WO2011027092A1 - Micro-fluidic structures - Google Patents

Micro-fluidic structures Download PDF

Info

Publication number
WO2011027092A1
WO2011027092A1 PCT/GB2009/051100 GB2009051100W WO2011027092A1 WO 2011027092 A1 WO2011027092 A1 WO 2011027092A1 GB 2009051100 W GB2009051100 W GB 2009051100W WO 2011027092 A1 WO2011027092 A1 WO 2011027092A1
Authority
WO
WIPO (PCT)
Prior art keywords
structure according
fluid
bridge
dispensing element
micro
Prior art date
Application number
PCT/GB2009/051100
Other languages
French (fr)
Inventor
Mark Hyland
Florent Crepineau
Peter Stephenson
Original Assignee
F. Hoffmann-La Roche Ag
Roche Diagnostics Gmbh
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 F. Hoffmann-La Roche Ag, Roche Diagnostics Gmbh filed Critical F. Hoffmann-La Roche Ag
Priority to PCT/GB2009/051100 priority Critical patent/WO2011027092A1/en
Publication of WO2011027092A1 publication Critical patent/WO2011027092A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L3/00Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
    • B01L3/50Containers for the purpose of retaining a material to be analysed, e.g. test tubes
    • B01L3/502Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures
    • B01L3/5027Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip
    • B01L3/502715Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip characterised by interfacing components, e.g. fluidic, electrical, optical or mechanical interfaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2200/00Solutions for specific problems relating to chemical or physical laboratory apparatus
    • B01L2200/02Adapting objects or devices to another
    • B01L2200/026Fluid interfacing between devices or objects, e.g. connectors, inlet details
    • B01L2200/027Fluid interfacing between devices or objects, e.g. connectors, inlet details for microfluidic devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2300/00Additional constructional details
    • B01L2300/06Auxiliary integrated devices, integrated components
    • B01L2300/0627Sensor or part of a sensor is integrated
    • B01L2300/0645Electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2300/00Additional constructional details
    • B01L2300/06Auxiliary integrated devices, integrated components
    • B01L2300/0681Filter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2300/00Additional constructional details
    • B01L2300/08Geometry, shape and general structure
    • B01L2300/0809Geometry, shape and general structure rectangular shaped
    • B01L2300/0825Test strips
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2300/00Additional constructional details
    • B01L2300/08Geometry, shape and general structure
    • B01L2300/0861Configuration of multiple channels and/or chambers in a single devices
    • B01L2300/0864Configuration of multiple channels and/or chambers in a single devices comprising only one inlet and multiple receiving wells, e.g. for separation, splitting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2300/00Additional constructional details
    • B01L2300/16Surface properties and coatings
    • B01L2300/161Control and use of surface tension forces, e.g. hydrophobic, hydrophilic
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2400/00Moving or stopping fluids
    • B01L2400/04Moving fluids with specific forces or mechanical means
    • B01L2400/0403Moving fluids with specific forces or mechanical means specific forces
    • B01L2400/0406Moving fluids with specific forces or mechanical means specific forces capillary forces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L2400/00Moving or stopping fluids
    • B01L2400/06Valves, specific forms thereof
    • B01L2400/0677Valves, specific forms thereof phase change valves; Meltable, freezing, dissolvable plugs; Destructible barriers

