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WO2001085341A1 - Dispositifs microfluidiques - Google Patents

Dispositifs microfluidiques Download PDF

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Publication number
WO2001085341A1
WO2001085341A1 PCT/GB2001/002119 GB0102119W WO0185341A1 WO 2001085341 A1 WO2001085341 A1 WO 2001085341A1 GB 0102119 W GB0102119 W GB 0102119W WO 0185341 A1 WO0185341 A1 WO 0185341A1
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WO
WIPO (PCT)
Prior art keywords
reaction
particles
flow
beads
reaction chamber
Prior art date
Application number
PCT/GB2001/002119
Other languages
English (en)
Inventor
Helen Andersson
Göran Stemme
Wouter Van Der Wijngaart
Original Assignee
Pyrosequencing Ab
Piesold, Alexander, James
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 Pyrosequencing Ab, Piesold, Alexander, James filed Critical Pyrosequencing Ab
Priority to JP2001581990A priority Critical patent/JP2003532400A/ja
Priority to EP01928128A priority patent/EP1280601A1/fr
Priority to AU54992/01A priority patent/AU5499201A/en
Publication of WO2001085341A1 publication Critical patent/WO2001085341A1/fr

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Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/4077Concentrating samples by other techniques involving separation of suspended solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/18Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0039Inorganic membrane manufacture
    • B01D67/0053Inorganic membrane manufacture by inducing porosity into non porous precursor membranes
    • B01D67/0058Inorganic membrane manufacture by inducing porosity into non porous precursor membranes by selective elimination of components, e.g. by leaching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/0213Silicon
    • 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
    • B01L3/502761Containers 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 specially adapted for handling suspended solids or molecules independently from the bulk fluid flow, e.g. for trapping or sorting beads, for physically stretching molecules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00274Sequential or parallel reactions; Apparatus and devices for combinatorial chemistry or for making arrays; Chemical library technology
    • B01J2219/00277Apparatus
    • B01J2219/00497Features relating to the solid phase supports
    • B01J2219/005Beads
    • 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
    • B01L2200/00Solutions for specific problems relating to chemical or physical laboratory apparatus
    • B01L2200/06Fluid handling related problems
    • B01L2200/0647Handling flowable solids, e.g. microscopic beads, cells, particles
    • B01L2200/0668Trapping microscopic beads
    • 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
    • B01L2400/00Moving or stopping fluids
    • B01L2400/04Moving fluids with specific forces or mechanical means
    • B01L2400/0475Moving fluids with specific forces or mechanical means specific mechanical means and fluid pressure
    • B01L2400/0487Moving fluids with specific forces or mechanical means specific mechanical means and fluid pressure fluid pressure, pneumatics
    • 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
    • B01L3/502753Containers 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 bulk separation arrangements on lab-on-a-chip devices, e.g. for filtration or centrifugation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L7/00Heating or cooling apparatus; Heat insulating devices
    • B01L7/52Heating or cooling apparatus; Heat insulating devices with provision for submitting samples to a predetermined sequence of different temperatures, e.g. for treating nucleic acid samples
    • 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
    • G01N35/0098Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor involving analyte bound to insoluble magnetic carrier, e.g. using magnetic separation

