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WO2001066947A1 - Liquid feeding device and analyzing device using the device - Google Patents

Liquid feeding device and analyzing device using the device Download PDF

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Publication number
WO2001066947A1
WO2001066947A1 PCT/JP2000/001332 JP0001332W WO0166947A1 WO 2001066947 A1 WO2001066947 A1 WO 2001066947A1 JP 0001332 W JP0001332 W JP 0001332W WO 0166947 A1 WO0166947 A1 WO 0166947A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
chamber
valve
inlet
diaphragm
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
Application number
PCT/JP2000/001332
Other languages
French (fr)
Japanese (ja)
Inventor
Yasuhiko Sasaki
Akira Koide
Yasuhiro Yoshimura
Ryo Miyake
Takao Terayama
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to PCT/JP2000/001332 priority Critical patent/WO2001066947A1/en
Publication of WO2001066947A1 publication Critical patent/WO2001066947A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B43/00Machines, pumps, or pumping installations having flexible working members
    • F04B43/02Machines, pumps, or pumping installations having flexible working members having plate-like flexible members, e.g. diaphragms
    • F04B43/04Pumps having electric drive
    • F04B43/043Micropumps
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N35/00Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor
    • G01N35/10Devices for transferring samples or any liquids to, in, or from, the analysis apparatus, e.g. suction devices, injection devices
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N35/00Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor
    • G01N35/10Devices for transferring samples or any liquids to, in, or from, the analysis apparatus, e.g. suction devices, injection devices
    • G01N2035/1027General features of the devices
    • G01N2035/1034Transferring microquantities of liquid
    • G01N2035/1039Micropipettes, e.g. microcapillary tubes