Definitions

  • the present invention relates to micro-fluidic structures.
  • Micro-fluidic structures are used in various applications and include micro-fluidic structures for use in devices for sampling and testing of fluids, particularly, but not exclusively biological fluids.
  • the invention has particular utility in micro-fluidic structures for devices used in medical diagnostic techniques, such as, for example, bio-sensor devices.
  • WO03/056319 discloses an electro-chemical micro-electrode bio-sensor device having an array of wells or other sites which is used for analysing fluids including biological fluids (for example blood) or non biological fluids.
  • the arrangement disclosed requires the fluid to be screened to be delivered to the one or more wells or other sites to be analysed and an electrical output produced.
  • the quantities of fluid delivered for screening are at the level of micro litre volumes.
  • a further example of a micro-electrode sensor for use in bio applications is disclosed in US2005/0072670.
  • the present invention provides a micro-fluidic structure comprising:
  • a bridge structure extending adjacent to the dispensing element and promoting fluid passage across the bridge structure from the dispensing element toward the destination zone, wherein the bridge structure is arranged to alter in extent during passage of the fluid.
  • the invention provides a microfluidic structure comprising: a dispensing element for dispensing fluid; a destination zone in communication with, and downstream of, the dispensing element; and, a bridge structure extending adjacent to the dispensing element and promoting fluid passage across the bridge structure from the dispensing element toward the destination zone; wherein during fluid passage a separation gap between the dispensing element and the bridge structure increases to a maximum (at which passage of the fluid across the gap is caused to cease).
  • the bridge structure locally bridges to the dispensing element and/or the fluid present on the facing surface of the dispensing element. This permits or accelerates passive flow of the fluid (for example plasma) into the downstream portions of the structure.
  • the dispensing element may comprise a red blood cell separation membrane and the invention enables plasma on the bottom of the membrane to flow off because there is bridging contact via the bridge structure.
  • the bridge When the bridge is locally created it propagates to substantially the entire adjacent surface area of the dispensing element, allowing free flow of fluid. In the absence of the bridge structure the fluid will coat the bottom surface of the dispensing element in its lowest energy configuration and flow may not be induced (other than by application of other force delivery means, such as for example applied pressure).
  • material of the bridge structure may be dissolvable in the fluid.
  • the bridge structure may shrink, collapse or otherwise alter in configuration.
  • the bridge structure includes a bridge surface, the bridge surface preferably being hydrophilic.
  • the bridge surface comprises a hydrophilic film or layer so that the solution will preferentially wet the bridge structure giving a lower interfacial energy between the solution and the bridge than between the solution and the underside of the dispensing element.
  • the bridge has an apex or zenith proximate the dispensing element.
  • the bridge has a convex bridge surface, and may for example have a part spherical surface such as a hemispherical surface. Curved, rather than stepped change edges and surfaces improves flow and are less hydrophobic.
  • a fluid flowpath extends downstream of the dispensing element.
  • the fluid flowpath comprises a capillary flowpath.
  • the fluid flowpath is a micro fluid flowpath having the capacity to transport micro litre volumes of fluid.
  • the capillary flowpath includes circular section channels, the diameter of the channels is preferably in the range 0.1mm to 5mm (more preferably in the range lOum to 500um).
  • channels having a rectilinear or other geometry section may be used, beneficially having a side dimension in the range 0.001 mm to 3 mm (more preferably in the range 0.05 mm to 1 mm).
  • the downstream flowpath may comprise a plurality of flowpaths such as a plurality of connected capillary flowpaths.
  • the connection may be dendritic.
  • the surface of the bridge structure may be contoured to promote flow along certain pre-defined paths. For example, this would promote flow to specific downstream flowpaths.
  • the contour of the bridge structure surface may comprise a sloped or valley path.
  • the dispensing element comprises a receiver element arranged to hold a volume of fluid.
  • the receiver element is fluid permeable.
  • the receiver element preferably acts to filter fluid.
  • the receiver element acts to filter a biological fluid, preferably filtering blood and permitting plasma to pass.
  • the dispensing element comprises a membrane.
  • the membrane is arranged such that a fluid sample is deposited on an obverse side of the membrane and dispensed via a reverse side.
  • the bridge structure may be configured to contact the dispensing element.
  • the bridge structure may be configured to be spaced from the dispensing element by a small gap substantially in the range 1 ⁇ to 30 ⁇ .
  • the required height of the bridge structure depends upon the fluid passing via the dispensing element, and consequently the surface tension of a hanging drop of the fluid. This in turn depends upon the viscosity of the fluid, the surface tension of the dispensing element (and pore size of the dispensing element).
  • the amount of time the fluid takes to pass through the dispensing element can be controlled by varying the spacing between the bridge and the dispensing element.
  • the destination zone comprises a destination station containing a reagent substance for reacting with the fluid delivered from the dispensing element.
  • the reagent substance may comprise, for example, an electro-active substance.
  • the destination zone may comprise a plurality of destination stations, respective stations containing a respective reagent substance for reacting with the fluid delivered from the dispensing structure.
  • separate destination stations contain different respective reagent substances.
  • the separate destinations may be served via separate delivery channels, as described above.
  • a respective destination zone may comprise a well.
  • a micro-fluidic capillary flowpath communicates with the respective well preferably via a connection at the bottom of the well.
  • the destination zone may comprise an array of wells, the structure preferably including a micro fluid capillary flowpath network leading to the array of wells.
  • the micro-fluidic capillary flowpath communicates with the respective well preferably via a connection at the top of the well.
  • Such specific embodiments described would be conveniently suitable for use in devices and structures such as those disclosed in WO03/056319 in which an electrochemical micro-electrode sensor may have an array of wells or other sites which is used for analysing fluids including biological fluids (for example blood) or non biological fluids.
  • the utilisation of the bridge structure, and the consequent promotion of flow of fluid from the dispensing element allows the fluid to be delivered via the downstream flowpath, to the destination zone as a discrete bolus of fluid rather than a trickle effect. This ensures more uniform and simultaneous delivery to the destination zones, particularly where delivery to a plurality of destination zones is required.
  • the structure of the invention comprises a test strip device having the dispensing element proximate a first end thereof and the destination zone proximate a second end thereof and a micro fluid capillary flowpath extending between the dispensing element and the destination zone.
  • the sample fluid is applied to a dispensing element and the sample passes to a reservoir below and then into a capillary channel flowpath.
  • This enables a large surface area (separation membrane) to filter, for example blood with less hematocrit dependence than prior art lateral delivery/separation systems. Faster separation/third passage is also achieved.
  • Figure 1 is a schematic sectional view of a first embodiment of micro-fluidic structure in accordance with the invention
  • Figure 2 is a detail view of a part of the structure of figure 1 ;
  • Figure 3 is a schematic view of a sloped surface embodiment of bridge structure
  • FIG. 4 shows alternative embodiments of bridge structure in accordance with the invention.
  • FIGS 5a and 5b are sequential schematic sectional views of an embodiment of micro-fluidic structure in accordance with the invention.
  • a bio-sensor device in the form of a micro-fluidic device comprising a biological fluid sample screening strip 1.
  • the strip 1 may be of a variety including a microband electrode electrochemical sensor, constructed in the same or similar fashion to sensors of the type disclosed in for example WO03/056319.
  • the sensor electrodes are not indicated in the drawings, in order to more clearly identify the micro-fluid flowpaths and the arrangement embodying the concept of the invention.
  • a blood separation membrane 2 acts as a dispensing element to dispense plasma into a micro-fluid capillary flowpath 5 which extends to connect with an array of wells, two of which (3,4) are shown in the drawings.
  • the strip is formed of a series of layers including a hydrophilic layer 6, a layer of spacer tape 7 including, integrally formed, the micro-fluid capillary flowpath 5 which is typically of rectilinear section having side dimensions of 500 ⁇ and ⁇ .
  • suitable separation membranes 2 are those commercially available from Whatman under the trade designations VF1, VF2 and GFD or BTS membrane available from PALL.
  • the sealing layer 8 may be a plastics material and for example of polyethylene terepthalate (PET) or polycarbonate (PC) and typically coated on one side with a pressure sensitive or heat sensitive adhesive layer.
