WO2003086960A1 - Microfluidic devices with new inner surfaces - Google Patents

Abstract

A microfluidic disc comprising one or more enclosed microchannel structures, each of which comprises a section that is defined between two essentially planar substrates (I and II) wherein one surface in either one or both substrates comprises microstructures in the form of grooves and/or projections that match each other so that they together define one or more microchannel structures when the two surfaces are apposed in the microfluidic device, said microchannel structures being intended for transport of liquids. The device is charactrized in that at least a part of the inner walls of said section of each of said one or more microchannel structures comprises a coat that has been deposited by treating at least the corresponding part of either one or both of said surfaces with a gas plasma comprising one or more organic precursor compounds. A method for producing the disc is also presented.

Description

MICROFLUIDIC DEVICES WITH NEW INNER SURFACES.

TECHNICAL FIELD

The present invention concerns a microfluidic device that has inner surfaces with chemical surface characteristics that have been introduced in a new way.

In the context of the invention a microfluidic device typically comprises one, two or more microchannel structures, which are defined between two essentially planar and parallel substrates that are apposed to each other. Thus either one or both of the two substrate surfaces that define the microchannel structures comprise microstructures in the form of grooves and/or projections such that the microchannel structures can be formed when the two surfaces are apposed.

In a more generalized variant each microchannel structure is defined between the surfaces of two or more planar substrates that are layered on top of each other. If different sections of a microchannel structure are defined between different pairs of planar substrates, there typically are holes in the substrates so that the sections are in communication with each other. Either one or both of the surfaces that are to define a section of a microchannel structure comprises microstructures such that the desired section of a microchannel structure will be formed when the surfaces are joined together.

Separate microchannel structures may be defined between additional essentially planar substrates.

The device is microfluidic in the sense that one or more liquid aliquots can be transported between different functional parts of the individual microchannel structures in order to process the aliquots. The purpose of the transport is to carry out predetermined process protocols, for instance for assaying one or more constituents of a sample aliquot or to synthesize an organic or an inorganic compound. The liquid aliquots are typically aqueous, i.e. based on water and mixtures between water and water-miscible organic solvents.

The terms "non-specific adsorption" and "fouling" mean undesired adsorption of compounds to inner walls of the microchannel structures. The term also includes inactivation of bioactive compounds by the walls, for instance denaturation of proteins. The compounds are present in the liquid used and are primarily reagents. For aqueous liquids the reagents may be proteins and/or other biopolymers and/or other bioorganic and synthetic organic compounds. Analytes are included in the term "reagent". 5

Patent applications and issued patents referred in this text are hereby incorporated by reference.

BACK-GROUND TECHNOLOGY

10 A number of different techniques for modifying substrate surfaces are well known.

One common method is to subject a substrate surface, for instance made in plastics, to various forms of plasma treatment (Chan et al., Surface Science Reports 24 (1996) 1-54; and Garbassi et al, Polymer Surfaces - From Physics to Technology, John Wiley (1998)

15 238-241). This is done in a plasma reactor, which is a vacuum vessel containing a gas at low pressure (typically 10 to 1000 mTorr). When a high frequency electric excitation field is applied over the reactor, a plasma (also called glow discharge) is formed, containing reactive species like ions, free radicals and vacuum-UN photons. These species may react with other species and/or with the surface and cause a chemical modification of the 0 substrate surface with properties depending on the nature of the gas and on the plasma parameters. Gases like oxygen and argon are typically used for hydrophilisation and/or adhesion improvement on plastics, while vapors of organic precursor compounds can be used to apply thin coatings for a number of different purposes (Yasuda, Plasma Polymerization, Academic Press 1985). 5

Previously, vapours of organic precursor compounds have been used to produce surfaces that are wettable by aqueous liquids but the hydrophilicity has been moderate and not utilized to facilitate transport of aqueous liquids in microchannels. In some cases the primary goal has been to introduce coats that have a low non-specific adsorption, for

30 instance of proteins and/or other biopolymers and/or other bioorganic molecules. See for instance discussions US 5,153,072 (Ratner et al), US 5,002,794 (Ratner et al), US 6,329,024 (Timmons et al), US 5,876,753 (Timmons et al), EP 896035 (Timmons et al). Strictly hydrophobic surfaces have also been produced. See for instance US 5,171,267 (Ratner et al). WO 0056808 (Ocklind, Larsson and Derand, Gyros AB) describes microfluidic devices comprising hydrophilic microchannel structures defined between two essentially planar substrates that are apposed. Before being apposed the surface of at least one of the substrates has been hydrophilized in gas plasma, which comprises a non-polymerisable gas. The surfaces obtained are hydrophilic and can be coated subsequent to gas plasma treatment in order to introduce further functionalities.

WO 9958245 (Larsson et al) and WO 9721090 (Mian et al) are examples of publications that in general terms suggest microfluidic devices in which the inner surfaces of the microchannel structures have been made hydrophilic by gas plasma treatment, coating of hydrophobic surfaces with hydrophilic polymer etc.

