は、液体60から生物由来物質61を分離する多孔膜である。具体的には、膜部20は、複数の貫通孔21を有する金属製薄膜である。実施の形態1において、膜部20は、円形の金属メッシュであり、互いに対向する一対の主面を有し、両主面を貫通する複数の貫通孔21を有する構造体である。
<Membrane part>
The membrane unit 20 is a porous membrane that separates the biological material 61 from the liquid 60. Specifically, the film part 20 is a metal thin film having a plurality of through holes 21. In the first embodiment, the film unit 20 is a circular metal mesh, and has a pair of main surfaces facing each other, and a structure having a plurality of through holes 21 penetrating both main surfaces.
 図1に示すように、膜部20は、液体容器30内の液体60を水平方向80に通過させることによって、生物由来物質61を液体60から分離している。実施の形態1においては、液体容器30側に位置する主面を第1主面HS1とし、排出口12側に位置する主面を第2主面HS2と定義する。実施の形態1において、膜部20は、容器部10の導入口11に設けられている。膜部20は、水平方向に対して第1主面HS1及び第2主面HS2が直交するように配置されている。即ち、膜部20の第1主面HS1及び第2主面HS2は、容器部10の導入口11から排出口12へ液体60が流れる方向(図1に示す矢印80)に対して直交するように配置されている。 As shown in FIG. 1, the membrane unit 20 separates the biological material 61 from the liquid 60 by allowing the liquid 60 in the liquid container 30 to pass in the horizontal direction 80. In the first embodiment, the main surface located on the liquid container 30 side is defined as a first main surface HS1, and the main surface located on the discharge port 12 side is defined as a second main surface HS2. In the first embodiment, the film part 20 is provided in the introduction port 11 of the container part 10. The film part 20 is disposed so that the first main surface HS1 and the second main surface HS2 are orthogonal to the horizontal direction. That is, the first main surface HS1 and the second main surface HS2 of the film unit 20 are orthogonal to the direction in which the liquid 60 flows from the introduction port 11 to the discharge port 12 of the container unit 10 (arrow 80 shown in FIG. 1). Are arranged.
 複数の貫通孔21は、膜部20の第1主面HS1及び第2主面HS2上の全体にわたって周期的に配置されている。膜部20は、例えば、ニッケルで形成されている。膜部20の寸法は、例えば、直径6mm、厚さ1.2μmである。膜部20の材料は、金、銀、銅、白金、鉄、ニッケル、クロム、ステンレス鋼、パラジウム、チタン、コバルト、およびこれらの酸化物又は合金であってもよい。特に、膜部20の材料としては、生物由来物質61を捕捉する場合、金、ニッケル、ステンレス、チタンが好ましい。膜部20の材料をニッケルとした場合、ニッケルの表面に金めっきしてもよい。 また、膜部20の材料は、ガンマ線照射、オートクレーブ、エチレンオキサイドガスなどの各種滅菌が可能な材料であることが好ましい。 The plurality of through holes 21 are periodically arranged over the first main surface HS1 and the second main surface HS2 of the film part 20. The film part 20 is made of nickel, for example. The dimensions of the film part 20 are, for example, a diameter of 6 mm and a thickness of 1.2 μm. The material of the film part 20 may be gold, silver, copper, platinum, iron, nickel, chromium, stainless steel, palladium, titanium, cobalt, and oxides or alloys thereof. In particular, as the material of the film part 20, when the biological substance 61 is captured, gold, nickel, stainless steel, and titanium are preferable. When the material of the film part 20 is nickel, the nickel surface may be plated with gold. The material of the film part 20 is preferably a material capable of various sterilizations such as gamma ray irradiation, autoclave, ethylene oxide gas, and the like.
 図2は、2次元周期構造体である膜部20の一部の概略構成図を示す。図2中のX、Y、Z方向は、それぞれ構造体の縦方向、横方向、厚み方向を示している。図3は、図2の膜部20の一部をZ方向から見た図を示す。図2及び図3に示すように、膜部20は、マトリックス状に一定の間隔で複数の貫通孔21が配置された板状構造体(格子状構造体)であってもよい。膜部20は、その主面側であるZ方向から見て正方形の貫通孔21が複数設けられた板状構造体である。複数の貫通孔21は、正方形の各辺と平行な2つの配列方向、即ち図2中のX方向とY方向に等しい間隔で設けられている。なお、貫通孔21は、正方形に限定されず、例えば長方形や円や楕円などでもよい。また、孔の配列も正方格子配列に限定されず、例えば方形配列であれば、2つの配列方向の間隔は等しくない長方形配列でもよく、三角格子配列や準周期配列などでもよい。なお、貫通孔21には、テーパが設けられていてもよい。 FIG. 2 shows a schematic configuration diagram of a part of the film part 20 which is a two-dimensional periodic structure. The X, Y, and Z directions in FIG. 2 indicate the vertical direction, horizontal direction, and thickness direction of the structure, respectively. FIG. 3 shows a view of a part of the film part 20 of FIG. 2 as viewed from the Z direction. As shown in FIGS. 2 and 3, the film part 20 may be a plate-like structure (lattice-like structure) in which a plurality of through holes 21 are arranged in a matrix at regular intervals. The film part 20 is a plate-like structure provided with a plurality of square through holes 21 when viewed from the Z direction which is the main surface side. The plurality of through holes 21 are provided at equal intervals in two arrangement directions parallel to each side of the square, that is, in the X direction and the Y direction in FIG. In addition, the through-hole 21 is not limited to a square, For example, a rectangle, a circle | round | yen, an ellipse etc. may be sufficient. Further, the arrangement of the holes is not limited to the square lattice arrangement, and for example, if the arrangement is a square arrangement, a rectangular arrangement in which the intervals in the two arrangement directions are not equal may be used, and a triangular lattice arrangement or a quasi-periodic arrangement may be used. The through hole 21 may be provided with a taper.
 膜部20の貫通孔21の形状や寸法は、濾過する生物由来物質61の大きさ、形状に応じて適宜設計されるものである。 The shape and dimensions of the through-hole 21 of the membrane part 20 are appropriately designed according to the size and shape of the biological substance 61 to be filtered.
<液体容器>
 液体容器30は、生物由来物質61を含む液体60を保持する容器である。液体容器30の上壁には、液体60にかかる圧力を逃がす通気口31が設けられている。実施の形態1においては、吸引部40によって液体60を吸引しているため、負圧により生物由来物質61に圧力がかかる。濾過装置100Aにおいては、通気口31によって液体60を外部に開放した状態にすることができるため、液体60中の生物由来物質61にかかる圧力を外部に逃がすことができる。
<Liquid container>
The liquid container 30 is a container that holds the liquid 60 containing the biological substance 61. The upper wall of the liquid container 30 is provided with a vent 31 for releasing the pressure applied to the liquid 60. In the first embodiment, since the liquid 60 is sucked by the suction unit 40, the biological substance 61 is pressurized by a negative pressure. In the filtering device 100A, since the liquid 60 can be opened to the outside by the vent 31, the pressure applied to the biological substance 61 in the liquid 60 can be released to the outside.
 また、液体容器30の側壁には、容器部10の導入口11が取り付けられる開口32が設けられている。図1に示すように、容器部10の導入口11は、液体容器30の側壁に設けられた開口32に挿入され、液体容器30に保持された液体60内に配置される。 Further, an opening 32 to which the inlet 11 of the container part 10 is attached is provided on the side wall of the liquid container 30. As shown in FIG. 1, the introduction port 11 of the container unit 10 is inserted into the opening 32 provided on the side wall of the liquid container 30 and is disposed in the liquid 60 held in the liquid container 30.
<吸引部>
 吸引部40は、液体容器30内に保持された液体60を、容器部10の導入口11から排出口12へ吸引するものである。吸引部40は、チューブ41を介して容器部10の排出口12に接続される。実施の形態1において、吸引部40は、シリンジである。図1に示すように、吸引部40は、シリンジのプランジャーを引っ張る(図1に示す矢印81)ことによって、液体容器30内に保持された液体60を吸引している。これにより、液体容器30内の液体60が、容器部10の導入口11から排出口12へ向かって膜部20を第1主面HS1から第2主面HS2へ水平方向に移動する(図1に示す矢印80)。
<Suction part>
The suction unit 40 sucks the liquid 60 held in the liquid container 30 from the introduction port 11 of the container unit 10 to the discharge port 12. The suction part 40 is connected to the discharge port 12 of the container part 10 via the tube 41. In the first embodiment, the suction unit 40 is a syringe. As shown in FIG. 1, the suction part 40 sucks the liquid 60 held in the liquid container 30 by pulling the plunger of the syringe (arrow 81 shown in FIG. 1). Thereby, the liquid 60 in the liquid container 30 moves in the horizontal direction from the first main surface HS1 to the second main surface HS2 through the film unit 20 from the inlet 11 to the outlet 12 of the container 10 (FIG. 1). Arrow 80).
[濾過方法]
 実施の形態1に係る濾過方法について、図4を用いて説明する。
 図4は、実施の形態1に係る濾過方法のフローチャートである。
[Filtration method]
The filtration method according to Embodiment 1 will be described with reference to FIG.
FIG. 4 is a flowchart of the filtration method according to the first embodiment.
 図4に示すように、ステップST11において、濾過装置100Aを準備する。具体的には、容器部10の導入口11を液体容器30の開口32に挿入する。容器部10の排出口12に、吸引部40を、チューブ41を介して取り付ける。 As shown in FIG. 4, in step ST11, a filtration device 100A is prepared. Specifically, the inlet 11 of the container unit 10 is inserted into the opening 32 of the liquid container 30. A suction part 40 is attached to the discharge port 12 of the container part 10 via a tube 41.
 ステップST12において、液体容器30内に生物由来物質61を含む液体60を導入する。 In step ST12, the liquid 60 containing the biological substance 61 is introduced into the liquid container 30.
 ステップST13において、膜部20に液体60を通過させることによって液体60から生物由来物質61を分離する。ステップST13は、吸引部40によって液体容器30内の液体60を吸引するステップST14を含む。 In step ST <b> 13, the biological material 61 is separated from the liquid 60 by allowing the liquid 60 to pass through the membrane unit 20. Step ST13 includes step ST14 of sucking the liquid 60 in the liquid container 30 by the suction unit 40.