  • the spacer tape 7 is typically plastics (for example of PET or PC) and maybe coated on both sides with either a pressure sensitive or heat sensitive adhesive layer.
  • the hydrophilic layer 6 may be of plastics (for example PET or PC) and may be coated on one side with pressure sensitive or heat sensitive layer with a mixed in surfactant. Acrylic based adhesives may be used as either pressure or heat sensitive adhesives.
  • the layer structure and materials described are exemplary only and other materials or structures may usefully be utilised and fall within the scope of the invention.
  • the upper layer structure 9 of the strip comprising electrochemical cell layer structure of the strip.
  • This upper electrochemical cell layer structure is not described in detail herein, but exemplary structures are disclosed in WO/03/056319.
  • An aperture defining a receiving station for the blood separation membrane 2 is defined through the upper layer structure 9, as are apertures defining the upper portions of the wells 3,4.
  • the wells 3,4 have diameters of about 0.8 to 1.0mm. Well diameters of 0.1mm to 5mm may be utilised dependent upon a particular application.
  • the length or width dimension will typically be in the range 0.1mm to 5mm (more typically 0.9 to 1mm).
  • the well depth will be in the range 50 ⁇ to ⁇ , more typically 200 ⁇ to 800 ⁇ , most typically 300 ⁇ to 600 ⁇ .
  • An electro-active substance is contained within the wells 3,4.
  • the electro-active substance 8 is freeze dried to form a porous cake.
  • the electro-active substance dissolves and an electrochemical reaction may occur and measurable current, voltage or charge may occur in the cell.
  • Electro-active substances are discussed in more detail in, for example WO 03/056319.
  • the micro-fluid capillary flowpath 5 connects via apertures in the sealing layer to the wells 3, 4 and also the blood separation membrane 2.
  • a blood sample is deposited on the obverse side 2a and the membrane 2 filters the blood such that filtered plasma emerges at the reverse side 2b of the membrane.
  • the plasma passes into the capillary flowpath 5 and enters into the wells 3, 4 at the respective bases of respective wells.
  • the volume of the plasma passing into the system is a microlitre volume, typically within the range 0.2 xL to 30 ⁇ ,.
  • a bridge structure 10 is positioned at the head of the capillary flowpath 5 and immediately adjacent the downstream side of the separation membrane 2.
  • the bridge structure 10 is a dimple formed by indentation 1 1 on the reverse side of the hydrophilic layer 6.
  • the purpose of the bridge structure is to form a localised bridge between the micro- fluidic capillary flowpath 5 and the plasma on the adjacent reverse surface 2b of the separation membrane 2.
  • the plasma is separated and flows along the reverse side of the membrane 2 to the dimple. The plasma then flows down the dimple 10 and fills the capillary channel 5.
  • the bridge structure dimple 10 locally touches the membrane 2 initiating the plasma bridge. Once the plasma bridge is set up, it allows free flow of plasma from the membrane into the head chamber 12 and thereafter into the capillary channel flowpath 5. The surface tension of the membrane 2 plasma interaction is broken by the solid hydrophilic film surface of the dimple bridge structure 10, in contact with it.
  • the bridge 10 in accordance with realisation of the invention, may be dissolvable in the fluid, or have a surface coating or layer that is dissolvable.
  • Preferred features of the bridge structure 10 are that it has a solid (preferably non porous, preferably hydrophilic) surface and that it has an apex or zenith (preferably a convex, domed, or at least part spherical) surface at the contact location with the membrane 2. Curved surfaces are preferred because stepped or slope angled surface formations tend to be hydrophobic.
  • a dimple structure 10 has been primarily described. It should be readily appreciated that other structural forms could be employed within the scope of the invention. For example, hydrophilic surface plastic spheres or domed elements could be utilised, bonded to the surface of layer 6, or formed integrally at manufacture. An array of dimples, spheres or domed elements could also be utilised.
  • non spherical (or part spherical) surface geometry structures could be usefully employed such as finger projections, sloping surfaces or other protuberances.
  • a bridge structure having a reticulated or mesh form has also been found to work effectively in certain applications.
  • the apex 10a of the dimple structure 10 is in contact with the reverse side 2b of the separation membrane 2. It is however envisaged that the apex 10a could be spaced by a very small gap and achieve the same result of effectively bridging to the membrane 2, provided that the apex 10a contacts with plasma accumulating on the reverse side 2b of the separation membrane 2. It has been found that a gap in the range 1 ⁇ to 30 ⁇ enables the invention to work effectively. Indeed by controlling the gap for specific fluids, it is possible to control the flow of fluid through the separation membrane 2 and from the separation membrane 2 into the downstream capillary flowpath 5.
  • the necessary spacing of the apex 10a from the membrane 2 depends upon the surface tension of the passing fluid (which hangs in drop-form from the underside of the separation membrane 2). This in turn depends upon the viscosity of the passing fluid, the surface tension of the membrane, the pore size of the membrane and other factors.
  • the dwell time of the fluid in the membrane may be controlled by the spacing distance of the apex 10a of the bridge structure 10 from the underside 2a of the membrane 2.
  • a lectin impregnated glass fiber doped membrane eg., GFD-VF2 from Whatman
  • a spaced bridge apex 10 a means that a drop takes several seconds to reach the required size to cross the bridge gap.
  • the flow of plasma into the capillary channel is dependent solely upon the pull of gravity, which is not large enough to overcome the surface tension interaction between the plasma and the membrane 2. In such circumstances the plasma will not flow. Centrifuge systems or applied pressure devices may be used to overcome this but such arrangements make systems more complex.
  • the bridge system of the present invention allows the wells 3, 4 to fill in a discrete pulse or wave of fluid which makes it more likely that the wells will fill at the same time.
  • the height of the hydrophilic surface apex 10a of the bridge structure 10 below the membrane 2 determines how quickly the plasma flows from the membrane. Surfaces in contact, or nearly in contact with the bottom of the membrane 2 draw plasma through it in less than 10s. Surfaces more than around 50 ⁇ below the bottom surface of the membrane do not assist in drawing plasma through the membrane.
  • the height of the bridge surface below the membrane is variable in a predetermined manner consequent on the flow of the plasma.
  • the present invention uses a dissolvable hydrophilic surface such as polyvinylpyrrolidone (PVP), sugar, or dissolvable plastic to ensure that the surface which is initially in contact with the membrane becomes further than 50 ⁇ away from the membrane as plasma flows.
  • a dissolvable hydrophilic surface such as polyvinylpyrrolidone (PVP), sugar, or dissolvable plastic.
  • PVP polyvinylpyrrolidone
  • sugar or dissolvable plastic
  • a bridge structure that shrinks or collapses in a predetermined way upon flowing of plasma may be used in accordance with the invention.
  • Effective electrochemical reaction in the wells 3, 4 requires a specific volume of plasma to resuspend into in order to give a well defined final reagent concentration.
  • resuspended reagents can diffuse into the plasma in contact with the reagents and also along the plasma contained within the channels connecting the reaction areas and the membrane system.
  • the present invention ensures that an accurate and controlled volume of plasma is delivered to resuspend the reagents and contact any measuring device such as the electrochemical electrodes.
  • the volume of the channels behind the metered plasma dose contains only air and thus reagents cannot diffuse between reaction areas and the membrane system.
  • the bridge 10 reduces from a maximum extent as shown in Figure 5a to a minimum extent as shown in Figure 5b in which the bridge apex is spaced more greatly from the underside of the separation membrane 2.
  • a slope form hydrophilic bridge surface 1 10 This can be used to direct, preferentially, the fluid from the membrane 102 into the capillary channel 105 (in a direction to the right in figure 3, for example).
  • a curve form bridge structure may be provided with valleys or channels extending downwardly away from the apex to direct flow into selected channels for onward delivery to a series of wells, 3, 4.
  • Other bridge form arrangements are shown in figures 4a to 4f. Each of the structures 4a to 4f is shown in transverse cross section.
  • a plurality of spheres 10 (for example spherical glass balls) is mounted on the base layer 6 to form the bridge.
  • the apexes of the balls 10 form the apex bridge surfaces and the fluid passes under capillary action downstream of the balls 10.
  • the other arrangements each include an array of apexes 10 of different geometries and profiles present on the base layers 6.
  • the invention provides a convenient and elegant means for enabling fluid flow into capillary flowpaths or other micro-fluidic structures in circumstances where other flow propagation means would need to be utilised otherwise.
  • the arrangement is particularly suited to sensors for biological fluid screening using micro litre fluid volumes, particularly of viscous fluids.
  • the invention has been described and exemplified for use in bio-sensors for sampling plasma, blood and saliva. The skilled addressee will readily realise that the invention has application in other micro-fluidic devices.

