EP1833608A1 - Microreactor - Google Patents

Microreactor

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Publication number
EP1833608A1
EP1833608A1 EP05850267A EP05850267A EP1833608A1 EP 1833608 A1 EP1833608 A1 EP 1833608A1 EP 05850267 A EP05850267 A EP 05850267A EP 05850267 A EP05850267 A EP 05850267A EP 1833608 A1 EP1833608 A1 EP 1833608A1
Authority
EP
European Patent Office
Prior art keywords
fluid
magnetic
microfluidic
beads
magnetic particle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP05850267A
Other languages
German (de)
French (fr)
Inventor
Matthias Franzreb
Tilmann Rogge
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Karlsruher Institut fuer Technologie KIT
Original Assignee
Forschungszentrum Karlsruhe 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 Forschungszentrum Karlsruhe GmbH filed Critical Forschungszentrum Karlsruhe GmbH
Publication of EP1833608A1 publication Critical patent/EP1833608A1/en
Withdrawn legal-status Critical Current

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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
    • B01L3/502761Containers 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
    • B01J2219/00457Dispensing or evacuation of the solid phase support
    • B01J2219/00459Beads
    • B01J2219/00466Beads in a slurry
    • 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
    • B01J2219/00457Dispensing or evacuation of the solid phase support
    • B01J2219/00459Beads
    • B01J2219/00468Beads by manipulation of individual beads
    • 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
    • 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
    • B01J2219/00583Features relative to the processes being carried out
    • B01J2219/00603Making arrays on substantially continuous surfaces
    • B01J2219/00605Making arrays on substantially continuous surfaces the compounds being directly bound or immobilised to solid supports
    • 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
    • B01J2219/00583Features relative to the processes being carried out
    • B01J2219/00603Making arrays on substantially continuous surfaces
    • B01J2219/00605Making arrays on substantially continuous surfaces the compounds being directly bound or immobilised to solid supports
    • B01J2219/00612Making arrays on substantially continuous surfaces the compounds being directly bound or immobilised to solid supports the surface being inorganic
    • 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
    • B01J2219/00583Features relative to the processes being carried out
    • B01J2219/00603Making arrays on substantially continuous surfaces
    • B01J2219/00605Making arrays on substantially continuous surfaces the compounds being directly bound or immobilised to solid supports
    • B01J2219/00614Delimitation of the attachment areas
    • B01J2219/00621Delimitation of the attachment areas by physical means, e.g. trenches, raised areas
    • 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
    • B01J2219/00718Type of compounds synthesised
    • B01J2219/0072Organic compounds
    • B01J2219/00722Nucleotides
    • 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
    • B01J2219/00718Type of compounds synthesised
    • B01J2219/0072Organic compounds
    • B01J2219/00725Peptides
    • 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
    • B01J2219/00718Type of compounds synthesised
    • B01J2219/0072Organic compounds
    • B01J2219/00731Saccharides
    • 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
    • B01L2300/08Geometry, shape and general structure
    • B01L2300/0809Geometry, shape and general structure rectangular shaped
    • B01L2300/0816Cards, e.g. flat sample carriers usually with flow in two horizontal directions
    • 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
    • B01L2300/0877Flow chambers
    • 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
    • B01L3/5025Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures for parallel transport of multiple samples

Definitions

  • the invention relates to a device for transporting at least one magnetic particle fraction through a microfluidic system according to the preamble of the first claim.
  • Microfluidic systems are central handling systems for fluids, such as liquids or gases, with or without solids in micro- and nanotechnology, and are found particularly in the field of life sciences or biomedicine, where nano-objects in the form of large biomolecules, e.g. Peptides or proteins, must be handled [I]. Since direct handling of such small objects is seldom possible, so-called beads are often used in the field of life sciences. Beads are polymer bodies, usually spheres, on the functionalized surface of which e.g. DNA or proteins bound and so become manageable for synthesis or analysis. In this growing market, commercial devices are already being offered today, with which analyzes are carried out with the aid of individual beads [2].
  • Magnetic beads are commonly used in biochemistry today and are distributed by several commercial vendors (eg http://www.magneticmicrosphere.com/supply.htm). Such beads are usually superparamagnetic and monodisperse with diameters from 1 micron to 10 microns available and are used for analysis and synthesis purposes.
  • the handling of magnetic microbeads can be done on a larger scale with the help of so-called high-gradient magnetic separators [7].
  • a separation or fixation of magnetic microbeads usually takes place by simple permanent magnets based on rare earths.
  • this approach is quite inflexible and requires to release the fixation always moving components that allow a spatial separation between the reaction vessel with Magnetbeads and permanent magnet.
  • the object of the invention is therefore to provide a microfluidic system in which particle fractions (beads) are guided serially and directionally through channels and reaction chambers without a net movement of the fluid taking place.
  • Mass transfer in fluidic systems usually takes place via the movement of the fluid, with which the substances contained therein are moved to different locations.
  • the mass transfer within the device according to the invention is not carried out as usual by the flowing fluid, but by the Transport of the beads on the principle of a "fluidic ratchet".
  • the beads By generating a blocking force during the movement of the fluid, the beads can be fixed.
  • Ratchet is the name for a device z. B. tool in which a locking device allows only one direction of movement (freewheel), in the opposite direction it locks and moves an object z. B. screw or belt.
  • the directions of movement can be reversible.
  • the device according to the invention involves the provision of a microfluidic system in which particle fractions (beads) can be guided serially and directionally through channels and reaction chambers without a larger-scale fluid movement taking place.
  • a small-scale fluid movement which causes a movement of the particles, combined with a switchable force (blocking force), which at least fixed but at least significantly reduces the speed of movement of the particles.
  • the fluid movement may be generated mechanically or electrically (e.g., electro-osmosis).
  • the blocking force can be generated by magnetic fields acting on magnetic beads, by electrochemical induced electro fields induced by electrostatic fields due to dielectric constant differences of fluid and particles (dielectrophoresis, electrostatics) by optical fields generating forces due to refractive effects according to laser tweezers Surface forces that attach to the bead surfaces.
  • An actuator generates a periodic, small-scale forward and backward movement (freewheeling) of the fluid in the channel system.
  • an inhomogeneous magnetic field blocking device
  • the beads can be fixed during the return movement. Due to the fixation during the return movement of the fluid and the solution of the fixation during the forward movement, a directed movement of the beads through the channel system results without a net movement of the fluid. The directions of movement can be reversed.
  • Superparamagnetic particles are introduced into a fluidic channel system. As long as no other forces act on these particles, These particles are carried along with every movement of the fluid in the channel system. If a movement direction of the particles is blocked during a periodic fluid movement, the particles are transported in one direction. The surrounding fluid is moved by this periodic movement only by the volume amount of the particles in the reverse direction. The periodic movement of the fluid otherwise leads to no significant mixing, since in the smallest channel systems, a turbulent mixture is extremely difficult to achieve. The volume of the reaction chambers is extremely low, whereby the required amount of reactants is very low. Channel dimensions of a few micrometers and volumes of the reaction chambers in the nanoliter range are achieved.
  • the magnetic blocking force on the superparamagnetic particles should preferably be in the range of 10-100 pN.
  • the magnetic force on the particles results from the volume and the susceptibility of the particles as well as from the product of field strength times the gradient of the magnetic field. While the achievable field strengths are limited to a few teslas, very soft field micrographs can generate very high field gradients over short distances.
  • the magnetic holding force is achieved by soft magnetic microstructures immediately adjacent to the fluid region, which distort an externally generated magnetic field.
  • the smallest, lateral dimensions of these structures should correspond approximately to the diameter of the beads used, while the vertical dimensions should be three to ten times.
  • the production takes place after resist structuring with mask technique by electroplating. Subsequently, the structures are cast with plastic.
  • the plastic fulfills two functions. On the one hand, this creates a flat surface, which does not affect the bead movement. adversely. On the other hand, the plastic serves as a bonding partner for the
  • Housing part with the fluidic channel structures Housing part with the fluidic channel structures.
