Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L3/00—Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
  • B01L3/50—Containers for the purpose of retaining a material to be analysed, e.g. test tubes
  • B01L3/502—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures
  • B01L3/5027—Containers 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
  • B01L3/502723—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip characterised by venting arrangements
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L3/00—Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
  • B01L3/50—Containers for the purpose of retaining a material to be analysed, e.g. test tubes
  • B01L3/502—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures
  • B01L3/5027—Containers 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
  • B01L3/502715—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip characterised by interfacing components, e.g. fluidic, electrical, optical or mechanical interfaces
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L3/00—Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
  • B01L3/56—Labware specially adapted for transferring fluids
  • B01L3/565—Seals
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
  • F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
  • F16L39/00—Joints or fittings for double-walled or multi-channel pipes or pipe assemblies
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
  • G01N27/26—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
  • G01N27/416—Systems
  • G01N27/447—Systems using electrophoresis
  • G01N27/44756—Apparatus specially adapted therefor
  • G01N27/44791—Microapparatus
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
  • B01J2219/00781—Aspects relating to microreactors
  • B01J2219/00783—Laminate assemblies, i.e. the reactor comprising a stack of plates
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
  • B01J2219/00781—Aspects relating to microreactors
  • B01J2219/00801—Means to assemble
  • B01J2219/0081—Plurality of modules
  • B01J2219/00813—Fluidic connections
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
  • B01J2219/00781—Aspects relating to microreactors
  • B01J2219/00819—Materials of construction
  • B01J2219/00833—Plastic
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
  • B01J2219/00781—Aspects relating to microreactors
  • B01J2219/00891—Feeding or evacuation
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
  • B01J2219/00781—Aspects relating to microreactors
  • B01J2219/00891—Feeding or evacuation
  • B01J2219/00898—Macro-to-Micro (M2M)
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
  • B01J2219/00781—Aspects relating to microreactors
  • B01J2219/00905—Separation
  • B01J2219/00907—Separation using membranes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2200/00—Solutions for specific problems relating to chemical or physical laboratory apparatus
  • B01L2200/02—Adapting objects or devices to another
  • B01L2200/026—Fluid interfacing between devices or objects, e.g. connectors, inlet details
  • B01L2200/027—Fluid interfacing between devices or objects, e.g. connectors, inlet details for microfluidic devices
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2200/00—Solutions for specific problems relating to chemical or physical laboratory apparatus
  • B01L2200/06—Fluid handling related problems
  • B01L2200/0689—Sealing
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2300/00—Additional constructional details
  • B01L2300/06—Auxiliary integrated devices, integrated components
  • B01L2300/0681—Filter
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2300/00—Additional constructional details
  • B01L2300/08—Geometry, shape and general structure
  • B01L2300/0809—Geometry, shape and general structure rectangular shaped
  • B01L2300/0816—Cards, e.g. flat sample carriers usually with flow in two horizontal directions
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2300/00—Additional constructional details
  • B01L2300/08—Geometry, shape and general structure
  • B01L2300/0861—Configuration of multiple channels and/or chambers in a single devices
  • B01L2300/0874—Three dimensional network
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2300/00—Additional constructional details
  • B01L2300/08—Geometry, shape and general structure
  • B01L2300/0887—Laminated structure
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2400/00—Moving or stopping fluids
  • B01L2400/04—Moving fluids with specific forces or mechanical means
  • B01L2400/0403—Moving fluids with specific forces or mechanical means specific forces
  • B01L2400/0415—Moving fluids with specific forces or mechanical means specific forces electrical forces, e.g. electrokinetic
  • B01L2400/0421—Moving fluids with specific forces or mechanical means specific forces electrical forces, e.g. electrokinetic electrophoretic flow
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L2400/00—Moving or stopping fluids
  • B01L2400/04—Moving fluids with specific forces or mechanical means
  • B01L2400/0475—Moving fluids with specific forces or mechanical means specific mechanical means and fluid pressure
  • B01L2400/0487—Moving fluids with specific forces or mechanical means specific mechanical means and fluid pressure fluid pressure, pneumatics
  • B01L2400/049—Moving fluids with specific forces or mechanical means specific mechanical means and fluid pressure fluid pressure, pneumatics vacuum
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
  • B01L3/00—Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
  • B01L3/50—Containers for the purpose of retaining a material to be analysed, e.g. test tubes
  • B01L3/502—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures
  • B01L3/5027—Containers 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
  • B01L3/502707—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip characterised by the manufacture of the container or its components

Definitions

• the present invention relates generally to microfluidic devices and particularly to means and methods for delivery or removal of fluids, including provision of vacuum, to microchannels and device elements in a microfluidic device. More specifically, the invention relates to fluid interconnects between a meso- or macroscaled environment to a microscaled environment. The invention also relates to means and methods for application of a vacuum to microfluidic channels in a microfluidic device to facilitate degassing of the channel and device. Specific applications of the internal degassing system are provided.
• microfluidic devices have proliferated and are now widely applied in environmental and biological analyses.
• a practical limitation of efficient, reliable and economic use of such devices is the interface between the microscale environment of the device and meso- and macroscale environments to be sampled or to which samples are passed for analyses.
• the interface is accomplished by interconnects which require the use of some type of seal.
• These interfaces can often be the weak link in a microfluidic system and because such small volumes are typically being processed, the smallest of leaks, or unplanned entrapments of air, can cause a microfluidic system to fail.
• Prior art methods for making interconnects to microfluidic devices include the use of glass tubes sealed with epoxy. Additionally, it is known to employ septa which are pierced by needles or tubes to make an interconnect.
• U.S. patent 6,090,251 of Sundberg et al. reports the use of a port in fluid communication with a microfluidic channel. A pipette or other device is used to deliver fluid to the port.
• This invention provides a fluid interconnect design which is readily implemented in microfluidic devices, particular in multiple layer laminate microfluidic devices, and which provides stronger, and more durable that are less susceptible to geometric irregularities.
• the invention also provides a fluid interconnect manifold which is readily adaptable to a number of interconnect configurations and provides for establishing a plurality of interconnects in a simple clamping operation.
• Supplying gases to and removing gases from liquids in a microfluidic device can be challenging, but represents an enabling method for performing a series of unique chemical and biological operations and microfluidic device and microsystem operations.
• Device wet out can be a significant practical problem with microfluidic devices and can be a particularly difficult problem in broad, flat microfluidic channel or chambers (e.g., those in which the aspect ratio, i.e., channel width/depth) is greater than or equal to about 25 and is typically much greater).
• Numerous instances exit where it is also advantageous to have highly localized control of gas injection or removal of gases. Some instances are coupled to electrochemical electrolysis products, others will make interactions with magnetically based microbead reactions advantageous.
• Wet out of a microfluidic channel can be facilitated by degassing of the channel.
• U.S. patent 5,053,060 reports a degasser which is used to remove gas bubbles or dissolved gases from a liquid stream.
• the degasser is formed from a hydrophobic membrane and two blocks: one having a grooved channel with an inlet and an outlet and the other with venting holes. The membrane is clamped between the two blocks over the channel. As liquid flows through the channel gas bubbles or dissolves gases pass through the membrane and are vented.
• the channel in the illustrated device is 0.2 mm deep, 1.5 mm wide and 120 mm long. The thin layer is said to facilitate rapid degassing. Degassing is reported to be facilitated by heat or vacuum.