Abstract

A micro-fluidic structure (1) such as a bio-sensor device has a dispensing element (2) for fluid and a destination zone (3, 4) in communication with, and downstream of, the dispensing element (2). A bridge structure (10) extends to the dispensing element (2) and promotes fluid passage across the bridge structure (10) from the dispensing element (2) toward the destination zone (3, 4). The bridge structure is arranged to change in extent upon flow of the fluid.

Description

Micro-fluidic Structures
The present invention relates to micro-fluidic structures. Micro-fluidic structures are used in various applications and include micro-fluidic structures for use in devices for sampling and testing of fluids, particularly, but not exclusively biological fluids. For example the invention has particular utility in micro-fluidic structures for devices used in medical diagnostic techniques, such as, for example, bio-sensor devices.
WO03/056319 discloses an electro-chemical micro-electrode bio-sensor device having an array of wells or other sites which is used for analysing fluids including biological fluids (for example blood) or non biological fluids. The arrangement disclosed requires the fluid to be screened to be delivered to the one or more wells or other sites to be analysed and an electrical output produced. The quantities of fluid delivered for screening are at the level of micro litre volumes. A further example of a micro-electrode sensor for use in bio applications is disclosed in US2005/0072670.
An improved micro-fluidic structure for use in micro-fluidic techniques has now been devised.
According to a first aspect, the present invention provides a micro-fluidic structure comprising:
a dispensing element for dispensing fluid;
a destination zone in communication with, and downstream of, the dispensing element; and
a bridge structure extending adjacent to the dispensing element and promoting fluid passage across the bridge structure from the dispensing element toward the destination zone, wherein the bridge structure is arranged to alter in extent during passage of the fluid.
According to a second aspect, the invention provides a microfluidic structure comprising: a dispensing element for dispensing fluid; a destination zone in communication with, and downstream of, the dispensing element; and, a bridge structure extending adjacent to the dispensing element and promoting fluid passage across the bridge structure from the dispensing element toward the destination zone; wherein during fluid passage a separation gap between the dispensing element and the bridge structure increases to a maximum (at which passage of the fluid across the gap is caused to cease).
The bridge structure locally bridges to the dispensing element and/or the fluid present on the facing surface of the dispensing element. This permits or accelerates passive flow of the fluid (for example plasma) into the downstream portions of the structure. In a preferred embodiment the dispensing element may comprise a red blood cell separation membrane and the invention enables plasma on the bottom of the membrane to flow off because there is bridging contact via the bridge structure. When the bridge is locally created it propagates to substantially the entire adjacent surface area of the dispensing element, allowing free flow of fluid. In the absence of the bridge structure the fluid will coat the bottom surface of the dispensing element in its lowest energy configuration and flow may not be induced (other than by application of other force delivery means, such as for example applied pressure).
In a certain embodiment, material of the bridge structure may be dissolvable in the fluid. In an alternative embodiment the bridge structure may shrink, collapse or otherwise alter in configuration.
It is preferred that the bridge structure includes a bridge surface, the bridge surface preferably being hydrophilic. Beneficially, the bridge surface comprises a hydrophilic film or layer so that the solution will preferentially wet the bridge structure giving a lower interfacial energy between the solution and the bridge than between the solution and the underside of the dispensing element. Desirably the bridge has an apex or zenith proximate the dispensing element. In one embodiment the bridge has a convex bridge surface, and may for example have a part spherical surface such as a hemispherical surface. Curved, rather than stepped change edges and surfaces improves flow and are less hydrophobic.
Preferably a fluid flowpath extends downstream of the dispensing element. In a preferred embodiment the fluid flowpath comprises a capillary flowpath. Beneficially the fluid flowpath is a micro fluid flowpath having the capacity to transport micro litre volumes of fluid. Beneficially, where the capillary flowpath includes circular section channels, the diameter of the channels is preferably in the range 0.1mm to 5mm (more preferably in the range lOum to 500um). Alternatively channels having a rectilinear or other geometry section may be used, beneficially having a side dimension in the range 0.001 mm to 3 mm (more preferably in the range 0.05 mm to 1 mm). The downstream flowpath may comprise a plurality of flowpaths such as a plurality of connected capillary flowpaths. The connection may be dendritic.
In a certain embodiment the surface of the bridge structure may be contoured to promote flow along certain pre-defined paths. For example, this would promote flow to specific downstream flowpaths. The contour of the bridge structure surface may comprise a sloped or valley path.
It is preferred that the dispensing element comprises a receiver element arranged to hold a volume of fluid. Beneficially the receiver element is fluid permeable. The receiver element preferably acts to filter fluid. In a preferred embodiment, the receiver element acts to filter a biological fluid, preferably filtering blood and permitting plasma to pass. In a preferred embodiment the dispensing element comprises a membrane. Beneficially the membrane is arranged such that a fluid sample is deposited on an obverse side of the membrane and dispensed via a reverse side.
In one embodiment, the bridge structure may be configured to contact the dispensing element. Alternatively, the bridge structure may be configured to be spaced from the dispensing element by a small gap substantially in the range 1 μηι to 30 μιη.
The required height of the bridge structure (ie the spacing from the dispensing element) depends upon the fluid passing via the dispensing element, and consequently the surface tension of a hanging drop of the fluid. This in turn depends upon the viscosity of the fluid, the surface tension of the dispensing element (and pore size of the dispensing element). The amount of time the fluid takes to pass through the dispensing element (the dwell time) can be controlled by varying the spacing between the bridge and the dispensing element.
Beneficially, the destination zone comprises a destination station containing a reagent substance for reacting with the fluid delivered from the dispensing element. The reagent substance may comprise, for example, an electro-active substance.
In a specific embodiment, the destination zone may comprise a plurality of destination stations, respective stations containing a respective reagent substance for reacting with the fluid delivered from the dispensing structure. In such an embodiment, separate destination stations contain different respective reagent substances. The separate destinations may be served via separate delivery channels, as described above.