  • the particle motion depends on the flow velocity of the fluid, and can be well realized with spheres [12] as well as biological entities such as cells [13]. If no turbulences are formed during the periodic fluid movement, it is expected that the mass transfer within the fluid will not be significantly greater than the diffusion rate. As the extensive literature in the field of micromixers shows [14], [8] the intended induction of turbulence in microfluidic systems is difficult to achieve.
  • the device according to the invention fulfills various requirements for this purpose.
  • the fluid movement must be large enough to move particles through the fluid. These are in the channel system flow rates of about 1 - 10 mm / s necessary. The speed of the
  • Particles in the fluid channels from the ratio of channel size to particle size, the fluid velocity, the adhesion of the particles to the channel walls and the shape of the particles from.
  • the fluid channels must be designed so that a periodic fluid movement within the fluidic structures can spread well. It is important that the system is sufficiently incompressible and does not store the fluid movement elastically. Since the flow rate and thus also the movement of the beads depends on the channel cross-section, the flow rate can also be varied within the system. Thus broadening of the channel cross-section in the region of the reaction chambers can extend the residence time. The filling of the reaction chambers and the continuous supply of reactants are ensured by a slow flow through the reaction chambers perpendicular to the direction of movement of the beads. This also allows the complete replacement of the ingredients of individual reaction chambers.
  • the fluidic channels should have a cross-section that approximately corresponds to the bead size. For example, with a bead size of 4 ⁇ m, the channel width and height should not exceed 10 ⁇ m. Structures with these dimensions can be produced both by photolithography and X-ray lithography. Which method is most suitable depends on the required structural quality and the suitable plastics.
  • microstructures are carried out in many ways: with optical lithography (SU8, polyimide), by hot stamping (mold insert production by LIGA method or machining technique) or by X-ray deep lithography.
  • optical lithography SU8, polyimide
  • hot stamping molding insert production by LIGA method or machining technique
  • X-ray deep lithography X-ray deep lithography
  • microfluidic actuators is necessary at least at one point.
  • a periodic fluid movements must be generated, and / or requires the work with minimal amounts of material, for example, a metering devices with fast switching times.
  • Piezo actuators are suitable for both tasks, for example.
  • actuators lies in the short switching times (typically one millisecond) and the large force generated thereby.
  • the coupling of the mechanical movement into the system can take place either directly or via a translation system.
  • actuators can be represented via pressure spring systems or by shafts to electrically operated motors.
  • the functional principle of the device according to the invention requires a periodic fluid movement, which can only be used efficiently if the system is incompressible and the fluid has only a freely movable interface at the exit (eg gas bubble). This requires Rigid fluid supply or high flow resistance in the fluid supply area. Furthermore, a simple Bead-removal is possible at any time. For this purpose, the beads are collected in at least one chamber and flushed out as needed.
  • the AMS to the desired peptide length.
  • the beads are guided through the individual reaction areas of the device.
  • the device according to the invention allows for purposes in which only small amounts of material are needed, a fast and material-saving synthesis of complex molecules, for example peptides, proteins, oligonucleotides, DNA, oligosaccharides or RNA, whose synthesis is carried out by successive individual reactions. Small quantities of substances, but with a wide range of variations, are needed, for example, in the context of drug discovery and development in pharmaceutics and biomedicine.
  • the quantities of substances and times required for sequencing proteins or DNA sections can be further reduced.
  • the proteins or DNA sections are bound to beads and analyzed stepwise during the passage of various reaction chambers.
  • the device according to the invention can by additional components be extended for detection, such as magnetoelectric [16], by (integrated) optical systems [2] or electrochemical [17].
  • a combination of synthesis, reaction and analysis can also be carried out with the device according to the invention. For example, molecules can be synthesized in a first area, exposed to various substances in a subsequent area, and then directly analyzed.
  • sensors can be introduced into the reaction chambers or the fluid channels to more precisely control the reactions.
  • FIG. 1 System elements and principle for magnetic ratchet Fig. 2 Exemplary microstructure for generating an inhomogeneous magnetic field
  • FIG. 4 Exemplary Production of a Fluid Structure
  • FIG. 5 Exemplary Production of a Bond Connection
  • FIG. 6 Exemplary Construction of a Device According to the Invention
  • Fig. 1 shows a schematic sectional view of the essential elements and the principle of a fluidic ratchet.
  • an actuator 1 for generating a fluid flow 8 in the fluid channels 6.
  • the fluid flow 8 moves the beads 4. Equipped with a mixing chamber volume 3 and a microstructured soft iron magnetic core 2 for generating a magnetic blocking force.
  • the device is completed with a housing 5.
  • the fluid moves 8 and with him the beads 7. If the blocking force is turned on, the beads are fixed in the direction of magnetic structure. 9
  • FIG. 2 shows a schematic sectional view with the field lines 10 of an inhomogeneous magnetic field which has been switched on, produced by an NEN soft iron magnetic core 2 in microstructure is embedded in plastic 11.
  • the magnetic beads 4 are fixed from the fluid-filled channel 6 direction 9 magnetic core 12.
  • FIG. 3 shows, by way of example, the schematic illustration of the production of the soft-magnetic microstructure in which an electroplating start layer 16 is deposited on substrate 13 (for example silicon or glass), then resist 15 is applied by spin coating and patterned, followed by electroplating with, for example Permalloy (NiFe in the ratio (80/20) and the spin coating of the sealing layer 14.
  • substrate 13 for example silicon or glass
  • resist 15 is applied by spin coating and patterned, followed by electroplating with, for example Permalloy (NiFe in the ratio (80/20) and the spin coating of the sealing layer 14.
  • FIG. 4 shows, by way of example, the schematic production of a microfluidic channel structure " .8 Openings 19, which serve to supply fluid, are introduced into the substrate 13. These holes can be introduced mechanically (for example drilling, lasing), wet-chemically or by reactive ion etching.
  • the trench structures are formed by structuring (stripping) the resist spun onto the substrate (for example SU8, PMMA, polyimide).
  • FIG. 5 shows the bonding of the structures produced in FIG. 3 and FIG. 4 by pressure 20 and heat 20, thereby creating the microfluidic channel structures 21.
  • FIG. 6 shows an exemplary embodiment of a device according to the invention consists of a microstructured magnet, a microfluidic channel structure, an actuator and fluidic connections.
  • the supervision of this system shows the fluidic structures.
  • the time required for bead transport 8 periodic fluid movement 7 is generated by an actuator 1, which is located at the beginning of the fluid system.
  • an actuator 1 located at the beginning of the fluid system.
  • the beads are introduced into the system and after the fluidic ratchet principle [Fig. 1] moves through the microfluidic channel.
  • a compensation chamber 24 at the end of the fluid structure with a free liquid level allows the periodic movement.
  • the residence time of the beads 4 can be regulated by the geometric shape, where column structures lead the beads 4 there.
  • the beads are collected and rinsed out if necessary.
  • the reaction substances are fed perpendicularly to the direction of movement via the microfluidic fluid guide.
  • introduction 26 and branch 22 the filling of the chambers is facilitated and also allows a continuous regulation of the substance concentration.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Dispersion Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Hematology (AREA)
  • Clinical Laboratory Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

The aim of the invention is to create a device that provides a microfluidic system in which particle fractions (beads) can be guided in a serial and directed manner through ducts and reactions chambers without creating a net fluid movement. Said aim is achieved by combining a small-scale fluid movement that causes the particles to move with a switchable force (blocking force) which fixes the particles. The inventive device can be used in bioanalysis or chemical synthesis.

Description

Mikroreaktormicroreactor
Die Erfindung betrifft eine Vorrichtung zum Transport von mindestens einer magnetischen Partikelfraktion durch ein mikrofluidisches System gemäß dem Oberbegriff des ersten Patentanspruchs.The invention relates to a device for transporting at least one magnetic particle fraction through a microfluidic system according to the preamble of the first claim.