• the present invention provides means and methods for selectively applying a vacuum to one or more microfluidic cavity elements in a microfluidic device.
• An internal degassing system for a microfluidic device is provided.
• the system provides for rapid degassing to facilitate device wet out and/or to remove gas bubbles or dissolved gases that can disrupt function of the device.
• the internal degassing system is particularly useful in combination with microfluidic devices that have wide, flat channels with width/depth aspect ratios greater than or equal to about 25 or devices in which vacuum must be supplied to different microfluidic cavity elements in the device.
• Such methods are of particular interest for introducing oxygen into bioreactors or for oxygenating biological fluids, such as blood.
• One particularly challenging application in the microsystems field is the maintenance of an environment for the growth and study of single cells for proteomics analysis or functional genomics research where responses to environmental perturbations provide key information.
• Gas introduction is also of interest in chemical or enzymatic reactors in which a gas, such as oxygen is a substrate. Chemical and enzymatic reactions involving gaseous substrates can be employed in various analytical procedures.
• an undesired gas the is dissolved in a liquid can be replaced by introduction of another more desirable gas into the liquid.
• dissolved oxygen which may react with a component in the liquid can be displaced from the liquid by bubbling a less reactive or non-reactive gas (e.g., nitrogen or an inert gas) through the liquid.
• a less reactive or non-reactive gas e.g., nitrogen or an inert gas
• the degasser device of U.S. patent 5,053,060 is also reported to function as a "Gasser" for introducing gases into liquids flowing though the channel formed between the blocks.
• the present invention therefore also provides means and methods for selectively introducing one or more gases to one or more microfluidic cavity elements in a microfluidic device.
• An internal "gassing" system for a microfluidic device is provided.
• the system provides for rapid introduction of one or more gases with capability for control of the rate and partial pressure of gases introduced.
• the gassing system can also be used to displaced undesired dissolved gases with desired gases without disrupting the function of the device.
• the internal gas introduction system is particularly useful in combination with microfluidic devices that have wide, flat channels with width/depth aspect ratios greater than or equal to about 25 or devices in which one or more gases must be supplied to different microfluidic cavity elements in the device.
• the present invention provides interconnect configurations and interconnect manifold devices that provide reliable, robust seals to microfluidic channels in microfluidic devices.
• the interconnects can provide for fluidic connection for fluid delivery or removal from a microfluidic device.
• the invention provides a fluid interconnect between a macro- or mesofluidic channel and a microfluidic channel in a microfluidic device which forms a face seal.
• the interconnect comprises a rigid tube with a selected sized bore and having a sealing end face with one or more ridges around the perimeter of the tubing bore and an elastomer seal layer.
• the ridge is of a selected height and shape. The ridge can be positioned at any place on the end face, however in preferred embodiments the ridge is positioned at the perimeter of the tube or centrally between the tube perimeter and the bore perimeter.
• the elastomer layer is preferably planar and flat and has an upper sealing face.
• the sealing end face of the rigid tube is positioned and held in contact with the upper sealing face of the elastomer seal layer such that the bore of the tube is aligned with a microvia of the elastomer seal layer and such that the force applied is sufficient to form a complete seal around the perimeter of the tubing bore.
• Force is typically applied to achieve a seal that withstands (i.e., does not leak) on application of a selected pressure. In a preferred embodiment, the force applied maximizes the seal engagement depth of the ridge in the elastomer.
• the sealing end face of the tube can have one or more ridges having the same or different heights above the plane of the tubing bore.
• the ridge may have a variety of shapes including those with a flat (square) ridge, a pointed ridge (V-ridge ) or a rounded ridge (e.g., semi-circle wave ridge).
• the invention provides a fluidic interconnect manifold for establishing one or more fluid connections between one or more macro- or mesofluidic channels and one or more microfluidic systems having one or more microfluidic devices and said devices being internally connected by microchannels.
• the microfluidic system (or module) has at least one planar elastomer layer having one or more microvias extending through the elastomer layer. The microvias are each of in fluid communication with a microfluidic channel within the microfluidic system.
• the manifold comprises a manifold body having a top and bottom surface and a plurality of tube cavities extending through the body from the top to bottom surface of the manifold for receiving an interconnect tube and a plurality of rigid interconnect tubes each having a microchannel dimension bores and a sealing end face at one end of the tube.
• the other end of the tube is connected to a mesoscaled fluid supply or a vacuum supply for fluid removal.
• the sealing end face of the tube optionally has a ridge as described above to facilitate seal formation.
• Each tube extends below the bottom surface of the manifold body a selected distance. The distance is selected to obtain a desired seal engagement depth with the elastomer.
• the tube end will extend outward (protrude) from the bottom surface of the manifold the height of the ridge.
• the plane of the tubing bore is approximately level with the bottom surface of the manifold body.
• the tube is selective positioned in the tube cavity with the desired protrusion and locked into place in the cavity.
• the tube can be selective locked into the cavity employing a variety of mechanical devices or may simply be bonded into the cavity with an appropriate glue or epoxy.
• a selectively adjustable claim is cooperative attached to the manifold body to receive a microfluidic device so that the planar elastomer layer of the microfluidic device is positioned with respect to the interconnect tubes extending from the manifold body.
• the microfluidic device is also aligned with respect to the interconnect tubes so that one or more microvias in the elastomer layer are each aligned with the bore of an extending interconnect tube.
• the clamp allows the force of a face seal formed between the sealing end face of the tube and the elastomer layer to be adjusted.
• Various mechanical, electromechanical and pneumatic devices can be used to activate the clamp of the manifold.
• the interconnect manifold of this invention provides a rapid, reproducible means for establishing fluid interconnects to a microfluidic device.
• the interconnect manifold of this invention may also be used to introduce electrical contacts that connect external electrical systems (e.g., power and voltage supplies, etc.) to internal microsystem electrical systems that are used for either device operation diagnostics, interconnect to internal electrical sensors, etc.
• the standard interconnect system may be configured to couple fiber optics with microsystem optical waveguides (fiber optic or otherwise). Magnetic microcoil probes may also be located employing the manifold in certain configurations.
• the present invention provides devices and methods for delivery of a gas or application of a vacuum to any microfluidic channel, reservoir, chamber or device element in a microfluidic device.
• Gas can be delivered to and vacuum can be applied continuously or selectively as desired and can be applied to any selected portion or region of a microfluidic cavity element (i.e., a channel, reservoir, chamber or device element).
• Gas can be delivered to and vacuum applied to one or more selected cavity elements within a microfluidic device that comprises a plurality of such cavities.
• GPLI gas-permeable substantially liquid impermeable membrane
• the membrane is, in turn, in fluid communication with one or more sources of gas(es) or vacuum.
• the selectively positioned membrane(s) with associated gas source or gas sources provides an internal gas delivery system for a microfluidic device. Controls external to the microfluidic device can be employed to control the type and amount of gas delivered to a given location or cavity element in a microfluidic device and/or control the time schedule or rate of delivery.
• the gas delivery system is readily adapted to any microfluidic device design and allows selective application of a gas to a selected portion of the device.
• the selectively positioned GPLI membrane(s) with associated vacuum source provides an internal degassing system for a microfluidic device. Controls external to the microfluidic device can be employed to control the schedule for vacuum application and to control the level of vacuum applied to a given location or cavity element in a microfluidic device.
• the degassing system is readily adapted to any microfluidic device design and allows selective application of vacuum to a selected portion of the device.
