Patent Application
20150166956
The invention relates to microfluidic systems, devices and methods useful for separating particulate materials from fluids. In a particular aspect, the invention relates to a method for separating cells from biological samples using the systems, devices and methods provided herein.
Preparation and manipulation of high quality cells or biomolecules are primary requirements for a variety of diagnostic or therapeutic applications. Though filtration techniques are commonly used for capturing cells, they pose various challenges including the inability to obtain high separation efficiencies for heterogeneous cell populations, clogging of pores or harsh filtration conditions causing cellular damage. The challenges are exacerbated when filtering larger volumes of crude biological samples. In addition to filtration, a number of microfluidic separation techniques exist that rely on the application of a force, which acts to push or pull cells in a direction perpendicular to the direction of flow of the sample fluid being processed. Several of these continuous flow techniques have recently proven useful in efficiently separating out cells from blood, including hydrodynamic filtration, inertial and deterministic lateral flow separation. However, most of the techniques require pre-dilution of the blood sample and are limited to relatively low volumetric flow rates.
Recent developments on “filter-free” mechanisms for biological sample preparation offer portable purification devices for limited volumes. Primary applications have been in point-of-care diagnostics, where relatively small samples are collected and directly processed within the collection vessel. However, there remains a need to expand these simple separation methods to larger volumetric flow rates to provide alternatives to large scale centrifugation and filtration techniques.
A well-known continuous flow separation technique is field flow fractionation (FFF) in which differential retention of particles being eluted through a microchannel results in separation of particles having different characteristics. However, the relevance of field flow fractionation for whole blood separation remains uncertain as most studies suggest the need for relatively dilute starting blood samples. Recent combinations of newer separation techniques, such as hydrodynamic filtration and inertial focusing, have increased the traditional throughput limits associated with continuous flow separations. However, each of these “high throughput” implementations requires carefully controlled flow rates and/or upstream sample pre-filtration or dilution.
Sedimentation-based devices may provide simpler methods of cell and/or particle separation from fluids containing them without the need for careful fluid flow control and/or excessive sample dilution. However, there exists a need to provide devices and methods that enable high speed separation of particulates such as cells and/or dispersed particles from fluids containing them without the need to augment sedimentation rates via capital intensive equipment, such as centrifuges. A fast and efficient separation and collection of particles or cells from a large sample volume without complex equipment is an unmet need. Therefore, inexpensive devices that can accelerate particle separation via sedimentation, and enable use of a large sample volume with minimal human intervention are highly desirable.
In one embodiment, the present invention provides a device for separating particulates dispersed within a base fluid and having a relative density difference compared to the base fluid, comprises a microchannel of length l and height h disposed between a fluid inlet and a fluid outlet; a microporous body defining at least a portion of the microchannel; and a collection chamber on an opposing side of the microporous body; wherein, the particulates and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber; and wherein the microporous body operationally generates a fluid flow regime comprising a first fluid flow having a first flow rate through the microchannel and a second fluid flow having a second flow rate through the collection chamber and the second flow rate is a fraction of the first flow rate.
One embodiment of a device for separating one or more cells dispersed within a base fluid and having a relative density difference compared to the base fluid, the device comprises a microchannel of length l and height h disposed between a fluid inlet and a fluid outlet; a microporous body defining at least a portion of the microchannel; and a collection chamber on an opposing side of the microporous body; wherein the cells and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber; and wherein the microporous body operationally generates a fluid flow regime comprising a first fluid flow having a first flow rate through the microchannel and a second fluid flow having a second flow rate through the collection chamber and the second flow rate is a fraction of the first flow rate.
In another embodiment, a method for separating particulates dispersed within a base fluid and having a relative density difference compared to the base fluid, comprises: providing a separation device comprising: a microchannel of length l and height h disposed between a fluid inlet and a fluid outlet; a microporous body defining at least a portion of the microchannel; and a collection chamber on an opposing side of the microporous body; wherein the particulates and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber; introducing a sample of unprocessed fluid comprising particulates dispersed within a base fluid into the microchannel via the fluid inlet; separating at least a portion of the particulates from the unprocessed fluid to provide a stream of processed fluid at the fluid outlet; and recovering at least a portion of the particulates initially present in the unprocessed fluid in the collection chamber; wherein the particulates and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber; and wherein the microporous body operationally generates a fluid flow regime comprising a first fluid flow having a first flow rate through the microchannel and a second fluid flow having a second flow rate through the collection chamber and the second flow rate is a fraction of the first flow rate.