Mikrofluidische Systeme sind zentrale Handlingsysteme für Fluide, wie Flüssigkeiten oder Gase, mit oder ohne Feststoffanteil in der Mikro- und Nanotechnologie und finden sich insbesondere im Bereich der Life Sciences oder Biomedizin, wo Nanoobjekte in Form großer Biomoleküle, wie z.B. Peptide oder Proteine, gehandhabt werden müssen [I]. Da eine direkte Handhabung solch kleiner Objekte selten möglich ist, wird im Bereich der Life Sciences häufig mit so genannten Beads gearbeitet. Beads sind Polymerkörper, meist Kugeln, an deren funktionalisierte Oberfläche z.B. DNA oder Proteine gebunden und so für eine Synthese oder Analyse handhabbar werden. In diesem wachsenden Markt werden schon heute kommerziell Geräte angeboten, mit denen Analysen mit Hilfe einzelner Beads vorgenommen werden [2] . Zudem existieren verschiedene auf Beads basierende Analyseverfahren bzw. -geraten, die einen hohen Grad an Parallelisierung aufweisen und mit Flüssigkeitsvolumen bis hinab zu 10 Mikrolitern arbeiten. Häufig werden zur gezielten Handhabung solcher Beads elektrische Felder [3] oder so genannte Laserpinzetten [4] [5] verwendet. Seltener werden in der Mikrotechnik magnetische Kräfte eingesetzt, da diese mikrotechnisch nur schwer zu erzeugen sind, wobei sich gerade magnetische Kräfte auf Grund der geringen Wechselwirkung mit biologischen Materialien und Prozessen besonders eignen [6] .Microfluidic systems are central handling systems for fluids, such as liquids or gases, with or without solids in micro- and nanotechnology, and are found particularly in the field of life sciences or biomedicine, where nano-objects in the form of large biomolecules, e.g. Peptides or proteins, must be handled [I]. Since direct handling of such small objects is seldom possible, so-called beads are often used in the field of life sciences. Beads are polymer bodies, usually spheres, on the functionalized surface of which e.g. DNA or proteins bound and so become manageable for synthesis or analysis. In this growing market, commercial devices are already being offered today, with which analyzes are carried out with the aid of individual beads [2]. In addition, there are several bead-based analytical methods or devices that have a high degree of parallelization and operate with liquid volumes as low as 10 microliters. Frequently, electrical fields [3] or so-called laser tweezers [4] [5] are used for the targeted handling of such beads. Magnetic forces are rarely used in microtechnology, as they are difficult to produce microtechnically, with magnetic forces being particularly suitable due to the low interaction with biological materials and processes [6].
Magnetische Beads werden heutzutage in der Biochemie standardmäßig verwendet und werden von etlichen kommerziellen Anbietern vertrieben (z.B. http://www.magneticmicrosphere.com/supply.htm) . Solche Beads sind in der Regel superparamagnetisch und auch monodispers mit Durchmessern von 1 μm bis 10 μm erhältlich und werden zu Analyse und Synthesezwecken verwendet. Die Handhabung magnetischer Mikrobeads kann im größeren Maßstab mit Hilfe so genannter Hochgradienten- Magnetseparatoren erfolgen [7] . Im Falle kleinerer Volumina erfolgt eine Abtrennung bzw. Fixierung magnetischer Mikrobeads in der Regel durch einfache Permanentmagnete auf Seltenerdbasis. Diese Vorgehensweise ist jedoch recht unflexibel und benötigt zum Lösen der Fixierung immer bewegliche Komponenten, die eine räumliche Trennung zwischen Reaktionsgefäß mit Magnetbeads und Permanentmagnet erlauben. Wesentlich flexibler ist dagegen eine Vorgehensweise, bei der die Magnetbeads in den Einflussbereich weichmagnetischer Strukturen gebracht werden. Zur Fixierung der Magnetbeads werden die Strukturen über ein äußeres Magnetfeld aufmagnetisiert. Zum Lösen muss lediglich das äußere Magnetfeld abgeschaltet werden, d.h. es ist keinerlei bewegliche Komponente notwendig. Ein entsprechender Aufbau wurde zur Abtrennung von Magnetbeads aus so genannten Mikrotiterplatten entwickelt und patentiert [DE 10 057 396] .Magnetic beads are commonly used in biochemistry today and are distributed by several commercial vendors (eg http://www.magneticmicrosphere.com/supply.htm). Such beads are usually superparamagnetic and monodisperse with diameters from 1 micron to 10 microns available and are used for analysis and synthesis purposes. The handling of magnetic microbeads can be done on a larger scale with the help of so-called high-gradient magnetic separators [7]. In the case of smaller volumes, a separation or fixation of magnetic microbeads usually takes place by simple permanent magnets based on rare earths. However, this approach is quite inflexible and requires to release the fixation always moving components that allow a spatial separation between the reaction vessel with Magnetbeads and permanent magnet. By contrast, a procedure in which the magnetic beads are brought into the area of influence of soft magnetic structures is considerably more flexible. To fix the magnetic beads, the structures are magnetized via an external magnetic field. To release only the external magnetic field has to be switched off, ie no moving component is necessary. A corresponding structure was developed and patented for the separation of magnetic beads from so-called microtiter plates [DE 10 057 396].
Kritischer Punkt bei der Arbeit mit biochemischen Stoffen in der Bio- und Pharmaforschung sind die hohen Kosten der zum Teil durch aufwendige Syntheseverfahren hergestellten Substanzen. Die eigentlichen Untersuchungen erfordern nur geringe Materialmengen wie neue Analyseverfahren zeigen (z.B. Genechip©, der Fa. Affymetrix, www.affymetrix.com), jedoch ist eine sparsame Handhabung dieser Stoffe schwierig. Mikrofluidische Systeme bieten sich auf Grund ihres geringen Totvolumens für die Arbeit mit solchen Stoffen an. Dieser Vorteil vermindert sich jedoch, wenn zur Einbringung eines neuen Stoffes in das mikrofluidische System, das System komplett gespült werden muss .Critical point in the work with biochemical substances in biopharmaceutical and pharmaceutical research are the high costs of the substances produced in part by elaborate synthesis methods. The actual investigations require only small quantities of material, as new analysis methods show (for example Genechip ©, the company Affymetrix, www.affymetrix.com), but an economical handling of these substances is difficult. Microfluidic systems are ideal for working with such materials due to their low dead volume. However, this advantage diminishes when it is necessary to flush the system completely to introduce a new substance into the microfluidic system.
Aufgabe der Erfindung ist daher, die Bereitstellung eines mikroflui- dischen Systems, in dem Partikelfraktionen (Beads) seriell und gerichtet durch Kanäle und Reaktionskammern geführt werden ohne dass eine Nettobewegung des Fluids erfolgt.The object of the invention is therefore to provide a microfluidic system in which particle fractions (beads) are guided serially and directionally through channels and reaction chambers without a net movement of the fluid taking place.
Die Aufgabe wird durch eine Vorrichtung mit den Merkmalen des ersten Patentanspruchs gelöst. Die Unteransprüche geben vorteilhafte Ausgestaltungen wieder.The object is achieved by a device having the features of the first patent claim. The dependent claims give advantageous embodiments again.
Stofftransport in fluidischen Systemen erfolgt gewöhnlich über die Bewegung des Fluids, mit dem darin enthaltene Stoffe zu verschiedenen Orten bewegt werden.Mass transfer in fluidic systems usually takes place via the movement of the fluid, with which the substances contained therein are moved to different locations.
Der Stofftransport innerhalb der erfindungsgemäßen Vorrichtung erfolgt nicht wie üblich durch das strömende Fluid, sondern durch den Transport der Beads nach dem Prinzip einer „fluidischen Ratsche".The mass transfer within the device according to the invention is not carried out as usual by the flowing fluid, but by the Transport of the beads on the principle of a "fluidic ratchet".