• the microfluidic gas delivery system comprises a microfluidic cavity element formed with a plurality of walls (including top and side walls). At least a portion of one wall forming the cavity element is a GPLI membrane. The remaining walls of the cavity element being substantially nonpermeable to fluids.
• the GPLI membrane has an outer surface and an inner surface (where outer and inner are defined with respect to the cavity of the cavity element). The inner surface is in contact with the microfluidic cavity of the cavity element for delivery of gas through the membrane to the cavity.
• a gas source which preferably comprises a microfluidic channel, is in fluid communication with the outer surface of the GPLI membrane to deliver gas to the cavity. Gas can be applied at a plurality of locations to the outer surface of the membrane employing a gas delivery plenum.
• the microfluidic degassing system comprises a microfluidic cavity element formed with a plurality of walls (including top and side walls). At least a portion of one wall forming the cavity element is a GPLI membrane. The remaining walls of the cavity element being substantially nonpermeable to fluids.
• the GPLI membrane has an outer surface and an inner surface (where outer and inner are defined with respect to the cavity of the cavity element). The inner surface is in contact with the microfluidic cavity of the cavity element for passage of gas through the membrane to be removed via the vacuum source.
• a vacuum source is in fluid communication with the outer surface of the GPLI membrane to apply vacuum to the cavity. Vacuum can be applied at a plurality of locations to the outer surface of the membrane employing a vacuum plenum.
• gases are delivered and vacuum is supplied to the GPLI membrane through one or more microfluidic channels formed in the microfluidic device.
• Microfluidic channels for gas and/or vacuum delivery are preferably distinct from any microfluidic cavity elements of the device that carry liquids.
• a selected microfluidic channel may, however, in one operating state deliver gases and in another operation state supply vacuum to the same microfluidic device.
• the use of microfluidic channels for gas or vacuum delivery allows selective delivery to one or more selected cavities of the device avoiding gas delivery or vacuum application to all cavities in the device. This is beneficial because application of a vacuum to certain device elements (e.g., a microfluidic valve or pump) can disrupt the function of the device element. Using the internal degassing device, vacuum can be applied to a microfluidic device without significant disruption of such device elements.
• a further benefit of the described systems is the ability to control the amount and type of gas within a selected region or cavity element of a microfluidic device.
• Gas can be delivered or vacuum applied to one GPLI membrane wall (or wall portion) of a given cavity element or more than one wall of a given cavity.
• Preferred GPLI membranes are made from poly(dimethylsiloxane).
• the internal degassing system can be used to facilitate wet out of microfluidic devices and is useful in combination with one or more microfluidic cavity elements having mesoscopic length and width (with dimensions greater than about 1 mm) and microscopic depth (less than about 300 ⁇ m).
• the internal degassing system is particularly useful in combination with one or more microfluidic cavity elements that have broad, flat geometry with width/depth aspect ratios of 25 or more.
• the internal degassing system can be used continuously or intermittently to remove gas bubbles from a microfluidic cavity element that might be generated during operation of a microfluidic device or device element.
• the internal gas delivery system can be used continuously or intermittently to introduce one or more gases into a microfluidic cavity element during operation of the microfluidic device or device element.
• the exemplary internal gas delivery and degassing system of this invention can be implemented in a multiple layer laminate microfluidic device (a microfluidic cartridge) by providing gas and/or vacuum routing layers and optionally gas and/or vacuum transfer layers to the desired location(s) in the microfluidic device. Routing and transfer layers have appropriately shaped holes and directional channels formed in the layer by precision etching or more preferably by precision laser cutting to provide the desired gas delivery pattern or vacuum application pattern.
• Other benefits and advantages of the interconnect seals, manifolds and gassing and/or degassing systems of this invention will become apparent on review of the following detailed description.
• Figure 1 A is a schematic cross-sectional view of a face seal formed between a tube and an elastomer layer.
• Figure IB illustrates the cross-sectional area of a flat (non-ridged) tubing end face.
• Figures 2A-E are schematic cross-sectional views of several failure modes for face seals.
• Figures 2D and E compare the effect of increasing force (F1 ⁇ F2) on channel occulsion.
• Figure 3 A is a schematic cross-sectional view of a face seal formed with a tube having a ridged end face.
• Figure 3B is a detailed view of the tube end face with ridge.
• Figures 4 A-E are exemplary interconnect tube sealing end face geometries.
• Figure 4A is a square ridge end face.
• Figure 4B is a center V-ridge.
• Figure 4C is a edge V-ridge.
• Figure 4D is an edge acute angle ridge (e.g. 30° angle with side of tube).
• Figure 4E is a semi- circle wave ridge
• Figure 5 A is a perspective view of an exemplary fluid interconnect manifold of this invention.
• Figure 5B is an exploded view of an exemplary fluid interconnect manifold of Figure 5 A.
• Figure 5C is a schematic view of a face seal formed between a ridged end face tube and the elastomer layer of a multi-layer laminate microfluidic device at a microvia in the elastomer in an interconnect manifold.
• Figure 6A-F illustrate fluid interconnect manifold of this invention with multilayer laminated microfluidic device inserted.
• Figure 6A illustrates a elastomer seal layer of a microfludic device.
• Figure 6B is an assembled exemplary multi-layer laminate microfluidic device (also called, a microfluidic device cartridge).
• Figures 6C-6F are, respectively, a top view, bottom view, a side and front view of the interconnect manifold of Figure 5 A and B with the microfluidic device of Figure 6B in place.
• Figure 7 schematically illustrates a gas delivery /removal system of this invention for delivery of one or more gases or for application of a vacuum to a microfluidic cavity element.
• FIG 8 schematically illustrates, in cross-section, a vacuum degassing system of this invention applied to a microfluidic sedimentation separation module. Vacuum is applied to the sedimentation channel and to the product channel. Vacuum is applied via a vacuum routing channel and distribution ribs.
• Figure 9A is an exploded view of a multiple layer laminate microfluidic device with 13 layers and a top and bottom planar rigid frame.
• the illustrated multiple layer device has the structure of the sedimentation module as illustrated in cross-section in Figure 8 and is implemented in a flat channel (high width/depth aspect ratio) design.
• the illustrated layers are aligned and assembled within the frame and secured through the top frame, the layers and the bottom frame.
• Figure 9B is a top view of an assembled multiple layer laminate microfluidic device of Figure 9A.
• Figure 9C illustrates an elastomer layer that is positioned on an outer layer of the laminate device to facilitate interconnect seal formation.
• Figure 10 is an exploded view of another multiple layer laminate microfluidic device with 13 layers and a top and bottom rigid planar frame.
• the illustrated multiple layer device has a flat channel (high width/depth aspect ratio) design.
• the illustrated device is an electrophoretic/isoelectric concentration module with electrodes above and below the separation channel.
• the electrodes are implemented as porous electrodes.
• a degassing system is incorporated on either side of the separation channel.
• the present invention provides means and methods for making fluid interconnects between microfluidic channels and macrofluidic or mesofluidic channels. These fluid interconnects provide a fluid interface between a microscale environment and a macro- and or mesoscale environment.
• microfluidic when used herein as in “microfluidic” refers to channels and fluid devices (valves, pumps, etc.) for storing or carrying fluids where the channel or device element (valve, pump, etc.) has at least one dimension (i.e., length, width or depth) that is less than about 500 ⁇ m.
