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WO2016006642A1 - Dispositif de manipulation de particules et procédé de classement de particules à l'aide de ce dispositif - Google Patents

Dispositif de manipulation de particules et procédé de classement de particules à l'aide de ce dispositif Download PDF

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Publication number
WO2016006642A1
WO2016006642A1 PCT/JP2015/069705 JP2015069705W WO2016006642A1 WO 2016006642 A1 WO2016006642 A1 WO 2016006642A1 JP 2015069705 W JP2015069705 W JP 2015069705W WO 2016006642 A1 WO2016006642 A1 WO 2016006642A1
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WIPO (PCT)
Prior art keywords
fluid
particle
flow
particles
flow path
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
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PCT/JP2015/069705
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English (en)
Japanese (ja)
Inventor
拓 小原
片山　晃治
桐谷　英昭
和樹 飯嶋
俊薫 豊嶋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tohoku University NUC
Tosoh Corp
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Tohoku University NUC
Tosoh Corp
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Priority to JP2016532960A priority Critical patent/JP6755178B2/ja
Publication of WO2016006642A1 publication Critical patent/WO2016006642A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/04—Cell isolation or sorting
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00—Washing granular, powdered or lumpy materials; Wet separating

Definitions

  • the present invention relates to a device for manipulating particles contained in a fluid and a method for manipulating particles contained in a fluid using the device.
  • solid materials composed of inorganic materials, organic materials, metals, etc. are supplied as a product.
  • These materials are designed by examining their physical properties in order to improve the performance of the final product.
  • spherical particles are applied as final products, such as grinding balls (alumina, zirconia, silica, etc.), liquid crystal spacers (resin, silica, etc.), chromatographic separation materials, other adsorbents, etc. Is mentioned.
  • such a particle product having a uniform shape, size, and density greatly affects the characteristics of the product as a final form, so that more uniform particles are required.
  • Patent Documents 1 and 2 As a method for producing such particles, a method of developing a technique for producing uniform particles from the beginning (Patent Documents 1 and 2) and a particle having a non-uniform distribution having a required size, density and shape are used. There are two extraction methods (Patent Documents 3 and 4). The former is a relatively new technology and requires a renewal of manufacturing equipment, but the latter can be added to the current equipment and is therefore easily incorporated into the manufacturing process. As the latter technique, there are, for example, a filter separation method (including sieve classification), a gravity classification method, a centrifugal separation method, a cyclone separation method and the like if the particles are several tens of ⁇ m or more.
  • the separation and classification methods listed above it is very difficult to separate particles of several tens of ⁇ m or less, particularly particles of 10 ⁇ m or less, and it is generally a batch type process and difficult to separate continuously. .
  • a batch type process since the amount of treatment per process is determined by the separation yield, relatively large equipment (stock container for raw materials, supply equipment, collection container for unnecessary products) is required.
  • the sieve classification method is suitable for mass processing, but it is necessary to gradually change the size of the sieve mesh, so that it is a batch process.
  • the gravitational classification method is basically a batch process similar to the sieving classification method, and it takes an enormous amount of time to process as the particle size decreases.
  • the centrifugal separation method and the cyclone separation method are suitable for high-speed processing, they require a large apparatus and are not suitable for a continuous process.
  • the target size can be determined from the mainstream flow trajectory using the Brownian vibrations of the particles, which are regularly arranged with micro-processed bowl-shaped projections called brownia ratchet.
  • this method is a split flow formation by Brownian vibration as a separation mode, the separation speed is slow, and the main flow formation is performed in the form of electrophoresis, and it takes time for the separation, especially with a diameter of 1 ⁇ m or more. For particles, it took a long time to separate, and due to the influence of disturbance during that time, there was a problem that it could not withstand practical use.
  • a method for measuring the size of cells by measuring forward scattered light using a flow cytometer As a method for separating or classifying cells based on their size, a method for measuring the size of cells by measuring forward scattered light using a flow cytometer is known.
  • the flow cytometer can roughly separate the target from a large amount of particles, but it is difficult to accurately separate a small amount due to the influence of cell shape and refractive index, and it is also vulnerable to impact. Things can be destroyed.
  • the first problem of the present invention is the development of a particle manipulation device and a particle manipulation method that enable manipulation of particles contained in a fluid.
  • a particle manipulating apparatus and a particle manipulating method that enable manipulation of particles having specific properties among particles having various properties contained in a fluid.
  • a second object of the present invention is an apparatus for manipulating particles from a fluid containing particles, which can be miniaturized, and an apparatus capable of classifying the particles by manipulating the particles. There is.
  • the present inventors have applied a reciprocating flow to a fluid containing particles having various properties, depending on the size, shape, mass, density, etc. of the particles. Focusing on the movement with the inherent mobility of particles, the inventors have come to the invention of an apparatus and method for manipulating particles contained in a fluid by reciprocating flow.
  • the present invention relates to: [1] A particle manipulating device including a flow path of a fluid containing particles and one or a plurality of pressurizing and depressurizing means for generating a reciprocating flow, wherein the particles in the fluid move in one direction of the reciprocating flow.
  • the particle manipulating device that enables movement, separation, or classification of particles by moving at a particle-specific mobility.
  • the particle manipulation device according to item 1 wherein the reciprocating flow is a periodic flow.
  • the waveform indicating the displacement of the fluid in the periodic flow has a non-symmetric waveform.
  • the particle manipulation device according to any one of items 1 to 3, wherein the flow path is formed between an upper surface substrate member, a lower surface substrate member, and a side surface member.
  • the pressurizing and depressurizing means is arranged for one or more members selected from the group consisting of the upper surface substrate member, the lower surface substrate member, and the side surface member.
  • the flow path includes one or more fluid inlets and one or more fluid outlets.
  • the fluid inlet and the fluid outlet are arranged so that the flow from the fluid inlet to the fluid outlet can be maintained in a direction intersecting the reciprocating flow direction.
  • a method for manipulating particles including a step of applying a reciprocating flow to a fluid containing particles; and a step of moving the particles in one direction of the reciprocating flow with a mobility inherent in the particles.
  • the particle manipulation method according to item 8 wherein the reciprocating flow is a periodic flow.
  • the particle manipulation method according to item 9 wherein the waveform indicating the displacement of the fluid in the periodic flow has a non-symmetric waveform.
  • the particle manipulation method according to any one of items 8 to 10 wherein the method includes a step of obtaining the moved particles, and enables classification or separation of the particles.
  • the fluid inlet and the fluid outlet are arranged in parallel to the reciprocating flow direction so that the flow from the fluid inlet to the fluid outlet can be maintained. The particle manipulator described.
  • the first aspect of the present invention of the second aspect is: A particle manipulating device comprising a fluid flow path containing particles and one or more pressure-reducing means for generating a reciprocating flow,
  • the pressure increasing / decreasing means is a means for generating a flow reciprocating in a direction intersecting with a direction of introduction of the fluid in the flow path;
  • the waveform indicating the amount of displacement of the fluid in the reciprocating flow has a non-symmetric waveform, And it is the said particle
  • the second aspect of the present invention of the second aspect is the particle manipulating device according to the first aspect, wherein the flow path is formed between an upper substrate member, a lower substrate member, and a side member. It is.
  • the concavo-convex portion is disposed on one or both of the upper substrate member and the lower substrate member, and is parallel to the fluid introduction direction in the flow path.
  • the fourth aspect of the present invention according to the second aspect is the particle manipulating apparatus according to the third aspect, wherein the concavo-convex portion provided in the flow path extends linearly.
  • the fifth aspect of the present invention of the second aspect is the particle manipulating apparatus according to the fourth aspect, wherein the cross section of the concavo-convex portion extending linearly has a non-symmetrical shape.
  • the pressure-reducing means is means for generating a flow that reciprocates in a direction perpendicular to the fluid introduction direction in the flow path.
  • a plurality of particle discharge ports are provided in the flow path of the fluid containing particles, and the particle discharge ports are provided in a direction perpendicular to the introduction direction of the fluid containing particles.
  • the eighth aspect of the present invention of the second aspect is the particle manipulating device according to the seventh aspect, wherein particles having different diameters are discharged from each particle discharge port.