 ステップST14において、吸引部40のプランジャーを引っ張ることで(図1に示す矢印81)、液体容器30内に保持された液体60を、容器部10の導入口11から排出口12へ吸引する(図1に示す矢印80)。吸引部40によって液体60を吸引することによって、液体60が膜部20の第1主面HS1から第2主面HS2へ水平方向に通過する。液体60が膜部20を通過する際、生物由来物質61は、貫通孔21を通過することができずに液体容器30内に残る。 In step ST14, by pulling the plunger of the suction part 40 (arrow 81 shown in FIG. 1), the liquid 60 held in the liquid container 30 is sucked from the inlet 11 of the container 10 to the outlet 12 ( Arrow 80 shown in FIG. By sucking the liquid 60 by the suction part 40, the liquid 60 passes in the horizontal direction from the first main surface HS1 of the film part 20 to the second main surface HS2. When the liquid 60 passes through the membrane part 20, the biological substance 61 cannot pass through the through hole 21 and remains in the liquid container 30.
 ステップST13において、液体容器30内に保持された液体60にかかる圧力を逃がすステップST15を含む。吸引部40によって液体容器30内の液体60に吸引圧力がかかると、生物由来物質61が変形する可能性がある。そのため、液体容器30の通気口31から液体60にかかる圧力を逃がすことによって、液体60中の生物由来物質61にかかる圧力を低減することができる。 Step ST13 includes step ST15 for releasing the pressure applied to the liquid 60 held in the liquid container 30. When the suction pressure is applied to the liquid 60 in the liquid container 30 by the suction unit 40, the biological material 61 may be deformed. Therefore, the pressure applied to the biological substance 61 in the liquid 60 can be reduced by releasing the pressure applied to the liquid 60 from the vent 31 of the liquid container 30.
 以上のように、実施の形態1に係る濾過方法では、ステップST11~ST15によって、液体60から生物由来物質61を分離している。また、実施の形態1に係る濾過方法では、膜部20を通過した液体60を回収することもできる。 As described above, in the filtration method according to the first embodiment, the biological material 61 is separated from the liquid 60 by steps ST11 to ST15. In the filtration method according to the first embodiment, the liquid 60 that has passed through the membrane unit 20 can also be recovered.
[濾過装置の動作]
 濾過装置100Aの動作について、図5A~図5Cを用いて詳細に説明する。
 図5A~図5Cは、濾過装置100Aの動作を示す。なお、図5A~図5Cは、説明を簡略化するために吸引部40、チューブ41を省略している。
[Operation of filtration device]
The operation of the filtration device 100A will be described in detail with reference to FIGS. 5A to 5C.
5A to 5C show the operation of the filtration device 100A. 5A to 5C omit the suction part 40 and the tube 41 for the sake of simplicity.
 図5Aに示すように、濾過を開始する前において、容器部10を取り付けた液体容器30の内部に液体60を導入する。 As shown in FIG. 5A, before starting filtration, the liquid 60 is introduced into the liquid container 30 to which the container unit 10 is attached.
 図5Bに示すように、吸引部40によって、容器部10の導入口11から排出口12へ液体60を吸引する(図5Bに示す矢印80)。液体容器30内の液体60は、膜部20の第1主面HS1から第2主面HS2へ水平方向に通過する。液体60が膜部20を通過する際、生物由来物質61が貫通孔21を通過できずに、膜部20に捕捉される。そのため、膜部20の第1主面HS1に生物由来物質61が集合し始める。 As shown in FIG. 5B, the liquid 60 is sucked from the inlet 11 to the outlet 12 of the container 10 by the suction part 40 (arrow 80 shown in FIG. 5B). The liquid 60 in the liquid container 30 passes in the horizontal direction from the first main surface HS1 of the film unit 20 to the second main surface HS2. When the liquid 60 passes through the membrane part 20, the biological substance 61 cannot be passed through the through hole 21 and is captured by the membrane part 20. Therefore, the biological material 61 starts to collect on the first main surface HS1 of the film unit 20.
 図5Cに示すように、液体60を方向80へ吸引し続けると、膜部20の第1主面HS1の鉛直方向下側では、生物由来物質61が更に集合することによってケーク層A1が形成される。膜部20の鉛直方向下側では、ケーク層A1によって目詰まりが発生するため、液体60が膜部20を通過できなくなる。一方、膜部20の第1主面HS1の鉛直方向上側の領域A2おいては、生物由来物質61の集合と離脱が繰り返される。このため、領域A2では、ケーク層による目詰まりが生じず、液体60が膜部20を通過することができる(図5Cに示す矢印82)。なお、本明細書では、鉛直方向上向きを上側とし、鉛直方向下向きを下側と定義する。 As illustrated in FIG. 5C, when the liquid 60 is continuously sucked in the direction 80, the cake layer A1 is formed by further gathering the biological material 61 on the lower side in the vertical direction of the first main surface HS1 of the film unit 20. The On the lower side in the vertical direction of the film part 20, clogging occurs due to the cake layer A <b> 1, so that the liquid 60 cannot pass through the film part 20. On the other hand, in the region A2 on the upper side in the vertical direction of the first main surface HS1 of the film part 20, the collection and separation of the biological material 61 are repeated. For this reason, in the region A2, clogging due to the cake layer does not occur, and the liquid 60 can pass through the film part 20 (arrow 82 shown in FIG. 5C). In the present specification, the upward direction in the vertical direction is defined as the upper side, and the downward direction in the vertical direction is defined as the lower side.
 濾過装置100Aにおいては、液体60中の生物由来物質61には、重力により鉛直下向きへの力が加わっている。したがって、液体60中の生物由来物質61には、吸引部40による容器部10の導入口11から排出口12への水平方向(図5B及び図5Cに示す矢印80)の吸引力と重力による鉛直下向きへの力が働く。このため、領域A2において、吸引部40による吸引力が重力よりも大きい場合、生物由来物質61が鉛直方向上側における膜部20に集合する。一方、吸引部40による吸引力が重力よりも小さい場合、生物由来物質61は、鉛直方向上側における膜部20から離脱し、鉛直方向下側に集合する。このように、領域A2においては、吸引部40の吸引力と、重力による鉛直下向きへの力とのバランスによって、生物由来物質61の集合と離脱が繰り返されている。また、生物由来物質61のケーク層A1からの離脱は、濾過装置100Aの振動によっても行うことができる。例えば、濾過装置100Aを上下及び/又は左右に振ることにより生じる振動によって、生物由来物質61をケーク層A1から離脱させてもよい。 In the filtering device 100A, a force directed vertically downward is applied to the biological material 61 in the liquid 60 by gravity. Therefore, the biological substance 61 in the liquid 60 is a vertical force due to the suction force in the horizontal direction (arrow 80 shown in FIGS. 5B and 5C) from the introduction port 11 to the discharge port 12 of the container unit 10 by the suction unit 40 and gravity. The downward force works. For this reason, in the region A2, when the suction force by the suction unit 40 is larger than the gravity, the biological material 61 collects in the film unit 20 on the upper side in the vertical direction. On the other hand, when the suction force by the suction part 40 is smaller than the gravity, the biological substance 61 separates from the film part 20 on the upper side in the vertical direction and collects on the lower side in the vertical direction. As described above, in the region A2, the collection and separation of the biological material 61 are repeated by the balance between the suction force of the suction unit 40 and the vertically downward force due to gravity. Moreover, the biological substance 61 can be detached from the cake layer A1 by vibration of the filtration device 100A. For example, the biological material 61 may be separated from the cake layer A1 by vibration generated by shaking the filtering device 100A up and down and / or left and right.
 このように、濾過装置100Aでは、膜部20の鉛直方向上側の領域A2においては、生物由来物質61が集合と離脱を繰り返すため、目詰まりが生じにくい。 As described above, in the filtering device 100A, in the region A2 on the upper side in the vertical direction of the membrane unit 20, the biological material 61 repeats the collection and the separation, so that clogging is unlikely to occur.
 また、膜部20の第1主面HS1の鉛直方向上側の領域A2においては、重力により鉛直下向きの力が働いているため、生物由来物質61が鉛直下方向に移動しやすい。そのため、領域A2においては、生物由来物質61が堆積しにくくなり、目詰まりが生じにくい。 Moreover, in the region A2 on the upper side in the vertical direction of the first main surface HS1 of the film part 20, since a downward force is applied due to gravity, the biological material 61 is likely to move downward in the vertical direction. Therefore, in the region A2, the biological material 61 is less likely to accumulate and clogging is less likely to occur.
 以上のように、濾過装置100Aでは、膜部20の鉛直方向上側の領域A2において生物由来物質61の堆積による目詰まりを抑制することができ、液体60から生物由来物質61を分離し続けることができる。 As described above, in the filtering device 100 </ b> A, clogging due to the deposition of the biological substance 61 can be suppressed in the region A <b> 2 on the upper side in the vertical direction of the membrane unit 20, and the biological substance 61 can be continuously separated from the liquid 60. it can.
 次に、比較のために、参考例の濾過装置について、図6A~図6Dを用いて説明する。 Next, for comparison, a filtering device of a reference example will be described with reference to FIGS. 6A to 6D.
 参考例の濾過装置は、液体60を導入する導入口111と液体60を排出する排出口112を有する容器部110と、複数の貫通孔を有する膜部120とを備える。参考例の濾過装置において、容器部110は、容器部110の軸方向が鉛直方向、即ち重力方向と同じ向きに配置されている。容器部110の導入口111は、排出口112より鉛直方向において上方に位置しており、膜部120は、容器部110の排出口112に設けられている。参考例の濾過装置においては、膜部120の第2主面VS12から第2主面VS12よりも鉛直方向下側に位置する第1主面VS11に液体60を通過させている。即ち、実施の形態1の濾過装置100Aは、水平方向に液体60を膜部20に通過させるのに対し、参考例の濾過装置は、鉛直方向上側から下側に向かって液体60を膜部120に通過させている。なお、参考例の濾過装置は、下方に設置された吸引ポンプによって液体60を吸引することにより、膜部120に液体60を通過させている。 The filtration device of the reference example includes a container part 110 having an introduction port 111 for introducing the liquid 60 and a discharge port 112 for discharging the liquid 60, and a membrane part 120 having a plurality of through holes. In the filtering device of the reference example, the container part 110 is arranged such that the axial direction of the container part 110 is the same as the vertical direction, that is, the gravity direction. The introduction port 111 of the container unit 110 is located above the discharge port 112 in the vertical direction, and the film unit 120 is provided at the discharge port 112 of the container unit 110. In the filtering device of the reference example, the liquid 60 is allowed to pass from the second main surface VS12 of the membrane unit 120 to the first main surface VS11 positioned on the lower side in the vertical direction than the second main surface VS12. That is, the filtering device 100A of the first embodiment allows the liquid 60 to pass through the membrane part 20 in the horizontal direction, whereas the filtering device of the reference example causes the liquid 60 to flow from the upper side to the lower side in the vertical direction. To pass. In the filtration device of the reference example, the liquid 60 is passed through the membrane part 120 by sucking the liquid 60 with a suction pump installed below.