Definitions

  • the present invention relates to a diaphragm-type micropump, and more particularly, to a micropump of several seconds per second.
  • the present invention relates to a liquid sending device that sends liquid from L to several hundreds / L and an analyzer using the same.
  • a micro-diaphragm pump is a diaphragm pump with a size of several tens of millimeters or less, and the volume of the liquid transfer chamber is changed by deforming the diaphragm that forms part of the liquid transfer chamber.
  • the liquid is introduced into the liquid feed chamber from the inlet, and by reducing the volume, the liquid is discharged from the outlet.
  • the most common microdiaphragm pump processes single-crystal silicon using an aqueous alkali solution (anisotropic etching technology), and joins single-crystal silicon and pyrex glass (positive bonding technology). They are assembled and manufactured.
  • the former diaphragm pump consists of three chambers: an inlet valve chamber, a liquid feed chamber, and an outlet valve chamber.
  • the position of the inlet from which the liquid enters the liquid feed chamber during priming is located at the center of the liquid feed chamber.
  • an aqueous solution containing at least one kind of water-soluble salt or polyhydric alcohol is once injected into the pump and dried, whereby the water-soluble salt or polyhydric alcohol is applied to the surface of the pump in contact with the liquid.
  • Adhesives are attached to improve the affinity for liquid, eliminating bubbles remaining during priming.
  • bubbles may remain in the initial liquid introduction. This is due to the shape of the flow path from the inlet valve to the liquid through the liquid feed chamber to the outlet valve, and particularly air bubbles remain near the valve structure.
  • an object of the present invention is to provide a diaphragm pump that suppresses the generation of residual air bubbles and realizes highly accurate liquid sending.
  • the step near the inlet valve is reduced, and the inlet is arranged at the outer periphery of the flow path plane shape so that the outer periphery side is opened to the greatest extent.
  • FIG. 1 is a schematic diagram of the first embodiment of the present invention
  • FIG. 2 is a diagram showing the relationship between the liquid sending chamber height and the remaining bubbles in the first embodiment of the present invention.
  • 3 is a schematic diagram of the second embodiment of the present invention
  • FIG. 4 is a schematic diagram of the third embodiment of the present invention
  • FIG. 5 is an analyzer of the liquid sending device of the present invention.
  • FIG. 6 is a detailed explanatory view of the first application example of the present invention
  • FIG. 7 is a second application example of the liquid supply apparatus of the present invention to the analysis apparatus.
  • FIG. 8 shows a third application example of the liquid sending device of the present invention to an analyzer.
  • FIG. 1 is a schematic diagram of a liquid feeding device according to a first embodiment of the present invention.
  • (a) is a cross-sectional view of the liquid sending device
  • (b) is a plan view of the liquid sending chamber.
  • the liquid transfer device is composed of three substrates: a diaphragm substrate 110, a liquid transfer chamber substrate 120, and an inlet / outlet substrate 130.
  • the material of these substrates is silicon, glass, ceramic, metal or resin.
  • the liquid supply chamber substrate 120 has a liquid supply chamber 121, an inlet valve 122, and an outlet port 123.
  • the outlet valve substrate 130 has an outlet valve 132, and an inlet port 1 3 3, suction port 1 3 4 and discharge port 1 3 5 are machined. Machining methods include photolithography, sand blasting, injection molding, honing, electric discharge machining, and electric power.
  • the substrate and the piezoelectric disk 112 serving as an actuator are fixed to each other to assemble a liquid sending device.
  • the fixing method is direct bonding, anodic bonding, diffusion bonding, eutectic bonding, brazing, surface activated bonding, Use at least one.
  • each part is as follows.
  • the thickness of the diaphragm substrate is 500 ⁇ m
  • the thickness of the liquid transfer chamber substrate is 500, "m
  • the thickness of the inlet / outlet substrate is 500 ⁇ m.
  • the height from the bottom of the liquid transfer chamber 1 2 1 to the diaphragm surface 1 2 9 (hereinafter referred to as the liquid transfer chamber height) is 500 / m, and the height from the inlet port 1 33 to the diaphragm surface.
  • the height 1 28 (hereinafter referred to as the height above the inlet) is 600 / im
  • the width 3 2 1 in the plan view of the liquid transfer chamber 1 2 1 is 8 mm
  • the length 3 2 2 is 9 mm.
  • the external dimensions in the plan view are 14 mm x 14 mm.
  • the shape of the liquid transfer chamber was gradually expanded from the valve part on the inlet side, with a parallel part in the middle, and formed so as to gradually reduce from the parallel part toward the outlet side. .
  • the inlet valve 122 has a cantilever structure supported by beams 124.
  • the beam 124 is provided toward the inside of the liquid sending chamber 121, and the inlet valve 122 is arranged close to one side of the liquid sending chamber 121. Further, an outlet port 123 is arranged close to the side opposite to the side on which the inlet valve 122 is close.
  • the outlet valve 13 2 has a doubly supported structure supported by two beams (not shown).
  • the priming procedure of this liquid feeding device is as follows.
  • a liquid introducing device for sending the liquid to be introduced is connected to the suction port 134 of the liquid sending device.
  • This liquid introduction device uses one agricultural land such as a syringe pump, a tube pump, and a gear pump.
  • the pressurized liquid reaches the inlet valve 1 2 2 through the inlet port 1 3 3, and the pressure increases.
  • the inlet valve 1 2 2 is opened and the liquid flows into the liquid supply chamber 1 2 1.
  • the inlet valve 1 2 2 supported by the beam 1 2 4 passes through the inlet valve 1 2 2 as indicated by the arrow in Fig. 1 (b) because it opens at the root of the beam 1 2 4 at the fulcrum.
  • the filled liquid fills the liquid transfer chamber 1 2 1 from the adjacent side. Then reach exit port 1 2 3.
  • the liquid as well as the gas opens the inlet valve 122, and the liquid flows from the inlet into the liquid supply chamber 122 and reaches the outlet port 123.
  • the suction pump connected to the discharge port 1 35 is separated, and the preparation for liquid transfer is completed.
  • the bombing operation is performed by applying a voltage to the piezoelectric disks 1 1 and 2 to expand and contract in the plane direction.
  • the piezoelectric disk 112 is contracted in the plane direction and the diaphragm 111 is pushed into the liquid supply chamber side like a drum, the volume of the liquid supply chamber 121 decreases.
  • the reduced volume of the liquid is pushed out of the outlet valve 13 2, flows out of the outlet port 12 3 to the outside of the liquid sending chamber 12 1, and is discharged from the discharge outlet 13 5.
  • the diaphragm 111 returns to the piezoelectric disk side, and the volume of the liquid sending chamber 122 becomes large. Then, the liquid corresponding to the increased volume pushes open the inlet valve 122 and flows into the liquid sending chamber 122 from the inlet port 133. The liquid is fed by repeating this operation.
  • the first feature is that the liquid transfer chamber height is 1 2 9 to 5 0
  • the point is that the height above the inlet is set to 600 ⁇ m, and the residual air bubbles during priming are prevented.
  • the presence or absence of bubbles in the inlet valve depends on the wettability in the liquid transfer chamber.
  • the wettability in the liquid transfer chamber depends on the surface tension T 8 (N / m) and density p (kg / m 3 ) of the liquid, the contact angle (°) between the liquid and the liquid contact part of the liquid transfer chamber, and the height of the liquid transfer chamber.
  • T 8 N / m
  • density p kg / m 3
  • This threshold value h is constant, and when the physical properties (surface tension and density) of the liquid and the contact angle between the liquid and the liquid contact part of the liquid supply chamber change, the liquid supply chamber height at that time changes. For example, if the wettability between the liquid and the inner surface of the liquid transfer chamber is better than in the case of Fig. 2, the liquid transfer chamber height needs to be set higher. Conversely, when wettability is poor, the height of the liquid transfer chamber can be set small.
  • the outlet port 123 with a higher potential energy than the inlet valve 122 with respect to the horizontal plane based on the direction of gravity, The liquid that has entered the channel receives an attractive force in the direction of gravity due to its own density.
  • this attractive force has a reaction force component with respect to the surface tension
  • the influence of the surface tension in the liquid supply chamber can be reduced.
  • the reaction force component of the attractive force becomes maximum.
  • the air bubbles mixed into the liquid sending chamber 122 move from the inlet valve 122 to the outlet port 123 by its own buoyancy, so that the air bubbles can be easily removed.
  • the line connecting the inlet and the outlet was perpendicular to the horizontal plane with respect to the direction of gravity. The same effect can be obtained if the outlet is installed at a position higher in potential energy than the inlet.
  • the second feature is that the inlet valve 1 2 2 has a cantilever structure supported by the beam 1 2 4, and the beam 1 2 4 is arranged toward the inside of the liquid transfer chamber 1 2 1, and the opening of the inlet valve It was arranged so that the side was close to one side of the liquid transfer chamber 1 2 1. Another point is that the outlet port 123 is arranged close to the side opposite to the side where the inlet valve 122 is close. As a result, at the time of opening the inlet, the inlet valve 122 opens the side of the liquid supply chamber 121 most widest so that the liquid flows. The liquid that has flowed during priming and bombing becomes a smooth flow with a large curvature streamline 126 as shown by the arrow in Fig. 1 (b), preventing bubbles from remaining and Easily remove air bubbles.
  • the force in the case where the height of the liquid transfer chamber 1 29 is smaller than the height above the inlet 1 2 8 is smaller. If the threshold value h is not more than 0.02 mm, the liquid transfer chamber height 1 29 should be equal to the inlet upper height 1 28 so that bubbles are less likely to remain. In this embodiment, there are restrictions in forming the valve structure of the liquid device. Such a structure is more realistic.
  • FIG. 3 is a schematic diagram of a liquid feeding device according to a second embodiment of the present invention.
  • (a) is a cross-sectional view of the liquid sending device
  • (b) is a plan view of the liquid sending chamber.
  • the same reference numerals as in FIG. 1 indicate the same configuration as in the first embodiment.
  • the liquid transfer device is composed of three substrates, the same as in the first embodiment, a diaphragm substrate 110, an entrance / exit substrate 130, and a liquid transfer chamber substrate 220.
  • the difference from the first embodiment is that the projections 225 are formed in the liquid transfer chamber 221 of the liquid transfer chamber substrate 220.
  • the projections 2 25 are arranged in such a shape that the two surrounding flow paths are intermittently reduced in flow path area (a substantially hexagonal shape according to the shape of the liquid transfer chamber as shown in the figure).
  • the liquid transfer chamber height 2 29 is 500 ⁇ m
  • the height 2 27 (hereinafter referred to as the height above the protrusion) between the upper surface of the protrusion 222 and the diaphragm surface is 100 ⁇ m. 0 / zm.
  • the priming procedure of this liquid sending device is as follows. First, in order to replace the gas in the liquid sending chamber 1 2 1 of the liquid sending device with the liquid, a liquid introducing device for sending the liquid to be introduced into the suction port 1 34 of the liquid sending device is connected.
  • a liquid introduction device one of a syringe pump, a tube pump, and a gear pump may be used.
  • the pressurized liquid reaches the inlet valve 1 2 2 through the inlet port 1 3 3, and the pressurized pressure is applied. As a result, the inlet valve 1 2 2 is opened, and the liquid flows into the liquid supply chamber 1 2 1.
  • the inlet valve 122 supported by the beam 124 opens at the fulcrum at the root of the beam 124, so that the liquid passing through the inlet valve 122 flows from the adjacent side to the liquid transfer chamber 1 2 1 is satisfied and reaches the projection 2 25 on the inlet valve side. Then, the flow path above the projections 225 is filled with the liquid by the capillary action of the liquid. Here, since the end of the flow path on the projection is open, no bubbles remain.
  • the two flow paths on both sides of the projection Since the flow path is a speed-up flow in which the cross-sectional area of the flow path is continuously reduced, the flow path resistance gradually increases. Therefore, when the liquid advances in one of the flow paths around the protrusion in advance, the flow resistance of the other flow path becomes larger, so that the speed of the liquid in the preceding flow path decreases. descend. Then, when the flow path resistance difference becomes small, the traveling speed increases again, and reaches the outlet port 123 simultaneously from the two flow paths.
  • the priming operation may be performed using a suction pump as in the first embodiment.
  • the bombing operation is the same as in the first embodiment.
  • This embodiment has two features.
  • the first feature is that a protrusion 2225 is provided in the liquid transfer chamber with a liquid transfer chamber height of 229 m and a height of 220 m above the protrusion is set to 100 m.
  • the flow path on the protrusion allows the liquid to flow by capillary force, thereby preventing bubbles from remaining in the center of the liquid transfer chamber 121. Therefore, a liquid having better wettability than in the first embodiment has an effect of preventing bubbles from remaining. In order to quickly flow the liquid into the projection-shaped space, it is most effective to move the projections 2 25 to the inlet valve 122.
  • the second is that the two flow paths around the protrusion are flow paths for the accelerated flow.
  • the flow path resistance increases.
  • the traveling speed of the liquid decreases, and the traveling speed of the liquid in the other flow path increases. Therefore, the liquid proceeds in the two flow paths in a well-balanced manner, so that bubbles can be prevented from remaining in the liquid transfer chamber.
  • Bubbles are caused by static pressure drop.
  • This static pressure is reduced from the atmospheric pressure by the amount of decrease in the static pressure in the liquid sending chamber due to expansion of the volume of the liquid sending chamber and the static pressure This is a value obtained by subtracting the decrease. Since the location where the flow velocity becomes the highest when the liquid is sucked is the location where the cross-sectional area of the flow path is the smallest, that is, the static pressure becomes the lowest between the inlet valve and the inlet port, and the initiation of bubbles easily occurs. Therefore, a method for reducing the flow velocity between the inlet valve and the inlet port by optimizing the shape of the inlet valve or the inlet port is described below.
  • FIG. 4 is a schematic diagram of a liquid feeding device inlet valve according to a third embodiment of the present invention.
  • (a) and (b) are cross-sectional views of each liquid feeding device.
  • the same reference numerals as in FIG. 1 have the same configuration as in the first embodiment.
  • the liquid feeder shown in FIG. 4 (a) is composed of three substrates, the same as in the first embodiment, a diaphragm substrate 110, a liquid feed chamber substrate 120, and an entrance / exit substrate 4330. .
  • the difference from the first embodiment is that the diameter of the inlet port 43 3 of the inlet / outlet substrate 43 is larger than the diameter of the outlet port of the liquid transfer chamber substrate 120.
  • the cross-sectional area between the inlet valve 122 and the inlet port 43 is equal to the outlet valve 132 and the outlet port.
  • the flow rate of liquid between inlet valve 122 and inlet port 43 is equal to the flow rate of the outlet valve 132 and outlet port.
  • the flow rate of the liquid passing between the points 123 is smaller than that of the liquid, so that the initiation of bubbles is less likely to occur.
  • the liquid transfer apparatus shown in FIG. 4 (b) is composed of three substrates, the same as in the first embodiment, a diaphragm substrate 110, an inlet / outlet substrate 130 and a liquid transfer chamber substrate 420. Have been. The difference from the first embodiment is that a depression 4 2 6 is formed in the inlet valve 4 2 2 of the liquid transfer chamber substrate 4.
  • the cross-sectional area of the flow path between the inlet valve 422 and the artificial port 133 is determined by the outlet valve. No larger than the cross-sectional area of the flow path between 1 32 and outlet port 123 Therefore, the flow velocity of the liquid between the inlet valve 4 2 2 and the inlet port 13 3 is less than the flow velocity of the liquid between the outlet valve 1 3 2 and the outlet port 1 2 3 This makes it less likely that bubbles will begin to form.
  • the lift amount of the inlet valve 122 during the pumping is made larger than that of the outlet valve 132, and the inlet valve
  • the cross-sectional area of the passage between 122 and the inlet port 133 is larger than the cross-sectional area of the passage between the outlet valve 132 and the outlet port 123. Therefore, the flow velocity of the liquid passing between the inlet valve 122 and the inlet port 133 is smaller than the flow velocity of the liquid passing between the outlet valve 132 and the outlet port 123, and the air bubbles are generated. It is difficult for the first time to occur.
  • the flow rate of the liquid passing between the inlet valve and the inlet port is further reduced by making the lift amount of the inlet valve larger than the outlet valve at the time of pumping. It becomes bad. Thus, by reducing the flow velocity between the inlet valve and the inlet port, the initiation of bubbles is prevented.
  • FIG. 5 is an overall configuration diagram of an analyzer provided with the reagent supply mechanism of the present invention
  • FIG. 6 is a detailed explanatory diagram of the reagent supply mechanism of the present invention.
  • FIG. 5A shows the device 511 viewed from the front
  • FIG. 5B shows the device 511 viewed from the top.
  • a test tube 521 which contains a sample 52, and a sample holder 52, which holds the test tube 521, on the circumference.
  • a sample pipe 531 for sucking the sample 52 in the test tube 52 1 is provided beside the sample holder 52 2.
  • the sample pitcher 531 which sucks the sample and holds it inside, a three-dimensional drive mechanism 5333, which gives the nozzle 532 an up-and-down rotation, is shown in the figure. Not shown to aspirate sample into nozzle or eject sample from nozzle Pump is provided.
  • the sample holder 522 is driven to rotate by the rotary drive mechanism 523. At the other descent position of the nozzle of the sample c 531, the reaction vessel 541 moves while rotating sequentially.
  • the plurality of reaction vessels 541 are held on the circumference of the reaction disk 542.
  • the lower half of the reaction vessel 542 is connected to a constant temperature bath 543 through which constant temperature water flows.
  • the reaction disk 542 is supported by a reaction disk rotation drive mechanism 544 in order to sequentially move the reaction container to the lower position of the nozzle of the sample pitcher.
  • the first reagent supply section 5 51 and the second reagent supply section 5 61 1 A container cleaning mechanism 571 and a spectrometer 581 are provided.
  • the reagent supply section 55 1 is largely composed of four parts: a reagent container 55 2, a reagent holder 55 3, a liquid feeder 55 4 4, and a reagent holder 1 rotation drive mechanism 55 5 5.
  • Reagent holder 553 is a reagent container around central axis 556
  • a discharge port 563 is provided in the liquid sending device 554 vertically downward.
  • a magnetic unit 528 On the side surface of the reagent container 552, there is provided a magnetic unit 528 on which data describing the type of reagent is written.
  • a magnetic reader 581 for reading data of the magnetic section 582 is provided at a circumferential position corresponding to the reagent holder 553.
  • the signal line from the magnetic leader 581 is sent to the judgment section 557. It is connected.
  • the judging section 557 is connected to the liquid feeding apparatus control section 558.
  • the liquid sending device 554 is driven by a liquid sending device control section 558.
  • the reagent holder 55 3 is configured to be rotated by a reagent holder rotation drive mechanism 55 5.
  • FIG. 1 is a block diagram showing a configuration of an embodiment of a liquid sample analyzer according to the present invention.
  • the application example shown in the figure consists of a reagent ejection system, sample ejection system, reaction observation system, multi-wavelength photometer, input / output and arithmetic control system.
  • the reagent ejection system consists of a plurality (12 in the figure) of reagent containers 611 each containing a different reagent, and 12 systems connected to the bottom of each of the 12 reagent containers 6 1 1 A thin tube 6 1 2, and 12 reagent feeding units units 6 1 3, each of which is a reagent injecting means having a suction side connected to one of the 12 thin tubes 6 1 2, It comprises 12 reagent ejection pipes 6 14 connected to the ejection sides of two liquid sending devices 6 13.
  • the liquid supply unit 613 has a liquid supply unit 615 inside, and the reagent container 611 and the reagent discharge pit 613 are different from each other. Connected at Eve 6 16.
  • the sample ejection system consists of a sample container 6 21, a sample suction tube 6 2 2 with one end open and inserted into the sample container 6 2 1, and a sample injection with the suction side connected to the sample suction tube 6 2 2
  • the sample container 6 21, the sample aspirating tubing 6 2 2, the sample discharge pump 6 2 3, and the sample discharge pipet 6 24 are set on the moving mechanism 6 25 and the reactions are arranged in a line. Inject predetermined amount of sample into container 6 3 1 sequentially Has functions.
  • the number of specimen ejection systems is one, but a plurality of specimen ejection systems may be provided.
  • the reaction observation system is composed of the same number of reagent vessels 6 1 1 (1 2 in this example) as reaction vessels 6 3 1 arranged in a row, and a temperature holding mechanism 6 serving also as a support for the reaction vessels 6 3 1. 3 and a stirring mechanism 635 which is a stirring means also serving as a support for the temperature holding mechanism 632.
  • the wall of the reaction vessel 631 is made of a transparent material that allows measurement light to pass through.
  • the multi-wavelength photometer which is a reaction detecting means, includes a light source 641, which emits measurement light toward the reaction vessel 631, a lens 642 disposed on the optical axis of the measurement light, and the reaction vessel A concave diffraction grating 643 disposed at a position opposite to the lens 642 with the 631 interposed therebetween; and a concave diffraction grating 643 disposed at a position where measurement light reflected by the concave diffraction grating 643 is incident. And a photo diode array 644 for photoelectrically converting the measurement light. These are provided to a photometer moving mechanism (not shown) that reciprocates in parallel along the reaction vessel row so that the measurement light can be irradiated to all of the reaction vessels 631 arranged in a line. It is installed.
  • the input / output and arithmetic control system is a sequence controller for controlling the operation of the moving mechanism 6 25, the liquid feeding device 6 13 for injecting the reagent, the sample discharge pump 6 23, the multi-wavelength photometer and the photometer moving mechanism.
  • Controller 655 a signal processing unit 656 connected to the photo diode array 644, and a signal storage unit 6557 connected to the signal processing unit 6556.
  • An operation unit 658 as operation means connected to the signal storage unit 657; and a control unit connected to the operation unit 658 and the sequence controller 655 to control them.
  • one capillary tube, one pump, and one reagent discharge pipe are connected in series to one reagent container, which is different from the conventional device. Since different reagents do not flow in the same tube, there is no need for washing and no possibility of contamination. In addition, by reducing the size of the flow path system including the pump, the distance between the reagent container and the reaction container can be reduced, reducing the amount of reagent remaining in the tube, and wasting expensive reagents. It can be eliminated.
  • the analyzer shown in the figure is a micro TAS for testing specific items, and consists of a sample supply unit, reagent supply unit, reaction unit, and detection unit.
  • the sample supply section consists of a sample supply port 711 and a sample liquid sending device 712, and the sample injected from the sample supply port 711 reacts by a predetermined amount by the sample liquid sending device 712. Supply to room 7 3 1.
  • the reagent supply section is composed of a reagent chamber 7 2 1 and a reagent sending device 7 2 2, and the reagent stored in the reagent chamber 7 2 1 is supplied to the reaction chamber 7 2 2 by a predetermined amount in the reagent sending device 7 2 2. Feed 1 In this embodiment, two reagent supply units are provided to supply two types of reagents.
  • the reaction section includes a reaction chamber 731 and a stirring mechanism 732, and the sample and the reagent supplied to the reaction chamber 731 are mixed by the stirring mechanism 732. The reaction process between the sample and the reagent is monitored by the detection sensor 741 in the detection section. Each mechanism is connected by a flow path 7 13.
  • the present invention relates to a microphone port pump for accurately quantifying and sending a small amount of liquid, and in particular, to a structure of a liquid sending device configured to prevent generation of bubbles that affect the amount of liquid sent,
  • the liquid feeding device is applied to an analyzer.

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Abstract

A liquid feeding device capable of feeding liquid at a rate of several νL to several hundred νL per second using a micro diaphragm pump of several ten mm square, wherein an inlet valve which is small in resistance when liquid comes into it and large when liquid goes out of it is formed integrally with an outlet valve which is small in resistance when liquid goes out of it to the atmosphere and large when liquid comes into it so as to easily remove air bubbles inside a liquid feeding chamber, and the shape of the liquid feeding chamber is formed so that the area of the chamber is increased from a liquid inlet side to a liquid outlet side, a parallel part is provided in the chamber between the inlet and outlet sides, and its area is reduced from the parallel part to the outlet side.