  • the ninth aspect of the present invention of the second aspect is a method for classifying particles contained in a fluid using the particle manipulating apparatus according to any one of the first to eighth aspects.
  • the tenth aspect of the present invention of the second aspect is A particle manipulating device comprising a fluid flow path containing particles and one or more pressure-reducing means for generating a reciprocating flow
  • the pressure increasing / decreasing means is a means for generating a flow reciprocating in a direction parallel to the direction of introduction of the fluid in the flow path;
  • the waveform indicating the amount of displacement of the fluid in the reciprocating flow has a non-symmetric waveform, And it is the said particle
  • the eleventh aspect of the present invention according to the second aspect is the particle operation according to the tenth aspect, wherein the flow path is formed between an upper substrate member, a lower substrate member, and a side member. Device.
  • a twelfth aspect of the present invention according to a second aspect is that the uneven portion is arranged on one or both of the upper substrate member and the lower substrate member and intersects with the fluid introduction direction in the flow path.
  • the particle manipulation device according to the eleventh aspect which extends in a direction.
  • the particles contained in the fluid can be moved at a specific mobility by classifying the particles by giving a flow that reciprocates in parallel or in a direction intersecting the flow path. It becomes possible to do.
  • the second aspect of the present invention provides a particle manipulating apparatus comprising a fluid flow path containing particles and one or more pressure increasing / decreasing means for generating a reciprocating flow.
  • a means for generating a reciprocating flow parallel to or in parallel with the direction of introduction of the fluid in the channel, wherein the waveform indicating the amount of displacement of the fluid in the reciprocating flow has a non-symmetrical waveform, and One or more uneven portions are provided.
  • the particles contained in the fluid can be classified continuously by the particle manipulation device of the present invention of the second aspect.
  • the particle manipulation device according to the second aspect of the present invention can be easily downsized because the device configuration is simple.
  • FIG. 1 is a side view of the particle manipulating apparatus according to the first aspect of the present invention.
  • FIG. 2A is a diagram schematically illustrating a side surface of the flow channel structure.
  • FIG. 2B is a perspective view of a lower surface substrate, a side member, and an upper surface member of a flow channel structure including a plurality of introduction ports and discharge ports.
  • FIG. 3A is a diagram schematically illustrating a liquid flow generated when the flow path is deformed by the vibration member.
  • FIG. 3B shows voltages applied to the vibrating members 9L and 9R.
  • FIG. 3C is a diagram illustrating expansion and contraction of the piezoelectric element when a voltage is applied.
  • FIG. 4A is a diagram schematically illustrating a side surface of the flow channel structure.
  • FIG. 4A is a diagram schematically illustrating a side surface of the flow channel structure.
  • FIG. 4B is a top view of the side member constituting the flow channel structure.
  • the side member is formed by hollowing out a 11 mm thick silicone rubber sheet, and the hollowed portion is sandwiched between the upper surface substrate and the lower surface substrate to form a flow path.
  • FIG. 5A is a top view of a side member constituting the flow channel structure in which a plurality of fluid discharge ports are provided for one fluid introduction port and the fluid discharge port is a particle acquisition port in the flow channel structure of FIG. It is.
  • FIG. 5B is a photograph of the particle manipulation device according to the first aspect of the present invention including the flow channel structure.
  • FIG. 6 shows a method for calculating the moving speed of the particles.
  • FIG. 7 shows the mobility of particles when the waveform of the applied voltage is deformed.
  • FIG. 7A shows the mobility when applying a waveform voltage with positive deformations (0 °, 30 °, 60 °, 120 °, and 150 °)
  • FIG. 7B shows the negative deformation ( ⁇ 0 °).
  • ⁇ 30 °, ⁇ 60 °, ⁇ 120 °, and ⁇ 150 ° the mobility is shown when a waveform voltage is applied.
  • FIG. 8 shows the mobility when a waveform having a positive deformation is applied.
  • FIG. 10A is a diagram schematically illustrating a side surface of the flow channel structure.
  • FIG. 10B is a top view of the side member constituting the flow channel structure. The side member is formed by hollowing out a 11 mm thick silicone rubber sheet, and the hollowed portion is sandwiched between the upper surface substrate and the lower surface substrate to form a flow path.
  • FIG. 11A is a photograph of a channel structure for cell separation.
  • FIG. 11B is an enlarged view of the flow path and shows that cancer cells and blood cells have been separated.
  • FIG. 12 is a side view of another embodiment of the particle manipulating apparatus of the present invention according to the first aspect.
  • FIG. 13 is a side view of still another embodiment of the particle manipulating apparatus of the present invention according to the first aspect.
  • FIG. 14 is a principle diagram of the particle manipulating apparatus of the present invention according to the first aspect capable of separating / measuring particles in batch units.
  • FIG. 15 is a configuration diagram showing an embodiment of the particle manipulation device of the present invention of the first aspect capable of separating / measuring particles in batch units. The figure (side view) which showed an example of the particle
  • FIG. 17 is a top view of a lower substrate member in the channel structure constituting the particle manipulation device shown in FIG. 16.
  • grain operating apparatus shown in FIG. The top view of a side member among the flow-path structures which comprise the particle
  • FIG. 7 is a top view of a side member in a flow channel structure that constitutes a particle manipulation device manufactured in Example 6.
  • FIG. 10 is a schematic diagram illustrating movement of particles in Example 6. The figure which showed the result of Example 7.
  • Black circles or black squares are the results for particles with ⁇ 200 ⁇ m, and white circles and white squares are the results for particles with ⁇ 80 ⁇ m.
  • FIG. Black circles or white circles are the results of particles having a diameter of 200 ⁇ m, white squares and white squares are the results of particles having a diameter of 80 ⁇ m, and black triangles and white triangles are the results of particles having a diameter of 40 ⁇ m.
  • FIG. 6 is a schematic diagram illustrating movement of particles in Comparative Example 1. The figure which showed an example of the lower substrate member of the flow-path structure which enables continuous classification, the upper substrate member, and the side member in the particle
  • the present invention of the first aspect relates to a particle manipulating apparatus including a flow path of a fluid containing particles and one or a plurality of pressure-reducing means for generating a reciprocating flow.
  • the second aspect of the present invention relates to a particle manipulating device comprising a flow path of a fluid containing particles, and a pressure-reducing means for generating a flow reciprocating in a direction intersecting the introduction direction of the fluid in the flow path.
  • the particle manipulating device of the present invention is a device that moves particles according to the inherent properties of the particles, such as, but not limited to, the size, density, shape, and mass.
  • the particle manipulating device of the present invention is based on the fact that particles in the fluid contained in the flow path move in one direction of the reciprocating flow with the inherent mobility of particles by generating the reciprocating flow. This allows manipulation of the particles, ie movement, separation or classification. Since the inherent mobility of particles changes depending on various conditions, a desired particle group can be selected by appropriately selecting, for example, a fluid, a flow path length, a position of a particle acquisition port, a waveform indicating a displacement amount of the fluid, and the like as conditions. It becomes possible to get.
  • the particles to be moved, separated or classified in the present invention are not particularly limited as long as they are insoluble in the fluid.
  • research and medical materials such as cells, DNA, vaccines, viruses, colloids, and micelles are also included. Since the present invention performs separation by reciprocating flow of fluid, separation is possible without depending on electrostatic charge or dielectric properties, and fragile particles such as cells, droplets, bubbles, separation substrates, catalysts, pharmaceutical granules More suitable for separating capsules.
  • Examples of the cell to be moved, separated, or classified include arbitrary cells.
  • cells in blood and cultured cells are used for migration, separation, or classification.
  • Cells in blood are roughly divided into red blood cells, white blood cells, and platelets as blood cells, but other cells such as cancer cells may exist.
  • the size of erythrocytes is about 7 to 8 ⁇ m in diameter and 2 ⁇ m in thickness, and occupies most of the blood cells.
  • Leukocytes include monocytes, lymphocytes (T cells, B cells, natural killer cells, etc.), neutrophils, eosinophils, and basophils, and the size is about 6-30 ⁇ m depending on the cell type. is there.
  • Platelets are about 1 to 4 ⁇ m.