OBJECTS OF THE INVENTION During the last decade sophisticated microfluidic devices have appeared with the goal to fully integrate complete process protocols in miniaturized form. This means integration of all steps of a protocol from sample preparation to recording of the results in one and the same microchannel structure. Ideally it would be nice if one and the same chemical surface characteristics could be used in all functional parts. Such surface characteristics hardly will be found because various steps often have different demands. However, it would be of advantage if the same kind of equipment could be used to produce surfaces corresponding to a spectra of chemical surface characteristics, for instance from extremely hydrophobic to extremely hydrophilic surfaces, and preferably with anti-fouling properties. A first object of the invention is to present a surface modification method that meets this desire. This object also includes a microfluidic device of the kind just mentioned wherein at least a part of the inner surface of its microchannel structures has been modified by this kind of method.

One important problem with respect to microfluidic devices is to obtain surfaces with a sufficient hydrophilicity to supportliquid transport through a microchannel structure combined with a sufficiently low non-specific adsorption (anti-fouling) of reagents in order to accomplish reliable and reproducible results. The severity of the fouling problem (non-specific adsorption) increases with the surface to volume ratio, i.e. it increases when a cross sectional dimension decreases, for instance from < 1000 μm to ≤ 100 μm to 10 μm and/or from < 1000 μl to < 100 μl to ≤ 10 μl to ≤ 1 μl to < 100 nl to < 50 nl. Even if it is often said that hydrophobic surfaces have prominent non-specific adsorption there are numerous systems for which also hydrophilic surfaces have a disturbing non-specific adsorption. A second object of the invention is to provide new surface modifications that have a sufficient wettability combined with a sufficiently low non-specific adsorption for a reliable and reproducible mass transport and processing of reagents by a liquid flow through a microchannel structure. This object thus aims at optimizing wettability and anti-fouling in relation to each other.

A third object is directed to a microchannel structure that is present in a microfluidic device and comprises two or more different functional parts, at least one of which comprises inner surfaces of a sufficient hydrophilicity for a liquid aliquot to penetrate completely the functional part by capillary force once having wetted the entrance of the part. The demand for a sufficiently low non-specific adsorption remains.

A fourth object is to accomplish a microfluidic device comprising coats that can be stored for > 7 days, such as > 30 days, while retaining the intended functionality of the surface, i.e. the surface may still be used for the intended purpose (= is essentially unchanged).

THE INVENTION

The present inventors have recognized that the above-mentioned objects can be achieved by treating the channel surfaces with gas plasma, which comprises one or more organic precursor compounds in gas form. The obtained surface characteristics (for instance hydrophhihcity or hydrophobicity) is determined by the selection of the organic precursor compound and/or the process parameters applied to create the gas plasma as outlined below.

FIRST ASPECT OF THE INVENTION (METHOD)

Accordingly the first aspect of the invention is a method for the manufacture of a microfluidic device of the kind described above in order to introduce a predetermined degree of wettability (hydrophilicity and/or hydrophobicity) on an inner surface of said microchannel structures. The method is characterized in comprising the steps of: (i) providing two essentially planar substrates (I and II) of the type described under the heading "Technical Field", (ii) placing either one or both of the substrates in a gas plasma reactor, and creating within said plasma reactor a gas plasma containing an organic precursor compound, said organic precursor compound and the conditions in the reactor being selected such that a coat of the predetermined degree of wettability is formed on a selected part of the surface of the substrate/substrates, (iii) removing the substrate/substrates from the plasma reactor (iv) adhering the surface of substrate I to the surface of substrate II so that at least an enclosed section of each of microchannel structures are formed between the two surfaces, (v) optionally joining further planar substrates to complete the microchannel structures. In the simplest variant complete enclosed microchannel structures are defined between substrate I and II, i.e. the section referred to under the heading "Technical Field" corresponds to a complete microchannel structure, except for various ports that may be present as holes in the substrates.

Additional steps and variations Between steps (i) and (ii), (ii) and (iii) and/or (iii) and (iv) there may be one or more additional steps for introducing one or more surface modifications with characteristics that are different from the coat introduced in step (ii). These additional steps may involve (a) a gas plasma treatment utilizing the same or another precursor compound and/or the same or other conditions, and/or (b) some other coating procedure.

Depending on the kind of surface modification, alternative (a) may be carried out without removing and re-inserting the substrate/substrates from/into the gas plasma reactor.

If only a part of a substrate surface is to be coated in step (ii) or in any of the additional steps, appropriate masking and/or unmasking may be done before or after such acoating step (including sequence of steps). Parts that are masked/unmasked maybe present in either one or both of the substrate surfaces, for instance on a part comprising microstructures. Washing steps may be included between steps if appropriate.

One variant of step (ii) is to introduce a coat that is wettable (hydrophilic)anα7or has a pronounced resistance to non-specific adsorption (= anti-fouling) on a major part of the microstructured part of the surface. Microstructured areas that are not going to be coated in this stepare typically masked. The precursor compound and the plasma conditions for the gas plasma are selected as outlined below. After step (ii) and unmasking, the uncoated areas thus exposed may be further processed, for instance to render them non-wettable (hydrophobic) in order to create passive (non-closing) valves and/or anti-wicking means and/or inlet or outlet vents to ambient atmosphere. These kinds of functionalities are illustrated in WO 9958245 (Larsson et al., Gyros AB), WO 0185602 (Larsson et al, Gyros AB & A ic AB), WO 0146465 (Andersson et al., Gyros AB), and WO 02074438 (Andersson et al., Gyros AB). In the case an uncoated area as such provides a sufficiently low wettability (i.e. are non-wettable), the surface at these positions may be used directly as a valve and/or as an anti-wicking means and/or as a vent after step (iv) without any extra processing. Many times, however, it is more appropriate to make these non-treated areas more non-wettable (increase the hydrophobicity), for instance by inserting steps according to alternatives (a) or (b) between steps (ii) and (iv). In the case alternative (a) is selected the precursor and gas plasma conditions are selected to give a non-wettable surface as known in the field and also discussed below. Spraying or printing may also be utilized as alternative (b). See for instance WO 0185602 (Larsson et al, Gyros AB & Amic AB), and WO 0146465 (Andersson et al., Gyros AB). In order to secure that the valve and/or anti-wicking means will be located to a desired position and/or have a desired geometry, appropriate masking is advantageous for an additional step.