 図6Aに示すように、参考例の濾過装置において、生物由来物質61を含む液体60が、容器部110の導入口111から排出口112へ流れる(図6Aに示す矢印80r)。このため、容器部110内を流れる液体60は、膜部120の第2主面VS12から第2主面VS12より鉛直方向下側に位置する第1主面VS11へ通過する。液体60が膜部120を通過する際に、生物由来物質61が膜部120によって捕捉される。このため、膜部120の第2主面VS112全体に、生物由来物質61が堆積していく。 As shown in FIG. 6A, in the filtration device of the reference example, the liquid 60 containing the biological substance 61 flows from the inlet 111 of the container 110 to the outlet 112 (arrow 80r shown in FIG. 6A). For this reason, the liquid 60 flowing in the container part 110 passes from the second principal surface VS12 of the film part 120 to the first principal surface VS11 located on the lower side in the vertical direction than the second principal surface VS12. When the liquid 60 passes through the membrane part 120, the biological substance 61 is captured by the membrane part 120. For this reason, the biological substance 61 is deposited on the entire second main surface VS112 of the film part 120.
 図6Bに示すように、方向80rに向かって液体60を流し続けると、膜部120の第2主面VS12上に生物由来物質61の堆積によるケーク層A3が形成される。 As shown in FIG. 6B, when the liquid 60 continues to flow in the direction 80r, the cake layer A3 is formed on the second main surface VS12 of the film part 120 due to the deposition of the biological material 61.
 図6Cに示すように、膜部120による生物由来物質61の捕捉が増えていくと、ケーク層A3の厚さが徐々に大きくなっていく。このとき、濾過は、膜部120の第2主面VS12からケーク層A3の上層A4に徐々に移行する。即ち、生物由来物質61の分離は、膜部120で行われるのではなくケーク層A3の上層A4で行われるようになる。 As shown in FIG. 6C, the thickness of the cake layer A3 gradually increases as the capture of the biological substance 61 by the membrane part 120 increases. At this time, the filtration gradually shifts from the second main surface VS12 of the film part 120 to the upper layer A4 of the cake layer A3. That is, the separation of the biological substance 61 is not performed in the membrane part 120 but in the upper layer A4 of the cake layer A3.
 図6Dに示すように、生物由来物質61が膜部120の第2主面VS12上に更に堆積すると、ケーク層A3の厚さが更に大きくなる。また、ケーク層A3の上層A4では、生物由来物質61の堆積による目詰まりが進行する。ケーク層A3の上層A4において、目詰まりが増加していくと、やがて液体60がケーク層A3の上層A4を通過できなくなる。 As shown in FIG. 6D, when the biological substance 61 is further deposited on the second main surface VS12 of the film part 120, the thickness of the cake layer A3 is further increased. In the upper layer A4 of the cake layer A3, clogging due to the deposition of the biological material 61 proceeds. If clogging increases in the upper layer A4 of the cake layer A3, the liquid 60 cannot pass through the upper layer A4 of the cake layer A3.
 このように、参考例の濾過装置では、膜部120によって捕捉された生物由来物質61が膜部120の第2主面VS12全体に堆積する。このため、膜部120の生物由来物質61の捕捉量の増大に伴い、ケーク層A3が徐々に大きくなっていくため、ケーク層A3の上層A4で目詰まりが生じる。その結果、参考例の濾過装置では、膜部120で捕捉した生物由来物質61の堆積による目詰まりによって濾過が停止し、液体60から生物由来物質61を分離することができなくなる。 Thus, in the filtration device of the reference example, the biological substance 61 captured by the membrane unit 120 is deposited on the entire second main surface VS12 of the membrane unit 120. For this reason, since the cake layer A3 gradually increases as the amount of the biological substance 61 captured by the membrane portion 120 increases, clogging occurs in the upper layer A4 of the cake layer A3. As a result, in the filtering device of the reference example, the filtration is stopped due to clogging due to the deposition of the biological substance 61 captured by the membrane part 120, and the biological substance 61 cannot be separated from the liquid 60.
 これに対し、実施の形態1の濾過装置100Aでは、容器部10を、容器部10の軸方向が水平方向になるように配置し、膜部20において液体60を水平方向に通過させている。このため、濾過装置100Aでは、膜部20の第1主面HS1の鉛直方向上側の領域A2において、生物由来物質61の堆積による目詰まりが発生するのを抑制することができる。そのため、濾過装置100Aは、参考例の濾過装置に比べて、目詰まりを抑制することによって、液体60から生物由来物質61を分離し続けることができる。 On the other hand, in the filtration device 100A of the first embodiment, the container part 10 is arranged so that the axial direction of the container part 10 is horizontal, and the liquid 60 is allowed to pass through the film part 20 in the horizontal direction. For this reason, in the filtering device 100A, it is possible to suppress the occurrence of clogging due to the deposition of the biological material 61 in the region A2 in the vertical direction above the first main surface HS1 of the film unit 20. Therefore, the filtering device 100A can continue to separate the biological material 61 from the liquid 60 by suppressing clogging as compared with the filtering device of the reference example.
[効果]
 実施の形態1に係る濾過装置100Aによれば、以下の効果を奏することができる。
[effect]
According to the filtering device 100A according to the first embodiment, the following effects can be obtained.
 濾過装置100Aにおいては、膜部20の第1主面HS1から第2主面HS2へ水平方向に生物由来物質61を含む液体60を通過させている。このような構成により、生物由来物質61の堆積による膜部20の目詰まりを抑制しながら、液体60から生物由来物質61を分離することができる。その結果、濾過装置100Aでは、鉛直方向上側から下側に向かって膜部120に液体60を通過させる参考例の濾過装置と比べて、液体60から生物由来物質61を効率良く分離することができる。また、濾過装置100Aは、参考例の濾過装置と比べて、膜部20の目詰まりを抑制することができるため、より短い期間で、より高い濃度の液体60を濾過することができる。また、参考例の濾過装置に比べて、再現性が高い濾過をすることができる。なお、実施の形態1において、濾過装置100Aは、生物由来物質61と液体60とを分離しているが、これに限定されない。例えば、濾過装置100Aは、液体60中の溶液と生物由来物質61とを通過させることにより、液体60に含まれる生物由来物質61よりもサイズの大きな異物を濾過してもよい。あるいは、濾過装置100Aは、溶液に含まれた大きさの異なる無機物又は有機物を濾過して分級してもよい。 In the filtration device 100A, the liquid 60 containing the biological substance 61 is passed in the horizontal direction from the first main surface HS1 of the membrane unit 20 to the second main surface HS2. With such a configuration, it is possible to separate the biological substance 61 from the liquid 60 while suppressing clogging of the film unit 20 due to the deposition of the biological substance 61. As a result, in the filtering device 100A, the biological substance 61 can be efficiently separated from the liquid 60 as compared with the filtering device of the reference example that allows the liquid 60 to pass through the membrane portion 120 from the upper side to the lower side in the vertical direction. . Moreover, since the filtering device 100A can suppress clogging of the membrane part 20 as compared with the filtering device of the reference example, it is possible to filter the liquid 60 having a higher concentration in a shorter period. Moreover, it can filter with high reproducibility compared with the filter apparatus of a reference example. In the first embodiment, the filtering device 100A separates the biological material 61 and the liquid 60, but is not limited to this. For example, the filtration device 100A may filter a foreign substance having a size larger than that of the biological substance 61 contained in the liquid 60 by allowing the solution in the liquid 60 and the biological substance 61 to pass therethrough. Or 100A of filtration apparatuses may filter and classify | categorize the inorganic substance or organic substance from which the magnitude | size contained in the solution differs.
 濾過装置100Aにおいて、膜部20は、多孔膜として金属製薄膜を用いている。このような構成により、膜部20に力がかかることによって膜部20が破損することを抑制することができる。また、液体60が膜部20を通過する際においても、膜部20の貫通孔21が変形しにくいため、貫通孔21の変形により生物由来物質61が膜部20を通過してしまうのを抑制することができる。さらには、液体60による膜部20の損傷も抑制することができる。 In the filtration device 100A, the membrane unit 20 uses a metal thin film as a porous membrane. With such a configuration, it is possible to prevent the membrane portion 20 from being damaged by applying a force to the membrane portion 20. Further, even when the liquid 60 passes through the membrane part 20, since the through-hole 21 of the membrane part 20 is not easily deformed, the biological substance 61 is prevented from passing through the membrane part 20 due to the deformation of the through-hole 21. can do. Furthermore, damage to the film part 20 due to the liquid 60 can also be suppressed.
 濾過装置100Aにおいて、液体容器30の上壁に、液体60にかかる圧力を逃がす通気口31を設けている。このような構成によって、液体容器30内の液体60を外部に開放した状態にすることができる。そのため、液体60にかかる圧力を通気口31から逃がし、液体60中の生物由来物質61にかかる圧力を低減することができる。その結果、生物由来物質61が変形することを抑制し、膜部20における目詰まりを低減することができる。尚、通気口31を通過するガスは滅菌されていることが好ましい。液体60に本来含まれている生物由来物質61以外の生物由来物質が混合することを防ぐためである。また、通気口31を介して、適度に二酸化炭素が含まれた生物由来物質が好むガスバッグと接続していてもよい。さらには、このガスバッグの容量が大きい場合には、吸引により液体60にかかる圧力を逃がしやすくすることができる。 In the filtration device 100A, a vent 31 for releasing the pressure applied to the liquid 60 is provided on the upper wall of the liquid container 30. With such a configuration, the liquid 60 in the liquid container 30 can be opened to the outside. Therefore, the pressure applied to the liquid 60 can be released from the vent 31 and the pressure applied to the biological substance 61 in the liquid 60 can be reduced. As a result, it is possible to suppress the biological material 61 from being deformed, and to reduce clogging in the film unit 20. The gas passing through the vent 31 is preferably sterilized. This is to prevent the mixing of biological materials other than the biological material 61 originally contained in the liquid 60. Moreover, you may connect via the vent 31 with the gas bag which the biological substance containing the carbon dioxide moderately likes. Furthermore, when the capacity of the gas bag is large, the pressure applied to the liquid 60 by suction can be easily released.