• Microfluidic devices, device elements (e.g., valves and pumps) and channels typically exhibit low Reynolds Numbers.
• microfluidics has evolved from the more general term "micro flow devices,” where such devices were defined to be very small devices that either controlled or sensed flow in the order of microliter/min. Most microfluidic devices are characterized by low Reynolds number, non-turbulent flows.
• a microfluidic device is composed of fluid channels, and/or device elements (pumps, valves, sensors, etc.) wherein at least one and typically all fluid channels and device elements are microfluidic. More specifically, microfluidic channels include those channels where at least one dimension (height, length or width) is less than about 500 ⁇ m.
• Preferred embodiments have at least one dimension less than 400 ⁇ m, more preferably less than 400 ⁇ m, more preferably 300 ⁇ m, more preferably 200 ⁇ m, more preferably 100 ⁇ m, and in some instances on the order of 1 ⁇ m. Preferred embodiments may have two primary dimensions in the microchannel dimension range.
• the terms "mesofluidic” and “macrofluidic” refer to fluid channels and fluid device elements and systems comprised of elements that are typically larger. Mesofluidic systems, or mesosystems are typically sized from the size of a sugar cube to fist sized. Macrofluidic systems, or macrosystems are larger.
• Devices or systems that are mesoscopic or macroscopic in size can contain microfluidic elements and as such are classified as microfluidic. Often, a microfluidic system, or mesofluidic system will have a limited lifetime and will be used in concert with a permanent instrument that has high capital cost electronics, optics, and data processing and display capabilities.
• the invention described herein is compatible with such instrument systems.
• the invention described herein is also compatible with a multitude of hybrid electro-optical-mechanical hybrid microsystem modules.
• Fluid is used broadly herein to refer to liquids and gases. Fluids may vary in viscosity and may include viscose fluids, such as gels or creams. The nature and properties of the fluid are selected as is known in the art for a given microfluidic application. Fluids may contain suspended or entrained particles and may be emulsions. Fluidic channels hold, carry or transport fluids. Fluidic channels deliver sample or reagent to a microfluidic device or device element Fluidic channels also remove sample, product or waste from a microfludic device or device element. A channel to which a vacuum is applied (i.e., to remove a fluid) is a fluidic channel.
• the fluid interconnect of this invention typically provides an interface between macro- or mesofluidic supply channels (sources of fluids, vacuum lines, etc.), sample or product collection channels, and channels to analytic instruments (various spectrometers, etc.) and microfluidic channels or device elements in microfluidic devices.
• macro- or mesofluidic supply channels sources of fluids, vacuum lines, etc.
• sample or product collection channels and channels to analytic instruments (various spectrometers, etc.) and microfluidic channels or device elements in microfluidic devices.
• top refers to the orientation of elements in the drawing referred to, which is not necessarily the orientation of the elements in operation.
• Figure 1A provides a cross-sectional view of a face seal formed between a rigid tube
• the microfluidic device (6) is illustrated as a multi-layer laminate device (with a partial cross-section of the layers shown).
• the elastomer layer has a microvia (7) in fluid communication (or fluid connection) with microfluidic channel (8) formed in the layers of the microfluidic device.
• the tube In the face seal configuration, the tube is normal to the seal surface (the elastomer) and the tubing end face (4, i.e., the sealing end face) is perpendicular to the tubing bore (3).
• the tubing bore (3) is aligned with the microvia.
• the tubing bore diameter (determined by tubing wall thickness (2)) is typically about the same size as or larger than the diameter of the microvia.
• the elastomer layer needed to form the seal is larger than the area of the tubing end face and is most over significantly larger.
• Force (F) is applied to the tubing, the elastomer or both (preferably substantially normal to the elastomer seal/ tube end face plane) to press the tubing end face against the elastomer seal layer to form a face seal.
• the effective seal area, A eff is the cross-sectional area of the tube, i.e., the area bordered by the I.D. (i.e., the tube bore diameter) and O.D. of the tube, see Figure IB.
• the normal stress applied is the force divided by the area of the seal (F/Aeff).
• the face seal approach requires a maximum applied force to insure a given level of interconnect normal stress at the interface between the tube end face and the elastomer.
• F/Aeff the area of the seal
• Figures 2A-E illustrate several failure modes for face seals of Figure 1.
• Figure 2A illustrates the case where the tubing delivery mechanism is not aligned perpendicular to the elastomer seal (i.e., the tube axis is not normal to the elastomer layer). This may be caused, for example, by poor hardware registry and/or by uncontrolled flexure in the interconnect tubing and/or poor planarity of the elastomer layer in the microfluidic device. To achieve a complete seal over the entire seal area in this failure mode requires over compression of the seal. The resulting seal can readily fail because it will have an uneven distribution of interfacial stress around the seal, with large interfacial normal stress on one side of the seal and a much smaller stress on the other.
• Figure 2B illustrates a similar seal failure mode where the tube end face (4) geometry is not square (i.e., the end face is not parallel to the elastomer surface). Again there will be non-uniform circumferential stress distribution for a given applied force which will weaken the seal and make it susceptible to failure.
• Figure 2C illustrates a generic failure mode in which the end face (4) geometry is irregular.
• Figure 2D and 2E illustrate the result of over compression in a face seal of Figure 1.
• Figure 2D illustrates partial microvia occlusion (7) and
• Figure 2E illustrates complete microvia (7) occlusion.
• the sealing action is distributed over the maximum area and as such more force is required in general to insure adequate interfacial seal stress at all locations circumferentialiy around the interconnect tube.
• Minor occlusion as illustrated in Figure 2D can be tolerated, however complete microvia occlusion (and seal failure) will result, if more force is applied to increase the barreling of the seal material.
• Over compression is commonly associated with the failure modes due to irregular tube alignment or geometry. In such cases, a seal leak occurs and additional force is applied to fix the leak which can lead to over compression of the seal material and barreling of the microvia. It might be considered that simply making the microvia larger would solve the problem with occlusion. However, this solution is not desirable because it is preferred in a microfluidic system to minimize dead or unswept volumes.
• this invention provides improved tube end face geometries that decrease the occurrence of seal failure in face seals between a rigid tube and an elastomer seal layer.
• the sealing end face of the tube is provided with one or more ridges which function to lock-in the position of the tube with respect to the elastomer, minimize barreling of the elastomer to close the microvia, significantly increase localized stress in the elastomer in the critical seal regions, and/or significantly increase the achievable seal engagement depth between the tube end face and the elastomer in the critical seal region.
• the use of ridged seal end faces generates stronger seals which are less sensitive to minor perturbations in tube normality and irregularities in tube end face geometry.
• Figure 3 A is a schematic cross-sectional view of a face seal formed with a tube (5) having a ridged end face.
• the sealing end face of the tube (11) is provided with a square ridge (12) extending circumferentialiy around the perimeter of the tube (an edge-positioned square ridge).
• the ridge extends a selected height (14) from the end of the tubing bore (15) and has two walls an outer wall (16, toward the perimeter of the tube) and an inner wall (17, toward the perimeter of the tubing bore) and a top surface (18) of selected width (19), as illustrated in Figure 3B.
• the walls of the ridge are parallel to each other and the top of the ridge is perpendicular to the walls to form the square ridge.