Another variant of step (ii) is to introduce a coat that is non-wettable (hydrophobic coat) on selected parts of the microstructures. Areas on which other surface characteristics are desired are then typically masked. The non-wettable coat may be introduced for creating local surface breaks of the same type as indicated in the preceding paragraph. The remaining parts may be intended for liquid transport and therefore typically need to be processed to surfaces that are wettable by inserting steps according to either alternative (a) or alternative (b) above after step (ii). Remasking for these additional steps is often advantageous for similar reasons as for the first variant. In the case the uncoated area after unmasking inherently comprises a desired wettability (either by being wettable or non- wettable), there is no need to introduce any additional surface treatment steps before step (iv).

A third variant of step (ii) is to introduce a coat that is sufficiently wettable or sufficiently non-wettable, but not with sufficiently low non-specific adsorption (anti-fouling), or vice versa. In this case, an additional step according to alternative (a) or (b) may be used to modify the coat to exhibit the missing characteristics while at the same time retaining an essential part of the surface characteristics created in step (ii). In this case the same masking can be utilized for the two coating steps. Demasking and remasking between step (ii) and an additional step may then not be required.

In the context of the invention the term "wettable" means that a surface have a water contact angle that is < 90° (hydrophilic surface). The term "non-wettable" refers to a surface that have a water contact angle > 90° (hydrophobic surface). In order to facilitate good transport of a liquid between different functional parts of the inventive microfluidic devices, the liquid contact angle in the individual parts should primarily be wettable, preferably with a water contact angle < 60° such as ≤ 50° or ≤ 40° or < 30° or < 20°. Local surface breaks that are to be used for valving and/or anti-wicking, for instance, are important exceptions from this general rule. Local surface breaks are typically non- wettable with water contact angles > 90°, such as > 100° or > 110° or > 120°. Typically the difference in wettability (in water contact angles) between a local surface break and a bordering surface are > 50°, such as > 60° or > 70°. All figures refer to values obtained at the temperature of use, typically 25 °C, and with water as the liquid.

Microchannels are typically defined by a limited number of well-defined walls, for instance a bottom wall, a top wall and two sidewalls. These walls may derive from different substrates. Locally at least the walls derived from the same substrate are wettable/non-wettable to the same extent. In the case the surface characteristics of a channel is intended to facilitate liquid transport and the walls derived from one of the substrates is non-wettable this can be compensated if the wall(s) derived from the other substrate is(are) sufficiently wettable (i.e. has/have a sufficiently low water contact angle). The substrates.

Each of the two planar substrates may comprise microstructures in the form of projections and/grooves as discussed above. In the preferred variants, however, only one of the two substrates comprises microstructures that then are in the form of open microchannel structures or open sections of the microchannel structures. The other substrate is used to cover these open structures. Either one or both of the substrates may have through-going holes that are associated with individual microchannel structures. These holes may be used as inlets or outlets for liquids and/or as inlet or outlet vents for air. In the case different sections of a microchannel structure are defined between different pairs of substrates this kind of holes may provide communication between the different sections.

The substrates may be made from inorganic or organic material. Typical inorganic materials are silicon, quartz, glass etc. Typical organic materials are polymer materials, for instance plastics including elastomers, such as silicone rubber (for instance poly dimethyl siloxane) etc. Polymer material as well as plastics comprises polymers obtained by condensation polymerisation, polymerisation of unsaturated organic compounds and/or other polymerisation reactions. The microstructures may be created by various techniques such as etching, laser ablation, lithography, replication by embossing, moulding, casting etc, etc. Each substrate material typically has its preferred techniques.

From the manufacturing point of view, substrates exposing surfaces and microstructures in plastics are many times preferred because the costs for plastics are normally low and mass production can easily be done, for instance by replication. Typical manufacturing processes involving replication are embossing, moulding, casting etc. See for instance WO 9116966 (Pharmacia Biotech AB, Oh an & Ekstrom). At the priority date of this invention the preferred plastics was polycarbonates and polyolefms based on polymerisable monomeric olefins that comprise straight, branched and/or cyclic non- aromatic structures. Typical examples are Zeonex™ and Zeonor™ from Nippon Zeon, Japan. This does not outrule the use of other plastics, for instance based on styrenes, methacrylates and/or the like. Suitable polymers may be copolymers comprising different monomers, for instance with at least one of the monomers discussed above.