Description

明 細 書  Specification

送液装置およびそれを用いた分析装置 技術分野 Technical Field of the Invention

本発明は、 ダイアフラム型のマイ クロポンプに係り、 特に、 毎秒数〃 The present invention relates to a diaphragm-type micropump, and more particularly, to a micropump of several seconds per second.

Lから数百// Lの送液を行う送液装置及びそれを用いた分析装置に関す る ものである。 背景技術 The present invention relates to a liquid sending device that sends liquid from L to several hundreds / L and an analyzer using the same. Background art

毎秒数// Lから数百 Lの送液を行う従来の送液装置と してはシリ ン ジポンプがある。 しかし、 送液量に対して装置の大き さが大き く コス ト もかかる。 そのため、 送液量に見合った装置の小型化と低コス ト化が望 まれており、 マイ ク ロマシニング技術を利用したマイ ク ロダイアフラム ポンプの開発が進んでいる。 マイ ク ロダイアフラムポンプとは、 数十ミ リ角以下の大き さのダイ アフラムポンプで、 送液室の容積を送液室の一 部を形成している ダイ ア フ ラムを変形させて、 容積を大き くすることで 入口から液体を送液室内に導入し、 容積を小さ く するこ とで出口から液 体を吐出する構成と したものである。 最も一般的なマイ クロダイアフ ラ ムポンプは、 単結晶シ リ コ ンをアルカ リ水溶液を用いて加工し (異方性 エツチング技術) 、 単結晶シリ コンとパイ レッ クスガラスとを接合 (陽 極接合技術) するこ とで組み立てて製作される。  There is a syringe pump as a conventional liquid feeding device that sends several to hundreds of liters per second. However, the size of the apparatus is large and the cost is high for the amount of liquid to be sent. Therefore, there is a demand for miniaturization and cost reduction of the device corresponding to the amount of liquid to be sent, and micro-diaphragm pumps using micro-machining technology are being developed. A micro-diaphragm pump is a diaphragm pump with a size of several tens of millimeters or less, and the volume of the liquid transfer chamber is changed by deforming the diaphragm that forms part of the liquid transfer chamber. By increasing the size, the liquid is introduced into the liquid feed chamber from the inlet, and by reducing the volume, the liquid is discharged from the outlet. The most common microdiaphragm pump processes single-crystal silicon using an aqueous alkali solution (anisotropic etching technology), and joins single-crystal silicon and pyrex glass (positive bonding technology). They are assembled and manufactured.

前述の技術によ り製作された、 数十ミ リ角以下のサイズのダイアフ ラ ムポンプでは、 送液室内に残留した気泡が送液効率低下の原因となる。 これは、 ダイ ァフ ラムが変形して送液室内の容積が変化しても、 その際 に送液室内圧力も変化するためその圧力変化によ り残留気泡の体積が変 ィ匕して、 ダイァフラムの変形による送液室内の容積変化を緩和してしま レ 、 送液量が減少する。 In a diaphragm pump manufactured by the above-mentioned technology and having a size of several tens of millimeters or less, bubbles remaining in the liquid transfer chamber cause a decrease in liquid transfer efficiency. This is because even if the diaphragm is deformed and the volume in the liquid sending chamber changes, the pressure in the liquid sending chamber also changes at that time, so that the volume of the residual bubbles changes due to the pressure change. This reduces the volume change in the liquid sending chamber due to the deformation of the diaphragm, and reduces the amount of liquid sent.

この問題を解決する方法は色々 と工夫されており、 代表的特許と して 特開平 4 - 5 0 2 7 9 6号公報及び特開平 5 — 3 0 6 6 8 3号公報に開 示がある。 前者のダイアフ ラムポンプは入口弁室、 送液室、 出口弁室、 の 3 つの部屋からな り、 プラ イ ミ ング時に送液室内へ液体が入つてい く 入口の位置を送液室中央よ り周辺部にずらすこ とで送液室内の入口のあ る反対側に気泡を集め、 その部分に出口となるオリ フィ スを設けてそこ から気泡を抜き取る という もので、 これによ り送液室内の気泡を効率的 に除去する。 後者のダィ ァフラムポンプはポンプ中に水可溶性塩または 多価アルコール類の一種類以上を含む水溶液を一旦注入し、 乾燥させる こ とによって、 ボンプの液体と接する面に水可溶性塩または多価アルコ ―ル類を付着させて、 液体との親和性を向上することによ り プライ ミ ン グ時の気泡の残留を無く している。  Various methods have been devised to solve this problem, and representative patents are disclosed in Japanese Patent Application Laid-Open Nos. Hei 4-520276 and Hei 5-306683. . The former diaphragm pump consists of three chambers: an inlet valve chamber, a liquid feed chamber, and an outlet valve chamber.The position of the inlet from which the liquid enters the liquid feed chamber during priming is located at the center of the liquid feed chamber. By shifting to the periphery, air bubbles are collected on the opposite side of the inlet of the liquid transfer chamber, and an orifice is provided in that part to extract the air bubbles from there. Bubbles are efficiently removed. In the latter diaphragm pump, an aqueous solution containing at least one kind of water-soluble salt or polyhydric alcohol is once injected into the pump and dried, whereby the water-soluble salt or polyhydric alcohol is applied to the surface of the pump in contact with the liquid. Adhesives are attached to improve the affinity for liquid, eliminating bubbles remaining during priming.

しかしながら、 上記の従来技術によっても初期の液体導入において気 泡の残留が生じる可能性がある。 この原因は、 入口弁から送液室を経て 出口弁まで液体が達するまでの流路の形状による もので、 特に弁構造近 傍に気泡が残留する。  However, even with the prior art described above, bubbles may remain in the initial liquid introduction. This is due to the shape of the flow path from the inlet valve to the liquid through the liquid feed chamber to the outlet valve, and particularly air bubbles remain near the valve structure.

従って、 本発明は、 ダイアフラムポンプにおいて、 残留気泡の発生を 抑制し、 高精度の送液を実現した装置を提供するこ とにある。  Therefore, an object of the present invention is to provide a diaphragm pump that suppresses the generation of residual air bubbles and realizes highly accurate liquid sending.

発明の開示 Disclosure of the invention

上記の問題を解決するために、 入口弁付近における段差を小さ く し、 また、 入口を流路平面形状の外周部に配置して外周部側が最も大き く 開 く よ う にし、 また、 送液室内における流路断面積を徐々に減少させ、 ま た、出口を入口よ り も位置エネルギ的に高い位置に配置するこ とによ り、 入口から出口へと気泡の流れをスムーズにし、 送液の際に圧力変動が問 題となる送液室内に気泡が残らないよ う にする。 図面の簡単な説明 In order to solve the above problem, the step near the inlet valve is reduced, and the inlet is arranged at the outer periphery of the flow path plane shape so that the outer periphery side is opened to the greatest extent. By gradually reducing the cross-sectional area of the flow path in the room and arranging the outlet at a position higher in potential energy than the inlet, Smooth the flow of air bubbles from the inlet to the outlet, and prevent air bubbles from remaining in the liquid transfer chamber where pressure fluctuations are a problem during liquid transfer. BRIEF DESCRIPTION OF THE FIGURES

第 1 図は、 本発明第一の実施例の概略図であり、 第 2図は、 本発明第 一の実施例における送液室高さ と気泡の残留の関係を示した図であり 、 第 3 図は、 本発明第二の実施例の概略図であ り、 第 4図は、 本発明第三 の実施例の概略図であり、 第 5図は、 本発明の送液装置の分析装置への 第一の適用例であ り、 第 6図は、 本発明の第一の適用例の詳細説明図で あ り 、 第 7図は、 本発明の送液装置の分析装置への第二の適用例であり、 第 8図は、 本発明の送液装置の分析装置への第三の適用例である。 発明を実施するための最良の形態  FIG. 1 is a schematic diagram of the first embodiment of the present invention, and FIG. 2 is a diagram showing the relationship between the liquid sending chamber height and the remaining bubbles in the first embodiment of the present invention. 3 is a schematic diagram of the second embodiment of the present invention, FIG. 4 is a schematic diagram of the third embodiment of the present invention, and FIG. 5 is an analyzer of the liquid sending device of the present invention. FIG. 6 is a detailed explanatory view of the first application example of the present invention, and FIG. 7 is a second application example of the liquid supply apparatus of the present invention to the analysis apparatus. FIG. 8 shows a third application example of the liquid sending device of the present invention to an analyzer. BEST MODE FOR CARRYING OUT THE INVENTION

図 1 に本発明第一の実施例の送液装置の概略図を示す。 同図において ( a ) は送液装置の断面図であり 、 ( b ) は送液室の平面図である。 送液装置は、 ダイアフ ラム基板 1 1 0、 送液室基板 1 2 0、 出入口基 板 1 3 0の 3枚の基板から構成されている。 これらの基板の素材はシリ コン、 ガラス、 セラ ミ ッ ク、 金属又は樹脂である。  FIG. 1 is a schematic diagram of a liquid feeding device according to a first embodiment of the present invention. In this figure, (a) is a cross-sectional view of the liquid sending device, and (b) is a plan view of the liquid sending chamber. The liquid transfer device is composed of three substrates: a diaphragm substrate 110, a liquid transfer chamber substrate 120, and an inlet / outlet substrate 130. The material of these substrates is silicon, glass, ceramic, metal or resin.

ダイ ア フラム基板 1 1 0 にはダイ アフ ラム 1 1 1 力?、 送液室基板 1 2 0 には送液室 1 2 1 と入口弁 1 2 2 と出口ポー ト 1 2 3カ^ 出入口弁基 板 1 3 0 には出口弁 1 3 2 と入口ポー ト 1 3 3 と吸入口 1 3 4 と吐出口 1 3 5が各々加工されている。 加工方法はフ ォ ト リ ソグラフィ 、 サン ド ブラス ト 、 射出成形、 ホーニング、 放電加工、 電铸等である。  Is the diaphragm 1 1 1 force on the diaphragm substrate 110? The liquid supply chamber substrate 120 has a liquid supply chamber 121, an inlet valve 122, and an outlet port 123.The outlet valve substrate 130 has an outlet valve 132, and an inlet port 1 3 3, suction port 1 3 4 and discharge port 1 3 5 are machined. Machining methods include photolithography, sand blasting, injection molding, honing, electric discharge machining, and electric power.

これらの基板とァクチユエータである圧電ディ スク 1 1 2 を、 各々固 着するこ と によ り送液装置を組み立てる。 固着方法は、 直接接合、 陽極 接合、 拡散接合、 共晶接合、 ろう付、 表面活性化接合、 接着の内の少な く と も 1 つを用いる。 The substrate and the piezoelectric disk 112 serving as an actuator are fixed to each other to assemble a liquid sending device. The fixing method is direct bonding, anodic bonding, diffusion bonding, eutectic bonding, brazing, surface activated bonding, Use at least one.

各部の寸法は以下の通りである。 ダイ アフラム基板の厚さは 5 0 0 μ m、 送液室基板の厚さは 5 0 0 ," m、 出入口基板の厚さは 5 0 0  The dimensions of each part are as follows. The thickness of the diaphragm substrate is 500 μm, the thickness of the liquid transfer chamber substrate is 500, "m, and the thickness of the inlet / outlet substrate is 500 μm.

送液室 1 2 1 の底面からダイアフラム面までの高さ 1 2 9 (以下、 送液 室高さ と称す) は 5 0 0 / m、 入口ポー ト 1 3 3からダイ アフラム面ま での高さ 1 2 8 (以下、 入口上高さ と称す) は 6 0 0 /i m、 送液室 1 2 1 の平面図における幅 3 2 1 は 8 mm、 長さ 3 2 2 は 9 mmである。 ま た、 平面図における外形寸法は 1 4 m m X 1 4 m mである。 図に示すよ う に送液室の形状を、 入口側の弁部から徐々に拡大し、 その途中に平行 部を有し、平行部から出口側に向かって徐々に縮小するよ う に形成した。 The height from the bottom of the liquid transfer chamber 1 2 1 to the diaphragm surface 1 2 9 (hereinafter referred to as the liquid transfer chamber height) is 500 / m, and the height from the inlet port 1 33 to the diaphragm surface. The height 1 28 (hereinafter referred to as the height above the inlet) is 600 / im, the width 3 2 1 in the plan view of the liquid transfer chamber 1 2 1 is 8 mm, and the length 3 2 2 is 9 mm. The external dimensions in the plan view are 14 mm x 14 mm. As shown in the figure, the shape of the liquid transfer chamber was gradually expanded from the valve part on the inlet side, with a parallel part in the middle, and formed so as to gradually reduce from the parallel part toward the outlet side. .