Definitions

  • the present invention relates to microfluidic devices and particularly, although not exclusively, to microfluidic devices for manipulating microbeads.
  • Microspheres also known as beads, are routinely used as the mobile solid phase in medical diagnostics, microbiology, cancer research, immunology and molecular biology for separation, synthesis and detection of molecules.
  • the uniformity of the beads and their precisely defined size ensure that each bead has identical chemical and physical properties. Beads are available in several different materials and sizes (a few nanometers to millimeters in diameter).
  • the surface chemistry of the beads can be modified with various functional groups rendering the beads hydrophobic, hydrophilic, fluorescent, or active towards special ligand binding proteins. In order to perform and detect chemical reactions on beads, they must be confined to a limited volume.
  • Microfluidic devices for manipulating microspheres have, to date, mainly involved magnetic microspheres and have primarily focused on magnetically activated separations, see for example P. Telleman, TJ. Larsen, J. Philip, G. Blankenstein, and A. Wolff, Cell sorting in microfluidic systems, Micro Total Analysis Systems '98, Banff Canada, Oct 13-16, 1998, 39-44.
  • Paramagnetic beads i.e. beads with a magnetite (Fe 3 O 4 ) core sealed in a polymer shell, are extensively used today because they can be conveniently separated by applying external magnets.
  • magnetic principles are not always advantageous in micro total analysis systems ( ⁇ -TAS) applications. External magnetic systems complicate precision handling and result in a bulky system. Incorporation of magnetic components on wafer level is also a very complicated process.
  • the invention provides a microfluidic reaction apparatus for trapping one or more particles of predetermined nominal size or range of sizes, comprising a flow inlet and a reaction zone having an enlarged cross-sectional area in comparison to said flow inlet, said reaction zone comprising a filter means having a plurality of holes defined therein, the holes being smaller than said nominal size or range of sizes and arranged so as to trap said particles while a fluid flows from the flow inlet through the filter means.
  • the apparatus may be used to implement multi-step reactions at a single location.
  • the enhanced flow characteristics which may be achieved in accordance with the invention, in particular a reduced tendency to clog are beneficial in whichever stage of a process it is required to pass fluid over the filter and not necessarily during the reaction itself.
  • the apparatus whilst some preferred applications of an apparatus in accordance with the invention involve flowing a reaction fluid over the particles in a through-flow process, it is equally possible for the apparatus to be used for 'stop-flow' measurements in which there is not a significant flow of reaction fluid through the filter. In such cases the improved fluid characteristics mentioned above are still beneficial when charging the filter with the particles using a fluid in which the particles are suspended and/or in performing washing steps between the respective stages of a multi-stage reaction.
  • the filter means could extend laterally across the flow zone, i.e. normal to the direction of liquid flow.
  • the filter means extends around the flow axis, i.e. it has at least some extent in a plane whose normal is not parallel with the flow axis. This is beneficial since it enhances the concentration of the trapped particles into a smaller space which aids detection of the reaction. This is important, for example, when the reaction is one which emits light since it will increase the intensity and thus ease of measurement of the potentially low level of light.
  • the filter means extends substantially completely around the flow axis so as to form a porous reaction chamber. This enables the particles to be trapped in a compact arrangement whilst still allowing good porosity for the fluid passing through.
  • the chamber is shaped so as to conform to the shape of a reaction monitoring device.
  • the enclosure is substantially rectangular to match the rectangular shape of a charge coupled device.
  • the charge-coupled device may not be rectangular - e.g. it may be hexagonal in which case the chamber would preferably be hexagonal too.
  • the chamber could be circular or partly or substantially spherical.
  • the invention provides a reaction apparatus comprising a porous reaction chamber for trapping one or more particles therein and a reaction monitoring means arranged to monitor the particles trapped in the reaction chamber; wherein the reaction chamber is arranged so as substantially to correspond in shape to the reaction monitoring means.
  • the holes may be of any convenient size or shape as long as they are smaller in at least one dimension than the nominal size or range of sizes of the particles. It should be understood that where particles are non-spherical it is the minimum dimension that is taken to represent the 'size' of the particle. The important criterion is that the particles are trapped by the holes without passing through.
  • the holes are elongate, most preferably rectangular. This promotes a substantially lateral flow with minimal 'dead spaces' i.e. regions with low or no flow.