One embodiment of a method for separating cells dispersed within a base fluid of whole blood sample, comprises providing a separation device comprising: a microchannel of length l and height h disposed between a fluid inlet and a fluid outlet; a microporous body defining at least a portion of the microchannel; and a collection chamber on an opposing side of the microporous body; wherein the particulates and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber; introducing the whole blood sample of unprocessed fluid comprising cells dispersed within a base fluid into the microchannel via the fluid inlet; separating at least a portion of the cells from the unprocessed fluid to provide a stream of processed fluid at the fluid outlet; and recovering at least a portion of the cells initially present in the unprocessed fluid in the collection chamber; wherein the particulates and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber; and wherein the microporous body operationally generates a fluid flow regime comprising a first fluid flow having a first flow rate through the microchannel and a second fluid flow having a second flow rate through the collection chamber and the second flow rate is a fraction of the first flow rate.
These and other features, aspects, and advantages of the present invention will become better understood when the following detailed description is read with reference to the accompanying drawings in which like characters represent like parts throughout the drawings, wherein:
Separation of particulates dispersed within a base fluid (collectively “the unprocessed fluid”), for example separation of blood cells dispersed within blood plasma, or separation of particulate impurities dispersed in water, may be effected using various embodiments of systems, devices and methods provided by the present invention. Embodiments of the device and its device components (e.g.
To more clearly and concisely describe the subject matter of the disclosed invention, the following definitions are provided for specific terms, which are used in the following description and the appended embodiments. Throughout the specification, exemplification of specific terms should be considered as non-limiting examples.
The terms “particulate” and “particle”, and their plural referents “particulates” and “particles”, are used interchangeably herein and are intended to have the same meaning, particle being treated as a synonym for particulate. As used herein, the term “particles” refers to a portion of the fluidic sample loaded into the device which excludes the base fluid. The term “particles” includes without limitation cells, inorganic colloids, polymers, biopolymers, immiscible liquids, heterogenous solids, and nominally gaseous/liquid materials in a solid phase. For example, blood cells, grains of sand, oil droplets, nucleic acids, or ice crystals are all particles.
The terms “microporous body” and “microporous surface” may be used interchangeably herein and are intended to have the same meaning.
As used herein, the term “operationally generates” refers to a function of generating one or more fluid flow regimes by microporous surface during operation of the device. For example, when a fluid sample loaded into the device and flows through the microchannel for separation of the particles from the fluid, the microporous surface generates a field of flow with two fluid flow regimes under the operating conditions of the device.
As used herein, the term “fluidic sample” refers to a mixture that comprises a non-fluid component and a fluid component. The mixture may be heterogeneous or homogenous in nature. The loaded sample is interchangeably used herein with a “sample”, “fluidic sample” or “fluid loaded into the device”. The sample may comprise without limitation, a fluid comprising one or more particles, a fluid comprising one or more cells, water with particles, water-oil emulsion, or a fluid with impurities. For example, a sample comprises a slurry of sand and water, or a fluidic sample comprises cells and plasma. The term “fluidic sample” is used interchangeably and without limitation with the term “dispersion”, “particle dispersion”, or “cellular dispersion” when identifying a generic class of fluidic sample. In some embodiments, a cellular dispersion refers to a sample of cells dispersed in a fluid, for example blood cells dispersed in plasma, cells dispersed in growth media, or cells dispersed in stabilization media.
As used herein, the term “base fluid” refers to a portion of the fluidic sample which excludes the particles. For example, a whole blood sample comprises blood cells in plasma, wherein the plasma is a base fluid. For another example, an aqueous sand dispersion comprises sand in water, wherein water is a base fluid.
As used herein, the term “relative density difference” refers to a difference between the density of the particulates present in the base fluid and the density of the base fluid.
As used herein, the term “sediment” refers to particle motion induced by an applied force field. Motion or movement of particulates in a fluid in response to a force may be active or passive, and the movement is referred to herein as sedimentation. For example, in cases where the force of gravity augments the action of an externally applied electric field in inducing particulate movement. Sedimentation usually provides a simple means of separating particulates from a base fluid. In one embodiment, in an aqueous sand dispersion, the sand particles have a density greater than that of the base fluid and sediment in the direction of the gravitational field. In another embodiment, in an oil-in-water emulsion, the oil droplets have a density less than that of the base fluid and transit in the direction opposing the gravitational field. In another embodiment, in a dispersion of magnetic particles, the magnetic particles are sediment in the direction of an applied magnetic field. In another embodiment, in a dispersion of charged particles, the charged particles differentially sediment based on their polarity within an applied electric field.
The singular forms “a”, “an” and “the” include plural referents unless the context clearly dictates otherwise.
Approximating language, as used herein throughout the specification and claims, may be applied to modify any quantitative representation that could permissibly vary without resulting in a change in the basic function to which it is related. Accordingly, a value modified by a term such as “about” is not to be limited to the precise value specified. In some instances, the approximating language may correspond to the precision of an instrument for measuring the value. Where necessary, ranges have been supplied, and those ranges are inclusive of all sub-ranges there between.