ここで、 入口弁 1 2 2 は、 梁 1 2 4 によって支持された片持ち梁構造 である。 梁 1 2 4 は、 送液室 1 2 1 の内側に向けて設けられ、 入口弁 1 2 2 は、 送液室 1 2 1 の一辺に近接して配置してある。 さ らに、 入口弁 1 2 2が近接している側の辺に対向する辺側に出口ポ一 ト 1 2 3 を近接 して配置している。 出口弁 1 3 2 は、 図示していない 2つの梁に支持さ られた、 両持ち梁構造と している。  Here, the inlet valve 122 has a cantilever structure supported by beams 124. The beam 124 is provided toward the inside of the liquid sending chamber 121, and the inlet valve 122 is arranged close to one side of the liquid sending chamber 121. Further, an outlet port 123 is arranged close to the side opposite to the side on which the inlet valve 122 is close. The outlet valve 13 2 has a doubly supported structure supported by two beams (not shown).

この送液装置のプライ ミ ング手順は以下の通りである。  The priming procedure of this liquid feeding device is as follows.

まず、 送液装置の送液室 1 2 1 内の気体を液体に置き換えるため、 送 液装置の吸入口 1 3 4 に、 導入する液体を送り込む液体導入装置を接続 する。 この液体導入装置は、 シリ ンジポンプ、 チューブポンプ、 ギアポ ンプなど農地 1 つを用いる。 液体導入装置によ り吸入口 1 3 4 から液体 が加圧送液される と、 入口ポー ト 1 3 3 を通って入口弁 1 2 2 に加圧さ れた液体が到達し、 その加圧力によ り入口弁 1 2 2が開いて液体が送液 室 1 2 1 内に流れ込む。 この時、 梁 1 2 4で支持されている入口弁 1 2 2 は、 梁 1 2 4の根本を支点に開口するため、 図 1 ( b ) の矢印のよ う に入口弁 1 2 2 を通過した液体は、 近接した辺側から送液室 1 2 1 を満 たして出口ポー ト 1 2 3 に達する。 First, in order to replace the gas in the liquid sending chamber 122 of the liquid sending device with the liquid, a liquid introducing device for sending the liquid to be introduced is connected to the suction port 134 of the liquid sending device. This liquid introduction device uses one agricultural land such as a syringe pump, a tube pump, and a gear pump. When the liquid is fed under pressure from the suction port 1 3 4 by the liquid introduction device, the pressurized liquid reaches the inlet valve 1 2 2 through the inlet port 1 3 3, and the pressure increases. Then, the inlet valve 1 2 2 is opened and the liquid flows into the liquid supply chamber 1 2 1. At this time, the inlet valve 1 2 2 supported by the beam 1 2 4 passes through the inlet valve 1 2 2 as indicated by the arrow in Fig. 1 (b) because it opens at the root of the beam 1 2 4 at the fulcrum. The filled liquid fills the liquid transfer chamber 1 2 1 from the adjacent side. Then reach exit port 1 2 3.

送液室内が液体で満たされたら、 吸入口 1 3 4 に吐出液体の入った容 器を接続し、 送液準備が完了する。  When the liquid transfer chamber is filled with liquid, connect the container containing the discharged liquid to the suction port 1 3 4 to complete preparation for liquid transfer.

なお、 送液室 1 2 1 内を気体から液体に置き換える方法と して、 吐出 口 1 3 5 に吸引ポンプを接続し、 吸入口 1 3 4 に吐出液体 (液体) の入 つた容器を接続しても前記と同様に行える。 すなわち、 吸引ポンプによ り吐出口 1 3 5から送液装置内の気体が吸い取られる と、 出口弁 1 2 3 の背圧が送液室 1 2 1 内圧力よ り低く なつて出口弁 1 3 2が開き、 送液 室 1 2 1 内の気体が吸い出される。 これによ り、 送液室 1 2 1 内の圧力 が入口ポー ト 1 3 3 の圧力よ り も低く な り、 入口弁 1 2 2が開く 。 さ ら に、 吸引ポンプで吸引続けることによ り 、 気体と同様に液体も入口弁 1 2 2 を開いて、 入口よ り液体が送液室 1 2 1 に流れ込み出口ポー ト 1 2 3 に達する。 送液室内が液体で満たされたら吐出口 1 3 5 に接続した吸 引ポンプを分離し、 送液準備が完了する。  In addition, as a method of replacing the inside of the liquid transfer chamber 1 2 1 with gas to liquid, connect a suction pump to the discharge port 1 3 5 and connect a container containing the discharge liquid (liquid) to the suction port 1 3 4. This can be performed in the same manner as described above. In other words, when the gas in the liquid sending device is sucked from the discharge port 135 by the suction pump, the back pressure of the outlet valve 123 becomes lower than the pressure inside the liquid sending chamber 121 and the outlet valve 133 2 opens, and the gas in the liquid transfer chamber 1 2 1 is sucked out. As a result, the pressure in the liquid sending chamber 12 1 becomes lower than the pressure in the inlet port 13 3, and the inlet valve 122 opens. Further, by continuing suction with the suction pump, the liquid as well as the gas opens the inlet valve 122, and the liquid flows from the inlet into the liquid supply chamber 122 and reaches the outlet port 123. . When the liquid transfer chamber is filled with liquid, the suction pump connected to the discharge port 1 35 is separated, and the preparation for liquid transfer is completed.

ボンビング動作は、 圧電ディ スク 1 1 2 に電圧を加えて平面方向に伸 び縮みさせるこ と によ り行う。 まず、 圧電ディ スク 1 1 2 を平面方向に 縮ませてダイ アフ ラム 1 1 1 を太鼓状に送液室側に押し込むと、 送液室 1 2 1 の容積が減少する。 その減少した容積分の液体が、 出口弁 1 3 2 を押し開けて出口ポー ト 1 2 3から送液室 1 2 1 の外へと流れ出し、 吐 出口 1 3 5 よ り吐出される。  The bombing operation is performed by applying a voltage to the piezoelectric disks 1 1 and 2 to expand and contract in the plane direction. First, when the piezoelectric disk 112 is contracted in the plane direction and the diaphragm 111 is pushed into the liquid supply chamber side like a drum, the volume of the liquid supply chamber 121 decreases. The reduced volume of the liquid is pushed out of the outlet valve 13 2, flows out of the outlet port 12 3 to the outside of the liquid sending chamber 12 1, and is discharged from the discharge outlet 13 5.

次に、 印可電圧を変化させて圧電ディ ス クを平面方向に伸ばすと、 ダ ィ ァフラム 1 1 1 は圧電ディ ス ク側へ戻り、 送液室 1 2 1 の容積が大き く なる。 そして、 増加した容積分だけの液体が入口弁 1 2 2 を押し開け て入口ポー ト 1 3 3から送液室 1 2 1 内に流入する。 この動作を繰り返 すこ とで送液が行われる。  Next, when the applied voltage is changed and the piezoelectric disk is extended in the plane direction, the diaphragm 111 returns to the piezoelectric disk side, and the volume of the liquid sending chamber 122 becomes large. Then, the liquid corresponding to the increased volume pushes open the inlet valve 122 and flows into the liquid sending chamber 122 from the inlet port 133. The liquid is fed by repeating this operation.

本実施例の特徴は 2つある。 第一の特徴は、 送液室高さ 1 2 9 を 5 0 0 μ , 入口上高さ 1 2 8 を 6 0 0 mと して、 プライ ミ ング時の気泡 残留を防止している点である。 入口弁における気泡残留の有無は送液室 での濡れ性に依存している。送液室での濡れ性は液体の表面張力 T 8 (N /m) と密度 p ( k g /m 3 ) 、 液体と送液室の接液部の接触角 (° ) - そして送液室高さ 1 2 9 d (m) に依存し、 2枚の板の間隔が dの時に 液体ののぼる高さ hは g (m/ s 2 ) : 重力定数とする と This embodiment has two features. The first feature is that the liquid transfer chamber height is 1 2 9 to 5 0 The point is that the height above the inlet is set to 600 μm, and the residual air bubbles during priming are prevented. The presence or absence of bubbles in the inlet valve depends on the wettability in the liquid transfer chamber. The wettability in the liquid transfer chamber depends on the surface tension T 8 (N / m) and density p (kg / m 3 ) of the liquid, the contact angle (°) between the liquid and the liquid contact part of the liquid transfer chamber, and the height of the liquid transfer chamber. Depends on 1 2 9 d (m), the height h at which the liquid rises when the distance between the two plates is d is g (m / s 2 ):

h = ( 2 T c 0 s ^ ) Z ( p g d ) h = (2 T c 0 s ^) Z (p g d)

となる。 本実施例の場合には、 液体は水であ り送液室 1 2 1 の接液部は A uであるため、 T = 7 2 m N Zm、 io = 1 0 0 0 k g /m 3 , θ = 2 0 とな り、 送液室高さ d と液体の昇る高さ hの関係は、 図 2 のよ う に なる。 図 2 は、 本実施例の場合でのプライ ミ ング時にぬれ性が支配的に なる力、、 または、 慣性が支配的になるかのしきい値が h 二 0 . 0 2 m m であるこ と を示してお り、 そのと きの送液室高さ 1 2 9 dは 1 0 0 m であるこ と を示している。 Becomes In the case of this embodiment, since the liquid Mizudea Ri delivering chamber 1 2 1 wetted parts are A u, T = 7 2 m N Zm, i o = 1 0 0 0 kg / m 3 , θ = 2 0 and Do Ri, the relationship of the fluid delivering chamber height d and the height h of rising of the liquid will jar good of Figure 2. Fig. 2 shows that the threshold value of the force that makes wettability dominant during priming or the threshold value that makes inertia dominant in the case of this embodiment is h20.02 mm. In this case, the height of the liquid supply chamber at that time, ie, the height of 129 d, is 100 m.

すなわち、 送液室高さ 1 2 9力? 1 0 0 m以上であれば、 プライ ミ ン グにおいて慣性が支配的である。 この場合には、 入口弁 1 2 2上の空間 が液体に満たされてから、 送液室 1 2 1 内に液体が流入するため、 気泡 は残留しない。 一方、 送液室高さ 1 2 9が 1 0 0 m未満であれば、 プ ライ ミ ング時において液体のぬれ性が支配的である。 この場合には、 入 口弁 1 2 2上の空間が液体に満たされる前に、 送液室 1 2 1 内に流入す るため、 気泡は入口弁 1 2 2上の空間に残留する。 このしきい値 hは一 定であり、 液体の物性 (表面張力、 密度) や液体と送液室の接液部の接 触角が変わった場合、 その時の送液室高さが変化する。 例えば、 図 2 の 場合に比べて、 液体と送液室内面とのぬれ性が良い場合には、 送液室高 さはよ り大き く 設定する必要がある。 反対にぬれ性が悪い場合には、 送 液室高さを小さ く設定するこ とができる。 また、 重力方向を基準と した水平面に対して出口ポー ト 1 2 3 を入口 弁 1 2 2 よ り も高い位置エネルギになるよ う に設置するこ とによ り、 送 液室 1 2 1 の流路に進入した液体は、 それ自体の密度によ り重力方向に 引力を受ける。 この引力は表面張力に対しての反力成分を有するため、 送液室内での表面張力の影響を小さ く するこ とが出来る。 そして、 入口 弁 1 2 2 と出口ポー ト 1 3 2 を通る線を重力方向に平行にした場合に、 引力の反力成分が最大となる。 また、 送液室 1 2 1 内に混入した気泡は、 それ自身の浮力によ り入口弁 1 2 2から出口ポー ト 1 2 3へと移動する ため、 気泡の除まが容易となる。 なお、 本実施例は液体に働く引力の表 面張力に対しての反力成分を最大とするために、 重力方向を基準と した 水平面に対して、 入口と出口を結ぶ線を垂直にした場合である力'、 出口 が入口よ り も位置エネルギ的に高い位置に設置されていれば、 同様な効 果は得られる。 That is, liquid chamber height 1 2 9 force? Above 100 m, inertia dominates in priming. In this case, after the space above the inlet valve 122 is filled with the liquid, the liquid flows into the liquid supply chamber 122, so that no bubbles remain. On the other hand, if the height of the liquid transfer chamber is less than 100 m, wettability of the liquid is dominant during priming. In this case, before the space above the inlet valve 122 is filled with the liquid, the gas flows into the liquid feed chamber 122 so that the air bubbles remain in the space above the inlet valve 122. This threshold value h is constant, and when the physical properties (surface tension and density) of the liquid and the contact angle between the liquid and the liquid contact part of the liquid supply chamber change, the liquid supply chamber height at that time changes. For example, if the wettability between the liquid and the inner surface of the liquid transfer chamber is better than in the case of Fig. 2, the liquid transfer chamber height needs to be set higher. Conversely, when wettability is poor, the height of the liquid transfer chamber can be set small. In addition, by installing the outlet port 123 with a higher potential energy than the inlet valve 122 with respect to the horizontal plane based on the direction of gravity, The liquid that has entered the channel receives an attractive force in the direction of gravity due to its own density. Since this attractive force has a reaction force component with respect to the surface tension, the influence of the surface tension in the liquid supply chamber can be reduced. When the line passing through the inlet valve 122 and the outlet port 132 is made parallel to the direction of gravity, the reaction force component of the attractive force becomes maximum. In addition, the air bubbles mixed into the liquid sending chamber 122 move from the inlet valve 122 to the outlet port 123 by its own buoyancy, so that the air bubbles can be easily removed. In this example, in order to maximize the reaction force component of the attractive force acting on the liquid with respect to the surface tension, the line connecting the inlet and the outlet was perpendicular to the horizontal plane with respect to the direction of gravity. The same effect can be obtained if the outlet is installed at a position higher in potential energy than the inlet.