Durch Erzeugung einer Sperrkraft während der Bewegung des Fluids, können die Beads fixiert werden.By generating a blocking force during the movement of the fluid, the beads can be fixed.
Ratsche ist die Bezeichnung für eine Vorrichtung z. B. Werkzeug bei dem eine Sperrvorrichtung nur eine Bewegungsrichtung (Freilauf) zu- lässt, in Gegenrichtung sperrt sie und bewegt einen Gegenstand z. B. Schraube oder Gurt. Die Bewegungsrichtungen können umkehrbar sein. Die erfindungsgemäße Vorrichtung beinhaltet, die Bereitstellung eines mikrofluidischen Systems, in dem Partikelfraktionen (Beads) seriell und gerichtet durch Kanäle und Reaktionskammern geführt werden können, ohne dass eine größerskalige Fluidbewegung erfolgt. Dazu wird eine kleinskalige Fluidbewegung, die eine Bewegung der Partikel bewirkt, mit einer schaltbaren Krafteinwirkung (Sperrkraft) kombiniert, welche die Partikel fixiert zumindest aber die Bewegungsgeschwindigkeit der Partikel deutlich vermindert. Die Fluidbewegung kann dabei mechanisch oder auch elektrisch (z.B. Elektroosmose) erzeugt werden. Die Sperrkraft kann erzeugt werden durch magnetischer Felder, die auf magnetische Beads wirken, durch elektrische Felder, die aufgrund der Dielektrizitätszahlunterschiede von Fluid und Partikeln (Dielektrophorese, Elektrostatik) wirken, durch optische Felder, die entsprechend der Laserpinzette aus Brechungseffekten Kräfte generieren, durch elektrochemisch induzierte Oberflächenkräfte, die an die Beadoberflachen ankoppeln.Ratchet is the name for a device z. B. tool in which a locking device allows only one direction of movement (freewheel), in the opposite direction it locks and moves an object z. B. screw or belt. The directions of movement can be reversible. The device according to the invention involves the provision of a microfluidic system in which particle fractions (beads) can be guided serially and directionally through channels and reaction chambers without a larger-scale fluid movement taking place. For this purpose, a small-scale fluid movement, which causes a movement of the particles, combined with a switchable force (blocking force), which at least fixed but at least significantly reduces the speed of movement of the particles. The fluid movement may be generated mechanically or electrically (e.g., electro-osmosis). The blocking force can be generated by magnetic fields acting on magnetic beads, by electrochemical induced electro fields induced by electrostatic fields due to dielectric constant differences of fluid and particles (dielectrophoresis, electrostatics) by optical fields generating forces due to refractive effects according to laser tweezers Surface forces that attach to the bead surfaces.
Ein Aktor erzeugt eine periodische, kleinskalige Vor- und Rückbewegung (Freilauf) des Fluids in dem Kanalsystem. Durch Erzeugung eines inhomogenen Magnetfeldes (Sperrvorrichtung) während der Rückbewegung des Fluids, können die Beads während der Rückbewegung fixiert werden. Aufgrund der Fixierung während der Rückbewegung des Fluids und der Lösung der Fixierung während der Vorwärtsbewegung resultiert eine gerichtete Bewegung der Beads durch das Kanalsystem, ohne dass eine Nettobewegung des Fluids erfolgt. Die Bewegungsrichtungen können umgekehrt werden.An actuator generates a periodic, small-scale forward and backward movement (freewheeling) of the fluid in the channel system. By generating an inhomogeneous magnetic field (blocking device) during the return movement of the fluid, the beads can be fixed during the return movement. Due to the fixation during the return movement of the fluid and the solution of the fixation during the forward movement, a directed movement of the beads through the channel system results without a net movement of the fluid. The directions of movement can be reversed.
Superparamagnetische Partikel werden in ein fluidisches Kanalsystem eingebracht. Solange keine anderen Kräfte auf diese Partikel wirken, werden diese Partikel mit jeder Bewegung des Fluids im Kanalsystem mitgeführt. Wird bei einer periodischen Fluidbewegung eine Bewegungsrichtung der Partikel gesperrt kommt es zu einem Transport der Partikel in eine Richtung. Das umgebende Fluid wird durch diese periodische Bewegung nur um den Volumenbetrag der Partikel in umgekehrter Richtung bewegt. Die periodische Bewegung des Fluids führt ansonsten zu keiner wesentlichen Vermischung, da in kleinsten Kanalsystemen eine turbulente Mischung nur extrem schwer zu erreichen ist. Das Volumen der Reaktionskammern ist äußerst gering, wodurch die benötigte Menge an Reaktanden sehr gering ist. Es werden Kanalabmessungen von einigen Mikrometern und Volumina der Reaktionskammern im Nanoliterbe- reich erreicht.Superparamagnetic particles are introduced into a fluidic channel system. As long as no other forces act on these particles, These particles are carried along with every movement of the fluid in the channel system. If a movement direction of the particles is blocked during a periodic fluid movement, the particles are transported in one direction. The surrounding fluid is moved by this periodic movement only by the volume amount of the particles in the reverse direction. The periodic movement of the fluid otherwise leads to no significant mixing, since in the smallest channel systems, a turbulent mixture is extremely difficult to achieve. The volume of the reaction chambers is extremely low, whereby the required amount of reactants is very low. Channel dimensions of a few micrometers and volumes of the reaction chambers in the nanoliter range are achieved.
Magnetische KräfteMagnetic forces
Um eine Beadbewegung nach dem Prinzip einer fluidischen Ratsche zu erzeugen müssen ausreichend große magnetische Kräfte erzeugt werden und geeignete magnetische Beads zu Verfügung stehen. Die magnetische Sperrkraft auf die superparamagnetischen Partikel sollte vorzugsweise im Bereich von 10-100 pN liegen. Wobei sich die magnetische Kraft auf die Partikel zum einem aus dem Volumen sowie der Suszeptibilität der Partikel und zum anderen aus dem Produkt aus Feldstärke mal Gradient des Magnetfeldes ergibt. Während die erreichbaren Feldstärken sich auf den Bereich von wenigen Tesla beschränken, können durch weichmagnetische Mikrostrukturen auf kurze Distanzen sehr hohe Feldgradienten erzeugt werden.In order to create a bead movement on the principle of a fluidic ratchet sufficiently large magnetic forces must be generated and suitable magnetic beads are available. The magnetic blocking force on the superparamagnetic particles should preferably be in the range of 10-100 pN. The magnetic force on the particles results from the volume and the susceptibility of the particles as well as from the product of field strength times the gradient of the magnetic field. While the achievable field strengths are limited to a few teslas, very soft field micrographs can generate very high field gradients over short distances.
Die magnetische Haltekraft wird durch unmittelbar an den Fluidbereich grenzende, weichmagnetische Mikrostrukturen erreicht, die ein extern erzeugtes Magnetfeld verzerren. Die kleinsten, lateralen Abmessungen dieser Strukturen sollten dabei etwa dem Durchmesser der verwendeten Beads entsprechen, während die vertikalen Abmessungen das drei bis zehnfache betragen sollte. Die Herstellung erfolgt nach der Re- siststrukturierung mit Maskentechnik durch Aufgalvanisieren. Anschließend werden die Strukturen mit Kunststoff eingegossen. Der Kunststoff erfüllt dabei zwei Funktionen. Zum einen werden entsteht dadurch eine ebene Oberfläche, welche die Beadbewegung nicht beein- trächtigt. Zum anderen dient der Kunststoff als Bondpartner für dasThe magnetic holding force is achieved by soft magnetic microstructures immediately adjacent to the fluid region, which distort an externally generated magnetic field. The smallest, lateral dimensions of these structures should correspond approximately to the diameter of the beads used, while the vertical dimensions should be three to ten times. The production takes place after resist structuring with mask technique by electroplating. Subsequently, the structures are cast with plastic. The plastic fulfills two functions. On the one hand, this creates a flat surface, which does not affect the bead movement. adversely. On the other hand, the plastic serves as a bonding partner for the
Gehäuseteil mit den fluidischen Kanalstrukturen.Housing part with the fluidic channel structures.