  • the holes could be defined as apertures in a wall or between the elements of a mesh, but preferably are defined between a plurality of preferably substantially parallel discrete wall elements which are preferably rectangular. Such wall elements preferably extend normally from a substrate to form pillars.
  • Apparatus in accordance with the invention could be open on one side, but are preferably closed to prevent contamination.
  • at least the reaction zone of the apparatus is closed by a substantially transparent cover. This allows reactions generating light or modifying incident light, for example fluorescence resulting from shining laser light onto the particles, to be monitored.
  • the apparatus is preferably formed on substantially planar substrate. Also preferred is that a flow outlet is provided, preferably substantially colinearly with the flow inlet and the reaction zone.
  • Apparatus in accordance with the invention can be manufactured using standard photolithographic procedures and bulk micromachining of silicon.
  • a mask fabrication process is used involving a deep reactive ion etching (DRIE).
  • DRIE deep reactive ion etching
  • a two stage process is used to form respective faces from a substantially planar substrate.
  • the bond is preferably effected by heating the mouth of the channel so as partially to melt the end of the tube.
  • the strength of the bond is enhanced by applying an adhesive around the base of the tube.
  • the adhesive is an epoxy glue.
  • the mouth of the channel is roughened prior to bonding the tube thereto. This enhances the strength of the bond.
  • the apparatus of the invention may be used for many different purposes.
  • a preferred use of the apparatus is in the analysis or sequencing of nucleic acid (i.e. DNA, RNA or cDNA).
  • a particularly preferred nucleic acid sequencing application is in sequencing-by-synthesis. Any suitable method of detecting nucleotide incorporation in sequencing by synthesis reactions may be used, i.e. use of fluorescently labelled nucleotides, colourimetric detection, radiolabels, or use of enzymatic detection systems.
  • Most preferably the apparatus is used in the Applicant's PyroSequencingTM sequencing-by-synthesis technique full details of which are given in WO98/13523.
  • the analyte in question comprises a nucleic acid, i.e. DNA fragment and that the liquid comprises a nucleotide.
  • the nucleic acid fragment is single-stranded.
  • Apparatus in accordance with the invention are particularly beneficial in such techniques since they allow different nucleotides to be cyclically pumped over the particles, preferably microbeads such as DynabeadsTM (available from Dynal Biotech ASA, Norway), which remain in the same position and thus are easy to monitor for the generation of light associated with the technique.
  • nucleotide will be understood to cover both deoxy and dideoxy nucleotide triphosphates (dNTPs and ddNTPs).
  • dNTPs and ddNTPs deoxy and dideoxy nucleotide triphosphates
  • analogues of dNTPs and ddNTPs which are normally incorporated into a growing DNA chain by a polymerase are also included.
  • a through-flow system for such techniques is novel and inventive in its own right and thus when viewed from a further aspect the invention provides a method of sequencing by synthesis comprising trapping a target immobilised on a plurality of beads, on a filter means provided in a through-flow channel and passing at least one nucleotide over said trapped beads.
  • Figure 2 shows schematically a plan view of an embodiment of an apparatus in accordance with the present invention using the filter arrangement of Fig. lc;
  • Figure 3 shows a scanning electron microscope (SEM) view of an embodiment of a device in accordance with the present invention
  • Figures 4a and 4b show SEM images of an embodiment of a reaction chamber in accordance with the present invention
  • Figure 5 shows a SEM view of pillars in the reaction chamber of figure 5;
  • Figures 6a-6d show respective stages in a method in accordance with an invention disclosed herein for attaching fluid connectors;
  • Figure 7 illustrates the principle of allele specific pyro-extension on a SNP
  • Figure 8 shows a plot of total collected light versus time
  • Figures 9a and 9b show snapshots of respectively match and mis-match pyro- extension.
  • FIG. la shows a known filter arrangement in which a planar filter A is placed laterally across a uniform channel B. This arrangement is prone to clogging when packed with beads C, thus impeding the free flow of liquid through the channel.
  • Fig. lb shows a filter arrangement in accordance with the invention.
  • the fluid inlet channel 2 opens into a zone 2a of enlarged cross section, compared to the inlet channel, in which a filter 4' is disposed laterally across it.
  • a filter 4' is disposed laterally across it.
  • a greater number of holes is provided than the arrangement of Fig. la. This significantly reduces the tendency for the filter 4' to clog in comparison with Fig. la, and results in more homogeneous flow characteristics over it.
  • Fig. lb is an improvement over that in Fig. la from the point of view of fluid flow characteristics.