 濾過装置100Aにおいて、吸引部40が液体容器30内に保持された液体60を吸引することによって、膜部20の第1主面HS1から第2主面HS2へ液体60を通過させている。このような構成によって、液体容器30内の液体60を膜部20に水平方向に通過させ、膜部20の目詰まりを抑制することができる。また、吸引部40によって、液体60を吸引することによって、より短い時間で濾過を行うことができる。 In the filtration device 100A, the suction part 40 sucks the liquid 60 held in the liquid container 30, thereby allowing the liquid 60 to pass from the first main surface HS1 of the film part 20 to the second main surface HS2. With such a configuration, the liquid 60 in the liquid container 30 can be passed through the film unit 20 in the horizontal direction, and clogging of the film unit 20 can be suppressed. Further, the suction can be performed in a shorter time by sucking the liquid 60 by the suction unit 40.
 なお、実施の形態1において、容器部10は、容器部10の軸方向が水平方向と同じになるように配置される構成について説明したが、これに限定されない。例えば、容器部10は、容器部10の軸方向が水平方向に対して斜めになるように配置されてもよい。このように、濾過装置100Aは、斜め方向に配置して濾過を行ってもよい。 In addition, in Embodiment 1, although the container part 10 demonstrated the structure arrange | positioned so that the axial direction of the container part 10 might become the same as a horizontal direction, it is not limited to this. For example, the container part 10 may be arrange | positioned so that the axial direction of the container part 10 may become diagonal with respect to a horizontal direction. As described above, the filtering device 100A may be arranged in an oblique direction to perform filtration.
 実施の形態1において、容器部10は、筒状体である構成について説明したが、これに限定されない。容器部10は、内部に液体60を導入し、膜部20を通過して液体60を排出可能な構成であればよく、例えば、四角柱等の多角柱の形状であってもよい。 In Embodiment 1, although the container part 10 demonstrated the structure which is a cylindrical body, it is not limited to this. The container unit 10 may be configured to introduce the liquid 60 therein, pass through the film unit 20 and discharge the liquid 60, and may have a polygonal column shape such as a square column.
 実施の形態1において、膜部20は、金属製薄膜を用いているが、これに限定されない。膜部20は、多孔膜であればよく、例えば、メンブレン、ろ紙、不織布等であってもよい。 In Embodiment 1, although the film part 20 uses the metal thin film, it is not limited to this. The membrane unit 20 may be a porous membrane, and may be a membrane, a filter paper, a nonwoven fabric, or the like, for example.
 実施の形態1において、膜部20は、容器部10の導入口11に設けられているが、これに限定されない。膜部20は、第1主面HS1から第2主面HS2へ水平方向に液体60が通過すればよく、膜部20の位置は限定されない。例えば、膜部20は、容器部10の導入口11と排出口12との間に設けられていればよい。膜部20は、排出口12に設けられていてもよい。また、実施の形態1において、1つの膜部20が、容器部10の導入口11に設けられている例について説明したが、これに限定されない。複数の膜部20が、容器部10の導入口11と排出口12との間に設けられていてもよい。例えば、容器部10の導入口11に第1膜部20を設け、且つ第1膜部20よりも排出口12側に第2膜部20を設けてもよい。このように、複数の膜部20を用いて多段の濾過装置100Aを構成することによって、回収率を向上させることができる。また、第1膜部20の貫通孔の大きさと第2膜部20の貫通孔の大きさとを異なるように設計することにより、2つの異なる大きさの細胞を濾過することができる。これにより、細胞を分級することができる。 In Embodiment 1, although the film | membrane part 20 is provided in the inlet 11 of the container part 10, it is not limited to this. The film part 20 is only required to allow the liquid 60 to pass in the horizontal direction from the first main surface HS1 to the second main surface HS2, and the position of the film part 20 is not limited. For example, the film part 20 may be provided between the inlet 11 and the outlet 12 of the container part 10. The film part 20 may be provided in the discharge port 12. In the first embodiment, the example in which one film unit 20 is provided in the introduction port 11 of the container unit 10 has been described. However, the present invention is not limited to this. A plurality of film parts 20 may be provided between the inlet 11 and the outlet 12 of the container part 10. For example, the first film part 20 may be provided at the inlet 11 of the container part 10, and the second film part 20 may be provided closer to the discharge port 12 than the first film part 20. Thus, the recovery rate can be improved by configuring the multistage filtration device 100A using the plurality of membrane portions 20. In addition, by designing the size of the through hole of the first film unit 20 and the size of the through hole of the second film unit 20 to be different, cells having two different sizes can be filtered. Thereby, a cell can be classified.
 実施の形態1において、膜部20は、容器部10の導入口11から排出口12へ向かって水平方向80に液体を通過させる例を説明したが、これに限定されない。実施の形態1において、「水平方向」とは、鉛直方向に直交する方向だけでなく、鉛直方向に対して所定の角度を有する斜めの方向を含んでもよい。即ち、膜部20において、液体60の通過する主方向が水平方向であればよく、液体60の通過する方向が水平方向に対して斜めの方向を含んでいてもよい。 In Embodiment 1, although the film part 20 demonstrated the example which passes a liquid in the horizontal direction 80 toward the discharge port 12 from the inlet 11 of the container part 10, it is not limited to this. In the first embodiment, the “horizontal direction” may include not only a direction orthogonal to the vertical direction but also an oblique direction having a predetermined angle with respect to the vertical direction. That is, in the film part 20, the main direction through which the liquid 60 passes may be a horizontal direction, and the direction through which the liquid 60 passes may include an oblique direction with respect to the horizontal direction.
 実施の形態1において、膜部20は、水平方向に対して第1主面HS1及び第2主面HS2がように配置されているが、これに限定されない。図7は、実施の形態1の変形例の濾過装置100Bを示す。図7に示す濾過装置100Bのように、膜部20を水平方向に対して所定の角度θを有して斜め方向に配置してもよい。言い換えると、膜部20は、鉛直方向に対して傾斜して配置されてもよい。また、膜部20の一部が、水平方向に対して斜め方向に配置されていてもよい。このような構成により、膜部20の第1主面HS1の鉛直方向下側において生物由来物質61が堆積するスペースを大きくすることができる。そのため、膜部20の第1主面HS1の鉛直方向上側において、ケーク層が更に形成されにくくなり、生物由来物質61による膜部20の目詰まりを更に抑制することができる。 In the first embodiment, the film part 20 is arranged so that the first main surface HS1 and the second main surface HS2 are arranged in the horizontal direction, but the present invention is not limited to this. FIG. 7 shows a filtration device 100B according to a modification of the first embodiment. As in the filtration device 100B shown in FIG. 7, the membrane unit 20 may be arranged in an oblique direction with a predetermined angle θ with respect to the horizontal direction. In other words, the film part 20 may be disposed to be inclined with respect to the vertical direction. Moreover, a part of film | membrane part 20 may be arrange | positioned in the diagonal direction with respect to the horizontal direction. With such a configuration, it is possible to increase the space in which the biological substance 61 is deposited on the lower side in the vertical direction of the first main surface HS1 of the film unit 20. Therefore, the cake layer is further hardly formed on the upper side in the vertical direction of the first main surface HS <b> 1 of the film part 20, and the clogging of the film part 20 due to the biological substance 61 can be further suppressed.
 実施の形態1において、液体容器30は、液体容器30の上壁に通気口31を設けているが、これに限定されない。例えば、液体容器30の側壁に孔を設けることによって、通気口31を形成してもよい。また、通気口31の代わりに通気フィルターを設けてもよい。 In the first embodiment, the liquid container 30 is provided with the vent 31 on the upper wall of the liquid container 30, but the present invention is not limited to this. For example, the vent 31 may be formed by providing a hole in the side wall of the liquid container 30. Further, a ventilation filter may be provided instead of the ventilation port 31.
 実施の形態1において、液体容器30は、液体にかかる圧力を逃がす通気口31を備える構成について説明したが、これに限定されない。例えば、液体容器30は、通気口31を設けず、液体60を外部に開放しない状態としてもよい。 In Embodiment 1, although the liquid container 30 demonstrated the structure provided with the vent 31 which releases the pressure concerning a liquid, it is not limited to this. For example, the liquid container 30 may be in a state where the vent 31 is not provided and the liquid 60 is not opened to the outside.
 実施の形態1において、吸引部40が液体容器30内の液体60を吸引することによって、液体60を膜部20に通過させる構成について説明したが、これに限定されない。例えば、液体容器30内の液体60を通気口31に相当する位置から加圧することによって、膜部20の第1主面HS1から第2主面HS2へ液体60を水平方向に通過させてもよい。また、遠心分離機を用いて液体容器30内の液体60に遠心力を加えることによって、膜部20の第1主面HS1から第2主面HS2へ液体60を水平方向に通過させてもよい。 In the first embodiment, the configuration in which the suction unit 40 passes the liquid 60 through the film unit 20 by sucking the liquid 60 in the liquid container 30 has been described, but the present invention is not limited thereto. For example, by pressing the liquid 60 in the liquid container 30 from a position corresponding to the vent 31, the liquid 60 may be passed in the horizontal direction from the first main surface HS <b> 1 to the second main surface HS <b> 2 of the film unit 20. . Further, by applying a centrifugal force to the liquid 60 in the liquid container 30 using a centrifuge, the liquid 60 may be passed in the horizontal direction from the first main surface HS1 to the second main surface HS2 of the membrane unit 20. .
 実施の形態1において、吸引部40は、シリンジである構成について説明したが、これに限定されない。吸引部40は、液体60を吸引できる装置であればよく、例えば、ポンプ等であってもよい。 In Embodiment 1, although the structure which the suction part 40 is a syringe was demonstrated, it is not limited to this. The suction unit 40 may be any device that can suck the liquid 60, and may be, for example, a pump.
 実施の形態1において、液体容器30、及び吸引部40は、必須の構成ではなく、これらの要素は、省略してもよいし、他の要素に置き換えてもよい。 In Embodiment 1, the liquid container 30 and the suction unit 40 are not essential components, and these elements may be omitted or replaced with other elements.