Beispielhafte Herstellung einer weichmagnetischen MikrostrukturExemplary production of a soft magnetic microstructure
1. Auf Substrat (Silizium oder Glas) Galvanikstartschicht abscheiden1. Deposit on substrate (silicon or glass) electroplating start layer
2. Resist aufschleudern und strukturieren2. Spin up the resist and structure it
3. NiFe-Galvanik3. NiFe electroplating
4. Siegelschicht aufschleudern4. Spin on the sealing layer
Wesentlich für den Einsatz von magnetischen Kräften in Mikrometerabmessungen ist die Erzeugung von stark inhomogenen Magnetfeldern, es ist gezeigt das schon ohne weichmagnetische Mikrostrukturen die >10pN für 4μm Partikel erreicht werden können [9] . Durch den Einsatz von weichmagnetischen Mikrostrukturen können die Partikel noch deutlich kleiner oder das Hintergrundmagnetfeld schwächer sein. Geeignet sind dazu u. a. weichmagnetische Strukturen aus Permalloy (80%Ni und 20%Fe) . So können etwa Permalloy-Säulen mit einem Durchmesser von 5 μm und einer Höhe von 90 μm durch Röntgenlithographie und Galvanik mit einer Sättigungsmagnetisierung von 0, 93 T hergestellt werden [10] .Essential for the use of magnetic forces in micrometer dimensions is the generation of highly inhomogeneous magnetic fields, it is shown that even without soft magnetic microstructures the> 10pN for 4μm particles can be achieved [9]. By using soft magnetic microstructures, the particles can be much smaller or the background magnetic field weaker. Suitable are u. a. soft magnetic structures made of permalloy (80% Ni and 20% Fe). For example, Permalloy columns with a diameter of 5 μm and a height of 90 μm can be produced by X-ray lithography and electroplating with a saturation magnetization of 0.93 T [10].
Fluidisches SystemFluidic system
Der fluidische Transport von Partikeln durch Kanäle und entlang von Oberflächen wird schon seit vielen Jahrzehnten untersucht und ist eingehend beschrieben [11] .The fluid transport of particles through channels and along surfaces has been studied for many decades and is described in detail [11].
Die Partikelbewegung hängt dabei neben den geometrischen Größen und den wirkenden Oberflächenkräften von der Strömungsgeschwindigkeit des Fluids ab, und lässt sich mit Kugeln [12] aber auch biologischen Einheiten wie Zellen gut realisieren [13] . Bilden sich bei der periodischen Fluidbewegung keine Turbulenzen, wird erwartet, dass der Stofftransport innerhalb des Fluids nicht deutlich größer als die Diffusionsgeschwindigkeit ist. Wie die umfangreiche Literatur im Bereich der Mikromischer zeigt [14] [8] , ist auch das beabsichtigte Herbeiführen von Turbulenzen in mikrofluidischen Systemen schwer zu erreichen. Die erfindungsgemäße Vorrichtung erfüllt hierzu verschiedene Anforderungen. Die Fluidbewegung muss groß genug sein, um Partikel durch das Fluid zu bewegen. Dazu sind im Kanalsystem Strömungsgeschwindigkeiten von etwa 1 - 10 mm/s notwendig. Dabei hängt die Geschwindigkeit derIn addition to the geometric parameters and the surface forces, the particle motion depends on the flow velocity of the fluid, and can be well realized with spheres [12] as well as biological entities such as cells [13]. If no turbulences are formed during the periodic fluid movement, it is expected that the mass transfer within the fluid will not be significantly greater than the diffusion rate. As the extensive literature in the field of micromixers shows [14], [8] the intended induction of turbulence in microfluidic systems is difficult to achieve. The device according to the invention fulfills various requirements for this purpose. The fluid movement must be large enough to move particles through the fluid. These are in the channel system flow rates of about 1 - 10 mm / s necessary. The speed of the
Partikel in den Fluidkanälen von dem Verhältnis Kanalgröße zu Partikelgröße, der Fluidgeschwindigkeit, der Haftung der Partikel an den Kanalwänden und der Form der Partikel ab.Particles in the fluid channels from the ratio of channel size to particle size, the fluid velocity, the adhesion of the particles to the channel walls and the shape of the particles from.
Die Fluidkanäle müssen so gestaltet sein, dass eine periodische FIu- idbewegung innerhalb der fluidischen Strukturen sich gut ausbreiten kann. Wichtig ist dabei, dass das System hinreichend inkompressible ist und die Fluidbewegung nicht elastisch speichert. Da die Strömungsgeschwindigkeit und damit auch die Bewegung der Beads von dem Kanalquerschnitt abhängt, kann die Fließgeschwindigkeit auch innerhalb des Systems variiert werden. So kann eine Verbreiterung des Kanalquerschnittes im Bereich der Reaktionskammern die Aufenthaltsdauer verlängern. Das Befüllen der Reaktionskammern und das kontinuierlich Nachliefern von Reaktionsstoffen werden durch ein langsames Durchströmen der Reaktionskammern senkrecht zur Bewegungsrichtung der Beads gewährleistet. Dies ermöglicht auch das komplette auswechseln der Inhaltsstoffe einzelner Reaktionskammern.The fluid channels must be designed so that a periodic fluid movement within the fluidic structures can spread well. It is important that the system is sufficiently incompressible and does not store the fluid movement elastically. Since the flow rate and thus also the movement of the beads depends on the channel cross-section, the flow rate can also be varied within the system. Thus broadening of the channel cross-section in the region of the reaction chambers can extend the residence time. The filling of the reaction chambers and the continuous supply of reactants are ensured by a slow flow through the reaction chambers perpendicular to the direction of movement of the beads. This also allows the complete replacement of the ingredients of individual reaction chambers.
Die fluidischen Kanäle sollten einen Querschnitt haben, der in etwa der Beadgröße entspricht. So sollte zum Beispiel, die Kanalbreite und Höhe bei einer Beadgröße von 4 μm nicht größer als 10 μm sein. Strukturen mit diesen Abmessungen lassen sich sowohl photo- als auch rönt- genlithographisch herstellen. Welches Verfahren am besten geeignet ist hängt von der erforderlichen Strukturqualität und den geeigneten Kunststoffen ab.The fluidic channels should have a cross-section that approximately corresponds to the bead size. For example, with a bead size of 4 μm, the channel width and height should not exceed 10 μm. Structures with these dimensions can be produced both by photolithography and X-ray lithography. Which method is most suitable depends on the required structural quality and the suitable plastics.
Die Herstellung von Mikrostrukturen erfolgt auf vielfältige Weise: mit optischer Lithographie (SU8, Polyimid) , durch Heißprägen (Formeinsatzherstellung durch LIGA-Verfahren oder Zerspanungstechnik) oder durch Röntgentiefen-Lithographie. Dadurch ist man in der Lage auch höchste Anforderung an Strukturabmessungen, bis in den Submikrometer- bereich, Seitenwandrauhigkeiten mit optischer Qualität und Aspektverhältnisse von 20 und mehr zu realisieren.The production of microstructures is carried out in many ways: with optical lithography (SU8, polyimide), by hot stamping (mold insert production by LIGA method or machining technique) or by X-ray deep lithography. As a result, it is possible to meet even the highest demands on structural dimensions, down to the submicrometer range, with optical quality of sidewall roughnesses and aspect ratios of 20 or more.