  • the beads 6 may be more spread out than in the Fig. la arrangement, e.g. where the reaction which takes place on surface of the beads generates a low level of light.
  • the arrangement shown in Fig. lc overcomes this problem.
  • the filter 4 is similarly disposed in a zone 2a of enlarged cross-section.
  • the filter 4 extends all the way around the flow axis 8 to form a porous reaction chamber 10.
  • FIG. 2 A more detailed plan view of the preferred embodiment is shown in Fig. 2.
  • the microfluidic reaction apparatus is described in a substantially planar, rectangular substrate 12. The method of fabrication is described in greater detail hereinafter. Fluid and particles are introduced to the apparatus by means of a vertically disposed inlet tube 14, extending normally from the other surface of the substrate 12. A similar exit tube 16 is disposed at the other end of the apparatus.
  • the inlet tube 14 is in fluid communication with the inlet channel 2.
  • the inlet channel 2 opens out into a reaction zone 2a of enlarged cross-section.
  • the filter 4 extends all the way around the flow axis 8 to form a box-like reaction chamber 10.
  • the remainder of the enlarged zone 2a forms a waste chamber 18 for collecting fluid that has passed through the filter 4.
  • the waste fluid is channeled into an outlet channel 16 of similar dimensions to the inlet channel 2 and which is in fluid communication with the exit tube 16.
  • FIGs. 3, 4a, 4b and 5 there may be seen various scanning electron microscope (SEM) images of the embodiment depicted in Fig. 2. From these it may be seen that the filter 4 is made up of a series of parallel vertical pillars 22 extending vertically from the floor of the enlarged zone 2a etched out of the substrate 12. The gaps between the pillars 22 define the holes which must be smaller than the beads or other particles which it is desired to trap.
  • the apparatus shown in Figs. 2 to 5 is fabricated as follows. First, one hundred millimetre diameter 525 ⁇ m thick p-doped silicon (100 off)-wafers are used as the starting material. Photoresist (1.5 ⁇ m thick) is used for two etch masks. First, the front side is patterned and etched with the first mask using deep reactive ion etching (DRIE) (Surface Technology Systems, UK) to define the inlet channel 2, reaction chamber 10, filter 4, waste chamber 18 and outlet channel 20. Gas switching in the DRIE process gives rise to the undulating surface pattern on the pillars 22 which may be observed in Fig. 5.
  • DRIE deep reactive ion etching
  • a 170, 300 or 500 ⁇ m thick Pyrex glass wafer is anodically bonded to the front side.
  • the backside is then patterned in a second DRIE step with the second mask to create fluid connectors for the inlet and outlet tubes 14, 16.
  • the silicon-glass stack is then sawn into 9x5 mm chips.
  • External polyethylene (PE) tubes are used as the inlet and outlet tubes 14, 16 and are fixed to the chip in a multi-step procedure as schematically shown in Figs. 6a to 6d.
  • a mask-defined silicon surface roughening is performed around the fluid openings 26 by the second DRIE step to ensure good adhesion of the PE tubes (Fig. 6a).
  • a guide wire 24 is used to align the PE tubes 14, 16 with the respective fluid openings on the chip during the tube fixing process (Fig. 5b).
  • the silicon-glass stack 28 is briefly heated to generate a local melting of the PE tube 14, 16 onto the chip (Fig. 6c).
  • the interface between the chip and the PE tubes 14, 16 is then covered with epoxy glue.
  • Several exemplary apparatus of the form shown in Fig. 2 were fabricated with varying sizes. The dimensions of these are shown in rows 1 to 8 of Table 1 below. Row 9 relates to a design similar to that in Fig. la and is included for the purposes of comparison.
  • Table 1 A summary of the different designs of the flow-through micromachmed device where is the filter chamber volume, Wthe pillar width, E the pillar length, and H the pillar height.
  • the dimensions of the micromachmed structures were measured using a scanning electron microscope and compared with the original specifications. The consistency of the filter pillar dimensions within a reaction chamber and between different reaction chambers was measured.
  • the dimensions of the measured structures were found to be in good agreement with the original specifications.
  • the micromachmed structures were found to have high uniformity indicating a uniform and reproducible fabrication process.
  • the melt-on method for fixing the external P ⁇ tubes to the chip was found to be very convenient and reliable. It resulted in robust, precisely positioned interconnections to the macroscopic world with low dead volumes. It is believed that the epoxy glue is important in giving the assembly the robustness.
  • the fluid behaviour of the flow-through micromachmed device was investigated.
  • streptavidin coated beads of two different materials and sizes were used, i.e. polystyrene beads with a diameter of 5.50 ⁇ m (Bangs Laboratories, IN, USA) and magnetic Dynabeads with a diameter of 2.8 ⁇ m (Dynal Biotech ASA, Norway).
  • the bead solutions were applied manually with a pipette under a standard light microscope with 40X objective.
  • the beads were applied at a low concentration (10 000 beads/mL). Samples at the outlet were collected and controlled under the microscope to confirm that beads do not pass through the filter.