Plasma variables and the gas plasma reactor The electric excitation field applied typically has a frequency in the radiowave or microwave region, i.e. kHz-MHz or GHz respectively. The modification on the polymer surface caused by the plasma will depend mainly on a number of internal plasma parameters such as: type of species present in the plasma, spatial distributions, energy distributions and directional distributions. The species typically derives from one or more organic precursor compounds. In turn these parameters depend in a complex way on the external plasma parameters: reactor geometry, type of excitation, applied power, type of process gas, gas pressure and gas flow rate.

The results of a treatment may depend on the design of the reactor vessel used meaning that the optimal interval to a certain degree will vary from one reactor design to another. The results may also depend on where in the reactor the surface is placed during the treatment.

A suitable reactor vessel should enable electric excitation power input for instance in the microwave or radio wave ranges. The required intensity of the plasma will depend on the variables discussed above. Satisfactory gas plasmas may be found in the case the electric excitation power applied is < 300 W, with preference for < 100 W. The pressures are typically < 200 mTorr, with preference for < 100 mTorr. The design of the reactor vessel should enable introduction of the vapour phase of the organic precursor into the reactor chamber. This includesthe option of heating of the reactor chamber and/or flask containing the organic precursor. The reactor vessel should be designed to facilitate homogenous plasma distribution in the reactor chamber. More details on parameters influencing plasma polymerisation can be found in h agaki, N., "Plasma surface modification and plasma polymerisation." Technomic Publisching company, Inc., USA, 1996.

The proper combination of different plasma and apparatus parameters is typically found by varying the values for one or more of these parameters and study how this affect the properties of the modified substrate surface, i.e. the resulting hydrophilicity, hydrophobicity, anti-fouling, stability etc. The chemical structure of the coat formed by plasma deposition and selection of organic precursor compound.

The chemical structure of the a coat such as degree and type of cross-linking, swelling, kinds of functional groups exposed to a surrounding liquid, etc determines the chemical surface characteristics, primarily wetting/non-wetting ability including hydrophilicity and hydrophobicity, and non-specific adsorption of various compounds such as proteins and/or other biopolymers and bioorganic compounds.

Surface characterisation of the coat can be carried out by a number of methods, such as X- ray photoelectron microscopy (XPS), static secondary ion mass spectrometry (static SIMS), liquid contact angle methods, atomic force microscopy (AFM), near edge X-ray adsorption fine structure (NEXAFS), FTIR and chemical derivatization. For a review see Johnston et al (J. Electron Spectroscopy and Related Phenomena 81 (1996) 303-317).

Preferably a sufficiently hydrophilic coat exposes neutral hydrophilic groups to a liquid in contact with the coat, in particular lower alkyl ether, such as ethylene oxy, hydroxy groups etc, and is essentially free of aromatic structures. The coat should also be essentially free of charged or chargeable groups, in particular if a low non-specific adsorption is required. Chargeable groups are karboxy (-COOH), amino (-NH ), etc). Non-chargeable groups are hydroxy bound to sp³-hybridized carbon, ether, amido etc.

There is a relatively large number of publications related to chemical structure of polymeric films deposited from gas plasmas that are based on organic precursor compounds (e.g. US 5,153,072 (Ratner et al) and US 5,002,794 (Ratner et al). A general idea has been that the incorporation of groups and/or properties that derive from a precursor compound can be related to the rate of fragmentation in the plasma and the rate of deposition of the coat on a substrate surface. It has been discussed that a lower power may decrease fragmentation and increase the incorporation of groups and properties that derive from the precursor compound. It has also been discussed that fragmentation of the precursor compound depends on W/FM where W is the RF power applied, and F and M are the flow rate and the molecular weight, respectively, of the organic precursor compound. Other variables that have been studied are: (a) the effect of pulsed radiofrequency (RF) discharges on fragmentation of the precursor compound in relation to an increase of the presence of precursor structures in the deposited coat, (b) the location of the substrate in the gas plasma reactor with the idea that a location adjacent but not submersed in the plasma will increase the degree of precursor structures in the coat etc. An increase in precursor structures in a deposited coat has also been suggested if there is a negative temperature gradient between the plasma and the substrate to be surface modified. See Ohkubo et al (J. Appl. Polym. Sci 41 (1990) 349-), Lopez et al (Langmuir 7 (1991) 766-, D'Agostino et al (J. Polym. Sci. Part A: Polym. Chem. Edn. 28 (1990) 3378- , Cho et al (J. Appl. Polym. Sci. 41 (1990) 1373-, Ward et al (Short, Surfasce Interface Anal. 22 (1994) 477-, Kiaei et al (J. Biomater. Sci.: Polym. Edn. 4 (1992) 35-, and Panchalingam et al (ASAIO J. (1993) M305.

The organic precursor compound typically is polymerisable by which is meant that the compound is capable of forming a high molecular weight insoluble aggregate on the surface of the substrate. This may involve traditional polymerization reactions or take place by degradation, rearrangement and extensive reactions of the precursor compound and/or of the intermediary species formed in the gas plasma.

In order for an organic precursor compound to function in the present invention it must have a sufficiently high vapour pressure at the selected temperature within the plasma reactor. This also means that precursor compounds that have a low tendency for hydrogen bonding may have advantages compared to precursor compounds of the same size that have a strong tendency for hydrogen bonding.

Small precursor compounds may also have advantages, e.g. with molecular weights < 2000 dalton, such as < 1000 dalton or < 500 dalton.