  • the size of circulating tumor cells (CTC) that circulate in the flow of blood or lymph and cause metastasis to distant organs is known to be 20-200 ⁇ m, which is considerably larger than blood cells. .
  • the ratio of CTCs present in blood is extremely low, and there are only a few to several tens of cells per 10 ml of blood, and detection and separation thereof are difficult.
  • separating a cultured cell for example, when differentiation induction is performed from a stem cell, the desired differentiated cell group can also be separated and acquired according to a magnitude
  • the present invention provides the following particle manipulation device: [1] A particle manipulating device including a flow path of a fluid containing particles and one or a plurality of pressurizing and depressurizing means for generating a reciprocating flow, wherein the particles in the fluid move in one direction of the reciprocating flow.
  • the particle manipulating device that enables movement, separation, or classification of particles by moving at a particle-specific mobility.
  • the flow path is provided with a fluid inlet and a fluid outlet, and fluid can flow from the fluid inlet to the fluid outlet.
  • the direction in which the fluid flows is defined as the main flow direction, and the flow is defined as the main flow.
  • the fluid outlet can be plugged, more preferably the fluid inlet can be plugged to keep the fluid in the flow path.
  • the particles can be manipulated in batch units.
  • a plurality of particle acquisition ports may be provided in order to acquire particles classified by processing in batch units.
  • the particle manipulating device of the present invention can be operated in a state where a fluid is continuously flowing from the fluid introduction port to the fluid discharge port, whereby the particles can be classified continuously.
  • the fluid discharge port of the flow path may be a particle acquisition port, or a particle acquisition port may be formed separately from the fluid discharge port.
  • the size of the particle acquisition port may be the same as or different from the size of the liquid discharge port, but from the viewpoint of not disturbing the main flow, it is 1/2 of the size of the fluid discharge port, more preferably 1 / 5, more preferably 1/10.
  • a plurality of fluid inlets and a plurality of fluid outlets can be provided from the viewpoint of reducing mainstream disturbance.
  • the reciprocating flow is applied in a direction intersecting the main flow direction.
  • the direction intersecting with the main flow direction means that the reciprocating flow direction and the main flow direction are not parallel. Therefore, the direction of the reciprocating flow is applied to the main flow direction and an arbitrary angle, more preferably, a direction orthogonal to the main flow direction.
  • the particle manipulating apparatus that enables continuous classification is more preferable in that the apparatus configuration can be reduced as compared with the batch type particle manipulating apparatus.
  • a reciprocating flow may be applied parallel to the main flow direction.
  • the liquid can be sent from the fluid introduction port at a constant flow rate, and after resting, the reciprocating flow is added in parallel to the main flow direction, whereby the same particle classification as in chromatography can be performed.
  • the above embodiment is preferable in that classification and measurement are easy even for particles of several tens of ⁇ m or less, which are difficult to classify by conventional methods.
  • the shape of the flow path may be any shape such as tubular or planar. When manipulating particles in batch units, tubular channels may be used. On the other hand, from the viewpoint of continuously obtaining classified particles, it is preferable to form a flow path in a planar shape and provide a plurality of particle acquisition ports for the flow path while forming a main flow.
  • the channel formed in the planar shape may be formed, for example, between the upper surface substrate member, the lower surface substrate member, and the side surface member.
  • the channel formed in a planar shape may have a shape for branching the reciprocating flow, or a shape for collecting particles that have moved with a certain range of inherent mobility, in order to enhance the separation performance due to the reciprocating flow. .
  • any material can be used as the upper surface substrate member and the lower surface substrate member as long as they are rigid flat plates. From the viewpoint of observing particles, a transparent member, preferably a glass plate, a polycarbonate plate, or the like is used.
  • the upper substrate member and the lower substrate member may have any shape, but the same shape is preferable, for example, a quadrangle.
  • the side member may be rigid, or may be a flexible or stretchable member. From the viewpoint of generating a reciprocating flow by applying the vibration member, a flexible or stretchable member is preferable. For example, silicone rubber, fluorine-based rubber, PDMS, elastomer resin, polymer gel, urethane resin, or the like is used.
  • the side member is sandwiched between the upper substrate member and the lower substrate member to form a flow path. Therefore, from the viewpoint of reducing fluid leakage from the flow path, the side member is preferably formed by cutting out the central portion of the plate-like member into an appropriate shape.
  • the length of the flow path can be appropriately selected according to the required separation performance of the particles, the properties of the particles to be separated and / or the properties of the fluid flowing through the flow paths and the flow velocity.
  • a length of 5 cm or more may be used from the viewpoint of achieving high separation ability, or a length of 10 cm or more may be used.
  • a length of 10 cm or more may be used.
  • it may be 30 cm or more.
  • the rigid upper substrate member and lower substrate member it is preferably 10 cm or less, more preferably 5 cm or less.
  • the length of the separation time is proportional to the separation ability, and therefore, the length of the flow path is preferably selected as appropriate within a range in which liquid feeding and reciprocating flow can be generated.
  • the fluid inlet is not particularly limited as long as a fluid can be introduced, but one or a plurality of fluid inlets may be formed.
  • the fluid introduction port may be connected to a liquid feeding pump via a liquid feeding tube.
  • a channel formed in a planar shape it is preferable to provide a plurality of fluid inlets from the viewpoint of reducing disturbance of the main flow.
  • particles to be separated from all of them may be introduced, but from the viewpoint of classifying particles according to the mobility in the direction intersecting the flow path from the fluid inlet,
  • the fluid introduction port to be introduced is preferably a part, more preferably at one place, and only the fluid containing no particles is preferably introduced from the other fluid introduction ports.
  • the fluid introduction port may be formed on any one or more of the upper substrate member, the lower substrate member, and / or the side member.
  • the introduction port is provided on the upper substrate member. It can also be provided.
  • the fluid outlet is not particularly limited as long as the fluid can be discharged, but one or a plurality of outlets may be formed.
  • the fluid discharge port may be connected to a drainage tank or a suction pump via a drainage tube, or a detection device capable of detecting the passage of separated particles or a detection device having a particle size is connected. It may also serve as a particle acquisition port, in which case the liquid containing the particles is dispensed via a particle acquisition tube or directly.
  • a plurality of fluid inlets can be provided, and the same or different number of fluid outlets can be provided from the viewpoint of reducing mainstream disturbance.
  • the fluid discharge port is formed in any one or more of the upper substrate member, the lower substrate member, and the side member. It may also be provided on the lower substrate member or the side member, particularly the lower substrate member.
  • the particle manipulating device of the present invention includes a pressure-reducing unit that generates a flow that reciprocates in a direction intersecting or parallel to the main flow direction.
  • a pressure increasing / decreasing means for example, a vibrating means such as an actuator or a piezoelectric element may be used, a liquid flow or air flow generating means such as a pump may be used, or a reciprocating flow separate from the flow path for separating particles.
  • a generator may be installed.
  • the vibration means is provided on any one or more of the upper surface substrate member, the lower surface substrate member, and / or the side surface member.
  • a reciprocating flow may be formed by deformation of each member.
  • the elastic member is used for the side member, and the vibration means is provided on the upper substrate member or the lower substrate member to vibrate the side edge of any of the substrate members up and down, thereby reciprocating liquid flow. Will occur.
  • a reciprocating liquid flow is generated by vibrating one side edge of the upper substrate member up and down, or by alternately vibrating two or more side edges up and down by two or more vibration means. Can do.
  • the frequency may be the same or different.
  • a liquid flow or air flow generation means such as a pump
  • a plurality of pump connection holes may be arranged on one side member, and the connection holes may be connected to the pump to alternately apply positive pressure and negative pressure. Good.
  • a plurality of pump connection holes may be disposed on the side members on both sides, and the connection holes may be connected to the pump to alternately apply positive pressure.
  • the plurality of pump connection holes arranged in one side member may be connected to one pump or may be connected to a plurality of pumps.
  • the reciprocating flow generated by the pressurizing / depressurizing means is preferably a periodic flow. It is preferable that the waveform indicating the displacement amount of the fluid in such a periodic flow has a non-symmetrical waveform.
  • the reciprocating flow can be generated by using a driving signal having a reciprocating waveform as a driving signal for the vibration means. Therefore, the waveform indicating the amount of displacement of the fluid may correspond to the waveform of the drive signal of the vibration means as it is.