(実施の形態2)
[全体構成]
 本発明に係る実施の形態2の濾過装置100Cについて図8を用いて説明する。
 図8は、実施の形態2の濾過装置100Cの概略構成を示す。実施の形態2では、主に実施の形態1と異なる点について説明する。実施の形態2においては、実施の形態1と同一又は同等の構成については同じ符号又は類似の符号を付して説明する。また、実施の形態2では、実施の形態1と重複する記載は省略する。
(Embodiment 2)
[overall structure]
A filtration device 100C according to the second embodiment of the present invention will be described with reference to FIG.
FIG. 8 shows a schematic configuration of a filtration device 100C according to the second embodiment. In the second embodiment, differences from the first embodiment will be mainly described. In the second embodiment, the same or similar components as those in the first embodiment will be described with the same or similar reference numerals. In the second embodiment, descriptions overlapping with those in the first embodiment are omitted.
 図8に示すように、実施の形態2の濾過装置100Cは、実施の形態1の濾過装置100Aと比べて、容器部10aの排出口12aから導入口11aの方向に遠心力を加えることによって液体60から生物由来物質61を分離可能な構成を有している点が異なる。また、濾過装置100Cは、吸引部40を備えていない。 As shown in FIG. 8, the filtration device 100C of the second embodiment is liquid by applying a centrifugal force in the direction from the discharge port 12a of the container part 10a to the introduction port 11a as compared with the filtration device 100A of the first embodiment. The difference is that the biological material 61 can be separated from 60. Further, the filtration device 100C does not include the suction unit 40.
 濾過装置100Cは、生物由来物質61を含む液体60を導入する導入口11aと液体60を排出する排出口12aとを有する容器部10aと、導入口11aと排出口12aとの間に配置され、複数の貫通孔21を有する膜部20aと、液体60を保持する液体容器30aを備える。容器部10aは、導入口11aと排出口12aが水平方向に位置するように配置されている。容器部10aの導入口11aは、液体容器30a内の液体60内に配置されている。膜部20aは、遠心力が負荷されたとき、遠心力と逆方向に液体容器30a内の液体60を通過させている。即ち、濾過装置100Cは、容器部10aの排出口12aから導入口11aの方向に遠心力を加えることによって、液体容器30a内の液体60を、膜部20aの第1主面HS1から第2主面HS2へ水平方向に通過させている。また、容器部10aには、脱気用の孔が設けられている。 The filtration device 100C is disposed between a container portion 10a having an introduction port 11a for introducing the liquid 60 containing the biological substance 61 and a discharge port 12a for discharging the liquid 60, and the introduction port 11a and the discharge port 12a. A film part 20 a having a plurality of through holes 21 and a liquid container 30 a for holding the liquid 60 are provided. The container part 10a is arrange | positioned so that the inlet 11a and the outlet 12a may be located in a horizontal direction. The inlet 11a of the container part 10a is arranged in the liquid 60 in the liquid container 30a. When the centrifugal force is applied, the membrane part 20a allows the liquid 60 in the liquid container 30a to pass in the direction opposite to the centrifugal force. That is, the filtering device 100C applies the centrifugal force in the direction from the discharge port 12a of the container part 10a to the introduction port 11a, thereby causing the liquid 60 in the liquid container 30a to flow from the first main surface HS1 of the film part 20a to the second main surface HS1. It passes through the surface HS2 in the horizontal direction. The container portion 10a is provided with a deaeration hole.
 実施の形態2においては、容器部10aが液体容器30a内に配置された状態で、液体容器30aの開口部分を覆う蓋50が取り付けられている。 In Embodiment 2, a lid 50 that covers the opening of the liquid container 30a is attached in a state where the container portion 10a is disposed in the liquid container 30a.
[濾過装置の動作]
 濾過装置100Cの動作について、図9A~図9Fを用いて説明する。
 図9A~図9Fは、濾過装置100Cにおける濾過の動作を示す。
[Operation of filtration device]
The operation of the filtering device 100C will be described with reference to FIGS. 9A to 9F.
9A to 9F show the filtration operation in the filtration device 100C.
 図9Aに示すように、液体容器30aから容器部10aを取り外し、液体容器30a内に生物由来物質61を含む液体60を導入する。 As shown in FIG. 9A, the container portion 10a is removed from the liquid container 30a, and the liquid 60 containing the biological substance 61 is introduced into the liquid container 30a.
 図9Bに示すように、容器部10aは、液体60を保持した液体容器30a内に取り付けられる。実施の形態2において、容器部10aを液体容器30aの内部に保持した状態で蓋50が液体容器30aに取り付けられる。即ち、容器部10aの導入口11aは、液体容器30a内の液体60内に配置される。蓋50の取り付けは、例えば、蓋50の内側に設けられた雌ねじと、液体容器30aの外壁に設けられた雄ねじを螺合することによって行われる。 As shown in FIG. 9B, the container portion 10a is mounted in a liquid container 30a holding the liquid 60. In the second embodiment, the lid 50 is attached to the liquid container 30a in a state where the container portion 10a is held inside the liquid container 30a. That is, the inlet 11a of the container part 10a is disposed in the liquid 60 in the liquid container 30a. The lid 50 is attached by, for example, screwing a female screw provided inside the lid 50 and a male screw provided on the outer wall of the liquid container 30a.
 液体容器30aの内部に容器部10aを取り付けることによって、液体容器30a内に保持された液体60は、容器部10aの外壁と液体容器30aの内壁との間に押し上げられる。この状態で、濾過装置100Cを遠心分離機にセットする。実施の形態2において、濾過装置100Cは、容器部10aの軸方向が水平方向になるように遠心分離機にセットされる。即ち、容器部10aの導入口11aと排出口12aとが水平方向に位置するように容器部10aを遠心分離機に配置する。 By attaching the container part 10a inside the liquid container 30a, the liquid 60 held in the liquid container 30a is pushed up between the outer wall of the container part 10a and the inner wall of the liquid container 30a. In this state, the filtration device 100C is set in the centrifuge. In the second embodiment, the filtration device 100C is set in the centrifuge so that the axial direction of the container portion 10a is horizontal. That is, the container part 10a is arranged in the centrifuge so that the inlet 11a and the outlet 12a of the container part 10a are positioned in the horizontal direction.
 図9Cに示すように、遠心分離機(図示せず)によって容器部10aの排出口12aから導入口11aの方向に遠心力(図9Cに示す矢印83)がかかると、容器部10aの外壁と液体容器30aの内壁との間に押し上げられた液体60が液体容器30aの底部に向かって流れる(図9Cに示す矢印84)。このとき、生物由来物質61は、液体容器30aの底部に集合する。一方、液体60は、膜部20aの第1主面HS1から第2主面HS2を水平方向に通過して、容器部10aの導入口11aから排出口12aに向かって流れる(図9Cに示す矢印85)。そして、容器部10aの外壁と液体容器30aの内壁との間の液体60の液面の高さと、膜部20aを通過した液体60の液面の高さが同じになる。なお、容器部10aの外壁と液体容器30aの内壁との間の液体60の液面の高さと、膜部20aを通過した液体60の液面の高さとは、それぞれの場所での液体容器30aの底面からの液体60の高さを意味する。 As shown in FIG. 9C, when a centrifugal force (arrow 83 shown in FIG. 9C) is applied in the direction from the discharge port 12a of the container part 10a to the introduction port 11a by a centrifuge (not shown), the outer wall of the container part 10a The liquid 60 pushed up between the inner wall of the liquid container 30a flows toward the bottom of the liquid container 30a (arrow 84 shown in FIG. 9C). At this time, the biological substance 61 collects at the bottom of the liquid container 30a. On the other hand, the liquid 60 passes through the first main surface HS1 to the second main surface HS2 of the film part 20a in the horizontal direction and flows from the introduction port 11a of the container unit 10a toward the discharge port 12a (arrow shown in FIG. 9C). 85). And the height of the liquid level of the liquid 60 between the outer wall of the container part 10a and the inner wall of the liquid container 30a and the height of the liquid level of the liquid 60 which passed the film | membrane part 20a become the same. The height of the liquid surface of the liquid 60 between the outer wall of the container portion 10a and the inner wall of the liquid container 30a and the height of the liquid surface of the liquid 60 that has passed through the film portion 20a are the liquid container 30a at each location. This means the height of the liquid 60 from the bottom surface.
 図9Dに示すように、遠心分離機を停止し、蓋50を液体容器30aから取り外す。蓋50を取り外した後、膜部20aを通過した液体60を排出する。液体60の排出は、容器部10aを液体容器30aに取り付けた状態で、液体容器30aを逆さまにすることによって行う。このとき、液体容器30aの底部に溜まっていた生物由来物質61は、膜部20aの貫通孔21を通過することができない。そのため、排出口12aからは、生物由来物質61を含まない液体60が排出される。 As shown in FIG. 9D, the centrifuge is stopped and the lid 50 is removed from the liquid container 30a. After removing the lid 50, the liquid 60 that has passed through the membrane portion 20a is discharged. The liquid 60 is discharged by turning the liquid container 30a upside down with the container portion 10a attached to the liquid container 30a. At this time, the biological substance 61 accumulated at the bottom of the liquid container 30a cannot pass through the through hole 21 of the membrane part 20a. Therefore, the liquid 60 not containing the biological substance 61 is discharged from the discharge port 12a.
 図9Eに示すように、液体容器30aに蓋50を取り付け、遠心分離機によって濾過装置100Cに排出口12aから導入口11aへの遠心力を加える(図9Eに示す矢印83)。濾過装置100Cに遠心力が加わると、図9Cに示す動作と同様に、容器部10aの外壁と液体容器30aの内壁との間の液体60が液体容器30aの底部に流れ(図9Eに示す矢印84)、生物由来物質61を含まない液体60が膜部20aを通過する(図9Eに示す矢印85)。そして、容器部10aの外壁と液体容器30aの内壁との間の液体60の液面の高さと、膜部20aを通過した液体60の液面の高さが同じになる。 As shown in FIG. 9E, a lid 50 is attached to the liquid container 30a, and centrifugal force from the outlet 12a to the inlet 11a is applied to the filtration device 100C by a centrifuge (arrow 83 shown in FIG. 9E). When centrifugal force is applied to the filtering device 100C, the liquid 60 between the outer wall of the container 10a and the inner wall of the liquid container 30a flows to the bottom of the liquid container 30a (the arrow shown in FIG. 9E), similar to the operation shown in FIG. 9C. 84) The liquid 60 that does not contain the biological substance 61 passes through the membrane part 20a (arrow 85 shown in FIG. 9E). And the height of the liquid level of the liquid 60 between the outer wall of the container part 10a and the inner wall of the liquid container 30a and the height of the liquid level of the liquid 60 which passed the film | membrane part 20a become the same.