第二の特徴は、 入口弁 1 2 2 を梁 1 2 4 に支持された片持ち梁構造と し、 梁 1 2 4 を送液室 1 2 1 の内側に向けて配置し、 入口弁の開口側が 送液室 1 2 1 の一辺に近接するよ う に配置した。 さ らに、 入口弁 1 2 2 が近接している辺に対向する辺側に、 出口ポー ト 1 2 3 を近接して配置 している点である。 これによ り、 入口開口時には、 入口弁 1 2 2 は、 送 液室 1 2 1 の辺側が最も大き く 開いて液体が流れ込む。 プライ ミ ング時 及びボンビング時に流れ込んだ液体は、 図 1 ( b ) の矢印で示すよ う に、 大きな曲率の流線 1 2 6でスムーズな流れとな り、気泡の残留を防止し、 混入した気泡の除去を容易にする。  The second feature is that the inlet valve 1 2 2 has a cantilever structure supported by the beam 1 2 4, and the beam 1 2 4 is arranged toward the inside of the liquid transfer chamber 1 2 1, and the opening of the inlet valve It was arranged so that the side was close to one side of the liquid transfer chamber 1 2 1. Another point is that the outlet port 123 is arranged close to the side opposite to the side where the inlet valve 122 is close. As a result, at the time of opening the inlet, the inlet valve 122 opens the side of the liquid supply chamber 121 most widest so that the liquid flows. The liquid that has flowed during priming and bombing becomes a smooth flow with a large curvature streamline 126 as shown by the arrow in Fig. 1 (b), preventing bubbles from remaining and Easily remove air bubbles.

なお、 本実施例は、 送液室高さ 1 2 9が入口上高さ 1 2 8 よ り も小さ い場合である力?、 しきい値 hが 0 . 0 2 m m以下であれば、 送液室高さ 1 2 9 は入口上高さ 1 2 8 と等しいく した方が気泡は残留しにく く なる ただし、 送液装置の弁構造を形成する上で制約を受けるため、 本実施例 のよ う な構造がよ り現実的である。 In this embodiment, the force in the case where the height of the liquid transfer chamber 1 29 is smaller than the height above the inlet 1 2 8 is smaller. If the threshold value h is not more than 0.02 mm, the liquid transfer chamber height 1 29 should be equal to the inlet upper height 1 28 so that bubbles are less likely to remain. In this embodiment, there are restrictions in forming the valve structure of the liquid device. Such a structure is more realistic.

図 3 に本発明第二の実施例の送液装置の概略図を示す。 同図において ( a ) は送液装置の断面図であ り、 ( b ) は送液室の平面図である。 な お、 図 1 と同一符号の箇所は第一の実施例と同一構成である。  FIG. 3 is a schematic diagram of a liquid feeding device according to a second embodiment of the present invention. In this figure, (a) is a cross-sectional view of the liquid sending device, and (b) is a plan view of the liquid sending chamber. The same reference numerals as in FIG. 1 indicate the same configuration as in the first embodiment.

送液装置は、 第一の実施例と同様なダイ アフラム基板 1 1 0、 出入口 基板 1 3 0 と送液室基板 2 2 0の 3枚の基板から構成されている。 第一 の実施例と異なる点は送液室基板 2 2 0の送液室 2 2 1 に突起 2 2 5 を 形成している点である。 この突起 2 2 5 は、 周囲の 2つの流路が流路断 面積が断続的に減少する形状(図のよ う に送液室の形状に合わせて略 6 角形の形状) に配置されている。 また、 送液室高さ 2 2 9 は 5 0 0 μ m で、 突起 2 2 5の上面と ダイアフラム面までの流路の高さ 2 2 7 (以下、 突起上高さ と称す) は 1 0 0 /z mである。  The liquid transfer device is composed of three substrates, the same as in the first embodiment, a diaphragm substrate 110, an entrance / exit substrate 130, and a liquid transfer chamber substrate 220. The difference from the first embodiment is that the projections 225 are formed in the liquid transfer chamber 221 of the liquid transfer chamber substrate 220. The projections 2 25 are arranged in such a shape that the two surrounding flow paths are intermittently reduced in flow path area (a substantially hexagonal shape according to the shape of the liquid transfer chamber as shown in the figure). . The liquid transfer chamber height 2 29 is 500 μm, and the height 2 27 (hereinafter referred to as the height above the protrusion) between the upper surface of the protrusion 222 and the diaphragm surface is 100 μm. 0 / zm.

この送液装置のプライ ミ ング手順は、 以下の通りである。 まず、 送液 装置の送液室 1 2 1 内の気体を液体に置き換えるため、 送液装置の吸入 口 1 3 4 に導入する液体を送り込む液体導入装置を接続する。 この液体 導入装置と しては、 シリ ンジポンプ、 チューブポンプ、 ギアポンプの内 1 つを用いれば良い。 液体導入装置によ り吸入口 1 3 4から液体が加圧 送液される と、 入口ポー ト 1 3 3 を通って入口弁 1 2 2 に加圧された液 体が到達し、 その加圧力によ り入口弁 1 2 2が開いて液体が送液室 1 2 1 に流れ込む。 この際、 梁 1 2 4 で支持されている入口弁 1 2 2 は梁 1 2 4 の根本を支点に開口するため、 入口弁 1 2 2 を通過した液体は近接 した辺側から送液室 1 2 1 を満たし、 入口弁側の突起 2 2 5部分に達す る。 そして、 突起 2 2 5の上の流路は液体の毛細管現象によ り液体が満 たされる。 ここで、 突起上の流路は端部が開放されているため気泡の残 留は生じない。  The priming procedure of this liquid sending device is as follows. First, in order to replace the gas in the liquid sending chamber 1 2 1 of the liquid sending device with the liquid, a liquid introducing device for sending the liquid to be introduced into the suction port 1 34 of the liquid sending device is connected. As this liquid introduction device, one of a syringe pump, a tube pump, and a gear pump may be used. When the liquid is fed under pressure from the suction port 1 3 4 by the liquid introduction device, the pressurized liquid reaches the inlet valve 1 2 2 through the inlet port 1 3 3, and the pressurized pressure is applied. As a result, the inlet valve 1 2 2 is opened, and the liquid flows into the liquid supply chamber 1 2 1. At this time, the inlet valve 122 supported by the beam 124 opens at the fulcrum at the root of the beam 124, so that the liquid passing through the inlet valve 122 flows from the adjacent side to the liquid transfer chamber 1 2 1 is satisfied and reaches the projection 2 25 on the inlet valve side. Then, the flow path above the projections 225 is filled with the liquid by the capillary action of the liquid. Here, since the end of the flow path on the projection is open, no bubbles remain.

また、 突起によ り区分された、 突起両側の 2つの流路は、 入口弁側は 連続的に流路断面積が減少する増速流れの流路となっているので、 徐々 に流路抵抗が大き く なる。 従って、 液体が突起周辺の一方の流路を先行 して進行した場合には、 他方の流路ょ り も流路抵抗が大き く なるため、 先行している流路での液体の進行速度が低下する。 そして、 流路抵抗差 が小さ く なる と再び進行速度が上昇し、 2つの流路から同時に出口ポー ト 1 2 3 に達する。 In addition, the two flow paths on both sides of the projection, separated by the projection, Since the flow path is a speed-up flow in which the cross-sectional area of the flow path is continuously reduced, the flow path resistance gradually increases. Therefore, when the liquid advances in one of the flow paths around the protrusion in advance, the flow resistance of the other flow path becomes larger, so that the speed of the liquid in the preceding flow path decreases. descend. Then, when the flow path resistance difference becomes small, the traveling speed increases again, and reaches the outlet port 123 simultaneously from the two flow paths.

送液室内が液体で満たされたら吸入口 1 3 4 に吐出液体の入った容器 を接続し、 送液準備が完了する。 なお、 第一の実施例と同様に吸引ボン プを用いてプライ ミ ング動作を行っても良い。 また、 ボンビング動作は 第一の実施例と同様である。  When the liquid transfer chamber is filled with liquid, connect the container containing the discharged liquid to the suction port 1 3 4 to complete the preparation for liquid transfer. The priming operation may be performed using a suction pump as in the first embodiment. The bombing operation is the same as in the first embodiment.

本実施例の特徴は 2点ある。  This embodiment has two features.

第一の特徴は、 送液室高さ 2 2 9が 5 0 0 mの送液室内に突起 2 2 5 を設けて突起上高さ 2 2 7 を 1 0 0 mとするこ とによ り、 突起上の 流路は毛細管力で液体を流れ込ませ、 送液室 1 2 1 の中央部での気泡の 残留を防止している点である。 従って、 第一の実施例よ り も濡れ性の良 い液体に対して、 気泡残留防止効果がある。 なお、 突起状の空間にいち 早く 液体を流すためには、 突起 2 2 5 を入口弁 1 2 2 に寄せておく こ と が最も効果的である。  The first feature is that a protrusion 2225 is provided in the liquid transfer chamber with a liquid transfer chamber height of 229 m and a height of 220 m above the protrusion is set to 100 m. On the other hand, the flow path on the protrusion allows the liquid to flow by capillary force, thereby preventing bubbles from remaining in the center of the liquid transfer chamber 121. Therefore, a liquid having better wettability than in the first embodiment has an effect of preventing bubbles from remaining. In order to quickly flow the liquid into the projection-shaped space, it is most effective to move the projections 2 25 to the inlet valve 122.

第二は突起周辺の 2つの流路が増速流れの流路になっている点である , これによ り 、 一方の流路だけを液体が進行した場合、 流路抵抗が大き く な り液体の進行速度が低下し、他方の流路を液体の進行速度が増加する。 したがって、 2つの流路を液体がバラ ンス良く進行するため、 送液室内 での気泡の残留を防止するこ とができる。  The second is that the two flow paths around the protrusion are flow paths for the accelerated flow. With this, when the liquid proceeds in only one flow path, the flow path resistance increases. The traveling speed of the liquid decreases, and the traveling speed of the liquid in the other flow path increases. Therefore, the liquid proceeds in the two flow paths in a well-balanced manner, so that bubbles can be prevented from remaining in the liquid transfer chamber.

次に、 気泡の初生防止についての実施例を記載する。 気泡の初生は静 圧力低下による ものが原因である。 この静圧力は大気圧から送液室内容 積の膨張による送液室内の静圧力の低下分と液体の流速による静圧力の 低下分を引いた値となる。 液体の吸入時に流速の最も速く なる箇所は、 流路断面積の最も小さい箇所であるから、 すなわち、 入口弁と入口ポー トの間が最も静圧力が低く な り気泡の初生が起こ り易い。 そこで、 入口 弁、 または、 入口ポー トの形状を最適化するこ とによ り入口弁と入口ポ ー トの間での流速を低下させる方法を以下に示す。 Next, an example of preventing the initiation of bubbles will be described. Bubbles are caused by static pressure drop. This static pressure is reduced from the atmospheric pressure by the amount of decrease in the static pressure in the liquid sending chamber due to expansion of the volume of the liquid sending chamber and the static pressure This is a value obtained by subtracting the decrease. Since the location where the flow velocity becomes the highest when the liquid is sucked is the location where the cross-sectional area of the flow path is the smallest, that is, the static pressure becomes the lowest between the inlet valve and the inlet port, and the initiation of bubbles easily occurs. Therefore, a method for reducing the flow velocity between the inlet valve and the inlet port by optimizing the shape of the inlet valve or the inlet port is described below.

図 4 に本発明第三の実施例の送液装置入口弁の概略図を示す。 同図に おいて ( a ) 、 ( b ) は各々の送液装置の断面図である。 なお、 図 1 と 同一符号の箇所は第一の実施例と同一構成である。  FIG. 4 is a schematic diagram of a liquid feeding device inlet valve according to a third embodiment of the present invention. In the figure, (a) and (b) are cross-sectional views of each liquid feeding device. The same reference numerals as in FIG. 1 have the same configuration as in the first embodiment.