In one or more embodiments, a device is configured to separate particulates present in a fluidic sample. The sample may comprise particulates dispersed in a base fluid and the particulates have a relative density difference compared to the base fluid. In these embodiments, the device for separating particulates from the base fluid comprises a microchannel of length l and height h disposed between a fluid inlet and a fluid outlet; a microporous body defining at least a portion of the microchannel; and a collection chamber on an opposing side of the microporous body. The particulates and a portion of the base fluid traverse the microporous body under the influence of an external force field, and are entered and collected in the collection chamber. The microporous body operationally generates a fluid flow regime comprising a first fluid flow having a first flow rate through the microchannel and a second fluid flow having a second flow rate through the collection chamber and the second flow rate is a fraction of the first flow rate. Non-limiting examples of an embodiment of the device are shown in
The term microchannel is used to describe the channel into which the particulates dispersed in a base fluid are introduced. As noted, the microchannel comprises an inlet and an outlet; and one or more walls, wherein the one or more walls comprise a microporous body, such as a microporous surface. The inlet of the microchannel may be configured to receive a sample, such as a biological sample, a water sample or an oil sample. The inlet and the outlet may be present, without limitation at the ends of the channel. The microchannel may comprise one or more walls, and a microporous surface constitutes the one or more walls of the microchannel.
The microchannel is further described as microfluidic channel since at least one of the dimensions of the microchannel is appropriately measured in microns. In various embodiments of the device, a microchannel has a length l and a height h. In some embodiments, the microchannel is a horizontal channel configured to permit the flow of a fluid at a predetermined flow rate. The device may be set for a specific flow rate as desired before operating the device. Typically, the microchannel has a length appropriately measured in units larger than microns, for example millimeters (mm), centimeters (cm) or meters (m). In some embodiments of the device, the microchannel has a length l between 5 mm and 25 cm. In another embodiment, the microchannel has a length l between 10 mm and 10 cm. In yet another embodiment, the microchannel has a length l between 10 mm and 25 mm
The microchannel may be of a regular shape (for example cylindrical) and be of uniform height h. In one embodiment, the average height of the microchannel is between about l and about 1000 microns (μm). In an alternate embodiment, the average height of the microchannel is between about 10 and about 500 microns. In yet another embodiment, the average height of the microchannel is between about 20 and about 250 microns. The microchannel may be of an irregular shape (for example a channel defined in part by an undulating wall) and be characterized by a plurality of heights h. Typically, however, the microchannel is rectangular in shape and is defined on three sides by walls enclosing the microchannel and on a fourth side by the microporous body.
As noted, the microchannel comprises a microporous body, in some embodiments, the microporous body is a microporous surface. In one embodiment, the microporous body constitutes one or more walls defining the microchannel. The microporous body may be a membrane or a solid body through which holes have been created. In one or more embodiments, the microporous body comprises pores originating at a first surface of the microporous body and terminating at a second surface of the microporous body. For example, pores traversing a film may be created by chemical etching techniques and/or laser ablative techniques.
The term “microporous” is used herein because the pores have dimensions appropriately measured in microns. In one embodiment, the pores have an average diameter between about 1 micron and about 500 microns. In an alternate embodiment, the pores have an average diameter between about 10 microns and about 250 microns. In yet another embodiment, the pores have an average diameter between about 20 microns and about 100 microns. In one embodiment, the porosity of the microporous body is between about 10 and about 75 percent. In an alternate embodiment, the porosity of the microporous body is between about 20 and about 65 percent. In yet another embodiment, the porosity of the microporous body is between about 30 and about 60 percent.
As noted, in one embodiment, the microporous body may be a microporous film such as a monofilament screen or mesh made from, for example, polyester, nylon, polypropylene. Alternatively, the microporous body may be a chemically-etched KAPTON, titanium, or NiTinol film. In one embodiment, the microporous body is a laser etched organic film made from an organic polymeric material such as KAPTON.
As noted, the microchannel is disposed between a fluid inlet and a fluid outlet. Fluid enters the microfluidic separation device via the fluid inlet as unprocessed fluid, travels the length of the microchannel to the fluid outlet. During the passage of fluid from the inlet to the outlet, particulates migrate out of the microchannel and enter into the collection chamber under the influence of the fluid flow through the microchannel and one or more additional forces such as the ambient gravitational field, an applied force field, or buoyancy forces. The action within the microchannel converts the unprocessed fluid introduced at the fluid inlet into processed fluid merging at the fluid outlet. In one embodiment, the fluid inlet is configured to receive and hold a fluid sample comprising particulates dispersed within a base fluid, and then to deliver the fluid sample to the microchannel under the influence of a device component, for example a vacuum line applied to the fluid outlet.