• the ridge may be positioned anywhere between the perimeter of the tube and the perimeter of the tubing bore, but is preferably positioned at the tube perimeter or between the tube perimeter and the perimeter of the bore, rather than at the perimeter of the bore. Positioning of the ridge at the bore requires careful machining and alignment to insure that the ridge engages the elastomer. However, in a specific embodiment, the ridge can be sized, shaped (typically round) and positioned to engage the microvia in the elastomer. In this case the ridge extends into the microvia to prevent its closure on compression to form the seal.
• the ridge illustrated in Figures 3 A and 3B is formed at the edge or perimeter of the tube and the outer wall of the ridge is the outer tube wall, i.e., the outer ridge wall extends from the tube perimeter.
• the inner wall of the ridge extends from the tubing bore perimeter.
• the width (19) of the square ridge is less than the tube wall thickness (2), preferably less than about Vi of the wall thickness and more preferably less than about 1/4 of the tube wall thickness.
• Tubes are typically round with round bores, as illustrated, in the Figures herein.
• end face ridges are generally circular extending around the tubing ring that is the tubing end face.
• Fluid interconnect tubes and bores may have other geometries (e.g., oval, square, etc.) and the shape of the bore perimeter need not be the same as the perimeter of the tube (e.g., a square bore in a round tube). In these cases the path of the ridge or ridges on the end face may take the shape of the perimeter of the tube or of the bore.
• the presence of the ridge or ridges at the tubing end face decreases the seal area and focuses stress from applied force such that a much higher interfacial stress can be achieved with a much lower applied force than required for a flat tubing end face.
• the presence of ridge(s) at the tubing end face and particularly at the perimeter of the tube also greatly reduces barreling of the microvias in the elastomer.
• Figures 4 A-E are exemplary interconnect tube sealing end face ridge geometries.
• Figure 4 A is a square ridge end face as illustrated in Figure 3 A.
• Figures 4B and C illustrate V-ridges (i.e., V-shaped ridges).
• the walls of a V-ridge (16) and (17) are sloped toward each other to come to a point at the top of the ridge (18) at a selected height (14) above the end of the tubing bore.
• the point of the V-ridge can, for example, be positioned intermediate between the inner and outer tube walls (e.g., the centered V-ridge with the point of the ridge positioned half the distance between the inner and outer tube walls).
• the V-ridge point can be posited at the tubing edge with the outer ridge wall sloping up from the outer tubing wall toward the bore (as illustrated in the edge V-ridge of Figure 4C).
• the V-ridge of the can also be positioned at the inner edge of the tubing with the inner wall of the ridge sloping up from the inner tubing wall toward the outer wall of the tube.
• One of the walls of the ridge can be sloped to form a point at the top of the ridge.
• Figure 4D illustrates an outer edge-positioned acute angle ridge (12) where the inner wall of the ridge is sloped and the outer wall is perpendicular to the outer tubing wall (e.g., the illustrated ridge slopes toward the outer edge of the tube making an acute angle of about 30° with outer wall of tube which forms the outer wall of the ridge).
• the point of the acute angle ridge can be positioned intermediate between the inner and outer wall of the tube.
• the point of the ridge or the edges of the square ridges may also be rounded.
• Each of the end face ridges illustrated in Figs. 3 A and 4A-D follow or trace a circular or round path around the end face which is symmetric with respect to the tubing bore. Ridges on the end faces may trace more convoluted, yet symmetric paths or may trace asymmetric paths on the end face. In any event the ridge, must circumlocate the tubing bore so that a complete face seal can be formed.
• the sealing end face of the tube may contain more than one ridge of the same or different heights.
• a given ridge preferably maintains the same height along its path around the bore to insure uniform seal formation.
• the top of a ridge may be indented to form multiple square or rounded ridges.
• one or both walls of the ridge may be stepped, indented, or otherwise shaped to provide additional pointed, square or rounded ridges.
• Figure 4E illustrates a multiple ridge geometry. In this case a semi-circle wave geometry is imposed on a square ridge to generate two rounded ridges.
• the selection of the number and geometry of ridge(s) on the sealing end face will, at least in part, depend upon the properties of the mating elastomeric seal.
• the square geometry of the ridge of Figure 4 A is preferred for use with a more pliable elastomer, such as poly dimethylsiloxane (PDMS), urethanes (e.g., 60A urethane), or latex rubber.
• a "biting" geometry like those having a pointed ridge top ( Figures 4B-D) are preferred for use with more rigid seal materials, such as shore 80A Buna-N-rubber. Elastomer materials exhibiting higher shore A hardness values are generally more rigid.
• the selection of the type of ridge also depends in part of the application and whether or not it is intended to reuse the elastomer seal. For example, the use of a "biting" geometry, such as a V-ridge may form a stronger face seal with a given material, but its use may decrease the useful lifetime of the elastomer which may be a layer in a laminated microfluidic device.
• the ridge (12) on the end face (4) of the interconnect tube is intended to compress and engage the elastomer.
• the height of the ridge (14) is selected to achieve a desired seal engagement depth which may be adjusted to achieve desired seal properties (e.g., seal strength, seal durability, seal reusability, etc.).
• the height of the ridge is less than the thickness of the elastomer layer. In preferred embodiments, the ridge height is equal to or less than about l the elastomer thickness and more preferably equal to or less than 1/4 of the elastomer thickness. In microfluidic devices illustrated herein ridge heights of 5-20 thousandths of an inch have been used successfully to form face seals.
• a ridged end face geometry can be readily selected for use in a given application with a given elastomer seal material by routine experimentation, for example, by pressure testing of seals formed by application of a selected force to a selected elastomer and tube end face geometry. Experiments can also be performed to assess the durability and reusability of a given seal elastomer with a given ridge geometry.
• Preferred seals are those that exhibit no substantial leakage up to about the maximum pressure that can be applied to the microfluidic device before massive structural failure. Seals that exhibit no leakage at pressures greater than about 50 psi are preferred for use with microfluidic devices. Seals that exhibit no leakage at pressures greater than about 25 psi are useful in microfluidic devices.
• Face seals as illustrated herein are used to form fluid interconnects to a microfluidic channel.
• the rigid tube (illustrated in Figures 1-4) has a bore that is a macrofluidic channel which can be used to provide a fluid connection to a macro- or mesofluidic device element or device.
• the dimension of the tube is typically varied by varying the bore diameter.
• the rigid tube provides a conduit for delivery of fluids to or removal of fluids from a microfluidic channel (typically within a microfluidic device).
• the interface of the microfluidic device is typically formed by introducing a microvia (7) in an elastomer seal top or outer layer (10) of the device.
• the elastomer seal layer may extend over all or a portion of the top or outer layer of the device.
• a microfluidic device may have multiple elastomer seal layers on the same or different surfaces, which access the same or different microchannels in the device.
• a given microfluidic device may have multiple seals made of different elastomers.
• elastomer layers may be positioned on different layers.
• a microvia is formed in the elastomer as is known in the art, for example by precise (to 1- 2 thousandths of an inch) laser cutting of the elastomer.
• a microfluidic channel or device element e.g.
• a valve is in fluidic communication with the microvia, either directly or via a mesofluidic channel or device element.
• the layer or layers under the elastomer form a microfluidic channel or device element and the microvia is in fluid communication with the microfluidic channel or device element.
• microfluidic devices containing microfluidic channels and device elements.
• the fluid interconnects of this invention are employed with microfluidic devices, also called microfluidic cartridges, formed as multiple layer laminates.