Bondenbonding
Eine durch das Fluid erzeugte Beadbewegung innerhalb des fluidischenA bead movement within the fluidic fluid generated by the fluid
Systems erfordert eine gute Ausbreitung der Fluidbewegung innerhalb des Flυidbereiches. Lufteinschlüsse oder Deformationen der Mikrostrukturen würden stören und müssen vermieden werden. Weiterhin führen Schwankungen der Kanalgeometrie zu Änderungen der Strömungsgeschwindigkeit. Daher ist die Herstellung einer druckfesten Bondverbindung mit geringer Varianz der Bondbereichdicke wichtig. Für KunststoffStrukturen eignen sich dazu Siegelverfahren bei denen dünne Siegelschichten durch Photodegradation (s. o.) oder Aufschleudern erzeugt und anschließend durch Druck und Wärme in einer entsprechenden Bondvorrichtung verbunden werden.Systems requires good propagation of fluid movement within of the fluid area. Air pockets or deformations of the microstructures would interfere and must be avoided. Furthermore, variations in the channel geometry lead to changes in the flow velocity. Therefore, it is important to make a pressure-resistant bond with little variation in bond area thickness. For plastic structures, sealing processes are suitable in which thin sealing layers are produced by photodegradation (see above) or spin-coating and then connected by pressure and heat in a corresponding bonding device.
Mit Hilfe von Bondverfahren ist es möglich auch deutlich kleinere fluidische Strukturen als bisher mit typischen Kanalquerschnitten von 50 μm x 50 μm herzustellen.With the help of bonding methods, it is also possible to produce much smaller fluidic structures than before with typical channel cross-sections of 50 μm x 50 μm.
Aktoractuator
Für den Aufbau der erfindungsgemäßen Vorrichtung ist mindestens an einer Stelle mikrofluidische Aktorik notwendig. Zum einen muss eine periodische Fluidbewegungen erzeugt werden, und / oder erfordert die Arbeit mit geringsten Stoffmengen, zum Beispiel eine Dosiervorrichtungen mit schnellen SchaltZeiten. Für beide Aufgaben eignen sich zum Beispiel Piezoaktoren. So steht ein piezogetriebenes Mikroventil mit Schaltzeiten von weniger als 2 ms, dessen Aufbauprinzip [DE 199 49 912] sich ebenfalls für die Erzeugung eines periodischen Hubes eignet, zur Verfügung.For the construction of the device according to the invention microfluidic actuators is necessary at least at one point. Firstly, a periodic fluid movements must be generated, and / or requires the work with minimal amounts of material, for example, a metering devices with fast switching times. Piezo actuators are suitable for both tasks, for example. Thus, a piezo-operated microvalve with switching times of less than 2 ms, whose design principle [DE 199 49 912] is likewise suitable for generating a periodic stroke, is available.
Besondere Vorteile dieser Aktoren liegt in den kurzen Schaltzeiten (typischer Wert eine Millisekunde) und der großen dabei erzeugten Kraft. Die Einkopplung der mechanischen Bewegung in das System kann entweder direkt oder über Übersetzungssystem erfolgen. Alternativ können Aktoren über Druck-Feder-Systeme oder durch Wellen an elektrisch betriebene Motoren dargestellt werden.Particular advantages of these actuators lies in the short switching times (typically one millisecond) and the large force generated thereby. The coupling of the mechanical movement into the system can take place either directly or via a translation system. Alternatively, actuators can be represented via pressure spring systems or by shafts to electrically operated motors.
Anschlusskonzept Fluidzuführung/ProduktentnähmeConnection concept of fluid supply / Produktentnähme
Das Funktionsprinzip der erfindungsgemäßen Vorrichtung erfordert eine periodische Fluidbewegung, die nur effizient genutzt werden kann, wenn das System inkompressible ist und das Fluid nur am Ausgang eine frei bewegliche Grenzfläche besitzt (z.B. Gasblase) . Dies erfordert — starre Fluidzuführung oder hohe Strömungswiderstände im Fluidzufüh- rungsbereich. Weiterhin ist jederzeit eine einfache Bead-Entnahme möglich. Dazu werden die Beads in mindestens einer Kammer gesammelt und bei Bedarf ausgeschwemmt.The functional principle of the device according to the invention requires a periodic fluid movement, which can only be used efficiently if the system is incompressible and the fluid has only a freely movable interface at the exit (eg gas bubble). This requires Rigid fluid supply or high flow resistance in the fluid supply area. Furthermore, a simple Bead-removal is possible at any time. For this purpose, the beads are collected in at least one chamber and flushed out as needed.
Die Synthese von Proteinen, Peptiden u. a. gewinnt in den letzten Jahren zunehmend an Bedeutung. Dabei ist nicht nur die kostengünstige Erzeugung großer Stoffmengen technisch interessant, sondern auch Methoden einer flexiblen Erzeugung kleiner Stoffmengen, die mit geringsten Mengen meist äußerst teurer Vorprodukte auskommen. Die benötigten Stoffmengen betragen dabei nur wenige Nanogramm, so dass bereits für einen einfachen Prototyp des Biosynthesereaktors mit der Produktion ausreichender Substanzmengen zu rechnen ist. Hierdurch ist eine Qualifizierung und Quantifizierung der Synthesereaktion bei Variation der Prozessparameter möglich. Bei einer auf magnetischen Beads adaptierten Merrifield-Festphasensynthese (AMS) werden gezielt Peptide erzeugt. An mit spezifisch spaltbaren Abstandshaltern (Spacer) versehenen Beads welche an Ihrem Ende die Ausgangsmoleküle für die AMS tragen wird mittels der erfindungsgemäßen Vorrichtung die AMS bis zur gewünschten Peptidlänge durchgeführt. Hierzu werden die Beads durch die einzelnen Reaktionsbereiche der Vorrichtung geführt. Die erfindungsgemäße Vorrichtung erlaubt für Zwecke bei denen nur kleine Stoffmengen benötigt werden, eine schnelle und Material sparende Synthese von komplexen Molekülen, zum Beispiel Peptide, Proteine, Oligonukleotide, DNA, Oligosaccharide oder RNA, deren Synthese durch sukzessive Einzelreaktionen erfolgt. Kleine Stoffmengen, jedoch in großer Variationsbreite, werden zum Beispiel im Rahmen der Wirk- stofffindung und Entwicklung in der Pharmazeutik und Biomedizin benötigt.The synthesis of proteins, peptides and the like a. has become increasingly important in recent years. It is not only the cost-effective production of large amounts of material technically interesting, but also methods of flexible production of small amounts of material that get along with very small amounts usually extremely expensive precursors. The required amounts of substance are only a few nanograms, so that even for a simple prototype of the biosynthetic reactor with the production of sufficient amounts of substance is to be expected. This makes it possible to qualify and quantify the synthesis reaction when the process parameters are varied. In a Merrifield solid phase synthesis (AMS) adapted to magnetic beads, targeted peptides are generated. To beads with specifically cleavable spacers (spacer) which carry at their end the starting molecules for the AMS is carried out by means of the device according to the invention, the AMS to the desired peptide length. For this purpose, the beads are guided through the individual reaction areas of the device. The device according to the invention allows for purposes in which only small amounts of material are needed, a fast and material-saving synthesis of complex molecules, for example peptides, proteins, oligonucleotides, DNA, oligosaccharides or RNA, whose synthesis is carried out by successive individual reactions. Small quantities of substances, but with a wide range of variations, are needed, for example, in the context of drug discovery and development in pharmaceutics and biomedicine.
Unter Einsatz der erfindungsgemäßen Vorrichtung, lässt sich die zur Sequenzierung von Proteinen oder DNA-Abschnitten benötigten Substanzenmengen und Zeiten weiter verringern. Hierzu werden die Proteine oder DNA-Abschnitte an Beads gebunden und im Verlauf der Passage verschiedener Reaktionskammern schrittweise analysiert werden. Die erfindungsgemäße Vorrichtung kann dabei durch zusätzliche Komponenten zur Detektion erweitert werden-, wie z.B. magnetoelektrisch [16], durch (integrierte) optische Systeme [2] oder elektrochemisch [17] . Auch eine Kombination von Synthese, Reaktion und Analyse können mit der erfindungsgemäßen Vorrichtung durchgeführt werden. So können in einem ersten Bereich Moleküle synthetisiert werden, in einem darauf folgenden Bereich verschiedenen Substanzen ausgesetzt und anschließend diese direkt analysiert werden. Des Weiteren können Sensoren in die Reaktionskammern oder die Fluidkanäle eingebracht werden um die Reaktionen präziser zu steuern.Using the device according to the invention, the quantities of substances and times required for sequencing proteins or DNA sections can be further reduced. For this purpose, the proteins or DNA sections are bound to beads and analyzed stepwise during the passage of various reaction chambers. The device according to the invention can by additional components be extended for detection, such as magnetoelectric [16], by (integrated) optical systems [2] or electrochemical [17]. A combination of synthesis, reaction and analysis can also be carried out with the device according to the invention. For example, molecules can be synthesized in a first area, exposed to various substances in a subsequent area, and then directly analyzed. Furthermore, sensors can be introduced into the reaction chambers or the fluid channels to more precisely control the reactions.