This "advantage" of small compounds and compounds with weak or no tendency for hydrogen bonding is based on the fact that hydrogen-bonding and increased molecular weight tends to increase the boiling point and the vapour pressure.

For hydrophilic coats suitable precursor compound can be found amongst organic compounds that have a high content of heteroatoms selected amongst oxygen, nitrogen and sulphur, provided that the other plasma parameters are properly set. By the term "high content" in this context is meant that the ratio between the total number of the heteroatoms, e.g. oxygen, and the number of carbon atoms should be > 0.1, such as > 0.25 or > 0.5 or > 0.75, in the precursor compound. From theoretical considerations this ratio is never larger than 2. In the case the organic precursor compound have certain properties that one would like to incorporate into a coat but a too low content of heteroatoms, this may be compensated for by including oxygen in the gas plasma. Alternatively, one may include one or more other organic compounds for which the content of heteroatoms is higher than in the desired precursor compound.

Typically compounds for creating hydrophobic coats are hydrocarbons and fluorinated hydrocarbons (e.g. perfluoinated hydrocarbons (PFH))

For hydrophobic coats suitable precursor compounds can be found amongst organic compounds having a low content of heteroatoms selected amongst oxygen, nitrogen and sulphur, provided that the other plasma variables are properly set. A "low content" in this context means that the ratio between the number of heteroatoms, e.g. oxygen, and the number of carbon atom should be < 0.75, such as < 0.50 or < 0.25 or < 0.10. In the case organic precursor compound have certain properties that one would like to incorporate into a coat but a too high content of heteroatoms, this might be compensated for by including one or more organic compounds for which the content of heteroatoms is lower than in the desired precursor compound.

Suitable precursor compounds may also be found amongst organic compounds that contain one, two or more structural units that are present in polymers that are known to give coats that are resistant to non-specific adsorption. These kinds of precursor compounds are in the innovative method combined with gas plasma conditions enabling this property to be retained in the coat deposited on the substrate.

There are a large number of polymers that are known to reduce non-specific adsorption. Typically they are non-ionic and hydrophilic, i.e. contains a plurality of neutral hydrophilic groups, such as hydroxy, amido, and lower alkoxy including alkyleneoxy (C_\. ₃ in particular C₂) and alkyl ether groups. See for instance US 6,337,212 (Caliper), WO 0147637 (Gyros AB), US 4,680,201 (Hjerten), US 5,840,388 (Karger et al), US 5,240,994 (Brink et al), and US 5,250,613 (Bergstrδm et al). Precursor compounds to be used in this variant of the invention can thus be found amongst low molecular weight compounds that comprise one or more of these structural units that are present in polymers that reduce non-specific adsorption. At the priority date one of the most promising precursor compounds comprise the structural unit -(CH₂)_nO-, where (a) n is an integer 1-3, with preference for 2, (b) the free valence at the carbon binds to hydrogen or an oxygen, and (c) the free valence at the oxygen binds to a hydrogen or a carbon. The carbon may be sp³-, sp²- or sp-hydridised and may thus be part of a saturated or unstarurated hydrocarbon group such as alkyl (for instance CI, C2, C3 to C5) and alkenyl, such as vinyl). This is line with the findings of Ratner et al (US 5,002,794 and US 5,153,072) and Timmons et al (US 6,329,024, US 5,876,753, and EP 896053 ) for precursor compounds comprising 1-4 repetitive ethylene oxide units either in straight form or in cyclic form (crown ethers). According to the same principles one can envisage that other suitable candidate precursor compounds can be found amongst low molecular weight compounds which comprise structural units selected amongst -CH₂OH, -CH₂ (OCH₃), and [-CH₂-CH (OH)]_n-, and [- CH₂-CH(OR)]_n- and corresponding monomers wherever applicable, where (a) n' is an integer 1-10 with preference for 1-5, (b) R is lower alkyl (C₁.₅), such as methyl, or lower acyl (Cι-₅, such as fortnyl or acetyl), and (c) the free valences binds to atoms selected amongst hydrogen, carbon, sulphur, nitrogen and oxygen. None of sulphur, nitrogen and oxygen binds a hydrogen when two or more of them binds to the same carbon. Other candidate precursor compounds are monomers or oligomers (2-10, such as 2-5, repeating monomeric units) corresponding to polymers that give coats that have low non-specific adsorption.

In preferred variants a coat providing low non-specific adsorption should also have a sufficient hydrophilicity in order to secure a reliable and reproducible transport of reagents by an aqueous liquid flow. One can thus envisage that candidates of precursor compounds can also be found among the precursor compounds that are candidates for the creation of hydrophilic coats. See above.

The thickness of the coat should be < 50 %, for instance < 20 % or < 10 %, of the smallest distance between two opposing sides of a microchannel part comprising the innovative coat. An optimal thickness will typically be < 1000 nm, for instance < 100 nm or < 50 nm, with the provision that the coat shall permit a desired flow to pass through. A lower limit is typically 0.1 nm. These figures refer to thickness after saturation with the liquid intended to pass through a microchannel part comprising the coat. The coat may or may not swell in contact with the liquid, which is passing through a microchannel structure.

It is important to control the selected process parameters so that they lead to predetermined surface characteristics, for instance preselected wetting/or non-wetting - properties and/or ability to reduce non-specific adsorption (anti-fouling). This can be accomplished as outlined in the experimental part that describes the determination of a) liquid contact angles, and b) adsorption of albumin, which is a measure of non-specific adsorption. Once the proper values/ranges of the process parameters have been found for the predetermined surface characteristics, the process can be run without testing.