  • the driving signal having a reciprocating waveform may be either voltage or current. Such a signal may be a pulse that changes sharply in a short time, or may be a continuous wave that changes continuously.
  • such a waveform is preferably periodic. Since the reciprocating flow occurs according to the waveform of the drive signal, if the drive signal is periodic, the reciprocating flow is also periodic. Examples of such a periodic waveform include an arbitrary waveform, and may be a point symmetric waveform, a non-point symmetric waveform, a line symmetric waveform, or a non-symmetric waveform. Point symmetry means that the waveform is symmetric when viewed from the point where the signal intensity becomes zero. Line symmetry means that the signal is inverted in polarity every half cycle of the shortest repetition period. In the case of line symmetry, the positive signal value and the negative signal value are symmetrical with respect to the time axis. It has become.
  • the fluid flowing in the flow path may be liquid or gas, but liquid is preferable from the viewpoint of achieving higher separation ability.
  • a liquid an arbitrary liquid can be selected according to the particles to be separated.
  • the solvent used in the production may be used as it is, or may be replaced with an inexpensive and harmless solvent such as water and used for a particle manipulation device.
  • the particles to be separated are biological materials such as cells, viruses, and antibodies, it is preferable to use a liquid in which these particles are originally dispersed, particularly when cells are used from the viewpoint of ensuring the survival of the cells.
  • Culture medium, blood, plasma, and physiological saline (PBS, TBS, etc.) can be used.
  • any excipient such as a pH adjusting agent, a stabilizer, a thickener, a preservative, an antibiotic and the like can be used. From the viewpoint of increasing the separation ability, an appropriate viscous liquid can be selected according to the size, density, and shape of the particles.
  • pressure generating means in addition to using vibration means as means for generating reciprocating flow.
  • the particle manipulation device is realized by, for example, the following flow path structure 2, reciprocating liquid flow generator 1, and liquid feed pump 3 (FIG. 1). Furthermore, in order to confirm that the particles are properly separated, particle observation devices 7 and 8 may be installed. A method for forming the periodically reciprocating liquid streams 26 and 27 used in the particle manipulating apparatus of the present invention according to the first aspect will be described in detail below.
  • the flow path structure 2 is formed by the upper surface substrate member 18, the lower surface substrate member 20, and the side surface member 19 (FIG. 2A).
  • An introduction port 22 and a discharge port 23 are provided in either the upper surface substrate member 18 or the lower surface substrate member 20, and the direction from the introduction port 22 to the discharge port 23 is referred to as a flow path direction or a main flow direction (FIG. 2).
  • the particle acquisition port 25 can be arranged at an arbitrary location on the upper substrate member 18 or the lower substrate member 20 (FIG. 2).
  • the vibration member adhesion point 21 is disposed on the non-flow path surface of the upper surface substrate member 18 (FIG. 2B).
  • a plurality of vibration member adhesion points 21 may be provided, preferably two.
  • the straight line connecting the two vibration member adhesion points 21 only needs to intersect the mainstream direction, and the two vibration member adhesion points 21 are preferably arranged to be perpendicular. More preferably, the two vibration member adhesion points 21 are arranged at equal positions across the center of gravity of the upper surface substrate member 18.
  • the side member 19 may be any member as long as a flow path can be formed, but preferably a stretchable member can be used.
  • the side member 19 may be a rubber sheet in which a portion that becomes the flow path 24 is hollowed out, or may be a rubber packing provided on the surface of the lower substrate member.
  • the oscillating flow forming device reciprocating liquid flow generating device 1 may include a substrate holder 11 having a mechanism for holding the flow path structure 2 and oscillating members 9L and 9R (FIG. 1).
  • the vibration members 9L and 9R can be connected to the vibration member drive power supplies 12L and 12R for driving the vibration members 9L and 9R via the vibration member drive signal outputs 13L and 13R.
  • Such vibration member drive power supplies 12L and 12R may be further connected to the waveform generator 15 via waveform outputs 16L and 16R.
  • the number of vibration members may be one, but a plurality of vibration members may be arranged. For example, when two vibrating members are used, the vibration waveform may be synchronized or may not be synchronized.
  • a waveform symmetrical with respect to the time axis can also be used (FIG. 3).
  • the vibrating members 9 ⁇ / b> L and 9 ⁇ / b> R are connected to the inlet / outlet of the particle separation channel 31 by the diaphragm channel 30 that is vibrated by the vibrating member.
  • a reciprocating liquid flow can be generated inside, it may be arranged separately from the particle separation channel 31 (FIG. 12).
  • the vibration member is disposed separately from the particle separation channel 31, only one vibration member 9L may be disposed (FIG. 13).
  • FIGS. 13 In the reciprocating liquid flow generator 1 shown in FIGS.
  • the reciprocating liquid flow is introduced into the introduction / discharge port 47 installed in the diaphragm flow path 30 and the introduction / discharge port 48 connected to the particle separation flow path 31. It is preferable to install a check valve that restricts the direction of the flow so as not to hinder the formation of the motor, or an electric valve synchronized with the vibration member 9L.
  • a particle observing device comprising a zoom lens 8 and a camera 7 capable of observing the central part of the flow channel structure can be installed in the vibration flow forming device (FIG. 1). Thereby, the movement of the particles can be monitored, and an appropriate frequency, flow velocity, and the like can be set.
  • the reciprocating liquid flows 26 and 27 are generated when the vibrating members 9L and 9R push up and down the upper surface substrate member (FIG. 3A).
  • a vibration flow may be formed in the particle separation flow path 31, as shown in FIGS. 12 and 13, the diaphragm flow path that pushes up and down the vibration members 9L and 9R and the upper surface substrate portion. 30 may be separated from the particle separation channel 31.
  • piezoelectric elements can be used as the vibrating members 9L and 9R, and piezoelectric drivers can be used as the vibrating member drive power supplies 12L and 12R.
  • An output drive member drive signal output 13L of the vibration member drive power supply 12L is connected to the vibration member 9L, and an output drive member drive signal output 8R of the vibration member drive power supply 13R is connected to the vibration member 9R.
  • the waveform output 16L, 16R of the waveform signal generator 15 is connected to the input vibration member drive source signal inputs 14L, 14R of the vibration member drive power supplies 12L, 12R (FIG. 1).
  • the waveforms of the waveform outputs 16L and 16R of the waveform signal generator 15 can be alternately driven to expand and contract the piezoelectric element by shifting the phase by 180 degrees or inverting the signal.
  • a reciprocating liquid flow may be formed (FIG. 3).
  • the waveform output 16L of the waveform signal generator 15 is supplied to the vibration member drive source signal input 14L of the vibration member drive power supply 12L, and the waveform output 16R of the waveform signal generator 15 is supplied to the vibration member drive source signal input 14R of the vibration member drive power supply 12R. Connecting.
  • the output waveform of the waveform signal generator 15 can be arbitrarily generated.
  • the waveform may be a point symmetric or non-point symmetric and / or line symmetric or non-line symmetric waveform.
  • a sine wave, a triangular wave, a square wave, a trapezoidal wave, and a sawtooth wave is typically, a sine wave, a triangular wave, a square wave, a trapezoidal wave, and a sawtooth wave.
  • the output waveform of the waveform signal generator is a waveform of a reciprocating liquid flow in the flow path. From the viewpoint of obtaining higher resolution, a sawtooth wave having a non-symmetrical waveform is preferable.
  • the inlet 22 and / or the outlet 23 are installed by forming a 1 mm diameter through hole in the upper substrate member 18 or the lower substrate member 20 in the flow channel structure 2 (FIG. 2B). .
  • a grommet having an outer diameter of 1 mm is fixed to the through hole with an adhesive, and the grommet and the liquid feeding pump 3 are connected by a liquid feeding tube 5 to introduce / discharge the particles 28 (FIG. 1).
  • the camera 5 it is desirable to use a high-speed camera (VFC-1000 manufactured by Sakae) when observing the vibration of particles, and a Sony CCD camera (XCD-V50) switched according to the situation when observing at low speed.
  • the upper substrate member 18 is preferably made of a transparent member such as glass or polycarbonate.