In a specific embodiment, a respective destination zone may comprise a well. Beneficially a micro-fluidic capillary flowpath communicates with the respective well preferably via a connection at the bottom of the well. In a specific embodiment, the destination zone may comprise an array of wells, the structure preferably including a micro fluid capillary flowpath network leading to the array of wells.
In an alternative embodiment, the micro-fluidic capillary flowpath communicates with the respective well preferably via a connection at the top of the well. Such specific embodiments described would be conveniently suitable for use in devices and structures such as those disclosed in WO03/056319 in which an electrochemical micro-electrode sensor may have an array of wells or other sites which is used for analysing fluids including biological fluids (for example blood) or non biological fluids. The utilisation of the bridge structure, and the consequent promotion of flow of fluid from the dispensing element allows the fluid to be delivered via the downstream flowpath, to the destination zone as a discrete bolus of fluid rather than a trickle effect. This ensures more uniform and simultaneous delivery to the destination zones, particularly where delivery to a plurality of destination zones is required.
In a preferred specific embodiment, the structure of the invention comprises a test strip device having the dispensing element proximate a first end thereof and the destination zone proximate a second end thereof and a micro fluid capillary flowpath extending between the dispensing element and the destination zone.
In the embodiments primarily described, the sample fluid is applied to a dispensing element and the sample passes to a reservoir below and then into a capillary channel flowpath. This enables a large surface area (separation membrane) to filter, for example blood with less hematocrit dependence than prior art lateral delivery/separation systems. Faster separation/third passage is also achieved.
The invention will now be further described, by way of example only, and with reference to the accompanying drawings, in which:
Figure 1 is a schematic sectional view of a first embodiment of micro-fluidic structure in accordance with the invention; Figure 2 is a detail view of a part of the structure of figure 1 ;
Figure 3 is a schematic view of a sloped surface embodiment of bridge structure;
Figure 4 shows alternative embodiments of bridge structure in accordance with the invention; and
Figures 5a and 5b are sequential schematic sectional views of an embodiment of micro-fluidic structure in accordance with the invention. Referring to the drawings and initially to figure 1 , there is shown a bio-sensor device in the form of a micro-fluidic device comprising a biological fluid sample screening strip 1. The strip 1 may be of a variety including a microband electrode electrochemical sensor, constructed in the same or similar fashion to sensors of the type disclosed in for example WO03/056319. For ease of reference, in this description, the sensor electrodes are not indicated in the drawings, in order to more clearly identify the micro-fluid flowpaths and the arrangement embodying the concept of the invention. In the arrangement shown in figure 1 a blood separation membrane 2 acts as a dispensing element to dispense plasma into a micro-fluid capillary flowpath 5 which extends to connect with an array of wells, two of which (3,4) are shown in the drawings. The strip is formed of a series of layers including a hydrophilic layer 6, a layer of spacer tape 7 including, integrally formed, the micro-fluid capillary flowpath 5 which is typically of rectilinear section having side dimensions of 500μηι and ΙΟΟμηι. Examples of suitable separation membranes 2 are those commercially available from Whatman under the trade designations VF1, VF2 and GFD or BTS membrane available from PALL. Above the spacer layer 7 is a sealing layer 8 including apertures defining the lowermost portions of wells 3, 4 and an aperture below the blood separation membrane 2. The sealing layer 8 may be a plastics material and for example of polyethylene terepthalate (PET) or polycarbonate (PC) and typically coated on one side with a pressure sensitive or heat sensitive adhesive layer. The spacer tape 7 is typically plastics (for example of PET or PC) and maybe coated on both sides with either a pressure sensitive or heat sensitive adhesive layer. The hydrophilic layer 6 may be of plastics (for example PET or PC) and may be coated on one side with pressure sensitive or heat sensitive layer with a mixed in surfactant. Acrylic based adhesives may be used as either pressure or heat sensitive adhesives. It will be readily appreciated that the layer structure and materials described are exemplary only and other materials or structures may usefully be utilised and fall within the scope of the invention. Above the sealing layer 8 is the upper layer structure 9 of the strip comprising electrochemical cell layer structure of the strip. This upper electrochemical cell layer structure is not described in detail herein, but exemplary structures are disclosed in WO/03/056319. An aperture defining a receiving station for the blood separation membrane 2 is defined through the upper layer structure 9, as are apertures defining the upper portions of the wells 3,4. Preferably, the wells 3,4 have diameters of about 0.8 to 1.0mm. Well diameters of 0.1mm to 5mm may be utilised dependent upon a particular application. Where non circular wells are used, the length or width dimension will typically be in the range 0.1mm to 5mm (more typically 0.9 to 1mm). Typically the well depth will be in the range 50μηι to ΙΟΟΟμη , more typically 200μηι to 800μπι, most typically 300μηι to 600μηι.
An electro-active substance is contained within the wells 3,4. The electro-active substance 8 is freeze dried to form a porous cake. On introduction of a measurement sample of plasma (as described henceforth) into the wells 3,4 the electro-active substance dissolves and an electrochemical reaction may occur and measurable current, voltage or charge may occur in the cell. Electro-active substances are discussed in more detail in, for example WO 03/056319. The micro-fluid capillary flowpath 5 connects via apertures in the sealing layer to the wells 3, 4 and also the blood separation membrane 2. A blood sample is deposited on the obverse side 2a and the membrane 2 filters the blood such that filtered plasma emerges at the reverse side 2b of the membrane. The plasma passes into the capillary flowpath 5 and enters into the wells 3, 4 at the respective bases of respective wells. Typically the volume of the plasma passing into the system is a microlitre volume, typically within the range 0.2 xL to 30 μΐ,.
It is difficult to promote flow of plasma from the separation membrane 2 into the capillary flowpath 5, gravitational force generally being insufficient. In accordance with the present invention a bridge structure 10 is positioned at the head of the capillary flowpath 5 and immediately adjacent the downstream side of the separation membrane 2. In the embodiment shown the bridge structure 10 is a dimple formed by indentation 1 1 on the reverse side of the hydrophilic layer 6. The purpose of the bridge structure is to form a localised bridge between the micro- fluidic capillary flowpath 5 and the plasma on the adjacent reverse surface 2b of the separation membrane 2. In the embodiment shown the plasma is separated and flows along the reverse side of the membrane 2 to the dimple. The plasma then flows down the dimple 10 and fills the capillary channel 5. The bridge structure dimple 10 locally touches the membrane 2 initiating the plasma bridge. Once the plasma bridge is set up, it allows free flow of plasma from the membrane into the head chamber 12 and thereafter into the capillary channel flowpath 5. The surface tension of the membrane 2 plasma interaction is broken by the solid hydrophilic film surface of the dimple bridge structure 10, in contact with it.