図 4 ( a ) の送液装置は、 第一の実施例と同様なダイア フ ラム基板 1 1 0 、 送液室基板 1 2 0 と出入口基板 4 3 0の 3枚の基板から構成され ている。 第一の実施例と異なる点は出入口基板 4 3 0の入口ポー ト 4 3 3 の口径が送液室基板 1 2 0の出口ポー トの口径よ り も大きいことであ これによ り、 ボンビング時における入口弁 1 2 2 と出口弁 1 3 2 のリ フ ト量が等しい場合、 入口弁 1 2 2 と入口ポー ト 4 3 3の間の流路断面 積は出口弁 1 3 2 と出口ポー ト 1 2 3 の間の流路断面積よ り も大き く な り、 したがって、 入口弁 1 2 2 と入口ポー ト 4 3 3の間を通る液体の流 速は出口弁 1 3 2 と出口ポー ト 1 2 3 の間を通る液体の流速よ り も小さ く な り、 気泡の初生が起こ り に く く なる。  The liquid feeder shown in FIG. 4 (a) is composed of three substrates, the same as in the first embodiment, a diaphragm substrate 110, a liquid feed chamber substrate 120, and an entrance / exit substrate 4330. . The difference from the first embodiment is that the diameter of the inlet port 43 3 of the inlet / outlet substrate 43 is larger than the diameter of the outlet port of the liquid transfer chamber substrate 120. When the lift amount of the inlet valve 122 and the outlet valve 132 is equal, the cross-sectional area between the inlet valve 122 and the inlet port 43 is equal to the outlet valve 132 and the outlet port. Is larger than the cross-sectional area of the flow path between ports 123 and, therefore, the flow rate of liquid between inlet valve 122 and inlet port 43 is equal to the flow rate of the outlet valve 132 and outlet port. The flow rate of the liquid passing between the points 123 is smaller than that of the liquid, so that the initiation of bubbles is less likely to occur.

また、 図 4 ( b ) の送液装置は、 第一の実施例と同様なダイ アフラ ム 基板 1 1 0、 出入口基板 1 3 0 と送液室基板 4 2 0の 3枚の基板から構 成されている。 第一の実施例と異なる点は送液室基板 4 2 0の入口弁 4 2 2 に窪み 4 2 6 を形成しているこ とである。  Further, the liquid transfer apparatus shown in FIG. 4 (b) is composed of three substrates, the same as in the first embodiment, a diaphragm substrate 110, an inlet / outlet substrate 130 and a liquid transfer chamber substrate 420. Have been. The difference from the first embodiment is that a depression 4 2 6 is formed in the inlet valve 4 2 2 of the liquid transfer chamber substrate 4.

これによ り、 ボンビング時における入口弁 4 2 2 と出口弁 1 3 2のリ フ ト量が等しい場合、 入口弁 4 2 2 と人口ポー ト 1 3 3の間の流路断面 積は出口弁 1 3 2 と出口ポー ト 1 2 3 の間の流路断面積よ り も大き く な り、 したがって、 入口弁 4 2 2 と入口ポー ト 1 3 3 の間を通る液体の流 速は出口弁 1 3 2 と出口ポー ト 1 2 3の間を通る液体の流速よ り も小さ く な り、 気泡の初生が起こ り にく く なる。 As a result, when the lift amounts of the inlet valve 422 and the outlet valve 132 during bombing are equal, the cross-sectional area of the flow path between the inlet valve 422 and the artificial port 133 is determined by the outlet valve. No larger than the cross-sectional area of the flow path between 1 32 and outlet port 123 Therefore, the flow velocity of the liquid between the inlet valve 4 2 2 and the inlet port 13 3 is less than the flow velocity of the liquid between the outlet valve 1 3 2 and the outlet port 1 2 3 This makes it less likely that bubbles will begin to form.

なお、 第一の実施例において、 入口弁の梁の剛性を低くすることによ り ボンピング時における入口弁 1 2 2のリ フ ト量が出口弁 1 3 2 よ り も 大き く し、 入口弁 1 2 2 と入口ポー ト 1 3 3 の間の流路断面積は出口弁 1 3 2 と出口ポー ト 1 2 3 の間の流路断面積よ り も大き く なる。従って、 入口弁 1 2 2 と入口ポー ト 1 3 3 の間を通る液体の流速は出口弁 1 3 2 と出口ポー ト 1 2 3 の間を通る液体の流速よ り も小さ く な り、 気泡の初 生が起こ り にく く なる。  In the first embodiment, by lowering the rigidity of the beam of the inlet valve, the lift amount of the inlet valve 122 during the pumping is made larger than that of the outlet valve 132, and the inlet valve The cross-sectional area of the passage between 122 and the inlet port 133 is larger than the cross-sectional area of the passage between the outlet valve 132 and the outlet port 123. Therefore, the flow velocity of the liquid passing between the inlet valve 122 and the inlet port 133 is smaller than the flow velocity of the liquid passing between the outlet valve 132 and the outlet port 123, and the air bubbles are generated. It is difficult for the first time to occur.

また、 本実施例において、 ポンビング時における入口弁のリ フ ト量が 出口弁よ り も大き くすることによ り、 入口弁と入口ポー トの間を通る液 体の流速はさ らに小さ く なる。 このよ う に、 入口弁と入口ポー トの間で の流速を低下させることによ り、 気泡の初生を防止している。  Also, in this embodiment, the flow rate of the liquid passing between the inlet valve and the inlet port is further reduced by making the lift amount of the inlet valve larger than the outlet valve at the time of pumping. It becomes bad. Thus, by reducing the flow velocity between the inlet valve and the inlet port, the initiation of bubbles is prevented.

本発明の送液装置を分析装置に実装する際の第一の適用例を図 5及び 図 6 を用いて説明する。 図 5 は本発明の試薬供給機構を備えた分析装置 の全体構成図、 図 6 は本発明の試薬供給機構の詳細説明図である。 なお、 図 5 ( a ) は正面から見た装置 5 1 1 を、 図 5 ( b ) は上面から見た装 置 5 1 2 を示している。  A first application example in mounting the liquid transfer device of the present invention on an analyzer will be described with reference to FIGS. FIG. 5 is an overall configuration diagram of an analyzer provided with the reagent supply mechanism of the present invention, and FIG. 6 is a detailed explanatory diagram of the reagent supply mechanism of the present invention. FIG. 5A shows the device 511 viewed from the front, and FIG. 5B shows the device 511 viewed from the top.

装置上面には試料 5 2 0の入った試験管 5 2 1 と、 試験管 5 2 1 を円 周上に保持するサンプルホルダ一 5 2 2が設けられている。 またサンプ ルホルダー 5 2 2 の脇には試験管 5 2 1 内の試料 5 2 0 を吸引するため のサンプルピぺッ 夕 5 3 1 が設けられている。 サンプルピぺッ タ 5 3 1 は、 試料を吸引して内部に保持するノズル 5 3 2 と、 ノ ズル 5 3 2 に上 昇 · 回転の動作を与える 3次元駆動機構 5 3 3 と、 図には示していない がノ ズル内に試料を吸引した り、 ノ ズル内の試料を吐出した りするため のポンプとが設けられている。 サンプルホルダ一中の試験管 5 2 1 を丁 度サンプルピぺッ 夕のノ ズルの直下に位置せしめるために、 サンプルホ ルダー 5 2 2 は回転駆動機構 5 2 3 にて回転駆動するよ う になっている c サンプルピぺッ タ 5 3 1 のノ ズルのも う一方の降下位置には、 反応容器 5 4 1 が順次回転しながら移動するよ う になつている。 On the upper surface of the apparatus, there are provided a test tube 521, which contains a sample 52, and a sample holder 52, which holds the test tube 521, on the circumference. A sample pipe 531 for sucking the sample 52 in the test tube 52 1 is provided beside the sample holder 52 2. The sample pitcher 531, which sucks the sample and holds it inside, a three-dimensional drive mechanism 5333, which gives the nozzle 532 an up-and-down rotation, is shown in the figure. Not shown to aspirate sample into nozzle or eject sample from nozzle Pump is provided. In order to position the test tube 522 in the sample holder just below the sample nozzle, the sample holder 522 is driven to rotate by the rotary drive mechanism 523. At the other descent position of the nozzle of the sample c 531, the reaction vessel 541 moves while rotating sequentially.

複数の反応容器 5 4 1 は、 反応ディ スク 5 4 2の円周上に保持されて いる。 また反応容器 5 4 2 の下半分は恒温水が流れる恒温槽 5 4 3 にな つている。 サンプルピぺッ タのノズルの降下位置に順次反応容器を移動 させるために、 反応ディ スク 5 4 2 は反応ディ スク回転駆動機構 5 4 4 で支持されている。 反応ディ スク 5 4 2 の円周上には前述したサンプル ピぺッ タの他、 反時計回り に第 1 の試薬供給部 5 5 1 と、 第 2の試薬供 給部 5 6 1 と、 反応容器洗浄機構 5 7 1 と、 分光計測部 5 8 1 とが設け られている。  The plurality of reaction vessels 541 are held on the circumference of the reaction disk 542. The lower half of the reaction vessel 542 is connected to a constant temperature bath 543 through which constant temperature water flows. The reaction disk 542 is supported by a reaction disk rotation drive mechanism 544 in order to sequentially move the reaction container to the lower position of the nozzle of the sample pitcher. On the circumference of the reaction disk 54 2, in addition to the sample pitcher described above, the first reagent supply section 5 51 and the second reagent supply section 5 61 1 A container cleaning mechanism 571 and a spectrometer 581 are provided.

試薬供給部 5 5 1 は、大き く試薬容器 5 5 2 と試薬ホルダ— 5 5 3 と、 送液装置 5 5 4 と、 試薬ホルダ一回転駆動機構 5 5 5 の 4 つの部分から 構成されている。 試薬ホルダ一 5 5 3 は中心軸 5 5 6の周り に試薬容器 The reagent supply section 55 1 is largely composed of four parts: a reagent container 55 2, a reagent holder 55 3, a liquid feeder 55 4 4, and a reagent holder 1 rotation drive mechanism 55 5 5. . Reagent holder 553 is a reagent container around central axis 556

5 5 2 を円周上に保持させる構造になっている。 保持される試薬容器の 数と同数の送液装置 5 5 4が試薬ホルダ一 5 5 3の底部に設けられてい る。 試薬容器 5 5 2 の底面には接続孔 5 5 9があり、 試薬ホルダ一 5 5 3 の底部に向かって強く押しつけるこ とで、 送液装置 5 5 4 の吸入孔 55 5 2 is held on the circumference. The same number of liquid feeders 554 as the number of reagent containers held are provided at the bottom of the reagent holder 553. There is a connection hole 559 on the bottom of the reagent container 552, and by strongly pressing it toward the bottom of the reagent holder 5553, the suction hole 5

6 2 と接続するよ う になっている。 また送液装置 5 5 4 には吐出口 5 6 3が鉛直下方に向かって設けられている。 Connects to 6 2. In addition, a discharge port 563 is provided in the liquid sending device 554 vertically downward.

試薬容器 5 5 2の側面には試薬の種類を記載したデータが書き込まれ た磁気部 5 8 2が設けられている。 また試薬ホルダー 5 5 3 の対応する 円周位置には磁気部 5 8 2のデータ を読み込むための磁気リーダ 5 8 1 が設けられている。 磁気リ ーダ 5 8 1 からの信号線は、 判断部 5 5 7 に 接続されている。 さ らに判断部 5 5 7 は送液装置制御部 5 5 8 と接続さ れている。 送液装置 5 5 4 は送液装置制御部 5 5 8 にて駆動される。 試 薬ホルダー 5 5 3 は、 試薬ホルダー回転駆動機構 5 5 5 にて回転移動さ れる構成となっている。 On the side surface of the reagent container 552, there is provided a magnetic unit 528 on which data describing the type of reagent is written. A magnetic reader 581 for reading data of the magnetic section 582 is provided at a circumferential position corresponding to the reagent holder 553. The signal line from the magnetic leader 581 is sent to the judgment section 557. It is connected. Further, the judging section 557 is connected to the liquid feeding apparatus control section 558. The liquid sending device 554 is driven by a liquid sending device control section 558. The reagent holder 55 3 is configured to be rotated by a reagent holder rotation drive mechanism 55 5.

送液装置を試薬容器単位に装備するこ とによ り、 試薬吐出部の洗浄が 不要とな り 、 測定時間が短縮される。  By equipping the reagent sending unit for each reagent container, the washing of the reagent discharge section is not required, and the measurement time is shortened.