  • Calculation method of particle moving speed A binarization process is performed on each image of one frame of an observation video by the high-speed camera of the camera 5 to detect encapsulated particles.
  • Software for measuring the position with respect to the center of gravity of the detected particles (FIG. 6) was prepared using LabVIEW (trade name). The movement trajectory of particles is measured by converting these information into data as changes over time.
  • the present invention provides the following particle manipulation device:
  • a particle manipulating device comprising a fluid flow path containing particles and one or more pressure-reducing means for generating a reciprocating flow
  • the pressure increasing / decreasing means is a means for generating a flow that reciprocates in a direction intersecting or parallel to the introduction direction of the fluid in the flow path,
  • the waveform indicating the amount of displacement of the fluid in the reciprocating flow has a non-symmetric waveform,
  • grain operation apparatus which provided the 1 or several uneven
  • the outlet side of the flow path of the fluid containing the particles is closed, more preferably the inlet side is also There is an operation of moving / classifying the particles in batch units by closing and retaining the fluid containing the particles in the flow path, and then generating a flow reciprocating in the direction intersecting or parallel to the flow path.
  • the flow path of the fluid containing particles is provided with a plurality of outlets, the particles with different diameters (classified) can be collected from each outlet by opening the outlet after the batch unit operation described above. Can do.
  • the fluid containing the particles is continuously introduced from the inlet side of the flow path and intersects the flow path.
  • the fluid containing the particles is continuously introduced from the inlet side of the flow path and intersects the flow path.
  • the particle outlet may be the same as the fluid outlet or a different outlet.
  • the diameter is 1 ⁇ 2 or less of the diameter of the fluid discharge port from the viewpoint of not disturbing the flow of the particle flow path contained in the fluid.
  • the diameter is preferably 1/5 or less, more preferably 1/10 or less.
  • the shape of the flow path of the fluid containing particles provided in the particle manipulation device of the present invention of the second aspect may be tubular or planar.
  • the particle manipulation device of the present invention of the second aspect is a device that continuously classifies particles contained in a fluid
  • An example of the planar flow path is a flow path formed between the upper substrate member, the lower substrate member, and the side member.
  • the flow path formed in a planar shape has a shape that branches the reciprocating flow and collects (classified) particles that have moved (classified) with a certain range of intrinsic mobility in order to improve the separation performance due to the reciprocating flow. It is good.
  • any material can be used as the upper substrate member and the lower substrate member as long as they are rigid flat plates, but from the viewpoint of observing particles, it is preferable to produce them with a transparent material such as a glass plate or a polycarbonate plate.
  • the upper substrate member and the lower substrate member may have any shape, but preferably have the same shape (for example, the same quadrangle).
  • the side member may be a rigid member, or may be a flexible or stretchable member. However, when a flexible or stretchable member is used as the side member, the upper substrate member and the lower substrate member are It is preferable in that a reciprocating flow can be generated by vibrating in the vertical direction.
  • the flexible or stretchable member examples include silicone rubber, fluorine rubber, PDMS, elastomer resin, polymer gel, and urethane resin.
  • the side member forms a flow path by being sandwiched between the upper substrate member and the lower substrate member. Therefore, the side member is preferably produced by hollowing out the central portion of the plate-like member into an appropriate shape from the viewpoint of reducing fluid leakage from the flow path.
  • the length of the flow path of the fluid containing the particles included in the particle manipulating apparatus of the present invention of the second aspect depends on the required separability of the particles, the nature of the particles to be separated and / or the flow path. What is necessary is just to select suitably according to the property and flow velocity of a fluid.
  • the length may be 5 cm or more, and may be 10 cm or more.
  • the length may be 30 cm or more. From the viewpoint of maintaining the rigidity of the upper substrate member and the lower substrate member, the length is preferably 10 cm or less, and more preferably 5 cm or less.
  • the length may be 1 cm or less.
  • the introduction port of the fluid channel containing particles provided in the particle manipulation device of the present invention of the second aspect is not particularly limited as long as the fluid can be introduced, and the number of introduction ports may be one, There may be a plurality.
  • the inlet of the flow path may be connected to a liquid feeding pump via a liquid feeding tube.
  • the flow path of the fluid containing particles is formed in a planar shape, it is preferable to provide a plurality of inlets from the viewpoint of reducing disturbance in the flow of the flow path.
  • a fluid containing particles to be separated from all the introduction ports may be introduced, but the particles are moved / removed by a flow reciprocating in a direction intersecting with the introduction direction of the fluid in the channel.
  • the inlet for introducing the fluid containing particles is preferably a part of the plurality, and more preferably limited to one place. Note that only the solvent may be introduced into the inlet other than the inlet through which the fluid containing particles is introduced.
  • the introduction port may be formed in one or more of the upper substrate member, the lower substrate member, and the side member. For example, the introduction port is formed in the upper substrate member. The aspect provided is illustrated.
  • the discharge port for fluid containing particles provided in the particle manipulation device of the present invention of the second aspect is not particularly limited as long as the fluid can be discharged, and the number of discharge ports may be one, There may be a plurality.
  • the fluid discharge port may be connected to a drainage tank or a suction pump via a drainage tube. When used together with a particle discharge port, the fluid discharge port may be connected via a particle acquisition tube or directly. From which the fluid containing the particles may be recovered.
  • the flow path of the fluid containing the particles is formed in a planar shape, it is preferable to provide a plurality of discharge ports as well as the introduction port from the viewpoint of reducing the disturbance of the flow of the flow path.
  • the number of outlets installed may be the same as the number of inlets or a different number.
  • the discharge port may be formed in one or more of the upper substrate member, the lower substrate member, and the side member.
  • the discharge port is formed in the lower substrate member. The aspect of providing can be illustrated (FIG. 26).
  • the pressure increasing / decreasing pressure that moves the particles by generating a flow that intersects or reciprocates in parallel with the introduction direction of the fluid in the fluid flow path including the particles there is a means for moving the particles by generating a reciprocating flow using a vibrating means such as an actuator or a piezoelectric element or a liquid flow generating means such as a pump.
  • a vibrating means such as an actuator or a piezoelectric element or a liquid flow generating means such as a pump.
  • the vibration means is provided to any one or more of the above-described members.
  • a reciprocating flow can be generated by vibrating one side edge of the upper substrate member up and down or alternately vibrating two or more side edges up and down by two or more vibration means. it can.
  • the frequency may be the same or different.
  • a plurality of pump connection holes are arranged on one side member, and the positive pressure is set while the connection holes are connected to the pump.
  • the flow may be generated by alternately applying a negative pressure.
  • a plurality of pump connection holes may be disposed on the side members on both sides, and a flow may be generated by alternately applying positive pressure in a state where the connection holes are connected to the pump.
  • a plurality of pump connection holes arranged in one side member may be connected to one pump or may be connected to a plurality of pumps.
  • the direction of reciprocating flow generated by the pressure-intensifying means may be a direction intersecting or parallel to the direction of introduction of the fluid in the fluid flow path containing particles, but a direction intersecting the direction of introduction of the fluid. In this case, it is preferable to use the vertical direction.
  • the reciprocating flow formed by the method described above is preferably a periodic flow.
  • the flow When the flow is generated by the vibration means, it can be generated by using a drive signal having a reciprocating waveform as the drive signal of the vibration means. Therefore, it can be said that the waveform indicating the amount of displacement of the fluid corresponds to the waveform of the drive signal of the vibration means as it is.
  • the drive signal having a reciprocating waveform may be either voltage or current.
  • the drive signal may be a pulse that changes sharply in a short time, or may be a continuous wave that changes continuously. From the viewpoint of ensuring the reproducibility of the resolution, such a waveform is preferably periodic.
  • the waveform of the reciprocating flow is a waveform having a non-symmetrical waveform such as a sawtooth wave, and by using the waveform, before and after switching of the flow traveling direction Therefore, the particles contained in the fluid can be moved efficiently.
  • line symmetry means that a signal is inverted in polarity every half cycle of the shortest repetition period. In the case of line symmetry, a positive signal value and a negative signal value are symmetrical with respect to the time axis. Yes.