Die Erfindung sowie dessen Details werden im Folgenden beispielhaft an Ausführungsformen anhand von Figuren näher erläutert. Es zeigenThe invention and its details are explained in more detail below by way of example with reference to embodiments with reference to figures. Show it
Fig. 1 Systemelemente und Prinzip für magnetische Ratsche Fig. 2 Beispielhafte Mikrostruktur zur Erzeugung eines inhomogenen MagnetfeldsFig. 1 System elements and principle for magnetic ratchet Fig. 2 Exemplary microstructure for generating an inhomogeneous magnetic field
Fig. 3 Beispielhafte Herstellung weichmagnetischer MikrostrukturenFig. 3 Exemplary production of soft magnetic microstructures
Fig. 4 Beispielhafte Herstellung einer Fluidstruktur Fig. 5 Beispielhafte Herstellung einer Bondverbindung Fig. 6 Beispielhafter Aufbau einer erfindungsgemäßen VorrichtungFIG. 4 Exemplary Production of a Fluid Structure FIG. 5 Exemplary Production of a Bond Connection FIG. 6 Exemplary Construction of a Device According to the Invention FIG
Fig. 1 zeigt eine schematische Schnittdarstellung der wesentlichen Elemente und das Prinzip einer fluidischen Ratsche. Mit einem Aktor 1 zur Erzeugung einer Fluidströmung 8 in den Fluidkanälen 6. Die FIu- idströmung 8 bewegt die Beads 4. Ausgestattet mit einem Mischkammervolumen 3 und einem mikrostrukturiertem Weicheisenmagnetkern 2 zur Erzeugung einer magnetischen Sperrkraft. Abgeschlossen wird Vorrichtung mit einem Gehäuse 5. Je nach Bewegungsrichtung des Aktors 1 bewegt sich das Fluid 8 und mit Ihm die Beads 7. Wird die Sperrkraft eingeschaltet werden die Beads in Richtung Magnetstruktur fixiert 9.Fig. 1 shows a schematic sectional view of the essential elements and the principle of a fluidic ratchet. With an actuator 1 for generating a fluid flow 8 in the fluid channels 6. The fluid flow 8 moves the beads 4. Equipped with a mixing chamber volume 3 and a microstructured soft iron magnetic core 2 for generating a magnetic blocking force. The device is completed with a housing 5. Depending on the direction of movement of the actuator 1, the fluid moves 8 and with him the beads 7. If the blocking force is turned on, the beads are fixed in the direction of magnetic structure. 9
Fig. 2 zeigt eine schematische Schnittdarstellung mit den Feldlinien 10 eines eingeschalteten inhomogenen Magnetfeldes, erzeugt durch ei- nen Weicheisenmagnetkern 2 in Mikrosrtruktur der in Kunststoff 11 eingebettet ist. Die magnetischen Beads 4 werden aus dem Fluid gefüllten Kanal 6 Richtung 9 Magnetkern 12 fixiert.FIG. 2 shows a schematic sectional view with the field lines 10 of an inhomogeneous magnetic field which has been switched on, produced by an NEN soft iron magnetic core 2 in microstructure is embedded in plastic 11. The magnetic beads 4 are fixed from the fluid-filled channel 6 direction 9 magnetic core 12.
Fig. 3 zeigt beispielhaft die schematische Darstellung der Herstellung der weichmagnetischen Mikrostruktur, in dem auf Substrat auf Substrat 13 (zum Beispiel Silizium oder Glas) eine Galvanikstartschicht 16 abgeschieden wird, dann Resist 15 aufschleudert und strukturiert wird, danach erfolgt die Galvanik, mit zum Beispiel Permalloy (NiFe im Verhältnis (80/20) und das aufschleudern der Siegelschicht 14.3 shows, by way of example, the schematic illustration of the production of the soft-magnetic microstructure in which an electroplating start layer 16 is deposited on substrate 13 (for example silicon or glass), then resist 15 is applied by spin coating and patterned, followed by electroplating with, for example Permalloy (NiFe in the ratio (80/20) and the spin coating of the sealing layer 14.
Fig. 4 zeigt beispielhaft die schematische Herstellung einer mikrofluidischen Kanalstruktur ".8. In das Substrat 13 werden Öffnungen 19 eingebracht, die der Fluidzuführung dienen. Diese Löcher können mechanisch (zum Beispiel Bohren, Lasern), nasschemisch oder auch durch reaktives Ionenätzen eingebracht werden. Die Grabenstrukturen entstehen durch die Strukturierung (Strippen) des auf dem Substrat aufgeschleuderten Resists (zum Beispiel SU8, PMMA, Polyimid) .4 shows, by way of example, the schematic production of a microfluidic channel structure " .8 Openings 19, which serve to supply fluid, are introduced into the substrate 13. These holes can be introduced mechanically (for example drilling, lasing), wet-chemically or by reactive ion etching. The trench structures are formed by structuring (stripping) the resist spun onto the substrate (for example SU8, PMMA, polyimide).
Fig. 5 zeigt das Bonden der Strukturen hergestellt in Fig 3 und Fig 4 durch Druck 20 und Wärme 20, dadurch entstehen die mikrofluidischen Kanalstrukturen 21.FIG. 5 shows the bonding of the structures produced in FIG. 3 and FIG. 4 by pressure 20 and heat 20, thereby creating the microfluidic channel structures 21.
Fig. 6 zeigt eine beispielhafte Ausführungsform einer erfindungsgemäßen Vorrichtung besteht aus einem mikrostrukturierten Magneten, einer mikrofluidischen Kanalstruktur, einem Aktor sowie aus fluidischen Anschlüssen.6 shows an exemplary embodiment of a device according to the invention consists of a microstructured magnet, a microfluidic channel structure, an actuator and fluidic connections.
Die Aufsicht auf dieses System zeigt die fluidischen Strukturen. Die zum Beadtransport 8 notwendige periodische Fluidbewegung 7 wird durch ein Aktor 1 erzeugt, der am Anfang des Fluidsystems befindet. Durch eine Öffnung 28 werden die Beads in das System eingebracht und nach dem fluidischen Ratschenprinzip [Fig. 1] durch den mikrofluidischen Kanal bewegt. Eine Ausgleichkammer 24 am Ende der Fluidstruktur mit einem freien Flüssigkeitsspiegel ermöglicht die periodische Bewegung. In den Mischkammervolumen 25 kann die Aufenthaltszeit der Beads 4 durch die geometrische Form reguliert werden, wobei dort Säulenstrukturen die Beads 4 führen. Im letzten Mischkammervolumen 23 des Systems werden die Beads angesammelt und bei Bedarf ausgespült. In die Mischkammervolumen 25 werden senkrecht 27 zur Bewegungsrichtung die Reaktionsstoffe über die mikrofluidische Fluidführung zugeführt. Durch Einleitung 26 und Abzweigung 22 wird das Befüllen der Kammern erleichtert und auch eine kontinuierliche Regulierung der Stoffkonzentration ermöglicht. The supervision of this system shows the fluidic structures. The time required for bead transport 8 periodic fluid movement 7 is generated by an actuator 1, which is located at the beginning of the fluid system. Through an opening 28, the beads are introduced into the system and after the fluidic ratchet principle [Fig. 1] moves through the microfluidic channel. A compensation chamber 24 at the end of the fluid structure with a free liquid level allows the periodic movement. In the mixing chamber volume 25, the residence time of the beads 4 can be regulated by the geometric shape, where column structures lead the beads 4 there. In the last mixing chamber volume 23 of the system, the beads are collected and rinsed out if necessary. Into the mixing chamber volume 25, the reaction substances are fed perpendicularly to the direction of movement via the microfluidic fluid guide. Through introduction 26 and branch 22, the filling of the chambers is facilitated and also allows a continuous regulation of the substance concentration.