For aqueous solutions the term "a reduction in non-specific adsorption" (anti-fouling effect) refers to bovine serum albumin as a reference/model substance and means that the ratio between adsorption of bovine serum albumin after and before a gas plasma treatment of a surface according to the invention is < 0.75, such as < 0.50 or < 0.25 (decrease ratio). The ratio can be even lower, for instance < 0.10.

Adhering the substrate surfaces to each other (step vi). There are a number of techniques suggested in the literature. Thus conventional bonding without use of a particular adhesive may be utilized, in particular in case the substrates are made of inorganic material such as silicon, glass, quartz and the like. In case the substrate surfaces comprise plastics, the two surfaces can be fixed to each other by pressing the surfaces together while heating selectively the surface not containing microstructures above its transition temperature, while the surface with the microstructures are maintained below its transition temperature. In other alternatives various kinds of adhesives or glues may be used. See further WO 9424900 (Ove Ohman), WO 9845693 (Soane et al), US 6,176,962 (Soane et al), WO 9956954 (Quine), and WO 0154810 (Derand et al, Gyros AB). Thermolaminating is important because this technology has been shown to be capable minimizing destruction of differences in chemical surface characteristics that are to be retained in the microfluidic device obtained after step (iv). See WO 0154810 (Derand et al, Gyros AB). Problems with so-called bond voids can be minimized if the open microchannel structures in a substrate surface is defined by walls arising from the surface. See WO 9832535 (Lindberg et al) and WO 0197974 (Chazan et al, Caliper).

In order to avoid that an adhesive is pressed into a microchannel during steps (iv) and (v) the microchannel structures are preferably defined by relief patterns that are present in either one or both of the substrate surfaces as outlined in PCT/SE02/02431 (Derand et al). h principle the adhesive may be selected as outlined in US 6,176,962 and WO 9845693 (Soane et al). Thus suitable bonding materials include elastomeric adhesive materials and curable bonding materials. These kinds of bonding material as well as others may be in liquid form when applied to a substrate surface. Bonding materials including adhesives thus comprises liquid curable adhesive material and liquid elastomeric material. After application the adhesive material is rendered more viscous or non-flowable for instance by solvent removal or partial curing before the other substrate is contacted with the adhesive. The term "liquid foπn" includes material of low viscosity and material of high viscosity.

Curable adhesive includes polymerizable adhesives and activatable adhesives. Theπno- curarable, moisture-curable, and bi-, three- and multi-component adhesives are also examples of curable adhesives.

THE SECOND ASPECT OF THE INVENTION: THE MICROFLUIDIC DEVICE OBTAINED AFTER STEP (iv) OR AFTER THE OPTIONAL STEP (V).

This aspect of the invention is primarily characterized in that a part of the inner surface of at least one of the microchannel structures has been modified by the use of gas plasma comprising an organic precursor compound selected according to the principles outlined for the first aspect, i.e. has one or more surface characteristics that is achievable by a plasma polymerisation coating method. Additional characteristic features are defined below.

The microfluidic device preferably contains a plurality of microchannel structures, each of which is defined between two or more planar substrates as discussed under the heading "Technical Field". Each microchannel structure may comprise one, two, three or more functional parts selected among: a) application chamber/cavity/area, b) conduit for liquid transport, c) reaction chamber/cavity; d) volume defining unit; e) mixing chamber/cavity; f) chamber for separating components in the sample, for instance by capillary electrophoresis, chromatography and the like; g) detection chamber/cavity; h) waste conduit/chamber/ cavity; i) internal valve; j) valve to ambient atmosphere; etc. Many of these parts may have one or more functionalities. There may also be collecting chambers/cavities in which a compound, which has been separated, formed or otherwise processed in a microchannel structure are collected and transferred to some other instrument, for instance an analytical instrument such as a mass spectrometer. In addition there are also one or more outlet vents for air. Inlets and outlets for liquids may also function as vents (inlet vent or outlet vent).

The preferred devices are typically disc-shaped with sizes/surface areas and/or forms similar to the conventional CD-format, e.g. their surface areas are in the interval from 10% up to 300 % of the surface area of a CD of the conventional CD-radii. The upper and/or lower sides of the disc may or may not be planar.

The preferred microfluidic discs have an axis of symmetry (C_n) that is perpendicular to the disc plane, where n is an integer > 2, 3, 4 or 5, preferably oo (C_∞). In other words the disc may be rectangular, such as square-shaped, or have other polygonal forms, but is preferably circular. Once the proper disc format has been selected centrifugal force may be used for driving liquid flow. Spinning the device around a spin axis that typically is perpendicular or parallel to the disc plane may create the necessary centrifugal force. In the most obvious variants at the priority date, the spin axis coincides with the above- mentioned axis of symmetry.

Different principles may be utilized for transporting the liquid aliquots within the microfluidic device/ microchannel structures between two or more of the functional parts described above. Inertia force may be used, for instance by spimiing the disc as discussed in the preceding paragraphs. Other forces that may be used are electrokinetic forces and non-electrokinetic forces, such as capillary forces, hydrostatic pressure etc. In preferred variants utilizing centrifugal force for liquid transport, each microchannel structure comprises an upstream section that is at a shorter radial distance than a downstream section relative to a spin axis.