  • the reciprocating flow waveform used in the particle manipulating device of the present invention is only required to have a non-symmetrical waveform, and may be a composite wave with other (sine, triangular, rectangular, etc.) waves. Good.
  • the fluid introduced in the particle manipulating apparatus of the second aspect of the present invention includes a liquid or a gas, but a liquid is preferable in that a higher separation ability can be achieved.
  • a liquid it can select suitably according to the particle
  • the solvent used in the production may be used as it is as the introduction liquid, or a liquid substituted with an inexpensive and harmless solvent such as water may be used.
  • the particles to be separated are biological materials such as cells, viruses, and antibodies, it is preferable to use a solvent in which the biological material is dispersed.
  • the culture medium is used from the viewpoint of ensuring the survival of the cells.
  • Blood, plasma, and physiological saline may be used as a solvent.
  • These liquids may further contain optional excipients such as pH adjusters, stabilizers, thickeners, preservatives, antibiotics and the like. From the viewpoint of increasing the separation ability, an appropriate viscous liquid may be selected according to the size, density, and shape of the particles.
  • the particle manipulating device of the present invention of the second aspect is characterized in that one or a plurality of uneven portions are provided in a flow path of a fluid containing particles.
  • the concavo-convex part may be constituted only by a convex part, may be constituted only by a concave part, or may be constituted by a combination of a concave part and a convex part.
  • the shape of the concavo-convex portion is not particularly limited, and examples thereof include a conical shape, a cylindrical shape, a pyramid shape, and a prism shape.
  • the concavo-convex part may extend linearly or curvedly in one direction.
  • the cross section thereof may have any shape, and may be, for example, a point symmetric, non-point symmetric, line symmetric, or non-line symmetric shape.
  • the uneven portion provided in the flow path of the fluid containing the particles is preferably an uneven portion extending linearly and having a non-symmetrical cross section, and extending non-linearly and linearly like a sawtooth shape. Adopting the concave and convex portions to be used is more preferable in that the particles contained in the fluid can efficiently move in one direction.
  • the position where the unevenness is provided is not particularly limited, and may be provided in a direction parallel to the fluid introduction direction, or may be provided in an intersecting direction, for example, in a vertical direction.
  • a means for generating a flow that reciprocates in a direction crossing the fluid introduction direction it is preferable that the fluid pressure is provided in a direction parallel to the fluid introduction direction in the flow path.
  • means for generating a flow that reciprocates in a direction parallel to the fluid introduction direction it is preferable to provide the fluid flow in a direction that intersects the fluid introduction direction in the flow path.
  • FIG. 16 An example of the particle manipulation device of the present invention is shown in FIG.
  • a particle manipulating device 2100 shown in FIG. 16 observes the movement of a flow channel structure 210 for introducing a liquid containing particles, a vibration flow generating device (pressurizing / depressurizing means) 220, and particles introduced into the flow channel structure 210. And a particle observation device 230.
  • the flow path structure 210 was formed by overlapping the lower substrate member 211, the side member 213, and the upper substrate member 212 in this order from the bottom (FIG. 16).
  • the lower substrate member 211 is a PC (polycarbonate) substrate having a thickness of 0.9 mm and a 10 cm square, and an uneven portion 11 a extending linearly having a sawtooth-like cross section with a width of 200 ⁇ m and a height of 5 ⁇ m is formed in a 50 mm ⁇ 90 mm region. A plurality were provided (FIG. 17).
  • the upper substrate member 212 is a glass substrate having a thickness of 1 mm and 10 cm square, and has two through holes 212a having a diameter of 1 cm as inlets and outlets on a central line on the substrate and 1 cm from the end surface (inlet 212aa and outlet 212ab). Formed (FIG. 18).
  • a metal electric eyelet is fixed to the through hole 212a with an adhesive for connection to the PTFE tube.
  • the liquid containing particle is introduced and discharged by connecting the electric eyelet and the PTFE tube with a syringe pump.
  • One observation port 212ab is sufficient when observing the movement state of particles.
  • the side member 13 is a silicon rubber sheet having a thickness of 1.5 mm and a 10 cm square, of which a 50 mm ⁇ 90 mm region (corresponding to a region provided with the concavo-convex portion 211 a extending linearly) is cut out to provide an opening 213 a.
  • a planar flow path was formed (FIG. 19).
  • the concavo-convex portion 211a extending linearly is formed in a direction parallel to the liquid introduction direction (that is, the direction from the introduction port 212aa to the discharge port 212ab) in the flow path of the liquid containing particles.
  • the flow path structure 210 described above is a preferable structure for classifying particles of several tens to several hundreds of ⁇ m.
  • the oscillating flow generator 220 includes a substrate holder (not shown) that holds the flow path structure 210, a piezoelectric element 221 that can be displaced in the thickness direction of the flow path structure 10, and a piezoelectric element 221. And a drive signal generator 223 (WF1646B manufactured by NF circuit block) and a drive signal generator 223 (WF1646B manufactured by NF circuit block) are provided for generating an oscillating flow (reciprocating flow).
  • the piezoelectric element 221 is provided at two locations so as to be in contact with a position 240 1 cm above the end of the substrate of the flow path structure 210 and the linear uneven portion 211a provided in the flow path structure 210.
  • the body 210 can be displaced by 100 ⁇ m in the thickness direction.
  • the piezoelectric element 221a and the output of the piezo driver 222a are connected to the output of the piezoelectric element 221b and the piezo driver 222b, respectively, and the input of the piezo drivers 222a and 222b and the output of the drive signal generator 223 are connected.
  • an oscillating flow is formed with respect to the liquid accommodated in the flow path structure 210.
  • the vibration flow is formed by shifting the phase of the output waveform of the drive signal generator 223 to the piezo driver 222a and the phase of the output waveform of the piezo driver 222b by 180 degrees or by inverting the signal to expand the piezoelectric element 221.
  • an oscillating flow is formed in a direction perpendicular to the liquid introduction direction (that is, the direction from the introduction port 212aa to the discharge port 212ab) in the flow path of the liquid containing particles (see FIG. 20).
  • An output waveform of the drive signal generator 223 to the piezo driver 222 can be arbitrarily generated, and examples thereof include a sine wave, a triangular wave, a square wave, and a sawtooth wave.
  • the particle observation device 230 includes a zoom lens 231 (manufactured by Moritex) and a camera 232 (SONY CCD camera XCD-V50, which can observe at least a region of the flow path structure 210 provided with the concavo-convex portion 211a extending linearly.
  • a high-speed camera VFC-1000 manufactured by Sakae
  • the camera 232 is preferably used by switching to a high-speed camera when observing up to particle vibration, and to a CCD camera when observing at low speed.
  • the position of the detected particles at the center of gravity is determined.
  • the movement trajectory of particles can be measured.
  • a silicone rubber sheet having a size of 10 cm ⁇ 10 cm and a thickness of 1 mm is cut out so as to form a circular portion having a diameter of 32 mm and a flow path having a width of 5 mm and a length of 42 mm. It was arrange
  • the upper substrate member, the lower substrate member, and the silicone rubber sheet were joined by the adhesive force of the silicone rubber sheet so as to minimize liquid leakage.
  • the position of the center of the circular cut-out portion of the silicone rubber sheet was set as the arrangement position of the vibration members 9L and 9R.
  • the sample introduction / discharge port allows the flexible tube to be connected so that liquid can be introduced and discharged, and the eyelet is fixed to the through hole of the upper lid substrate member with an adhesive so that the tube can be connected. Manufactured.
  • the substrate holder 11 having a mechanism for holding the flow path structure 2 and the vibration member arrangement position of the flow path structure 2 are displaced by 100 ⁇ m in the substrate thickness direction at a position 1 cm from the substrate edge.
  • Possible piezoelectric elements (manufactured by Shoei System) were arranged as vibration members 9L and 9R.
  • Two piezoelectric drivers SSL-140-1CH (manufactured by Shoei System Co., Ltd.) were installed as vibration member drive power sources to generate vibration flow for the two piezoelectric elements.
  • WF1646B (made by NF circuit block) was connected as the waveform signal generator 15 (FIG. 1).