 図9Fに示すように、遠心分離機を停止し、蓋50を液体容器30aから取り外す。その後、図9Dに示す動作と同様に、膜部20aを通過し、容器部10aの内側に溜まった液体60を排出口12aから排出する。 As shown in FIG. 9F, the centrifuge is stopped and the lid 50 is removed from the liquid container 30a. Thereafter, similarly to the operation shown in FIG. 9D, the liquid 60 that has passed through the film part 20a and accumulated inside the container part 10a is discharged from the discharge port 12a.
 このように、濾過装置100Cは、図9A~図9Fに示す動作を行うことによって、遠心力を用いて、液体60から生物由来物質61を分離している。さらに、濾過装置100Cは、図9A~図9Fに示す動作を繰り返すことによって、生物由来物質61を濃縮する
ことができる。また、濾過装置100Cにおいては、濃縮後、洗浄水を導入して生物由来物質61を洗浄することもできる。また、濾過装置100Cにおいては、生物由来物質61を分離した後、置換液を導入することによって液体60を別の液体に置換することもできる。
As described above, the filtering device 100C separates the biological substance 61 from the liquid 60 by using the centrifugal force by performing the operations shown in FIGS. 9A to 9F. Furthermore, the filtration device 100C can concentrate the biological material 61 by repeating the operations shown in FIGS. 9A to 9F. Further, in the filtering device 100C, after concentration, the biological material 61 can be washed by introducing washing water. Further, in the filtering device 100C, after separating the biological material 61, the liquid 60 can be replaced with another liquid by introducing a replacement liquid.
[効果]
 実施の形態2に係る濾過装置100Cによれば、以下の効果を奏することができる。
[effect]
According to the filter device 100C according to the second embodiment, the following effects can be obtained.
 濾過装置100Cにおいては、遠心力を負荷したときに、膜部20aにおいて遠心力がかかる方向と逆方向に液体60を通過させている。具体的には、濾過装置100Cは、遠心力を負荷したとき、容器部10aの外壁と液体容器30aの内壁との間の液体60の液面の高さと、膜部20aを通過した液体60の液面の高さとの高低差を利用して液体60を膜部20aに水平方向に通過させている。このような構成により、膜部20aが生物由来物質61で目詰まりすることなく、液体60から生物由来物質61を分離することができる。また、濾過装置100Cにおいては、遠心分離による濾過を繰り返して行うことによって、生物由来物質61の濃縮を容易に行うことができる。 In the filtering device 100C, when a centrifugal force is applied, the liquid 60 is passed in the direction opposite to the direction in which the centrifugal force is applied in the membrane portion 20a. Specifically, when a centrifugal force is applied to the filtration device 100C, the height of the liquid surface between the outer wall of the container portion 10a and the inner wall of the liquid container 30a and the liquid 60 that has passed through the membrane portion 20a. The liquid 60 is allowed to pass through the film part 20a in the horizontal direction by utilizing the difference in height from the liquid level. With such a configuration, the biological substance 61 can be separated from the liquid 60 without clogging the membrane part 20 a with the biological substance 61. Further, in the filtration device 100C, the biological substance 61 can be easily concentrated by repeatedly performing filtration by centrifugation.
 濾過装置100Cにおいては、膜部20aを通過した液体60を取り出す際に、例えば、濾過装置100Cを逆さまにすることで容易に液体60を排出することができる。このように、濾過装置100Cにおいては、作業者によるピペッティングが不要となり、作業者に特別な技能を要求することなく、液体60の排出が可能となる。その結果、濾過装置100Cにおいては、ピペッティングによる生物由来物質61の回収率の低下が生じない。なお、液体60の排出は、吸引等によって行ってもよい。 In the filtering device 100C, when the liquid 60 that has passed through the membrane portion 20a is taken out, for example, the liquid 60 can be easily discharged by turning the filtering device 100C upside down. Thus, in the filtering device 100C, pipetting by the operator is unnecessary, and the liquid 60 can be discharged without requiring a special skill from the operator. As a result, in the filtration device 100C, the recovery rate of the biological material 61 is not reduced by pipetting. The liquid 60 may be discharged by suction or the like.
 濾過装置100Cにおいては、生物由来物質61を分離した後、洗浄水を導入して遠心分離を行うことによって、生物由来物質61の洗浄を容易に行うことができる。また、濾過装置100Cにおいては、生物由来物質61を分離した後、置換液を導入することによって液体の置換を容易に行うことができる。 In the filtration device 100C, after separating the biological substance 61, the biological substance 61 can be easily washed by introducing washing water and performing centrifugation. Further, in the filtering device 100C, after the biological material 61 is separated, the liquid can be easily replaced by introducing the replacement liquid.
 濾過装置100Cにおいては、遠心分離機に取り付ける際に、容器部10aの軸方向が遠心力の加わる方向と同じ方向にしてセットすることができる。このため、遠心力が生物由来物質61に伝わりやすく、液体60から生物由来物質61を分離し易い。 The filtration device 100C can be set with the axial direction of the container portion 10a being the same as the direction in which the centrifugal force is applied when it is attached to the centrifuge. For this reason, the centrifugal force is easily transmitted to the biological material 61, and the biological material 61 is easily separated from the liquid 60.
 より詳しく説明すると、一般的に遠心分離に用いられている遠沈管は、遠心分離機に取り付ける際に、遠心力の負荷される方向に対して斜めにセットされる。遠沈管の場合、遠沈管の軸方向を遠心力と同じ方向にセットすると、遠心分離した後、分離した生物由来物質61が再び液体60と混ざってしまう。このため、遠沈管は、遠心分離した生物由来物質61を遠沈管の底部に集めた状態を維持するため、遠心力の負荷される方向に対して遠沈管が斜めに配置される。しかし、遠心力の加わる方向に対して斜めに遠沈管を配置すると、生物由来物質61に遠心力が伝わりにくくなる。これに対し、濾過装置100Cにおいては、遠心分離機に容器部10aの軸方向を遠心力の加わる方向と同じになるようにセットすることができるため、生物由来物質61に遠心力が伝わり易い。そのため、濾過装置100Cは、遠心力を生物由来物質61に効率良く伝えることによって、遠沈管に比べて、少ない回転数、又は短い時間の回転条件で遠心分離することができる。 More specifically, a centrifuge tube generally used for centrifugation is set obliquely with respect to the direction in which centrifugal force is applied when it is attached to a centrifuge. In the case of a centrifuge tube, if the axial direction of the centrifuge tube is set in the same direction as the centrifugal force, the separated biological material 61 is mixed with the liquid 60 again after centrifugation. For this reason, the centrifuge tube is disposed obliquely with respect to the direction in which the centrifugal force is applied in order to maintain the state where the centrifuged biological substance 61 is collected at the bottom of the centrifuge tube. However, if the centrifuge tube is disposed obliquely with respect to the direction in which the centrifugal force is applied, the centrifugal force is hardly transmitted to the biological material 61. On the other hand, in the filtration device 100C, the axial direction of the container portion 10a can be set in the centrifuge so as to be the same as the direction in which the centrifugal force is applied, so that the centrifugal force is easily transmitted to the biological material 61. Therefore, the filtration device 100C can perform centrifugal separation under a rotation condition with a smaller number of rotations or a shorter time than a centrifuge tube by efficiently transmitting a centrifugal force to the biological material 61.
 なお、実施の形態2において、濾過装置100Cは、容器部10aの軸方向が遠心力の加わる方向と同じになるように遠心分離機にセットする例について説明したが、これに限定されない。例えば、濾過装置100Cは、容器部10aの軸方向が遠心力の加わる方向に対して斜めになるように遠心分離機にセットされてもよい。 In the second embodiment, the example in which the filtering device 100C is set in the centrifuge so that the axial direction of the container portion 10a is the same as the direction in which the centrifugal force is applied has been described, but is not limited thereto. For example, the filtration device 100C may be set in the centrifuge so that the axial direction of the container portion 10a is inclined with respect to the direction in which the centrifugal force is applied.
(実施の形態3)
[全体構成]
 本発明に係る実施の形態3の濾過装置100Dについて図10及び図11を用いて説明する。
 図10は、実施の形態3の濾過装置100Dの概略構成を示す。図11は、濾過装置1
00Dを上から見た図を示す。なお、説明を簡略化するため、図11において、蓋部10bbを省略している。図11に示す黒矢印は、濾過装置100Dの回転方向を示す。実施の形態3では、主に実施の形態1と異なる点について説明する。実施の形態3においては、実施の形態1と同一又は同等の構成については同じ符号又は類似の符号を付して説明する。また、実施の形態3では、実施の形態1と重複する記載は省略する。
(Embodiment 3)
[overall structure]
A filtration device 100D according to Embodiment 3 of the present invention will be described with reference to FIGS.
FIG. 10 shows a schematic configuration of the filtration device 100D of the third embodiment. FIG. 11 shows the filtration device 1
The figure which saw 00D from the top is shown. In order to simplify the description, the lid 10bb is omitted in FIG. A black arrow shown in FIG. 11 indicates the rotation direction of the filtration device 100D. In the third embodiment, differences from the first embodiment will be mainly described. In the third embodiment, the same or similar components as those in the first embodiment will be described with the same or similar reference numerals. In the third embodiment, descriptions overlapping with those in the first embodiment are omitted.
 図10及び図11に示すように、実施の形態3の濾過装置100Dは、実施の形態1の濾過装置100Aと比べて、容器部10bの中心軸CLを中心に容器部10bを回転させることによって生じる遠心力により液体60から生物由来物質61を分離可能な構成を有している点が異なる。また、濾過装置100Dは、液体容器30及び吸引部40を備えていない。 As shown in FIGS. 10 and 11, the filtering device 100D of the third embodiment rotates the container portion 10b around the central axis CL of the container portion 10b as compared with the filtering device 100A of the first embodiment. The difference is that the biological material 61 can be separated from the liquid 60 by the generated centrifugal force. Further, the filtration device 100D does not include the liquid container 30 and the suction unit 40.