  • the smallest reaction chamber (design 1, 5, 6) has a volume of 0.5 nL and can hold about 50 beads with a diameter of 5.50 ⁇ m.
  • the flow-through volume of liquid or gas There is no upper limitation of the flow-through volume of liquid or gas, which is important when working with very- low sample concentrations.
  • the smallest volume required to fill the device is 3.0 nL (the volume of the inlet channel and reaction chamber).
  • Equation 1 is valid when 2 ⁇ L/D h ⁇ 50 where L is the length of the channel [8].
  • Design 9 is a channel with only 20 pillars constituting the filter compared to 70-790 pillars for design 1-8. 12
  • the beads can easily be removed out of the reaction chamber by applying back-pressure. After removing the beads and carefully cleaning of the micromachmed flow-through device, it can be reused.
  • the flow-through micromachined reaction chamber presented here collects both nonmagnetic and magnetic beads.
  • Nonmagnetic beads have lower density resulting in improved fluid dynamic behaviour in ⁇ -TAS compared to magnetic beads.
  • the batch fabrication process of the flow-through microfluidic device is simple and reproducible, involving only two masks and two different processing techniques. These are important factors in terms of parallellization and producing cost effective economical ⁇ -TAS.
  • the chip dimensions (9x5 mm) were chosen to simplify practical handling and can be further reduced if required.
  • the smallest reaction chamber of 0.5 nL, collecting approximate 50 beads, can also be further miniaturized if a reduced number of beads or flow-through volume are of interest.
  • an apparatus as shown in Fig. 2 was used in the Applicant's PyrosequencingTM sequencing-by-synthesis technique. This technique is performed by hybridizing a sequencing primer to the single-stranded nucleic acid template and incubation with the enzymes DNA poiymerase, ATP sulfurylase and luciferase. A specific deoxynucleotide triphosphate (dNTP, nucleotide) is added to the reaction. DNA poiymerase catalyses the 13
  • SNP single nucleotide polymorphisms
  • the outer PCR was followed by an inner PCR generating ⁇ 80 bp fragments.
  • One of the inner primers was biotinylated at the 5 '-end to allow immobilization. Biotinylated inner PCR product was immobilized onto the streptavidin coated beads. Single-stranded DNA was obtained by incubating the immobilized PCR product in NaOH. The immobilized strand was resuspended in H 2 O and annealing buffer was added to the single-stranded templates. The solution was then divided into two wells and primers were added in each well. The primers vary in their 3 '-ends and have the sequence 5'- GCTGCTGGTGCAGGGGCCACGG-3' and 5'-
  • sample flow-through rate is adjustable, which is important when performing chemical reactions on beads [10]. Effectively unlimited flow- through volumes of gas and liquid are possible allowing detection of rare molecules or biological species (at or below 100 copies/mL) [11].
  • the flow-through microfluidic reaction chamber reduces the accumulation of by-products resulting in increased reaction and detection sensitivity compared to a closed system (i.e. microtiter plates).
  • reaction chamber of designs 1-8 included in the study do not significantly affect the device performance (i.e., bead capture, air bubble sensitivity, pressure drop) for bead assays as long as the pillars constitute a mechanical barrier. Analytical calculations showed that the largest pressure drop is located across the inlet and outlet channels.
  • the reaction chamber and filter dimensions can therefore be optimized for bead size and chemical reaction parameters.
  • the filter dimensions are important. For example, when filtering cells it is important that the cells pass through the filter as quickly as possible to reduce cell activation, stiction and cell rupture [12].
  • the flow resistance remains low when the reaction chamber is packed with beads. Otherwise, it is difficult to pump the reactants through the reaction chamber.
  • the flow rate decreases with 40% when the reaction chamber is packed with beads. This corresponds to a flow of about 2 ⁇ L/min, which still is well within the margins for ⁇ -TAS. 15
  • At least preferred embodiments of the present invention can be used for solid- phase DNA sequencing, automatic introduction of beads by using micropumps, parallellization and device fabrication using plastic replication techniques.
  • the filter has been described as being made up of discrete pillars it is also conceivable to form a filter of walls which have slits which have openings which are narrower than the diameters of the beads being filtered. It is also possible to have one or several laterally arranged slits along the perimeter of the reaction chamber. These lateral slits should be narrower than the diameters of the beads being filtered.
  • the pillar filter design creates vertical filter openings which provides a substantially lateral flow with minimal "dead volumes" in the fluidic device (i.e. no or small volumes with low or zero flow). This is a very attractive feature since it improves the quality of the chemical and biochemical analysis.
  • the beads in the reaction chamber are collected in a "point" configuration (e.g.