The microfluidic device may also comprise common channels connecting different microchannel structures, for instance common distribution channels for introduction of liquids and common waste channels including waste reservoirs. Common channels including their various parts such as inlet ports, outlet ports, vents, etc., are considered to be part of each of the microchannel structures they are connecting. Common microchannels may also fluidly connect groups of microchannel structures that are in different planes or in the same plane.

The term "plurality" means two, three, four, five or more microchannel structures. Preferably "plurality" means that the number of microchannel structures on the microfluidic device is > 10, such as > 25 or > 90 or > 180 or > 270 or > 360.

The terms "microchannel", "microconduit", etc., contemplate that a channel structure comprises one or more cavities and/or channels/conduits that have a cross-sectional dimension that is < 10³ μm, preferably < 0.5 x 10³ μm or < IO² μm. The lower limit for cross sectional dimensions is typically significantly larger than the size of the largest constituent of a liquid that is to pass through a microchannel of the innovative device. The volumes of microcavities/microchambers are typically < 1000 nl, such as < 500 nl or < 100 nl or < 50 nl or < 25 nl. This does not exclude larger chambers/cavities, for instance in the intervals 1-1000 μl, such as 1-100 μl or 1-10 μl which typically are directly connected to inlet ports and intended for application of sample and/or washing liquids. Microformat means that one, two, three or more liquid aliquots that are transported within the device are within the intervals specified for the microchambers/microcavities.

The invention will now be described by a number of illustrative and non-limiting experiments. The invention is further defined in the appended claims that constitute a part of the descriptive part. EXPERIMENTAL PART

Plasma treatment with diethylene glycol dimethyl ether

A polycarbonate CD disc (Macrolon DP-1265, Bayer AG, Germany), and pieces cut from a polycarbonate CD disc were placed in a plasma reactor (CVD Piccolo, Plasma Electronic, Germany), and subjected to argon plasma treatment at 24 W for 2 min. Subsequently, the polycarbonate surfaces were treated with plasma of diethylene glycol dimethyl ether (diglyme; Aldrich, USA) at 24 W for 5 min. The water contact angle (sessile drop) of the resulting surfaces was measured on a Rame-Hart manual goniometer bench. The average of six equilibrium measurements (three droplets) was 48°.

Plasma treatment with diethylene glycol dimethyl ether and allylic alchohol

A polycarbonate CD disc (Macrolon DP-1265, Bayer AG, Germany), and pieces cut from a polycarbonate CD disc were placed in a plasma reactor (CVD Piccolo, Plasma Electronic, Germany), and subjected to argon plasma treatment at 24 w for 2 min. Subsequently, the polycarbonate surfaces were treated with plasma of diethylene glycol dimethyl ether (diglyme; Aldrich, USA) at 24 W for 5 min. Finally, they were subjected to plasma of allylic alcohol (Merck, Germany) at 12 W for 5 min. The water contact angle (sessile drop) of the resulting surfaces was measured on a Rame-Hart manual goniometer bench. The average of six equilibrium measurements (three droplets) was <10°.

Plasma treatment with ethylene glycol vinyl ether

A polycarbonate CD disc (Macrolon DP-1265, Bayer AG, Germany), and pieces cut from a polycarbonate CD disc were placed in a plasma reactor (CVD Piccolo, Plasma Electronic, Germany), and subjected to argon plasma treatment at 24 w for 2 min. Subsequently, the polycarbonate surfaces were treated with plasma of ethylene glycol vinyl ether (Aldrich, USA) at 12 W for 5 min.

The water contact angle (sessile drop) of the resulting surfaces was measured on a Rame- Hart manual goniometer bench. The average of six equilibrium measurements (three droplets) was 22°. Microfluidic test

A silicone rubber lid (polydimethylsiloxane) was placed on a polycarbonate CD with recessed microchannel pattern, (50-200 μm wide, 50-100 μm deep), that had been treated either with diglyme plasma, or with diglyme plasma with subsequent allylic alcohol plasma treatment, as described above. Alternatively silicone rubber with recessed microchannel pattern (1000 μm wide, 100 μm deep) was placed on flat polycarbonate surfaces that had been treated either with diglyme plasma, or with diglyme plasma with subsequent allylic alcohol plasma treatment, as described above. Resulting flow channels were examined using a solution of Cibacron Brilliant Red (CTBA limited) in MilliQ water (Millipore). A drop was placed at the channel inlet and it was concluded that flow rate into channels on surfaces that had been subjected to diglyme plasma with subsequent allylic alcohol plasma treatment was significantly higher than on surfaces that had only been treated with diglyme plasma.

Protein adsorption studied with Total Internal Reflection Fluorescence (TIRF) spectroscopy

The theory of TIRF spectroscopy, as well as the experimental set-up used in the present work has been described in detail in [1].

Bovine serum albumm (BSA; fraction V, Sigma, USA) was chosen as model protein for adsorption studies, and labelled with fluorescein-5-isothiocyanate (FITC; isomer I; Molecular Probes), as described in [Lassen, B. and Malmsten, M., Competitive protein adsorption studied with TIRF and ellipsometry. Journal of colloid and interface science, 1996. 179: p. 470-477]. The molar ratio of FITC to proteins was found to be approximately unity in all cases.