 図10及び図11に示すように、濾過装置100Dは、生物由来物質61を含む液体60を導入する容器部10bと、複数の貫通孔21を有する膜部20bを備える。容器部10bは、液体60を導入する導入口11bを有する容器本体10baと、液体60を排出する排出口12bと容器本体10ba内を減圧する減圧口70とを有する蓋部10bbを備える。 As shown in FIGS. 10 and 11, the filtration device 100 </ b> D includes a container portion 10 b for introducing a liquid 60 containing a biological substance 61 and a membrane portion 20 b having a plurality of through holes 21. The container part 10b includes a container body 10ba having an introduction port 11b for introducing the liquid 60, a lid part 10bb having a discharge port 12b for discharging the liquid 60, and a decompression port 70 for decompressing the inside of the container body 10ba.
 濾過装置100Dは、容器本体10baと膜部20bによって2重の筒構造を形成している。濾過装置100Dにおいて、内側の筒は円筒状の膜部20bで形成され、外側の筒は容器本体10baの側壁で形成されている。また、膜部20bと容器本体10baの側壁との間には、液体60を導入する空間が形成されている。容器本体10baの底部は、容器本体10baの中心に向かって鉛直下方向に傾斜している。膜部20bは、容器部10bの導入口11bと排出口12bとの間に配置されており、容器本体10baの側壁から一定の距離だけ離れて配置されている。 The filtration device 100D forms a double cylinder structure by the container body 10ba and the membrane part 20b. In the filtration device 100D, the inner cylinder is formed by a cylindrical film portion 20b, and the outer cylinder is formed by a side wall of the container body 10ba. A space for introducing the liquid 60 is formed between the membrane portion 20b and the side wall of the container body 10ba. The bottom of the container body 10ba is inclined vertically downward toward the center of the container body 10ba. The film part 20b is arranged between the inlet 11b and the outlet 12b of the container part 10b, and is arranged at a certain distance from the side wall of the container main body 10ba.
 濾過装置100Dは、容器部10bの中心軸CLを中心に回転することによって、中心軸CLから容器部10bの側壁へ遠心力を負荷している。濾過装置100Dに遠心力が負荷されたとき、容器本体10ba内の液体60は、遠心力のかかる方向と逆方向に移動し、膜部20aの第1主面HS1から第2主面HS2へ水平方向に通過する。 The filtration device 100D applies a centrifugal force from the central axis CL to the side wall of the container part 10b by rotating around the central axis CL of the container part 10b. When a centrifugal force is applied to the filtration device 100D, the liquid 60 in the container body 10ba moves in a direction opposite to the direction in which the centrifugal force is applied, and is horizontal from the first main surface HS1 to the second main surface HS2 of the film part 20a. Pass in the direction.
[濾過装置の動作]
 濾過装置100Dの動作について、図12A~図12Cを用いて説明する。
 図12A~図12Cは、濾過装置100Dにおける濾過の動作を示す。
[Operation of filtration device]
The operation of the filtration device 100D will be described with reference to FIGS. 12A to 12C.
12A to 12C show the filtration operation in the filtration device 100D.
 図12Aに示すように、容器本体10baから蓋部10bbを取り外し、導入口11bから容器本体10baの内部に生物由来物質61を含む液体60を導入する(図12Aに示す矢印86)。 As shown in FIG. 12A, the lid portion 10bb is removed from the container body 10ba, and the liquid 60 containing the biological substance 61 is introduced into the container body 10ba from the introduction port 11b (arrow 86 shown in FIG. 12A).
 図12Bに示すように、容器本体10baに密閉用の蓋部10bcを取り付けて液体60を容器本体10ba内に密閉する。その後、容器部10bを、容器部10bの中心軸CLを中心に回転させる(図12Bに示す矢印87)。容器部10bの回転条件は、例えば、遠心分離に用いられる一般的な遠沈管を回転させる場合の条件よりも低回転に設定されてもよい。 As shown in FIG. 12B, a sealing lid 10bc is attached to the container body 10ba to seal the liquid 60 in the container body 10ba. Thereafter, the container portion 10b is rotated around the central axis CL of the container portion 10b (arrow 87 shown in FIG. 12B). The rotation condition of the container part 10b may be set to a lower rotation than, for example, a condition for rotating a general centrifuge tube used for centrifugation.
 容器部10bを回転させることによって、中心軸CLから容器本体10baの側壁への遠心力が負荷されるため、生物由来物質61は、容器本体10baの側壁に集合する。そのため、膜部20bの第1主面HS1に位置する液体は、生物由来物質61の濃度が低い状態となる。 Since the centrifugal force from the central axis CL to the side wall of the container body 10ba is loaded by rotating the container part 10b, the biological substance 61 gathers on the side wall of the container body 10ba. Therefore, the liquid located on the first main surface HS1 of the film part 20b is in a state where the concentration of the biological substance 61 is low.
 図12Cに示すように、密閉用の蓋部10bcを取り外し、蓋部10bbを取り付ける。次に、蓋部10bbの上部に設けられた減圧口70から容器部10b内部の圧力を下げることによって、容器部10b内を減圧状態にする。容器部10b内を減圧状態にすることで、液体60が容器本体10baの回転中心である中心軸CLに向かって移動する。そのため、液体60は、膜部20bの第1主面HS1から第2主面HS2を水平方向に通過し、容器本体10baの底部の中央に集まる。容器本体10baの底部の中央に集まった液体60は、排出口12bから吸引されることによって外部に排出される(図12Cに示す矢印88)。 As shown in FIG. 12C, the lid portion 10bc for sealing is removed and the lid portion 10bb is attached. Next, the inside of the container part 10b is made into a pressure-reduced state by reducing the pressure inside the container part 10b from the decompression port 70 provided in the upper part of the cover part 10bb. By making the inside of the container part 10b into a pressure-reduced state, the liquid 60 moves toward the central axis CL that is the rotation center of the container body 10ba. Therefore, the liquid 60 passes through the first main surface HS1 to the second main surface HS2 of the film part 20b in the horizontal direction and collects at the center of the bottom of the container body 10ba. The liquid 60 collected at the center of the bottom of the container body 10ba is discharged to the outside by being sucked from the discharge port 12b (arrow 88 shown in FIG. 12C).
 このように、濾過装置100Dでは、遠心力を負荷することによって容器本体10baの側壁に生物由来物質61を集め、容器本体10ba内を減圧することによって液体60を遠心力と逆の方向に移動させている。これにより、液体60を容器本体10baの中央に集めて液体60を排出することによって、液体60と生物由来物質61とを分離している。また、濾過装置100Dは、図12A~図12Cに示す動作を繰り返すことで、液体60の交換、洗浄、及び濃縮処理を行うこともできる。 Thus, in the filtration device 100D, the biological material 61 is collected on the side wall of the container body 10ba by applying a centrifugal force, and the liquid 60 is moved in the direction opposite to the centrifugal force by reducing the pressure inside the container body 10ba. ing. Thereby, the liquid 60 and the biological material 61 are separated by collecting the liquid 60 in the center of the container body 10ba and discharging the liquid 60. Further, the filtration device 100D can perform the replacement, cleaning, and concentration processing of the liquid 60 by repeating the operations shown in FIGS. 12A to 12C.
[効果]
 実施の形態3に係る濾過装置100Dによれば、以下の効果を奏することができる。
[effect]
According to the filtration device 100D according to Embodiment 3, the following effects can be obtained.
 濾過装置100Dにおいては、容器部10bの中心軸CLを中心に容器部10bを回転させることによって生じる中心軸CLから容器本体10baの側壁への遠心力により液体60から生物由来物質61を分離可能な構成を有している。このような構成により、濾過装置100Dは、遠心力によって生物由来物質61を容器本体10baの側壁に集合させることができる。また、膜部20bの第1主面HS1に位置する生物由来物質61の濃度が低い液体60を、遠心力の加わる方向と逆方向に液体60を移動させることによって、膜部20bの第1主面HS1から第2主面HS2へ水平方向に液体60を通過させることができる。その結果、膜部20bにおいて、生物由来物質61による目詰まりを抑制する
ことができる。
In the filtration device 100D, the biological substance 61 can be separated from the liquid 60 by the centrifugal force from the central axis CL generated by rotating the container part 10b around the central axis CL of the container part 10b to the side wall of the container body 10ba. It has a configuration. With such a configuration, the filtration device 100D can collect the biological material 61 on the side wall of the container body 10ba by centrifugal force. Further, the liquid 60 having a low concentration of the biological substance 61 located on the first main surface HS1 of the film part 20b is moved in the direction opposite to the direction in which the centrifugal force is applied, thereby moving the first main part of the film part 20b. The liquid 60 can be passed in the horizontal direction from the surface HS1 to the second main surface HS2. As a result, clogging due to the biological material 61 can be suppressed in the film part 20b.
 また、生物由来物質61が遠心作用によって、容器本体10baの側壁に集合するため、膜部20bの第1主面HS1に生物由来物質61が堆積しにくい。そのため、膜部20bの貫通孔21の寸法は、特許文献1の濾過に用いるフィルターの貫通孔の寸法に比べて、大きくすることができる。その結果、濾過装置100Dにおいては、液体60の抽出に優位な条件での濾過が可能となる。 Moreover, since the biological material 61 collects on the side wall of the container body 10ba by the centrifugal action, the biological material 61 is unlikely to be deposited on the first main surface HS1 of the film part 20b. Therefore, the dimension of the through-hole 21 of the film part 20b can be made larger than the dimension of the through-hole of the filter used for filtration of Patent Document 1. As a result, in the filtering device 100D, it is possible to perform filtration under conditions superior to the extraction of the liquid 60.
 濾過装置100Dにおいて、遠心分離を終了した後、減圧口70から容器部10bの内部を減圧することによって、膜部20bの貫通孔21から生物由来物質61を含まない液体60を抽出することができる。 In the filtering device 100D, after ending the centrifugal separation, the liquid 60 not containing the biological substance 61 can be extracted from the through-hole 21 of the membrane part 20b by reducing the pressure inside the container part 10b from the pressure reducing port 70. .
 濾過装置100Dにおいては、容器部10bが中心軸CLを中心に回転することによって遠心力を発生させているため、遠沈管を用いて遠心分離を行う装置と比べて、回転数を低くしたり、遠心分離の時間を短くしたりすることができる。その結果、遠心分離によって死亡する生物由来物質61の数を減らすことができる。 In the filtering device 100D, since the container portion 10b generates a centrifugal force by rotating around the central axis CL, the number of rotations can be reduced compared to a device that performs centrifugation using a centrifuge tube, Centrifugation time can be shortened. As a result, the number of organism-derived substances 61 that die due to centrifugation can be reduced.