• a multilayer laminate is formed as is known in the art by providing structural features, channels of varying dimensions and shapes, fluid storage chambers, fluid routing schemes, e.g., distribution channels, and device elements, such as valves in overlaid layers, which are held in desired relative alignment in a rigid support frame (e.g., made, for example, of acrylic or other rigid plastic or an appropriate metal, such as stainless steel)
• a rigid support frame e.g., made, for example, of acrylic or other rigid plastic or an appropriate metal, such as stainless steel
• Exemplary multiple layer laminate microfluidic devices are illustrated in the exploded views of a multiple layer sedimentation device of Figure 9A and the electrophoretic/isoelectric focusing device of Figure 10.
• a given microfluidic device can have one or more fluid inlets or outlets (each formed with a microvia in an elastomer) each of which may be formed in the same elastomer layer or in different elastomer layers and the material used in different elastomer layers may be the same or different.
• a face seal is formed by positioning the interconnect tube (5) such that the bore of the tube (3) is aligned with a microfluidic via (7) of the elastomer seal layer (10) and such that the end face of the tube (4) is in contact with the planar elastomer seal layer of the microfluidic device.
• Sufficient force is applied to the tube and or the microfluidic device substantially normal to the tube end face and elastomer layer to form a complete seal.
• the force applied is preferably sufficient to form a complete face seal that will exhibit no leakage on application of a pressure of 25 psi or greater in a pressure test of the seal. More preferably, the force applied is sufficient to maximize seal ridge engagement depth (preferably the entire ridge and its walls engage the elastomer) and bring the elastomer into mating contact with the flat (non-ridged) areas of the tubing end face.
• the interface components can be applied to either or both the tube and the elastomer (e.g., by applying force to the microfluidic device carrying the elastomer) and is substantially normal to the end face and elastomer sealing surface.
• the interface components (tube with end face ridge(s), elastomer and microvia) are typically clamped together to form the face seal.
• the interface components are sealed together in a multiple interconnect manifold that provides for a plurality of interconnects to one or more microfluidic devices.
• the fluid interconnects of this invention can be formed using an interface manifold as illustrated herein.
• the manifold of this invention provides for the formation of interconnects with one or more fluid inlets or outlets in one or more microfluidic device.
• the manifold provides for selective relative positioning of one or more interconnect tubes with microvias of one or more microfluidic devices.
• the manifold also provides for application of force simultaneously to more than one interconnect face seal.
• Figure 5 A provides a perspective view of an exemplary fluid interconnect manifold
• the illustrated manifold consists of a manifold body (102) , a strain relief element (105) and a clamping mechanism (110).
• the manifold body and the strain relief element have a plurality of selectively positioned cavities each for receiving one of a plurality of interconnect tubes (103).
• the strain relief element is mounted (e.g., detachably mounted with screws(107)) on the manifold body with strain relief element tube cavities 104 and manifold body tube cavities 106 (shown in Fig. 5B) aligned.
• a tube (103) enters a cavity on the strain relief element (104) and passes through the tube cavity (106) in the manifold body.
• the tube has a bore that is microfluidic.
• a locking element (111) selectively locks a tube in place in a cavity.
• the locking element in the exemplified manifold comprises a strain relief collar (112) (shown in Figure 5B) and a set screw (113). The length that each tube extends from the bottom of the manifold body can be adjusted prior to locking a tube in place.
• Clamp frame (120) is indirectly attached to the manifold body via a clamp offset element
• a clamp pad (114) is cooperatively linked to the clamp frame and moveable between the frame and the bottom surface of the manifold (1 17) by adjusting screw (121).
• the clamp pad (114) and the manifold body (102) form a cavity (125) for receiving a microfluidic device.
• the manifold body has a plurality of alignment or registry pins (122) extending from its bottom surface.
• a microfluidic device having registry holes is introduced into the clamp cavity in appropriate orientation to engage the registry pins (122) in the registry holes (not shown).
• Figure 5B provides for detail of the exemplary manifold of Figure 5 A.
• the tube cavities in the manifold body (106) can be seen. Further, the components of the locking element can be seen.
• a set screw (113) is provided in a threaded hole (114) that enters the tube cavity of the strain relief element. Tightening the set screw in the threaded hole, applies lateral force to the collar (112) which deforms to lock a tube (103) in the tube cavity.
• the ends (123) of each tube protrudes from the bottom surface of the manifold. The distance that each tube protrudes can be selectively adjusted prior to locking the tube in place.
• the set screw mechanism for locking illustrates a selectively adjustable lock.
• tubes can be locked in place by any mechanical or adhesive means, for example, the tubes may be locked in place with glue or epoxy.
• the microfluidic device clamp is illustrated in more detail in Figure 5B.
• the clamp cavity(125) is shown between the clamp pad and the bottom of the manifold.
• the clamp pad is slidably engaged with the clamp frame via two clamp guides (128). Tightening screw (121) in threaded hole (129) exerts upward force on the clamp pad to raise or lower the pad with respect to the manifold bottom (117).
• the screw (121) When a microfluidic device, is positioned in the clamp cavity with registry pins engaged and elastomer layer facing upward opposite the manifold body, the screw (121) is tightened to raise the microfluidic device and bring the elastomer layer into contact with the bottom of the manifold body and the protruding tube ends.
• the clamp is tightened to form a complete seal between the end faces of all of the interconnect tubes and the elastomer layer(s) on the microfluidic device.
• Figure 5C illustrates the formation of a face seal between a seal end face and an interconnect tube in the manifold of Figures 5 A and B.
• the tube illustrates in this figure has a ridged end face.
• the tube protrudes from the bottom of the manifold.
• the length of protrusion (P) from the top of the ridge to the plane of the end face having the bore opening is adjustable as desired, but is illustrated as about the equal to the height (114) of the ridge present on the end face.
• Microfluidic device (6) shown as a multiple layer laminate, has an elastomer layer (10) with a microvia (7) in fluid communication with a microfluidic channel(8). The device is clamped between the manifold bottom surface (117) and the clamp pad (1 14).
• the clamp has been adjusted to bring the elastomer into contact with the tube end face.
• sufficient force (F') is applied to achieve a seal of desired strength, as noted above.
• force is preferably applied through the clamp until a maximum seal engagement depth is achieved (i.e., the end face ridge fully engages the elastomer) and the non-engaged elastomer comes into flat facial contact with the bottom surface of the manifold.
• the manifold is illustrated with a tube having an end face ridge. Tubes without end face ridges can be employed in the manifold as well.
• Another seal configuration employs a tube with a ridge at the bore perimeter that is sized and aligned to enter the microvia in the elastomer. Such a configuration insures that the microvia remains open on compression, but the use of this configuration requires very precise machining of the ridge matched to the microvia and very precise alignment of the microvia and the tube.
• tube cavities in the manifold body are formed to a precision of about 1-2 thousandths of an inch to provide a very close sliding fit with the interconnect tube.
• the tube cavities in the strain relief cavity are sized to accommodate the strain relief collar which in turn is sized to receive the interconnect tube.
• the tube end face extends or protrudes from the manifold body tube cavity at the bottom surface of the manifold (distance P).
• the length of the tube protrusion can be individually set for each tube in the manifold. It may be desired to have increased or decreases lengths for different tubes. For example, it may be desired to increase the stress at one or more selected interconnects in the manifold which can be achieved by increasing the protrusion length of the selected tubes.
• protrusion lengths ranging from about 5-20 thousandths of an inch have been used.