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  • Engineering & Computer Science (AREA)
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  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Fluid Mechanics (AREA)
  • Dispersion Chemistry (AREA)
  • Hematology (AREA)
  • Clinical Laboratory Science (AREA)
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  • Measuring Or Testing Involving Enzymes Or Micro-Organisms (AREA)

Abstract

L'invention concerne un dispositif microfluidique destiné à piéger des billes (6) non magnétiques et magnétiques (6), le dispositif comprenant une entrée (2), une sortie (20) et un filtre de piégeage de bille (4) ce filtre comportant une paroi dotée de fentes dont les ouvertures sont plus petites que le diamètre des billes. Le filtre (4) est disposé dans une zone plus large (2a) et peut s'étendre autour de l'axe d'écoulement, par exemple sous une forme de type boîte. Le dispositif peut être utilisé dans un procédé de séquençage par synthèse.
PCT/GB2001/002119 2000-05-12 2001-05-14 Dispositifs microfluidiques WO2001085341A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2001581990A JP2003532400A (ja) 2000-05-12 2001-05-14 微小流体装置
EP01928128A EP1280601A1 (fr) 2000-05-12 2001-05-14 Dispositifs microfluidiques
AU54992/01A AU5499201A (en) 2000-05-12 2001-05-14 Microfluidic devices

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE0001768A SE0001768D0 (sv) 2000-05-12 2000-05-12 Mikrofluidisk flödescell för manipulering av partiklar
SE0001768-1 2000-05-12

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WO2001085341A1 true WO2001085341A1 (fr) 2001-11-15

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EP (1) EP1280601A1 (fr)
JP (1) JP2003532400A (fr)
AU (1) AU5499201A (fr)
SE (1) SE0001768D0 (fr)
WO (1) WO2001085341A1 (fr)

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AU5499201A (en) 2001-11-20
EP1280601A1 (fr) 2003-02-05
SE0001768D0 (sv) 2000-05-12

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