本発明の送液装置を分析装置に実装する際の第二の適用例を図 7 を用 いて説明する。 同図は本発明による液体試料の分析装置の一実施例の構 成を示すブロ ッ ク図である。 同図に示す適用例は、 試薬吐出系、 検体吐 出系、 反応観察系、 多波長光度計、 入出力および演算制御系からなる。 試薬吐出系は、 それぞれ異なる試薬を入れた複数 (図では 1 2個) の試 薬容器 6 1 1 と、 この 1 2個の試薬容器 6 1 1 それぞれの底部に接続さ れた 1 2系統の細管 6 1 2 と、 それぞれこの 1 2系統の細管 6 1 2のど れかに吸入側を接続した試薬注入手段である 1 2基の試薬注入用の送液 装置ュニッ ト 6 1 3 と、 これら 1 2基の送液装置 6 1 3の吐出側に接続 された 1 2個の試薬吐出ピぺッ ト 6 1 4 と を含んでなっている。 送液装 置ュニッ ト 6 1 3 は内部に送液装置 6 1 5そ装備しており、 試薬容器 6 1 1 及び試薬吐出ピぺッ ト 6 1 3 とはノ、。イ ブ 6 1 6で接続している。 検体吐出系は、 検体容器 6 2 1 と、 一端が開放されて検体容器 6 2 1 に挿入された検体吸引用細管 6 2 2 と、 検体吸引用細管 6 2 2 に吸入側 を接続した検体注入手段である検体吐出ポンプ 6 2 3 と、 一端が検体吐 出ポンプ 6 2 3の吐出側に接続され他端が開放された検体吐出ピぺッ ト 6 2 4 と、 これらを同時に移動させる移動機構 6 2 5 と、 を含んで構成 されている。 検体容器 6 2 1 、 検体吸引用細管 6 2 2 と、 検体吐出ポン プ 6 2 3、 及び検体吐出ピペッ ト 6 2 4 は、 移動機構 6 2 5の上に設置 され、 一列に並べられた反応容器 6 3 1 に順次、 検体を所定量注入する 機能を持つ。 本実施例では検体吐出系は、 一組であるが、 複数組設けて も差し支えない。 A second application example in mounting the liquid transfer device of the present invention on an analyzer will be described with reference to FIG. FIG. 1 is a block diagram showing a configuration of an embodiment of a liquid sample analyzer according to the present invention. The application example shown in the figure consists of a reagent ejection system, sample ejection system, reaction observation system, multi-wavelength photometer, input / output and arithmetic control system. The reagent ejection system consists of a plurality (12 in the figure) of reagent containers 611 each containing a different reagent, and 12 systems connected to the bottom of each of the 12 reagent containers 6 1 1 A thin tube 6 1 2, and 12 reagent feeding units units 6 1 3, each of which is a reagent injecting means having a suction side connected to one of the 12 thin tubes 6 1 2, It comprises 12 reagent ejection pipes 6 14 connected to the ejection sides of two liquid sending devices 6 13. The liquid supply unit 613 has a liquid supply unit 615 inside, and the reagent container 611 and the reagent discharge pit 613 are different from each other. Connected at Eve 6 16. The sample ejection system consists of a sample container 6 21, a sample suction tube 6 2 2 with one end open and inserted into the sample container 6 2 1, and a sample injection with the suction side connected to the sample suction tube 6 2 2 A sample discharge pump 62 3 as a means, a sample discharge pipe 62 4 having one end connected to the discharge side of the sample discharge pump 62 3 and having the other end opened, and a moving mechanism for simultaneously moving these. 6 2 5 and. The sample container 6 21, the sample aspirating tubing 6 2 2, the sample discharge pump 6 2 3, and the sample discharge pipet 6 24 are set on the moving mechanism 6 25 and the reactions are arranged in a line. Inject predetermined amount of sample into container 6 3 1 sequentially Has functions. In this embodiment, the number of specimen ejection systems is one, but a plurality of specimen ejection systems may be provided.

反応観察系は、 試薬容器 6 1 1 と同数 (本実施例では 1 2個) の 1列 に配列された反応容器 6 3 1 と、 反応容器 6 3 1 の支持台を兼ねた温度 保持機構 6 3 2 と、 温度保持機構 6 3 2 の支持台を兼ねた撹拌手段であ る撹拌機構 6 3 5 を含んで構成されている。 反応容器 6 3 1 の壁面は測 定光を通す透明な材料からなっている。 反応検出手段である多波長光度 計は、 反応容器 6 3 1 に向けて測定光を出射する光源 6 4 1 と、 該測定 光の光軸上に配置されたレンズ 6 4 2 と、 前記反応容器 6 3 1 を挟んで 前記レンズ 6 4 2 に対向する位置に配置された凹面回折格子 6 4 3 と、 該凹面回折格子 6 4 3で反射された測定光が入射する位置に配置され入 射した測定光を光電変換するフ ォ ト ダイ オー ドア レイ 6 4 4 とを含んで 構成される。 これらは、 一列に並べられた反応容器 6 3 1 のすべてに対 して測定光を照射できる よ う に、 反応容器列に沿って平行に往復移動す る光度計移動機構 (図示せず) に搭載されている。  The reaction observation system is composed of the same number of reagent vessels 6 1 1 (1 2 in this example) as reaction vessels 6 3 1 arranged in a row, and a temperature holding mechanism 6 serving also as a support for the reaction vessels 6 3 1. 3 and a stirring mechanism 635 which is a stirring means also serving as a support for the temperature holding mechanism 632. The wall of the reaction vessel 631 is made of a transparent material that allows measurement light to pass through. The multi-wavelength photometer, which is a reaction detecting means, includes a light source 641, which emits measurement light toward the reaction vessel 631, a lens 642 disposed on the optical axis of the measurement light, and the reaction vessel A concave diffraction grating 643 disposed at a position opposite to the lens 642 with the 631 interposed therebetween; and a concave diffraction grating 643 disposed at a position where measurement light reflected by the concave diffraction grating 643 is incident. And a photo diode array 644 for photoelectrically converting the measurement light. These are provided to a photometer moving mechanism (not shown) that reciprocates in parallel along the reaction vessel row so that the measurement light can be irradiated to all of the reaction vessels 631 arranged in a line. It is installed.

入出力および演算制御系は、 前記移動機構 6 2 5、 試薬注入用の送液 装置 6 1 3 、 検体吐出ポンプ 6 2 3、 多波長光度計及び光度計移動機構 の動作を制御するシーケ ンス コ ン ト ロ一ラ 6 5 5 と、 フ ォ ト ダイオー ド ア レイ 6 4 4 に接続された信号処理部 6 5 6 と、 信号処理部 6 5 6 に接 続された信号記憶部 6 5 7 と、 信号記憶部 6 5 7 に接続された演算手段 である演算部 6 5 8 と、 該演算部 6 5 8及び前記シーケ ンス コ ン ト ロー ラ 6 5 5 に接続されてそれらを制御する制御部 6 5 1 と、 制御部 6 5 1 にそれぞれ接続された入力手段である操作パネル 6 5 2、 ディ スプレイ 6 5 3、 記憶手段である シーケ ンスチャー ト記憶部 6 5 4 、 プリ ン 夕 6 5 9、 レコーダ 6 6 0 と、 外部記憶媒体 6 6 1 と、 を含んで構成されて いる。 ここで強調されるべき ことは、 一つの試薬容器に、 一つの細管、 一つ のポンプ、 および一つの試薬吐出ピぺッ トが直列に連結されているこ と であり 、 従来の装置のよ う に同一の管内を異なる試薬が流れるこ とが無 いから、 洗浄の必要性、 コ ン タ ミ ネ一シ ョ ンの可能性が全く無い。 また、 ポンプを含めた流路系を小さ くするこ とによ り試薬容器と反応容器の間 隔を小さ く でき、 管内に滞留する試薬量を少な く な り、 高価な試薬の無 駄を排除するこ とができる。 The input / output and arithmetic control system is a sequence controller for controlling the operation of the moving mechanism 6 25, the liquid feeding device 6 13 for injecting the reagent, the sample discharge pump 6 23, the multi-wavelength photometer and the photometer moving mechanism. Controller 655, a signal processing unit 656 connected to the photo diode array 644, and a signal storage unit 6557 connected to the signal processing unit 6556. An operation unit 658 as operation means connected to the signal storage unit 657; and a control unit connected to the operation unit 658 and the sequence controller 655 to control them. The operation panel 652, the display 653, which is an input means connected to the control section 651, and the control section 651, respectively, the sequence chart storage section 654, which is storage means, and the printer 659 , A recorder 660, and an external storage medium 661. It should be emphasized here that one capillary tube, one pump, and one reagent discharge pipe are connected in series to one reagent container, which is different from the conventional device. Since different reagents do not flow in the same tube, there is no need for washing and no possibility of contamination. In addition, by reducing the size of the flow path system including the pump, the distance between the reagent container and the reaction container can be reduced, reducing the amount of reagent remaining in the tube, and wasting expensive reagents. It can be eliminated.

本発明の送液装置を分析装置に実装する際の第三の適用例を図 8 を用 いて説明する。 同図の分析装置は特定の項目の検査を行う ためにマイ ク 口 T A S化したもので、 試料供給部、 試薬供給部、 反応部、 検出部から 構成される。 試料供給部は試料供給口 7 1 1 、 試料用送液装置 7 1 2か ら成り、 試料供給口 7 1 1 から注入された試料を試料用送液装置 7 1 2 によ り所定量だけ反応室 7 3 1 に供給する。試薬供給部は試薬室 7 2 1 、 試薬用送液装置 7 2 2から成り、 試薬室 7 2 1 に保管されている試薬を 試薬用送液装置 7 2 2 にて所定量だけ反応室 7 3 1 に供給する。 なお、 本実施例では 2種類の試薬を供給するために、 試薬供給部を 2系統装備 している。 反応部は反応室 7 3 1 、 撹拌機構 7 3 2から成り、 反応室 7 3 1 に供給された試料及び試薬を撹拌機構 7 3 2 によ り混合する。 試料 と試薬の反応過程は検出部の検出センサ 7 4 1 によ りモニタ 一される。 各機構間は各々流路 7 1 3 によ り接続している。  A third application example of mounting the liquid sending device of the present invention on an analyzer will be described with reference to FIG. The analyzer shown in the figure is a micro TAS for testing specific items, and consists of a sample supply unit, reagent supply unit, reaction unit, and detection unit. The sample supply section consists of a sample supply port 711 and a sample liquid sending device 712, and the sample injected from the sample supply port 711 reacts by a predetermined amount by the sample liquid sending device 712. Supply to room 7 3 1. The reagent supply section is composed of a reagent chamber 7 2 1 and a reagent sending device 7 2 2, and the reagent stored in the reagent chamber 7 2 1 is supplied to the reaction chamber 7 2 2 by a predetermined amount in the reagent sending device 7 2 2. Feed 1 In this embodiment, two reagent supply units are provided to supply two types of reagents. The reaction section includes a reaction chamber 731 and a stirring mechanism 732, and the sample and the reagent supplied to the reaction chamber 731 are mixed by the stirring mechanism 732. The reaction process between the sample and the reagent is monitored by the detection sensor 741 in the detection section. Each mechanism is connected by a flow path 7 13.

このよ う に、 試料と試薬の供給、 反応、 検出に関する機能をマイ クロ T A S化することによ り 、 任意の場所での分析が可能となる。  In this way, by making the functions relating to the supply, reaction, and detection of the sample and the reagent into micro TAS, analysis at an arbitrary place becomes possible.

産業上の利用可能性 Industrial applicability

本発明は、 微量の液を正確に定量して送液するためのマイ ク口ポンプ に関し、 特に送液量に影響を及ぼす気泡の発生を防止する構成と した送 液装置の構成と し、 本送液装置を分析装置に適用したものである。  The present invention relates to a microphone port pump for accurately quantifying and sending a small amount of liquid, and in particular, to a structure of a liquid sending device configured to prevent generation of bubbles that affect the amount of liquid sent, The liquid feeding device is applied to an analyzer.