The bridge 10, in accordance with realisation of the invention, may be dissolvable in the fluid, or have a surface coating or layer that is dissolvable.
Preferred features of the bridge structure 10 are that it has a solid (preferably non porous, preferably hydrophilic) surface and that it has an apex or zenith (preferably a convex, domed, or at least part spherical) surface at the contact location with the membrane 2. Curved surfaces are preferred because stepped or slope angled surface formations tend to be hydrophobic. In the embodiment described a dimple structure 10 has been primarily described. It should be readily appreciated that other structural forms could be employed within the scope of the invention. For example, hydrophilic surface plastic spheres or domed elements could be utilised, bonded to the surface of layer 6, or formed integrally at manufacture. An array of dimples, spheres or domed elements could also be utilised. Furthermore, it is envisaged that non spherical (or part spherical) surface geometry structures could be usefully employed such as finger projections, sloping surfaces or other protuberances. A bridge structure having a reticulated or mesh form has also been found to work effectively in certain applications.
In the embodiment shown, the apex 10a of the dimple structure 10 is in contact with the reverse side 2b of the separation membrane 2. It is however envisaged that the apex 10a could be spaced by a very small gap and achieve the same result of effectively bridging to the membrane 2, provided that the apex 10a contacts with plasma accumulating on the reverse side 2b of the separation membrane 2. It has been found that a gap in the range 1 μηι to 30 μπι enables the invention to work effectively. Indeed by controlling the gap for specific fluids, it is possible to control the flow of fluid through the separation membrane 2 and from the separation membrane 2 into the downstream capillary flowpath 5. The necessary spacing of the apex 10a from the membrane 2 depends upon the surface tension of the passing fluid (which hangs in drop-form from the underside of the separation membrane 2). This in turn depends upon the viscosity of the passing fluid, the surface tension of the membrane, the pore size of the membrane and other factors.
Additionally, the dwell time of the fluid in the membrane may be controlled by the spacing distance of the apex 10a of the bridge structure 10 from the underside 2a of the membrane 2. For example, with a lectin impregnated glass fiber doped membrane (eg., GFD-VF2 from Whatman), it is required to retain the fluid sample within the membrane for a few seconds in order to allow time for the lectins to work. A spaced bridge apex 10 a means that a drop takes several seconds to reach the required size to cross the bridge gap.
If the bridge structure dimple 10 is not present the flow of plasma into the capillary channel is dependent solely upon the pull of gravity, which is not large enough to overcome the surface tension interaction between the plasma and the membrane 2. In such circumstances the plasma will not flow. Centrifuge systems or applied pressure devices may be used to overcome this but such arrangements make systems more complex. The bridge system of the present invention allows the wells 3, 4 to fill in a discrete pulse or wave of fluid which makes it more likely that the wells will fill at the same time.
Specifically, in accordance with the present invention, the height of the hydrophilic surface apex 10a of the bridge structure 10 below the membrane 2 determines how quickly the plasma flows from the membrane. Surfaces in contact, or nearly in contact with the bottom of the membrane 2 draw plasma through it in less than 10s. Surfaces more than around 50μιη below the bottom surface of the membrane do not assist in drawing plasma through the membrane. In accordance with the present invention, the height of the bridge surface below the membrane is variable in a predetermined manner consequent on the flow of the plasma. In one embodiment, the present invention uses a dissolvable hydrophilic surface such as polyvinylpyrrolidone (PVP), sugar, or dissolvable plastic to ensure that the surface which is initially in contact with the membrane becomes further than 50μηι away from the membrane as plasma flows. The time taken for the hydrophilic surface to lose contact with the membrane and consequently for plasma to stop flowing is determined by the physical properties of the material providing the hydrophilic surface. Consequently the hydrophilic dissolvable material can be tailored to give a dissolution rate that provides the required dose of plasma before the plasma flow stops.
In an alternative embodiment a bridge structure that shrinks or collapses in a predetermined way upon flowing of plasma may be used in accordance with the invention. Effective electrochemical reaction in the wells 3, 4 requires a specific volume of plasma to resuspend into in order to give a well defined final reagent concentration. In previously trialled techniques resuspended reagents can diffuse into the plasma in contact with the reagents and also along the plasma contained within the channels connecting the reaction areas and the membrane system. The present invention ensures that an accurate and controlled volume of plasma is delivered to resuspend the reagents and contact any measuring device such as the electrochemical electrodes. The volume of the channels behind the metered plasma dose contains only air and thus reagents cannot diffuse between reaction areas and the membrane system.
As shown in Figures 5 and 5a during flow of the plasma the bridge 10 reduces from a maximum extent as shown in Figure 5a to a minimum extent as shown in Figure 5b in which the bridge apex is spaced more greatly from the underside of the separation membrane 2.
It is possible to further control the form of the surface of the bridge structure in order to control the characteristics of flow of the fluid. For example, and with reference to figure 3, it is possible to have a slope form hydrophilic bridge surface 1 10. This can be used to direct, preferentially, the fluid from the membrane 102 into the capillary channel 105 (in a direction to the right in figure 3, for example). Alternatively, a curve form bridge structure may be provided with valleys or channels extending downwardly away from the apex to direct flow into selected channels for onward delivery to a series of wells, 3, 4. Other bridge form arrangements are shown in figures 4a to 4f. Each of the structures 4a to 4f is shown in transverse cross section. In the arrangement of figure 4a a plurality of spheres 10 (for example spherical glass balls) is mounted on the base layer 6 to form the bridge. The apexes of the balls 10 form the apex bridge surfaces and the fluid passes under capillary action downstream of the balls 10. The other arrangements each include an array of apexes 10 of different geometries and profiles present on the base layers 6.
The invention provides a convenient and elegant means for enabling fluid flow into capillary flowpaths or other micro-fluidic structures in circumstances where other flow propagation means would need to be utilised otherwise. The arrangement is particularly suited to sensors for biological fluid screening using micro litre fluid volumes, particularly of viscous fluids. The invention has been described and exemplified for use in bio-sensors for sampling plasma, blood and saliva. The skilled addressee will readily realise that the invention has application in other micro-fluidic devices.