 濾過装置100Dにおいては、膜部20bを通過した液体60を取り出す際に、例えば、排出口12bから吸引することで容易に液体60を排出することができる。このように、濾過装置100Dにおいては、作業者によるピペッティングが不要となり、作業者に特別な技能を要求することなく、液体60の排出が可能となる。その結果、濾過装置100Dにおいては、ピペッティングによる生物由来物質61の回収率の低下が生じない。 In the filtering device 100D, when the liquid 60 that has passed through the membrane portion 20b is taken out, for example, the liquid 60 can be easily discharged by suction from the discharge port 12b. Thus, in the filtration device 100D, pipetting by the operator is unnecessary, and the liquid 60 can be discharged without requiring a special skill from the operator. As a result, in the filtration device 100D, the recovery rate of the biological material 61 is not reduced by pipetting.
 なお、実施の形態3において、容器部10bを回転する際に、密閉用の蓋部10bcを用いたが、これに限定されない。例えば、容器部10bの回転時においても排出口12bを有する蓋部10bbを使用してもよい。このような構成により、容器部10bの回転と液体60の排出を同時に行うことができる。 In the third embodiment, the sealing lid 10bc is used when rotating the container 10b. However, the present invention is not limited to this. For example, the lid portion 10bb having the discharge port 12b may be used even when the container portion 10b is rotated. With such a configuration, the rotation of the container portion 10b and the discharge of the liquid 60 can be performed simultaneously.
 実施の形態3において、膜部20bは、円筒状の複数の貫通孔21を有する金属製薄膜として説明したが、これに限定されない。膜部20bは、少なくとも一部が貫通孔21を有する金属性薄膜であってもよい。また、膜部20bの形状は、多角形の筒状であってもよい。 In Embodiment 3, although the film part 20b was demonstrated as a metal thin film which has the some cylindrical through-hole 21, it is not limited to this. The film part 20 b may be a metallic thin film having at least a part of the through hole 21. Further, the shape of the film part 20b may be a polygonal cylindrical shape.
 実施の形態3において、容器部10bは、蓋部10bbに排出口12bを設ける構成について説明したが、これに限定されない。排出口12bは、容器部10b内部から液体60を排出できる位置にあればよい。図13は、変形例の濾過装置100Eの概略構成を示す。図13に示すように、濾過装置100Eは、容器本体10baの底部の中央付近に排出口12cを設けてもよい。このような構成により、液体60を吸引せずとも液体60を排出することができる(図13に示す矢印89)。 In Embodiment 3, the container portion 10b has been described with respect to the configuration in which the discharge port 12b is provided in the lid portion 10bb, but is not limited thereto. The discharge port 12b should just be in the position which can discharge | emit the liquid 60 from the inside of the container part 10b. FIG. 13 shows a schematic configuration of a filtration device 100E according to a modification. As shown in FIG. 13, the filtration device 100E may be provided with a discharge port 12c near the center of the bottom of the container body 10ba. With such a configuration, the liquid 60 can be discharged without sucking the liquid 60 (arrow 89 shown in FIG. 13).
 実施の形態3において、容器部10bの蓋部10bbに減圧口70を設ける構成について説明したが、これに限定されない。減圧口70は、膜部20bの第1主面HS1から第2主面HS2へ水平方向に液体60を通過させやすくするために設けたものであり、必須の構成ではない。 In Embodiment 3, the configuration in which the decompression port 70 is provided in the lid portion 10bb of the container portion 10b has been described, but the configuration is not limited thereto. The decompression port 70 is provided to facilitate passage of the liquid 60 in the horizontal direction from the first main surface HS1 of the film part 20b to the second main surface HS2, and is not an essential configuration.
 本発明は、添付図面を参照しながら好ましい実施形態に関連して充分に記載されているが、この技術の熟練した人々にとっては種々の変形や修正は明白である。そのような変形や修正は、添付した特許請求の範囲による本発明の範囲から外れない限りにおいて、その中に含まれると理解されるべきである。 Although the present invention has been fully described in connection with preferred embodiments with reference to the accompanying drawings, various variations and modifications will be apparent to those skilled in the art. Such changes and modifications are to be understood as included within the scope of the present invention as long as they do not depart from the scope of the present invention.
 本発明は、濾過装置及び濾過方法に関する発明であり、高濃度の液体を濾過する点及び短時間で濾過する点で優れている。例えば、化学分析、装薬・製薬、臨床検査、公衆衛生管理、環境計測、等の分野に有用である。 The present invention relates to a filtration device and a filtration method, and is excellent in terms of filtering a high concentration liquid and filtering in a short time. For example, it is useful in the fields of chemical analysis, charge / pharmaceuticals, clinical examination, public health management, environmental measurement, and the like.
  10 容器部
  11 導入口
  12 排出口
  20 膜部
  21 貫通孔
  30 液体容器
  31 通気口
  32 開口
  40 吸引部
  41 チューブ
  50 蓋
  60 液体
  61 生物由来物質
  70 減圧口
  100 濾過装置
DESCRIPTION OF SYMBOLS 10 Container part 11 Introduction port 12 Discharge port 20 Membrane part 21 Through-hole 30 Liquid container 31 Ventilation port 32 Opening 40 Suction part 41 Tube 50 Lid 60 Liquid 61 Biological substance 70 Pressure-reducing port 100 Filter

Claims (11)

  1.  生物由来物質を含む液体を導入する導入口と前記液体を排出する排出口とを有する容器部と、
     前記容器部の前記導入口と前記排出口との間に設けられ、複数の貫通孔を有する膜部と、
    を備え、
     前記膜部へ水平方向に前記液体を通過させることによって、前記生物由来物質を前記液体から分離する、濾過装置。
    A container having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid;
    A membrane part provided between the inlet and the outlet of the container part and having a plurality of through holes;
    With
    A filtration device that separates the biological substance from the liquid by passing the liquid in a horizontal direction to the membrane part.
  2.  前記膜部は、金属製薄膜である、請求項1に記載の濾過装置。 The filtration device according to claim 1, wherein the membrane part is a metal thin film.
  3.  前記膜部の少なくとも一部は、水平方向に対して斜めに設けられた、請求項1または2に記載の濾過装置。 The filtration device according to claim 1 or 2, wherein at least a part of the membrane part is provided obliquely with respect to a horizontal direction.
  4.  更に、前記容器部の前記導入口から前記排出口へ前記液体を吸引する吸引部を備える、
    請求項1~3のいずれか一項に記載の濾過装置。
    Furthermore, a suction part for sucking the liquid from the inlet to the outlet of the container part is provided.
    The filtration device according to any one of claims 1 to 3.
  5.  更に、前記液体を保持する液体容器を備え、
     前記容器部の前記導入口は、前記液体容器内に保持された前記液体内に配置され、
     前記液体容器には、前記液体にかかる圧力を逃がす通気口が設けられた、
    請求項4に記載の濾過装置。
    A liquid container for holding the liquid;
    The inlet of the container portion is disposed in the liquid held in the liquid container,
    The liquid container is provided with a vent for releasing the pressure applied to the liquid.
    The filtration device according to claim 4.
  6.  更に、前記液体を保持する液体容器を備え、
     前記容器部は、前記導入口と前記排出口とが水平方向に位置するように配置され、
     前記容器部の前記導入口は、前記液体容器内に配置され、
     前記膜部は、遠心力を負荷したときにおいて、前記遠心力とは逆の方向に前記液体容器内の前記液体を通過させる、
    請求項1~3のいずれか一項に記載の濾過装置。
    A liquid container for holding the liquid;
    The container portion is arranged such that the introduction port and the discharge port are positioned in a horizontal direction,
    The inlet of the container portion is disposed in the liquid container;
    The membrane portion allows the liquid in the liquid container to pass in a direction opposite to the centrifugal force when a centrifugal force is applied.
    The filtration device according to any one of claims 1 to 3.
  7.  液体から生物由来物質を濾過する方法であって、
     生物由来物質を含む液体を導入する導入口と前記液体を排出する排出口とを備える容器部と、前記容器部の前記導入口と前記排出口との間に設けられ、複数の貫通孔を有する膜部と、を備えた濾過装置を準備する工程、
     前記膜部へ水平方向に前記液体を通過させることによって、前記生物由来物質を分離する工程、
    を含む、濾過方法。
    A method of filtering biological material from a liquid,
    A container part having an inlet for introducing a liquid containing a biological substance and an outlet for discharging the liquid, and provided between the inlet and the outlet of the container part, and having a plurality of through holes A step of preparing a filtration device comprising a membrane part,
    Separating the biological material by passing the liquid in a horizontal direction to the membrane part;
    A filtration method comprising:
  8.  前記分離する工程は、水平方向に対して少なくとも一部が斜めに設けられた前記膜部に前記液体を通過させる、請求項7に記載の濾過方法。 The filtration method according to claim 7, wherein in the separating step, the liquid is passed through the membrane part provided at least partially obliquely with respect to a horizontal direction.
  9.  前記分離する工程は、前記容器部の前記導入口から前記排出口へ前記液体を吸引する工程を含む、請求項7または8に記載の濾過方法。 The filtration method according to claim 7 or 8, wherein the separating step includes a step of sucking the liquid from the introduction port of the container portion to the discharge port.
  10.  前記分離する工程は、前記液体にかかる圧力を逃がす工程を含む、請求項9に記載の濾過方法。 The filtration method according to claim 9, wherein the separating step includes a step of releasing pressure applied to the liquid.
  11.  前記分離する工程は、
      前記容器部の前記導入口と前記排出口とが水平方向に位置するように前記容器部を配置する工程、
      前記液体内に前記容器部の前記導入口を配置する工程、
      前記液体に遠心力を負荷したとき、前記膜部において前記遠心力とは逆の方向に前記液体を通過させる工程、
    を含む、請求項7または8に記載の濾過方法。
    The separating step includes
    Arranging the container part such that the inlet and the outlet of the container part are positioned in a horizontal direction;
    Disposing the inlet of the container in the liquid;
    A step of passing the liquid in a direction opposite to the centrifugal force in the membrane portion when a centrifugal force is applied to the liquid;
    The filtration method of Claim 7 or 8 containing these.
PCT/JP2016/068917 2015-06-26 2016-06-24 Filtration device and filtration method WO2016208753A1 (en)

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