• Precise adjustment of tubing protrusion can be accomplished using a set of custom jigs that are inserted into the clamp cavity of the manifold and clamped in facial contact with the bottom surface of the manifold body.
• a tube is inserted into the manifold body via the stress relief element with the desired jig in place to come to a hard stop against the jig. The tube is then locked in place by tightening the set screw or applying another locking mechanism.
• FIG. 5C-F illustrate fluid interconnect manifold of this invention with multilayer laminated microfluidic device (130) inserted in the manifold clamp.
• Figure 6B is an exemplary assembled multiple layer laminate microfluidic device (130) (also called, a microfluidic device cartridge) with an elastomer seal (10) and a plurality of microvias (7) on the seal layer. Registry pin holes are illustrated in the device (133) at the elastomer layer which extended through the device.
• Figure 6A illustrates a elastomer seal layer of the microfludic device of Figure 6B again illustrating microvias (7) and registry holes (13).
• Figures 6C-6F are, respectively, a top view, bottom view, a side and front view of the interconnect manifold of Figure 5 A and B with the microfluidic device of Figure 6A in place.
• microfluidic device (113) illustrated in combination with the manifold is unimportant in the context of this embodiment.
• One or more elastomer seals (10) may be mounted in any appropriate location on such a device for use with manifolds of this invention.
• the manifold is illustrated with nine interconnect tubes (103) in a linear array.
• a manifold is readily constructed to accommodate more or less interconnect tubes and the manifold body can be readily modified to any array geometry.
• Interconnects are shown on one surface of the microfluidic (e.g., a top surface), but can be provided on different surfaces of the microfluidic device (e.g., a bottom surface).
• the interconnects are illustrated on one side of the top surface, but may be provided on any point on a surface of the microfluidic device e.g., interconnects can be provided at both sides of the top or bottom surface or near the center of a surface.
• the manifold body, strain relief element, clamp frame and clamp offset are illustrated as selectively detachable (attachable to each other with screw fasteners).
• These parts of the manifold can be formed in as a unitary body by means known in the art.
• the shape and size of the clamp and manifold can be readily adapted for use with any microfluidic device.
• the manifold can be readily adapted for use with different types and sizes (either different O.D. or I.D.) Of tubes.
• Exemplary manifolds employ rigid PEEK (polyetheretherketone) tubing (Upchurch) which is available in a variety of sizes.
• the clamping mechanism illustrated in achieved by tightening a screw.
• Alternate mechanical, electromechanical, and pneumatic clamping means can be employed to apply a desired force to the elastomer and the tube end face to form the face seal. The force applied by the clamp can be monitored and/or controlled for reproducibility.
• devices and methods for internal delivery and removal of gas from microfluidic devices is provided.
• Figure 7 is a schematic drawing of a cross section of a microscale channel system for delivery or removal of gases from a microfluidic cavity element (150) with fluid inlet (151) and fluid exit (153). The direction of fluid flow in the cavity is shown by an arrow in the figure.
• the upper wall of the channel is formed from a gas-permeable, substantially liquid impermeable planar membrane (155).
• a microfluidic supply channel (157) is in fluid communication with a plurality of slots (159) which extend to the outer side of the membrane (156).
• only one wall contains a GPLI membrane, the other walls that form the cavity are substantially impermeable to gases and liquids.
• both the top and bottom (as illustrated in the drawing) walls of the cavity can be formed from GPLI membrane. This configuration provides for improved degassing efficiency.
• the supply channel 157 is connected to one or more gas sources. Valves and gas flow control can be provided external to the microfluidic device. When gas is introduced into the supply line, it is distributed through slots 159, passes through the GPLI membrane and enters cavity 150. When the system is employed for degassing, the supply channel 157 is connected to a vacuum supply, such as a vacuum pump. Valves can be provided external to the microfluidic device and vacuum pressure applied can be controlled externally. When vacuum is applied to supply channel 157, it is distributed by the slots 159 to the membrane to remove gases from the channel and from liquid in the channel. In a given device, the same supply channel can be used to apply vacuum and to supply gases, but not at the same time.
• Control valves can be provided external to the microfluidic device to switch between gas flow and vacuum.
• vacuum can be applied to facilitate system wet out, and thereafter, with the vacuum switched off or diverted, a gas can be supplied to the degassed cavity through the supply channel.
• FIG 8 is a schematic drawing of the cross-section of a sedimentation separation module (200) employing a degassing system of this invention.
• the operation of the sedimentation device illustrated is described in M. R. Holl, K. Macounova, and P. Yager (2000) Micro Total Analysis Systems 2000 pp. 319-322 (A. van den Berg et al., eds.) Kluwer Academic Publishers, which is incorporated by reference in its entirety herein.
• the module functions to separate particles by size and density and its operation is based on the principles of sedimentation field flow fractionation.
• the module has a main sedimentation cavity 205 with an upper (201) and a lower (202) wall. Sample is introduced into the cavity at inlet 151.
• a product collection channel 207 is in fluid communication with the sedimentation channel at its upper wall at a selected distance R from the sample inlet.
• the sedimentation cavity as illustrated, is operated with the cavity at an incline (illustrated at 45° from horizontal).
• the sedimentation length is determined based on the incline angle, liquid flow rate and the characteristics of the particles to be separated, as is discussed in Holl et al. (2000) supra.
• the length of the sedimentation cavity is typically selected to be longer than the sedimentation length (preferably about 2-3 times longer).
• Liquid containing a mixture of particles flows along the length of the sedimentation cavity (L) and the particles are separated by size and density. Smaller, less dense particles rise in the liquid flow towards the upper wall of the sedimentation cavity and flow into the product collection channel 207. Larger, denser particles do not rise and ultimately remain in the sediment sump 208 at the end of the sedimentation cavity.
• Separated product can be removed from the module at product exit port
• Separated product may flow into another functional microfluidic device after leaving the sedimentation module.
• the lower wall of the sedimentation cavity is formed from GPLI membrane 155a and vacuum is applied to the backside of the membrane through a plurality of slots (159a) in fluid communication with vacuum supply line 157a.
• the upper wall of the product collection channel is formed from GPLI membrane 155b and vacuum is applied to the membrane through a second vacuum supply channel 159b and a second set of slots 159b.
• Vacuum supply lines 159a and b may converge at a single vacuum inlet to the device or may be supplied independently. Application of vacuum to the sedimentation cavity and the product channel during operation of the sedimentation module did not adversely affect device function for particle separation.
• GPLI membranes suitable for use in the devices of this invention can be made of any material that is permeable to gases and substantially impermeable to liquids, such as water or aqueous solutions.
• Suitable membranes include semipermeable or microporous polymeric membranes, such as those formed from polydimethylsiloxanes (PDMS), polyurethanes, polyolefins (including polyethylenes, polypropylenes, ethylene propylene polymers, and phenolic polyethylenes), polytetrafluoroethylenes (TFE), fluorinated ethylene propylene (FEP) or polysulfones.
• GPLI polymeric materials are commercially available (e.g., PTFE materials available as MuporTM (Porex Corp., Fairburn GA), or can be prepared by methods known in the art or by routine adaptation of well-known methods.
• Micro- and nanoporous solids, such as hydrophobic nanoporous silicon, can also be employed as GPLI membranes.
• Nanoporous silica is described in U.S. patents 6,022,812; 6,037,275; 6,045,677; 6,048,804; 6,054,206.