Claims

Claims:
1. A micro-fluidic structure comprising:
a dispensing element for fluid,
a destination zone in communication with, and downstream of, the dispensing element; and
a bridge structure extending adjacent to the dispensing element and promoting fluid passage across the bridge structure from the dispensing element towards the destination zone, wherein the bridge structure is arranged to change in extent during passage of the fluid.
2. A micro-fluidic structure comprising:
a dispensing element for fluid,
a destination zone in communication with, and downstream of, the dispensing element; and
a bridge structure extending to the dispensing element and promoting fluid passage across the bridge structure from the dispensing element towards the destination zone, wherein during fluid passage a separation gap between the dispensing element and the bridge structure increases to a maximum.
3. A structure according to claim 1 and claim 2, wherein the bridge structure is arranged to reduce in extent upon flow of the liquid.
4. A structure according to any preceding claim, wherein the bridge structure retreats from the dispensing element opening an increasing gap between the dispensing element and the bridge structure.
5. A structure according to any preceding claim, wherein the bridge structure is dissolvable in the fluid.
6. A structure according to any preceding claim, wherein the bridge structure includes a bridge surface.
7. A structure according to any preceding claim, wherein the bridge surface is hydrophilic.
8. A structure according to claim 7, wherein the bridge surface comprises a hydrophilic film or layer.
9. A structure according to any preceding claim, wherein the bridge has an apex or zenith proximate the dispensing element.
10. A structure according to any preceding claim, wherein the bridge has a convex bridge surface.
11. A structure according to any preceding claim, wherein a fluid flowpath extends downstream of the dispensing element.
12. A structure according to claim 11, wherein the fluid flowpath comprises a capillary flowpath.
13. A structure according to any preceding claim wherein the structure is dimensioned to operate with micro litre fluid volumes or less.
14. A structure according to any preceding claim, wherein the dispensing element comprises a receiver element arranged to hold a volume of fluid.
15. A structure according to claim 14, wherein the receiver element is fluid permeable.
16. A structure according to claim 15 wherein the receiver element acts to filter fluid.
17. A structure according to claim 16, wherein the receiver element acts to filter blood whereby to permit plasma to pass.
18. A structure according to any preceding claim, wherein the bridge structure is configured to contact the receiver present at the receiving zone.
19. A structure according to any preceding claim, wherein the bridge structure is spaced apart from the dispensing element by a small gap substantially in the range 1 μπι to 30 μηι.
20. A structure according to any preceding claim wherein the bridge structure changes in extent, during flow of the fluid, from a maximum extent to a minimum extent.
21. A structure according to claim 20, wherein at minimum extent of the bridge structure fluid flow is ceased.
22. A structure according to claim 20 or claim 21, wherein at minimum bridge structure extent the spacing between the bridge structure and the dispensing element is 50μιη or more.
23. A structure according to any preceding claim, wherein the destination zone comprises a destination station containing a reagent substance for reacting with the fluid delivered from the dispensing element.
24. A structure according to claim 23, wherein the reagent substance comprises an electro-active substance.
25. A structure according to any preceding claim, wherein the destination zone comprises a plurality of destination stations, respective stations containing a respective reagent substance for reacting with the fluid delivered from the dispensing structure.
26. A structure according to claim 25, wherein separate destinations contain different respective reagent substances.
27. A structure according to any preceding claim, wherein the destination zone comprises a well.
28. A structure according to any preceding claim, wherein the destination zone comprises an array of wells.
29. A structure according to claim 27 or claim 28, wherein the structure includes a micro fluid capillary flowpath leading to the well or array of wells.
30. A structure according to any preceding claim comprising an electro-chemical electrode sensor.
31. A structure according to any preceding claim wherein the dispensing element is arranged to receive a fluid sample via an obverse side and dispense fluid via a reverse side.
32. A structure according to any preceding claim comprising a test strip device having the dispensing element proximate a first end thereof and the destination zone proximate a second end thereof and a micro fluid capillary flow-path extending between the dispensing element and the destination zone.
33. A structure according to any preceding claim, wherein the fluid passes across the dispensing element and bridge in a first general direction and subsequently flows in a second direction transverse to the first direction downstream of the bridge structure and to the destination zone.
34. A structure according to claim 33, wherein the fluid flows downwardly across the dispensing element and bridge and subsequently laterally downstream of the bridge element.
A device including a micro-fluidic structure according to any preceding claim.
36. A bio-sensor device including a micro-fluidic structure according to any preceding claim.
PCT/GB2009/051100 2009-09-01 2009-09-01 Micro-fluidic structures WO2011027092A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/GB2009/051100 WO2011027092A1 (en) 2009-09-01 2009-09-01 Micro-fluidic structures