Claims

請 求 の 範 囲 The scope of the claims 1 . ダイアフラムを有する 1枚の枚基板と、 弁座または弁ポ一 トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口弁と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口弁と力 送液室内に一体形成され、 前記 送液室を構成する少な く と も一つの面が変形可能なダイァフ ラムで構成 した送液装置において、  1. An inlet consisting of a single substrate with a diaphragm and two substrates with different valve seats or valve ports, with low resistance when liquid enters from outside and high resistance when exiting liquid A valve and an outlet valve having a low resistance when the liquid flows out to the outside and a high resistance when the liquid enters the power supply, and is integrally formed in the liquid supply chamber, and at least one surface constituting the liquid supply chamber is deformed. In a liquid feeder composed of possible diaphragms, 液体の表面張力 T ( N / m ) と密度 p ( k g / m 3 ) 、 液体と送液室 の接液部の接触角 ( ° ) 、 重力定数 g ( m Z s 2 ) の場合、 送液室の ダイアフラム面下の高さ d ( m ) 力 0 . 0 2 p g / ( 2 T c o s ^ ) よ り も大きいこ とを特徴とする送液装置。 Liquid surface tension T (N / m) and the density p (kg / m 3), the contact angle of the liquid contact portion of the liquid and delivering chamber (°), when the gravitational constant g (m Z s 2), feeding A liquid transfer device characterized in that the height d (m) of the chamber below the diaphragm surface is greater than 0.02 pg / (2T cos ^). 2 . ダイ アフラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口弁と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口弁と力 5'、 送液室内に一体形成され、 送液 室を構成する少な く と も一つの面が変形可能な前記ダイ アフ ラムであ り . 前記ダイ アフ ラムを送液室の容積が増加する方向に変形させるこ とで送 液室に入口弁よ り液体を導入し、 送液室の容積が減少する方向に変形さ せるこ とで送液室から出口弁を介して液体を吐出する送液装置において. 前記入口弁が流路の平面形状の外周部にあ り、 前記入口弁が開いて外 界から送液室内に液体が入る と きに、 前記入口弁の外周部に近接する側 が最も大き く 開く こ と を特徴とする送液装置。 2. An inlet consisting of one substrate with a diaphragm and two substrates with different valve seats or valve ports, with low resistance when liquid enters from outside and high resistance when exiting liquid A valve and an outlet valve with low resistance when liquid enters the outside and high resistance when entering the liquid 5 ', at least one surface that is integrally formed in the liquid supply chamber and constitutes the liquid supply chamber Is a deformable diaphragm. The diaphragm is deformed in a direction to increase the volume of the liquid sending chamber, so that liquid is introduced from the inlet valve into the liquid sending chamber, and the volume of the liquid sending chamber is changed. In a liquid feeder that discharges liquid from a liquid feed chamber via an outlet valve by deforming in a direction in which the pressure decreases, the inlet valve is located at the outer peripheral portion of the flow path in a planar shape, and the inlet valve is opened. Close to the outer periphery of the inlet valve when liquid enters the liquid transfer chamber from outside There feeding apparatus according to claim that you open most size rather. 3 . ダイ アフラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口弁と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口弁と力 、 送液室内に一体形成され、 送液 室を構成する少な く と も一つの面が変形可能なダイ アフラムであり、 そ のダイアフラムを送液室の容積が増加する方向に変形させることで送液 室に入口よ り液体を導入し、 送液室の容積が減少する方向に変形させる こ とで送液室から出口を介して液体を吐出する送液装置において、 送液室内に凸部を有し、 プライ ミ ング時に凸部上の流路を毛細管現象 によ り気体から液体に置換するこ と を特徴とする送液装置。 3. A single substrate with a diaphragm and two substrates with different valve seats or valve ports, with low resistance when liquid enters from outside and high resistance when exiting liquid A valve and an outlet valve with low resistance when liquid enters the outside and low resistance when entering the liquid. At least one surface of the chamber is a deformable diaphragm, and the diaphragm is deformed in a direction to increase the volume of the liquid transfer chamber, thereby introducing liquid from the inlet to the liquid transfer chamber. A liquid transfer device that discharges a liquid from a liquid transfer chamber through an outlet by deforming the liquid transfer chamber in a direction in which the volume of the liquid transfer chamber decreases has a protrusion in the liquid transfer chamber, and the protrusion on the protrusion during priming. A liquid transfer device characterized in that a flow path is replaced from a gas to a liquid by capillary action. 4 . ダイアフ ラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口弁と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口弁と力 送液室内に一体形成され、 送液 室を構成する少な く と も一つの面が変形可能なダイアフラムであり、 そ のダイ アフ ラムを送液室の容積が増加する方向に変形させるこ とで送液 室に入口よ り液体を導入し、 送液室の容積が減少する方向に変形させる こ とで送液室から出口を介して液体を吐出する送液装置において、 前記送液室内に突部を有し、 突部周辺の流路断面積が連続的、 或いは、 断続的に減少するこ と を特徴とする送液装置。  4. An inlet consisting of one substrate with a diaphragm and two substrates with different valve seats or valve ports, with low resistance when liquid enters from outside and high resistance when exiting liquid A valve and an outlet valve with low resistance when the liquid flows out to the outside and high resistance when entering the liquid.Integrally formed in the liquid supply chamber, at least one surface of the liquid supply chamber can be deformed. The diaphragm is deformed in the direction in which the volume of the liquid transfer chamber increases, so that liquid is introduced from the inlet into the liquid transfer chamber and deformed in the direction in which the volume of the liquid transfer chamber decreases. Thus, in the liquid-feeding device that discharges the liquid from the liquid-feeding chamber via the outlet, the liquid-feeding chamber has a protrusion, and the flow path cross-sectional area around the protrusion decreases continuously or intermittently. A liquid feeding device characterized by this. 5 . ダイ アフラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口弁と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口弁と力?、 送液室内に一体形成され、 送液 室を構成する少な く と も一つの面が変形可能なダイァフ ラムであり、 そ のダイ アフ ラムを送液室の容積が増加する方向に変形させるこ とで送液 室に入口よ り液体を導入し、 送液室の容積が減少する方向に変形させる こ とで送液室から出口を介して液体を吐出する送液装置において、 出口を入口よ り も位置エネルギー的に高い位置に設置すること を特徴 とする送液装置。 5. One board with a diaphragm and two boards with different valve seats or valve ports, with low resistance when liquid enters from outside and high resistance when exiting liquid A valve and an outlet valve with low resistance when liquid enters the outside and low resistance when entering? The diaphragm is integrally formed in the liquid transfer chamber, and at least one surface of the liquid transfer chamber is a deformable diaphragm. The diaphragm can be deformed in a direction to increase the volume of the liquid transfer chamber. In this case, the liquid is introduced from the inlet into the liquid transfer chamber through the inlet, and is deformed in a direction in which the volume of the liquid transfer chamber is reduced, thereby discharging the liquid from the liquid transfer chamber through the outlet. A liquid feeder, which is installed at a higher position in terms of potential energy. 6 . ダイアフ ラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口と力 送液室内に一体形成され、 送液室を 構成する少な く と も一つの面が変形可能なダイアフラムであり、 そのダ ィァフラムを送液室の容積が増加する方向に変形させるこ とで送液室に 入口よ り液体を導入し、 送液室の容積が減少する方向に変形させるこ と で送液室から出口を介して液体を吐出する送液装置において、 6. An inlet consisting of one substrate with a diaphragm and two substrates with different valve seats or valve ports, with low resistance when liquid enters from outside and high resistance when exiting liquid When the liquid flows out to the outside, the resistance is low and when it enters the liquid, the outlet has a high resistance and the force is integrally formed in the liquid transfer chamber, and at least one surface of the liquid transfer chamber is deformable. By deforming the diaphragm in the direction in which the volume of the liquid sending chamber increases, liquid is introduced from the inlet into the liquid sending chamber, and the liquid is sent in the direction in which the volume of the liquid sending chamber decreases. In a liquid feeding device that discharges a liquid from a liquid chamber through an outlet, 入口ポ一 トの口径が出口ポー トの口径よ り も大きいこと を特徴とする 送液装置。  A liquid transfer device, wherein the diameter of the inlet port is larger than the diameter of the outlet port. 7 . ダイアフラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口とカ^ 送液室内に一体形成され、 送液室を 構成する少な く と も一つの面が変形可能なダイアフラムであり、 そのダ ィ ァフ ラムを送液室の容積が増加する方向に変形させるこ とで送液室に 入口よ り液体を導入し、 送液室の容積が減少する方向に変形させるこ と で送液室から出口を介して液体を吐出する送液装置において、  7. One substrate with a diaphragm and two substrates with different shapes of valve seats or valve ports. An inlet with a low resistance when liquid enters from outside and a high resistance when out of liquid. When the liquid flows out to the outside, the resistance is low. When the liquid enters, an outlet with high resistance is formed integrally with the outlet chamber, and at least one surface of the diaphragm that forms the chamber is deformable. By deforming the diaphragm in the direction in which the volume of the liquid sending chamber increases, liquid is introduced from the inlet into the liquid sending chamber and deformed in the direction in which the volume of the liquid sending chamber decreases. In a liquid feeder that discharges a liquid from a liquid feed chamber through an outlet at and, 入口弁のシール面に入口ポー トの口径よ り も大きな窪みを有するこ と を特徴とする送液装置。  A liquid transfer device, characterized in that the seal surface of the inlet valve has a recess larger than the diameter of the inlet port. 8 . ダイ アフ ラムを有する 1枚の枚基板と、 弁座または弁ポー トの形状 が異なる 2枚の基板から成り、 外界から液体が入る と きは抵抗が小さ く 出る と きは抵抗が大きい入口と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口と力 送液室内に一体形成され、  8. Consists of a single substrate with a diaphragm and two substrates with different valve seat or valve port shapes, with low resistance when liquid enters from outside and high resistance when exiting liquid The inlet and the outlet that have low resistance when the liquid flows out to the outside are formed integrally with the power transfer chamber, 送液室を構成する少な く と も一つの面が変形可能なダイアフ ラムであ り そのダイア フ ラムを送液室の容積が増加する方向に変形させるこ とで送 液室に入口よ り液体を導入し、 送液室の容積が減少する方向に変形させ るこ とで送液室から出口を介して液体を吐出する送液装置において、 入口弁の梁の剛性が出口弁の梁の剛性よ り も低いこと を特徴とする送 液装置。 At least one surface of the liquid transfer chamber is a deformable diaphragm, and the diaphragm is deformed in a direction to increase the volume of the liquid transfer chamber. In a liquid feeder that discharges liquid from the liquid transfer chamber through the outlet by introducing liquid into the liquid chamber from the inlet and deforming the liquid in a direction that reduces the volume of the liquid transfer chamber, the rigidity of the beam of the inlet valve The liquid supply device is characterized in that the pressure is lower than the rigidity of the beam of the outlet valve. 9 . 複数の反応容器と、 複数の試薬容器を備え、 前記試薬容器の各々に 送液装置を備え、 所定の位置でサンプルおよび試薬が供給される反応容 器を収納したホルダと、 前記サンプルの物性を計測する計測装置と を備 えた分析装置において、  9. A plurality of reaction vessels, a plurality of reagent vessels, a holder for accommodating a liquid supply device in each of the reagent vessels, and a reaction vessel for supplying a sample and a reagent at a predetermined position; An analyzer equipped with a measuring device for measuring physical properties and 前記送液装置が、 ダイ アフ ラムを有する 1枚の枚基板と、 弁座または 弁ポー トの形状が異なる 2枚の基板から成り、 外界から液体が入る と き は抵抗が小さ く 出る と きは抵抗が大きい入口弁と、 外界に液体が出る と きは抵抗が小さ く 入る と きは抵抗が大きい出口弁と力 、 送液室内に一体 形成され、 前記送液室の形状を液入口側から出口側に向かって面積が拡 大し、 かつ、 途中に平行部を有し、 平行部から出口側に向かって面積が 縮小するよ う に形成したこ と を特徴とする分析装置。  The liquid sending device is composed of one substrate having a diaphragm and two substrates having different shapes of a valve seat or a valve port. When a liquid enters from outside, the resistance is small and the liquid exits. Are formed integrally with the inlet valve having a large resistance and the outlet valve having a small resistance when the liquid enters the outside when the liquid flows out.The shape of the liquid supply chamber is changed to the liquid inlet side. An analyzer characterized by having an area that increases from the outlet to the outlet side, has a parallel part in the middle, and is formed so that the area decreases from the parallel part toward the outlet side. 1 0 . 請求項 9記載の分析装置において、  10. The analyzer according to claim 9, 複数の試薬と、 試薬を反応室に送液する送液装置と、 試薬と試料を混 合する手段と、試薬と試料の反応過程を検出する検出器とを一体形成し、 前記送液室にほぼ 6角形状の突起部をも う けたこ とを特徴とする分析 装置。  A plurality of reagents, a liquid feeding device for sending the reagents to the reaction chamber, a means for mixing the reagents and the sample, and a detector for detecting a reaction process between the reagents and the sample are integrally formed; An analyzer characterized by having a substantially hexagonal projection.
PCT/JP2000/001332 2000-03-06 2000-03-06 Liquid feeding device and analyzing device using the device Ceased WO2001066947A1 (en)

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JP2003166910A (en) * 2001-11-30 2003-06-13 Asahi Kasei Corp Liquid sending mechanism and analyzer provided with the liquid sending mechanism
JP2005001104A (en) * 2003-06-10 2005-01-06 Samsung Electronics Co Ltd Microactuator and fluid transfer device using the same
WO2005012729A1 (en) * 2003-08-04 2005-02-10 Nec Corporation Diaphragm pump and cooling system with the diaphragm pump
JP2010002229A (en) * 2008-06-18 2010-01-07 Nippon Telegr & Teleph Corp <Ntt> Flow cell
US8308453B2 (en) 2007-01-23 2012-11-13 Nec Corporation Diaphragm pump
US9914116B2 (en) 2015-09-10 2018-03-13 Panasonic Intellectual Property Management Co., Ltd. Microelement

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003166910A (en) * 2001-11-30 2003-06-13 Asahi Kasei Corp Liquid sending mechanism and analyzer provided with the liquid sending mechanism
JP2005001104A (en) * 2003-06-10 2005-01-06 Samsung Electronics Co Ltd Microactuator and fluid transfer device using the same
WO2005012729A1 (en) * 2003-08-04 2005-02-10 Nec Corporation Diaphragm pump and cooling system with the diaphragm pump
US8308453B2 (en) 2007-01-23 2012-11-13 Nec Corporation Diaphragm pump
JP2010002229A (en) * 2008-06-18 2010-01-07 Nippon Telegr & Teleph Corp <Ntt> Flow cell
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