• Hydrophobic nanoporous silica is described in published International applications: WO 00/13222 (March 3, 2000) and WO 00/44036 (July 27, 2000). All of these U.S.
• PDMS membranes are presently preferred for degassing applications.
• Spun cast PDMS membranes (0.20 inch thick) were found to provide significantly faster degassing in multiple layer laminate devices compared to PTFE membranes of comparable thickness.
• PDMS membranes (0.020" thick) were prepared by spin casting of Sylgand 184 (Dow Corning) 10 parts silicone elastomer to 1 part curing agent by weight.
• PDMS membranes have higher gas permeabilities than comparable thickness PFE membranes. Membranes with higher gas permeabilities are generally preferred for use in degassing applications. For gas delivery applications high permeability membranes are also preferred. However, it may be desirable in a given application to select a lower permeability to achieve selective gas introduction.
• Figure 9A is a perspective exploded view of a sedimentation module, as illustrated in Figure 8, implemented in a 13 layer laminate assembled between a top (201) and bottom (203) acrylic frame.
• the assembled device 200 is illustrated in Figure 9B. Note that the exploded device in the Figure 9A is inclined as it would be in operation.
• the layers are Mylar or adhesive-carrier-adhesive laminates (ACA), where the adhesive is a pressure sensitive adhesive, design features are etched or more preferably laser cut into the layers and device elements, such as channels or cavities, are formed on assembly of the layers into a laminate.
• Mylar and ACA layers and the frames are typically provided with registry holes which facilitate alignment of the layers for assembly.
• Preferred ACA layers are pressure sensitive adhesive (e.g., 3M-1151 adhesive (produced by 3M)) on a Mylar carrier.
• the sedimentation cavity is formed in an ACA layer 210 between a ribbon splitter layer 212 and a GPLI membrane 211 (0.02 inch thick spun cast PDMS was used) and a vacuum plenum layer 213 (Mylar) at the outer surface of the membrane.
• the ribbon splitter layer has a slot (215) cut to form the connection between the product collection channel() and the sedimentation cavity().
• the product channel is formed from a cavity (216) laser cut into ACA layer 214.
• a routing channel 217 from the product channel to an exit channel is also provided in layer 214.
• the product channel is formed with layer 214 between ribbon splitter layer 212 and a second GPLI membrane 218 which conforms in shape to the product channel cavity in layer 214.
• a second vacuum plenum layer (219) is positioned at the outer surface of the membrane.
• the vacuum plenum layers have a plurality of holes or slots (220) extending through the layer and distributed over the area of the layer that will contact the GPLI membrane.
• Vacuum transfer layers 221 and 222 are positioned adjacent the vacuum plenum layers.
• the outer surface of the vacuum transfer layers has a row of hole extending into the layer (see outer layer of layer 222) and the inner surface of the vacuum transfer layer, as shown on the inner surface of layer 221, has a plurality of slots (223) in fluid communication with at least one hole on the outer surface of the layer.
• the slots function for distribution of the vacuum over the area of the plenum.
• Upper and lower vacuum routing channel layers (224 and 225) are positioned adjacent the vacuum transfer layers.
• the channels in the routing layers are aligned with the holes on the outer surface of the vacuum transfer layers and extend to the side of the layer to a vacuum inlet port.
• a top and bottom Mylar capping layer (226 and 228, respectively) finish the layer assembly.
• the routing channels are formed between a vacuum routing layer and a capping layer.
• An elastomer layer (230) with microvias (7) illustrated in Figure 6B is bonded to the upper cap layer (226) via a seal attach layer. As described above the elastomer provides for the formation of interconnects to fluid channels.
• the layer assembly can be secured between the top and bottom frame with clamps, screws or other appropriate fasteners, illustrated in Figure 9B. Assembly of the layers of the device provide the internal structure as illustrated in Figure 8.
• Figure 9B is a top view of the assembled multiple layer laminate device (250) of Figure 9A.
• the elastomer is removed to show the various input and exit ports from the device.
• Various internal channels are illustrated in this view.
• Sample input 260, product output 261, and sediment output 262 connect respectively to channels 263, 264, and 265.
• Vacuum inlet 266 connects to both of channels 267 and 268 to supply vacuum to both GPLI membranes.
• This figure provides a view of the width W and length (L) of the device.
• the device is broad and flat with length and width in the mesoscopic range and depth (i.e., cavity depth, the distance between the layers that form the cavities) in the microscopic range less than or equal to 300 ⁇ m (with typically depths between about 100-300 ⁇ m).
• Vacuum is applied to the sedimentation cavity and the product channel to facilitate wet out of the device.
• the degassing system of this invention is particularly useful in wet out of devices with cavities elements having high width/depth aspect ratios.
• the system is particularly useful for cavity elements having aspect ratio greater than or equal to about 25.
• Broad, flat microfluidic device can have width/depth aspect ratios ranging from about 25 to several hundred. Device wet out, in general, becomes more difficult as the aspect ration increases above 25.
• FIG. 10 illustrates an exploded view of an electrophoretic/isoelectric module which has a degassing system of this invention (300).
• vacuum is applied to the upper and lower walls of the electrophoretic/isoelectric separation chamber.
• a broad, flat separation chamber is formed by combining layers 301-303. These layers provide the upper (302) and lower (303) separation chamber and the intervening splitter plane (301).
• the separation chamber is formed between electrode layers 304 and 305.
• Porous electrodes (307 and 308) are prepared by sputtering gold on to a plenum layer.
• the electrode layers are porous to gases and liquids.
• a plenum layer has a distribution of holes or slots through the layer and which in this case are distributed over an area matching the area of the separation chamber. Gold is sputtered on both sides of the plenum without obstructing the passages through the layer. Electrical connections are provided for application of voltage to the electrodes.
• a GPLI permeable membrane (309 and 310) covers the outer surface of the porous electrode and vacuum is supplied to the membrane via vacuum transfer layers (311 and 312) and vacuum routing layers (313 and 314) and Mylar cap layers.
• An elastomer layer can be attached to the upper Mylar cap layer with an adhesive seal attach layer to provide for seals to input and output ports on the device, as discussed above.
• Microfluidic devices incorporating the internal gas delivery and/or degassing systems of this invention can be employed in combination with the fluid interconnect and interconnect manifold devices of this invention.
• the multiple layer laminate microfluidic sedimentation device illustrated in Figure 9B is provided with an elastomer layer over the sample input, vacuum inlet, product output, and sediment output ports with microvias aligned with the ports. Registry pin holes are also provided in the illustrated device.
• the device is inserted into the clamp of the manifold as illustrated in Figures 6C-6F with the elastomer seal facing towards the bottom of the manifold body to engage registry pins extending from the body.
• Interconnect tubes are provided in the manifold for each of the active inlets and outlets.
• each of the interconnect tubes is selected and the tubes are locked into position.
• face seals are formed with the inlet and outlet microvias.
• Samples are introduced and vacuum is applied through the appropriate interconnect tubes.
• Product and sediment can be extracted from the device through the appropriate interconnect tubes.
• an electrophoretic/isoelectric concentration module assembled from the layers illustrated in
• Figure 10 can be employed in combination with the fluid interconnect module of this invention.
• FIG. 9A , 9B and 10 are illustrated for degassing of one or more microfluidic cavity elements.
• Analogous GPLI membranes and supply microfluidic channels as illustrated in these figures can be used as gas transfer and gas distribution channels for delivery of selected partial pressures of gases to selected microfluidic cavity elements.

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