  • Particle observation device A zoom lens (MORITEX), CCD camera (SONY XCD-V50) or high-speed camera (Seiei VFC-1000) capable of observing the center of the micro-channel structure is added to the center of the substrate. (Fig. 1).
  • Example 1 Movement of particles having a particle diameter of 200 ⁇ m in ethanol
  • a flow path structure is set in a reciprocating liquid flow generator equipped with the above particle observation apparatus, and a liquid containing particles is contained in the flow path structure.
  • the introduced particles were Tosoh Pearl gel made by Tosoh having a particle size of about 200 ⁇ m, and used by being substituted and dispersed in 99.5% ethanol (density: 0.7892 g / cm 3 ).
  • the sample introduction / discharge port was sealed with a grommet fixed to the port with an adhesive, and the sample was sealed for batch processing.
  • FIG. 3C shows the flow change due to compression / extension of the circular portion at this time so that it can be easily considered.
  • one period of the waveform is expressed as 360 °
  • the vertex of the triangular wave is expressed as 0 ° as a line-symmetric vibration in FIG. 3C. From this state, the vertex of the triangular wave was changed up to ⁇ 180 ° to observe the movement of particles.
  • the frequency of the driving waveform at this time was set to 5 Hz, and the maximum driving voltage of the piezoelectric element was set to 2 V (100 ⁇ m variation at 5 Vmax) and the piezoelectric element extended to 40 ⁇ m.
  • the movement trajectory of the particles due to the vibration of the piezoelectric element was measured by automatic measurement of the particle position by image analysis as shown in FIG.
  • the reciprocal signal waveform is axisymmetric with respect to the time axis, that is, the apex of the triangular wave is 0 ° (that is, the triangular wave of 0 ° in FIG. 3C).
  • the 200 ⁇ m particles vibrated but could not be observed to move in one direction.
  • the axis is not symmetrical with respect to the time axis (that is, when the apex of the triangular wave is 0 °), that is, with a non-symmetrical waveform of 60 ° to 150 °
  • the amount of displacement of the reciprocating fluid is also a non-symmetrical waveform.
  • the positions of the particles at this time were measured, it was confirmed that they moved to the right as shown in FIG. 7A.
  • Example 2 Example 1 except that Ficoll (density 1.077 g / cm 3 ) was used as a solvent for dispersing moving particles having a particle size of 200 ⁇ m in Ficoll and the driving waveform was changed. The experiment was conducted in the same manner. As the driving waveform of the piezoelectric element, a waveform changed by + 150 ° and ⁇ 150 ° from the apex of the triangular wave was used.
  • Ficoll density 1.077 g / cm 3
  • the frequency of the drive waveform is 5 Hz
  • the maximum drive voltage of the piezoelectric element is set to 2 V (100 ⁇ m fluctuation at 5 Vmax)
  • the piezoelectric element is expanded to 40 ⁇ m
  • the movement trajectory of particles due to the vibration of the piezoelectric element is an image as shown in FIG. It was measured by automatic measurement of particle position by analysis.
  • Example 3 In a flow channel structure used for moving 20 ⁇ m particles of polystyrene beads in a continuous flow system, a linear flow channel portion having a width of 10 mm has one particle introduction port and 5 on the opposite side. A silicone rubber sheet was cut out so as to form a particle acquisition port, and a through hole was formed in the upper substrate (FIG. 5). The eyelet was fixed to the through hole with an adhesive so that the tube could be connected. The channel was filled with water in advance, the outlet on the opposite side of the silicone tube attached to the outlets 1, 3, and 5 was installed in the collection container, and the tip of the silicone tube attached to the outlets 2 and 4 was closed .
  • the driving waveforms of the two piezoelectric elements in the photograph were set so that the expansion and contraction of the two piezoelectric elements were reversed.
  • a drive waveform shape of the piezoelectric element a sawtooth waveform was given as in the case of 180 ° in FIG. 3C.
  • the frequency of the driving waveform at this time was set to 5 Hz, and the maximum driving voltage of the piezoelectric element was set to 2 V (5 ⁇ m variation at 100 ⁇ m) and the piezoelectric element extended to 40 ⁇ m.
  • a particle sample As a particle sample, two kinds of polymer standard particles (Duke Standards CatNo. 4220A) having a particle size of 20 ⁇ m and fluorescent particles (Fluoro-Max (TM) Cat No. G0100) having a particle size of 1.0 ⁇ m are dispersed in pure water.
  • the syringe port was introduced at 100 ⁇ L / min into an introduction port that communicated with a flow path that communicates the two circular portions.
  • the liquid discharged from the discharge ports 1, 3, and 5 was collected for a certain period of time.
  • the liquid volumes from the collected ports 1, 3, and 5 were 0.65 g, 0.74 g, and 0.60 g, respectively.
  • 50 ⁇ L of the collected liquid was collected with uniform stirring and observed with a microscope.
  • the content of 20 ⁇ m particles was counted, it was 9, 57, and 43 from the ports 1, 3, and 5, respectively.
  • a large number of 1 ⁇ m particles were detected from any port. As described above, it was confirmed that the particles to be separated can be efficiently separated from the discharge port formed with a plurality of particles.
  • Example 4 Separation of cancer cells and blood cells As shown in FIG. 10, the flow path used was 10 cm square as a top substrate member and two through holes having a diameter of 1 mm as a sample introduction / discharge port on a blue plate glass having a thickness of 1.1 mm. processed.
  • a lower substrate member having no through hole is used, and a silicon rubber sheet having a thickness of 1 mm is pressed between the upper substrate member and the lower substrate member by a piezoelectric element having a diameter of 32 mm as shown in FIG.
  • Two circular sections were created that generated the flow. The circular portion is cut out so as to communicate with the through hole of the upper substrate.
  • a linear flow path having a width of 5 mm was formed so as to communicate the two circular portions.
  • the upper substrate member substrate and the silicon rubber sheet and the lower substrate member thus produced were subjected to comb patterning and joined with the adhesive force of the silicon rubber sheet to obtain a structure that minimizes liquid leakage.
  • the sample introduction / discharge port is configured such that the eyelet is fixed to the through hole of the upper surface substrate member substrate with an adhesive so that the flexible tube can be connected so that liquid can be introduced and discharged.
  • a particle introduction port 29 was created in the center of the flow path communicating with the circular portion of the piezoelectric element compression portion with an injection needle, and a diluted solution of blood cells and cancer cells was introduced.
  • a solution in which cancer cells (SKBR) are added to whole blood diluted to 1% with mannitol is introduced from the particle introduction port 29 after filling the mannitol solution in advance from the introduction / discharge port 22/23. / 23 was sealed with adhesive tape.
  • the center of the expansion / contraction portion 3 of the piezoelectric elements 2L and 2R is aligned with the piezoelectric element contact point (near the center of the circle) in FIG.
  • the drive waveforms of the two piezoelectric elements in FIG. 1 the drive waveforms were set so that the expansion and contraction of 2L and 2R was reversed as shown in FIG. 3B.
  • 3C shows the flow change due to compression / extension of the circular portion at this time so that it can be easily considered.
  • one period of the waveform is expressed as 360 degrees
  • the vertex of the triangular wave is expressed as 0 ° as symmetric vibration in FIG. 3C.
  • the apex of the triangular wave was set to + 180 °, and the movement state of blood cells and cancer cells was observed.
  • the frequency of the driving waveform at this time was set to 1 Hz
  • the maximum driving voltage of the piezoelectric element was set to 3 V (variation of 100 ⁇ m at 5 Vmax) and the extension of the piezoelectric element was 60 ⁇ m.
  • Example 5 Apparatus for Manipulating Particles in Batch Units
  • FIGS. 14 principle diagram
  • 15 one embodiment of configuration
  • a fixed amount of fluid is introduced from the sample introduction port 33 and then closed.
  • the vibration flow forming device 38 causes the discharge port to be discharged from the introduction port 32.
  • the oscillating flow 36 in parallel with the flow direction (main flow direction) to 34, particles contained in the sample introduced from the sample introduction port 33 are separated toward the discharge port 34 based on the particle diameter.
  • an optical detector 44 such as a UV detector is connected to the outlet 34 side, the separation peak 45 can be detected, and the particle size distribution can be measured in the same manner as in chromatography. If a light scattering detector is used as the optical detection device 44, particle size can be measured.