A TIRF fluorescence intensity graph resulting from adsorption of 400 ppm FITC-BSA on untreated polycarbonate (PC) is shown in figure 1, together with a graph representing the same experiment on a diglyme plasma-treated surface. TIRF fluorescence intensity graphs using diglyme plasma + allylic alcohol plasma (figure 2), and ethylene glycol vinyl ether plasma (figure 3) are also presented here. It is apparent from the figures that the ratio between adsorption of protein on the treated surface and the untreated surface always is < 0.25.

Legends to the figures Figure 1. TIRF with FITC-BSA on untreated PC (squares), and on PC treated with diglyme (24 W) in the plasma reactor (circles). Protein solution (400 ppm) enters the flow cell (filled arrow) and is replaced by PBS buffer (dashed arrow). Figure 2. TIRF with FITC-BSA on PC treated with diglyme (24 W), and allylic alcohol

(12 W) in the plasma reactor. Protein solution (400 ppm) enters the flow cell (filled arrow) and is replaced by PBS buffer (dashed arrow).

Figure 3. TIRF with FITC-BSA on PC treated with ethylene glycol vinyl ether-plasma

(24 W) in the Gyros reactor. Protein solution (400 ppm) enters the flow cell (filled arrow) and is replaced by PBS buffer (dashed arrow).

Claims

C L A I M S

1. A method for the manufacture of a microfluidic device comprising one or more enclosed microchannel structures, each of which comprises a section that is defined between two essentially planar substrates (I and II) wherein one surface in either one or both of the substrates comprises microstructures in the form of grooves and/or projections that match each other so that they together define said section for each of said one or more microchannel structures when the two surfaces are apposed in the microfluidic device, characterized in comprising the steps of:

(i) providing the planar substrates (I and II),

(ii) placing either one or both of the substrates in a gas plasma reactor, and creating within said plasma reactor a gas plasma containing an organic precursor compound, said organic precursor compound and the conditions in the reactor being selected such that a coat of the predetermined degree of wettability is formed on a selected part of the surface of the substrate/substrates, iii) removing the substrate/substrates from the plasma reactor, and (iv) adhering the surface of substrate I to the surface of substrate II so that said section of each of said microchannel structures is formed between the two surfaces (v) optionally joining further substrates to complete other sections of each of the microchannel structures, with the proviso that step (v) is not present in the case that said section corresponds to a complete microchannel structure.

2. The method of claim 1, characterized in that said section is a complete microchannel structure, and that step (v) is not present.

3. The method of any of claims 1 -2, characterized in that the precursor compound and the conditions in the reactor are selected to give a coat in step (ii) that is wettable with a water contact angle < 90°, preferably < 60°.

4. The method of any of claims 1 -2, characterized in that the precursor compound and the conditions in the reactor have been selected to give a coat in step (ii) that is non-wettable with a water contact angle that is > 90°.

5. The method according to any of claims 1-4, characterized in that the precursor compound and the conditions are selected in step (ii) so that a wettable or non- wettable first coat is introduced on selected parts of individual microchannel structures, and that a second coat is introduced on other selected parts of the microchamiel structures by an additional coating step introduced either between steps (i) and (ii) or between steps (ii) and (iv).

6. The method according to claims 5, characterized in that the first coat is wettable and the second coat non-wettable, or vice versa.

7. The method of any of claims 1-3 3and 5-6, characterized in that the precursor compound and reaction conditions provided by the gas plasma in step (ii) are selected to introduce a wettable first coat that also is anti-fouling.

8. The method according to claim 7, characterized in that the coat introduced in step (ii) has been modified by an additional step between step (ii) and step (iii) also utilizing a gas plasma.

9. The method of claim 8, characterized in that step (ii) introduces a coat that is anti-fouling and that the additional step strengthens the wettability of the coat without essentially destroying the anti-fouling property accomplished in step (ii).

10. A microfluidic device comprising one or more enclosed microchannel structures, each of which comprises a section that is defined between two essentially planar substrates (I and II) wherein one surface in either one or both substrates comprises microstructures in the form of grooves and/or projections that match each other so that they together define one or more microchannel structures when the two surfaces are apposed in the microfluidic device, said microchannel structures being intended for transporting a liquid, characterized in that at least a part of the inner walls of said section of each of said one or more microchannel structures comprises a coat (coat I) that has been deposited by treating at least the corresponding part of either one or both of said surfaces with a gas plasma comprising one or more organic precursor compounds.

11. The microfluidic device of claim 10, characterized in that said section comprises a complete microchannel structure.

12. The microfluidic device of claim 11, characterized in that coat I is wettable, preferably with a water contact angle that is < 40°.

13. The microfluidic device of claim 11, characterized in that coat I is non-wettable, preferably with a water contact angle that is > 100°.

14. The microfluidic device of claim 12, characterized in that coat I is anti-fouling with respect to bovine serum albumin with a decrease ratio that is < 0.50.

15. The microfluidic device of any of claims 10-15, characterized in that a) a non- wettable and a wettable coat are present edge-to-edge in at least one, preferably in everyone, of the microchannel structures, b) at least one of the coats has been introduced by the use of a gas plasma comprising an organic precursor compound, and c) the non-wettable coat define a valve function and/or a non-wicking function.