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BezugszeichenlisteLIST OF REFERENCE NUMBERS
1 Aktor1 actuator
2 Weicheisenmagnetkern in Mikrostruktur2 soft iron magnetic core in microstructure
3 Reaktionskammer3 reaction chamber
4 Magnetischer Bead4 magnetic bead
5 Gehäuse5 housing
6 Mikrofluidischer Kanal gefüllt mit einem Fluid6 Microfluidic channel filled with a fluid
7 Bewegungsrichtung der magnetischen Beads, abhängig von der Fluidströmung und der magnetischen Sperrkraft7 Movement direction of the magnetic beads, depending on the fluid flow and the magnetic blocking force
8 Erzeugte, gerichtete Fluidströmung8 Generated, directed fluid flow
9 Fixierungsrichtung der magnetischen Beads9 Fixing direction of the magnetic beads
10 Feldlinien10 field lines
11 Kunstcff oder andere geeigneten Polymere11 Kunstcff or other suitable polymers
12 Fixierung in Richtung des Weicheisenmagnetkerns12 Fixation in the direction of the soft iron magnetic core
13 Substrat13 substrate
14 Siegelschicht14 sealing layer
15 Resist15 resist
16 Galvanikschicht16 electroplated layer
17 Mikrostrukturierter Weicheisenmagnet17 Microstructured soft iron magnet
18 Mikrofluidischer Kanal18 Microfluidic channel
19 Öffnungen19 openings
20 Druck und/oder Wärme20 pressure and / or heat
21 Mikrofluidischer Kanal21 Microfluidic channel
22 Abzweigung22 diversion
23 Mischkammervolumen zum entnehmen der Beads23 mixing chamber volume for removing the beads
24 Öffnung als Ausgleichskammer24 Opening as compensation chamber
25 Mischkammervolumen25 mixing chamber volume
26 Einleitung26 Introduction
27 Transportrichtung der Reaktionsstoffe in der mikroflui- dischen Fluidführung27 Transport direction of the reactants in the microfluidic fluid guide
28 Öffnungen zum Einbringen der Beads ins mikrofluidische System 28 openings for introducing the beads into the microfluidic system

Claims

Patentansprüche claims
1. Vorrichtung zum Transport von mindestens einer magnetischen Partikelfraktion durch ein mikrofluidisches System umfassend, a) Mindestens einem mikrofluidischem Kanal mit einem Fluid, umfassend die magnetische Partikelfraktion, b) Mittel zur Erzeugung einer Fluidströmung axial zum mikroflui- dischem Kanal mit zwei Schaltstellungen entsprechend der beiden Fließrichtungen, c) hinzu schaltbares äußeres Magnetfeld im Kanal zur temporären Fixierung der magnetischen Partikelfraktionen, wobei in einem Betriebszustand ein zyklischer Wechsel der beiden Schaltstellungen erfolgt und wobei das Magnetfeld nur bei einer Schaltstellung hinzu geschaltet ist.1. A device for transporting at least one magnetic particle fraction through a microfluidic system comprising, a) at least one microfluidic channel with a fluid comprising the magnetic particle fraction, b) means for generating a fluid flow axially to the microfluidic channel with two switching positions corresponding to the two Flow directions, c) can be added external magnetic field in the channel for temporary fixation of the magnetic particle fractions, wherein in an operating condition, a cyclic change of the two switching positions takes place and wherein the magnetic field is connected only in a switching position.
2. Vorrichtung nach Anspruch 1 dadurch gekennzeichnet, dass der mikrofluidische Kanal in seiner vollen Länge an weichmagnetisches Material angrenzt.2. Apparatus according to claim 1, characterized in that the microfluidic channel adjacent to its full length of soft magnetic material.
3. Vorrichtung nach einem der Ansprüche 1 oder 2, dadurch gekennzeichnet, dass das der mikrofluidische System ganz oder teilweise durch optische Lithographie, Heißprägen, Spritzguss oder durch Röntgen-Lithographie in ein Substrat eingearbeitet ist.3. Device according to one of claims 1 or 2, characterized in that the microfluidic system is wholly or partially incorporated by optical lithography, hot stamping, injection molding or by X-ray lithography in a substrate.
4. Vorrichtung nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, dass das mikrofluidische System formschlüssigen mit einer Deckplatte verschlossen ist.4. Device according to one of claims 1 to 3, characterized in that the microfluidic system is positively closed with a cover plate.
5. Vorrichtung nach Anspruch 4, dadurch gekennzeichnet, dass die Deckplatte mindestens zwei durch den mikrofluidischen Kanal miteinander verbundenen Öffnungen aufweist.5. Apparatus according to claim 4, characterized in that the cover plate has at least two interconnected by the microfluidic channel openings.
6. Vorrichtung nach einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, dass das Mittel einen direkt auf das Fluid wirkenden Aktor umfasst.6. Device according to one of claims 1 to 5, characterized in that the means acting directly on the fluid Actuator includes.
7. Vorrichtung nach Anspruch 6, dadurch gekennzeichnet, dass der Aktor einen Piezo-Biegeaktor oder Druck-Feder-System umfasst.7. Apparatus according to claim 6, characterized in that the actuator comprises a piezo-bending actuator or pressure-spring system.
8. Vorrichtung nach einem der Ansprüche 1 bis 7, dadurch gekennzeichnet, dass die Vorrichtung mindestens einen weiteren mikrofluidische Fluidführung aufweist, welche den mikrofluidi- schen Kanal unter Bildung eines Mischkammervolumens kreuzt.8. Device according to one of claims 1 to 7, characterized in that the device comprises at least one further microfluidic fluid guide, which crosses the microfluidic channel to form a mixing chamber volume.
9. Vorrichtung nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, dass der mikrofluidische Kanal mindestens eine Einleitung oder Abzweigung für ein weiteres Fluid aufweist.9. Device according to one of claims 1 to 8, characterized in that the microfluidic channel has at least one introduction or branch for another fluid.
10. Verwendung der Vorrichtung gemäß einem der Ansprüche 1 bis 9 zur Durchführung einer Festphasensynthese an magnetischen Partikelfraktionen.10. Use of the device according to one of claims 1 to 9 for carrying out a solid phase synthesis of magnetic particle fractions.
11. Verwendung der Vorrichtung gemäß einem der Ansprüche 1 bis 9 zur Bioanalytik mit auf mindestens einer magnetischen Partikelfraktion fixierten Biomolekülen.11. Use of the device according to one of claims 1 to 9 for bioanalytics with fixed on at least one magnetic particle fraction biomolecules.
12. Verwendung nach Anspruch 11, dadurch gekennzeichnet, dass die Biomoleküle Proteine, Peptide, DNA, RNA oder Zellen, prokaryo- tisch oder eukaryotisch umfassen.12. Use according to claim 11, characterized in that the biomolecules comprise proteins, peptides, DNA, RNA or cells, prokaryotic or eukaryotic.
13. Verwendung der Vorrichtung gemäß einem der Ansprüche 1 bis 9 zur chemischen Analytik oder Produktion mit auf mindestens einer magnetischen Partikelfraktion fixierten chemischen Reaktanten oder Katalysatoren. 13. Use of the device according to one of claims 1 to 9 for chemical analysis or production with fixed on at least one magnetic particle fraction chemical reactants or catalysts.
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