  • Example 6 A particle manipulation device 2100 of the present invention shown below was produced.
  • (1-1) Lower substrate member 211 A PC (polycarbonate) substrate having a thickness of 0.9 mm and a 10 cm square, and an uneven portion 211 a having a sawtooth-like cross section having a width of 200 ⁇ m and a height of 20 ⁇ m extending linearly is provided in a 50 mm ⁇ 90 mm region (FIG. 17).
  • (1-2) Upper substrate member 212 This is the same as the particle manipulation device 2100 of the present invention shown in FIG.
  • Side member 213 A silicon rubber sheet having a thickness of 1.5 mm and a 10 cm square, of which a hexagonal region of 70 mm ⁇ 90 mm was cut out, and an opening 213 a was provided to form a planar flow path (FIG. 21).
  • Example 7 An apparatus similar to the particle manipulating apparatus 2100 produced in Example 6 (1), except that the concave and convex portion 211a extending in a sawtooth linear shape provided on the lower substrate member 211 has a width of 200 ⁇ m and a height of 5 ⁇ m.
  • (2) As a solution containing particles, except that a 99.5% ethanol solution containing Toyopearl (Tosoh) particles of ⁇ 200 ⁇ m and ⁇ 80 ⁇ m was used, the same method as described in Example 6 (2) to (3) Toyopearl particles were moved.
  • Toyopearl Toyopearl
  • a binarization process is applied to each image of one frame of the observation video obtained by the particle observation device 230 (camera 232 uses a high-speed camera VFC-1000 manufactured by Sakae). After the detected particles were detected, the position at the center of gravity of the detected particles was measured, and the position trajectory was converted into data as a temporal change to measure the movement trajectory of the Toyopearl particles. The results are shown in FIG. It can be seen that the moving speed of Toyopearl particles having a large particle diameter of ⁇ 200 ⁇ m is high, and the moving speed of Toyopearl particles having a small particle diameter of ⁇ 80 ⁇ m is low. It can also be seen that when the particle vibration width exceeds the interval (200 ⁇ m) between the concave and convex portions 211a extending in a sawtooth shape, the moving speed of the particles is dramatically increased.
  • Example 8 A device similar to the particle manipulating device 2100 prepared in Example 7 was prepared, except that the concave and convex portion 211a extending in a sawtooth-like linear shape provided on the lower substrate member 211 was set to a width of 50 ⁇ m and a height of 1 ⁇ m. .
  • (2) The same as described in Example 7 (2) and (3), except that a 99.5% ethanol solution containing Toyopearl (Tosoh) particles of ⁇ 200 ⁇ m, ⁇ 80 ⁇ m and ⁇ 40 ⁇ m was used as the solution containing the particles.
  • the Toyopearl particles were moved by the method.
  • the movement trajectory of Toyopearl particles was measured by the same method as described in Example 7 (3). The results are shown in FIG.
  • the moving speed of the Toyopearl particles is relatively high in the order of the particle diameter ( ⁇ 200 ⁇ m> ⁇ 80 ⁇ m> ⁇ 40 ⁇ m). Further, it can be seen that when the particle vibration width exceeds the interval (50 ⁇ m) of 211 a extending in a saw-tooth linear shape, the moving speed of the particles is remarkably increased. From the results shown in FIG. 23 and FIG. 24, in the particle manipulating device of the second aspect of the present invention, the liquid containing the particles is introduced in a direction perpendicular to the introduction direction of the liquid containing the particles (that is, the direction from the introduction port 212aa to the discharge port 212ab). It is suggested that classification by particle size (diameter) is possible by providing a particle outlet.
  • Comparative Example 1 (1) Using the particle manipulation device 2100 produced in Example 6, a solution containing particles was introduced until the opening 213a was filled with the solution in the same manner as in Example 7 (2). (2) The sine wave shown in pattern (a) and pattern (b) in FIG. 25 was output from the drive signal generator 223 to move the Toyopearl particles. As a result, when any pattern of sine wave was output, Toyopearl particles only vibrated, and physical movement could not be confirmed. The same result was obtained even when the sine wave was changed to a triangular wave or a rectangular wave.
  • the waveform indicating the amount of displacement of the liquid in the oscillating flow is only a point symmetric waveform or only a line symmetric waveform, the particles do not move.

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Abstract

L'invention concerne un dispositif de manipulation de particules comprenant une voie d'écoulement destinée à un fluide qui contient des particules, ainsi qu'au moins un moyen d'augmentation-diminution de la pression destiné à générer un écoulement alternatif. Dans ce dispositif de manipulation de particules, les particules présentes dans le fluide se déplacent dans un sens de l'écoulement alternatif avec un degré de mobilité unique pour les particules, de manière à permettre le déplacement, la séparation ou la classification de ces particules.
PCT/JP2015/069705 2014-07-08 2015-07-08 Dispositif de manipulation de particules et procédé de classement de particules à l'aide de ce dispositif Ceased WO2016006642A1 (fr)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017177083A (ja) * 2016-03-31 2017-10-05 東ソー株式会社 粒子分離装置
JP2018189389A (ja) * 2017-04-28 2018-11-29 東ソー株式会社 キャピラリーと流動発生手段を組み合わせた粒子分離方法およびその装置
US11225639B2 (en) 2016-03-17 2022-01-18 National University Corporation Nagoya University Cell sorting device
JP2024116416A (ja) * 2016-09-16 2024-08-27 株式会社オンチップ・バイオテクノロジーズ 微粒子分注装置、微粒子解析装置、及び反応検出装置、並びにそれらを用いる方法
WO2025146819A1 (fr) * 2024-01-05 2025-07-10 国立大学法人九州大学 Dispositif de commande de trajectoire de particules et procédé de commande de trajectoire de particules

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63214348A (ja) * 1987-03-02 1988-09-07 Advance Co Ltd 微粒子操作装置
JPS63214347A (ja) * 1987-03-02 1988-09-07 Advance Co Ltd 微粒子操作装置
JPH1082723A (ja) * 1996-09-06 1998-03-31 Hitachi Ltd 微粒子処理装置
JP2006297333A (ja) * 2005-04-25 2006-11-02 Matsushita Electric Ind Co Ltd 成分分離デバイスおよびこれを用いた成分の分離方法
US20110163013A1 (en) * 2008-05-30 2011-07-07 Eppendorf Ag Apparatus and Method for Moving Particles in a Fluid
US8162149B1 (en) * 2009-01-21 2012-04-24 Sandia Corporation Particle sorter comprising a fluid displacer in a closed-loop fluid circuit

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63214348A (ja) * 1987-03-02 1988-09-07 Advance Co Ltd 微粒子操作装置
JPS63214347A (ja) * 1987-03-02 1988-09-07 Advance Co Ltd 微粒子操作装置
JPH1082723A (ja) * 1996-09-06 1998-03-31 Hitachi Ltd 微粒子処理装置
JP2006297333A (ja) * 2005-04-25 2006-11-02 Matsushita Electric Ind Co Ltd 成分分離デバイスおよびこれを用いた成分の分離方法
US20110163013A1 (en) * 2008-05-30 2011-07-07 Eppendorf Ag Apparatus and Method for Moving Particles in a Fluid
US8162149B1 (en) * 2009-01-21 2012-04-24 Sandia Corporation Particle sorter comprising a fluid displacer in a closed-loop fluid circuit

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11225639B2 (en) 2016-03-17 2022-01-18 National University Corporation Nagoya University Cell sorting device
JP2017177083A (ja) * 2016-03-31 2017-10-05 東ソー株式会社 粒子分離装置
JP2024116416A (ja) * 2016-09-16 2024-08-27 株式会社オンチップ・バイオテクノロジーズ 微粒子分注装置、微粒子解析装置、及び反応検出装置、並びにそれらを用いる方法
JP2018189389A (ja) * 2017-04-28 2018-11-29 東ソー株式会社 キャピラリーと流動発生手段を組み合わせた粒子分離方法およびその装置
WO2025146819A1 (fr) * 2024-01-05 2025-07-10 国立大学法人九州大学 Dispositif de commande de trajectoire de particules et procédé de commande de trajectoire de particules

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