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/GB2009/051100 WO2011027092A1 (en) 2009-09-01 2009-09-01 Micro-fluidic structures

Publications (1)

Publication Number Publication Date
WO2011027092A1 true WO2011027092A1 (en) 2011-03-10

Family

ID=42199190

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB2009/051100 WO2011027092A1 (en) 2009-09-01 2009-09-01 Micro-fluidic structures

Country Status (1)

Country Link
WO (1) WO2011027092A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2688672A2 (en) * 2011-03-24 2014-01-29 Boehringer Ingelheim Microparts GmbH Device and method for filtering blood
US9075042B2 (en) 2012-05-15 2015-07-07 Wellstat Diagnostics, Llc Diagnostic systems and cartridges
US9213043B2 (en) 2012-05-15 2015-12-15 Wellstat Diagnostics, Llc Clinical diagnostic system including instrument and cartridge
US9625465B2 (en) 2012-05-15 2017-04-18 Defined Diagnostics, Llc Clinical diagnostic systems
EP3078956A4 (en) * 2013-12-03 2017-06-28 The University of Tokyo Separation unit, separation method, fluid device, and composite fluid device and kit
US10029041B2 (en) 2011-11-30 2018-07-24 Pdl Biopharma, Inc. Filtration module

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4549952A (en) * 1982-11-22 1985-10-29 Eastman Kodak Company Capillary transport device having means for increasing the viscosity of the transported liquid
US5354538A (en) * 1989-03-23 1994-10-11 Bunce Roger A Liquid transfer devices
EP1482307A1 (en) * 2002-03-01 2004-12-01 Matsushita Electric Industrial Co., Ltd. Biosensor
WO2006044841A2 (en) * 2004-10-18 2006-04-27 Applera Corporation Fluid processing device including size-changing barrier
WO2007071989A1 (en) * 2005-12-21 2007-06-28 Oxford Biosensors Limited Micro-fluidic structures

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4549952A (en) * 1982-11-22 1985-10-29 Eastman Kodak Company Capillary transport device having means for increasing the viscosity of the transported liquid
US5354538A (en) * 1989-03-23 1994-10-11 Bunce Roger A Liquid transfer devices
EP1482307A1 (en) * 2002-03-01 2004-12-01 Matsushita Electric Industrial Co., Ltd. Biosensor
WO2006044841A2 (en) * 2004-10-18 2006-04-27 Applera Corporation Fluid processing device including size-changing barrier
WO2007071989A1 (en) * 2005-12-21 2007-06-28 Oxford Biosensors Limited Micro-fluidic structures

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2688672A2 (en) * 2011-03-24 2014-01-29 Boehringer Ingelheim Microparts GmbH Device and method for filtering blood
US10029041B2 (en) 2011-11-30 2018-07-24 Pdl Biopharma, Inc. Filtration module
US9075042B2 (en) 2012-05-15 2015-07-07 Wellstat Diagnostics, Llc Diagnostic systems and cartridges
US9081001B2 (en) 2012-05-15 2015-07-14 Wellstat Diagnostics, Llc Diagnostic systems and instruments
US9213043B2 (en) 2012-05-15 2015-12-15 Wellstat Diagnostics, Llc Clinical diagnostic system including instrument and cartridge
US9625465B2 (en) 2012-05-15 2017-04-18 Defined Diagnostics, Llc Clinical diagnostic systems
EP3078956A4 (en) * 2013-12-03 2017-06-28 The University of Tokyo Separation unit, separation method, fluid device, and composite fluid device and kit

Similar Documents

Publication Publication Date Title
US20080305008A1 (en) Micro-Fluidic Structures
WO2011027092A1 (en) Micro-fluidic structures
JP5861737B2 (en) Plasma separation reservoir
US9383293B2 (en) Device for plasma separation by means of a central channel structure
US11717827B2 (en) Automatic plasma separation and metering
US7927474B2 (en) Cell electrophysiological sensor
US7332348B2 (en) Sample substrate having a divided sample chamber and method of loading thereof
CA2957728C (en) Lateral-flow assay device with filtration flow control
WO2005026665A2 (en) Microfluidic flow monitoring device
JP4102796B2 (en) Analytical test element comprising a network forming a capillary channel
TW201213797A (en) Electrochemical sensing testing sheet
KR20240026458A (en) microfluidic device
AU2019202987A1 (en) Sampling plate with variable height testing zones
KR20170082843A (en) Biomolecular preconcentrating device
US20140093980A1 (en) Dissolvable bridges for manipulating fluid volumes and associated devices, systems and methods
US9017995B2 (en) Liquid-transport and analytical test device
CN117642228A (en) Microfluidic device

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 09785560

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 09785560

Country of ref document: EP

Kind code of ref document: A1