As noted, the device comprises a collection chamber in fluid communication with the microchannel configured such that the collection chamber is situated on an opposing side of the microporous body. Typically, the collection chamber is configured such that every pore of the microporous body enables direct fluid communication between the microchannel and the collection chamber. The portion of the microchannel-microporous body interface is referred to herein as the separation zone, wherein the condition of direct fluid communication between the microchannel and the collection chamber through each of the pores is met. The collection chamber is configured to collect particles, which sediment from the fluid sample during processing. For example, the collection chamber collects the cells from a blood sample that is loaded to the microchannel of the device. In the collection chamber, the fluid may be in a quasi-static flow during operation. In some embodiments, the particles sediment and pass through the pores of the microporous surface and are entrapped within the collection chamber. The collection chamber may comprise one or more outlets for collecting the particles which sediment through the microporous surface. The outlet may be connected to a conduit or a syringe to retrieve the particles from the collection chamber of the device. For example, in the case of a blood sample, the separated cells are recovered from the collection chamber using a tube or syringe for downstream applications. In one or more embodiments, the collection chamber is coupled to a pump to recover the particles from the collection chamber during operation.
In various embodiments, the collection chamber is primed, may be partially or completely filled with a priming fluid (e.g. buffer solution) prior to the introduction of the unprocessed fluid into the microchannel. In some embodiments, the collection chamber is filled with a priming fluid prior to initiate a flow through the microchannel. As fluid flows through the device, a first flow regime is established in the microchannel and a second flow regime is established in the collection chamber, the second flow regime being characterized by a lower overall flow rate than that of the first flow regime. In various embodiments, an average time required for the particles to sediment through the microporous body is less than the time required for the particles to transit across the length l of the microchannel.
In one or more embodiments, the device further comprises an applied force field across one or more dimensions of the microchannel, for example across the height h of the microchannel to cause the particles to pass through the microporous surface and into the collection chamber. The applied force field may function across the height h of the microchannel under operating conditions of the device. The applied force field may decrease the time required for the particles being impelled through the microchannel by the moving fluid at relatively high flow rate to sediment through the microchannel and be trapped within the collection chamber, wherein the fluid flow rate is relatively low.
In one or more embodiments, an external force causes the particulates to migrate through the microporous body. For example, the external force may be ambient gravity at times herein referred to as ambient gravitational forces. In some embodiments, the applied force field is selected from a magnetic field, an electric field, an electrophoretic field or combinations thereof. In an alternate embodiment, the external force may be a combination of the ambient gravitational forces present together with an applied force field, such as an applied electric field or magnetic field. In an alternate embodiment, the forces causing the particulates to migrate across the microporous body are exerted by the fluid being processed. For example, buoyancy forces may dominate gravitational forces in the separation of oil in water emulsions. In some embodiments, the device further comprises one or more controllers for controlling the applied force field.
In one embodiment, the microfluidic separation device is configured such that the ambient gravitational force acts across the height h of the microchannel and causes particulates dispersed within the base fluid to sediment through the microporous body and into the collection chamber.
The particulates dispersed in the base fluid and traverse together with a portion of the base fluid itself under the influence of passive and/or active forces through the microporous body and are separated from the base fluid. The particulates and a portion of the base fluid are collected in a collection chamber disposed on an opposing side of the microporous body. The fluid sample comprises a plurality of particles in a fluid base, wherein the particles may have a relative density difference compared to the fluid base.
In various embodiments, the separation of particulates from the base fluid occurs as the fluid is flowing through the microchannel for processing. Having traversed the microporous body, the particulates continue to migrate away from the microporous body under the influence of the passive and/or active forces. The base fluid is typically much less susceptible to the influence of the passive and/or active forces as compared to the particulates, and in various embodiments the base fluid entering the collection chamber may remain in relatively close proximity to the microporous body, and is subject to return to the microchannel by re-traversing the microporous surface. This dynamic of particulates and base fluid traversing and base fluid re-traversing the microporous surface creates a flow regime within the collection chamber which has a lower flow rate relative to the flow rate of the fluid being processed through the microchannel. In some embodiments, the microporous surface operationally generates a fluid flow regime comprising a fluid with high flow rate flowing through the microchannel and a fluid with low flow rate flowing through the collection chamber.
As noted, the device for separating particles from a fluid sample comprises a plurality of particulates having a relative density difference when compared to the fluid base. The relative density difference, at least in part, enables the particles to sediment through the microporous surface. The separation of particles using the device and the associated methods, at least in part, is based on sedimentation of the particles through a microporous body (surface).
Sedimentation is one of the simplest methods of cell or particle separation, wherein the separation is based on the density and size of the particle itself. However, sedimentation is typically only thought of as a useful method of high speed cell separation if coupled to a centrifuge and/or density gradient medium (DGM). In the device, as noted, the force which causes the particulates to traverse the microporous body may be an active force such as an applied electric field, a passive force such as the ambient gravitational field, or a combination thereof. For example, in cases where the force of gravity augments the action of an externally applied electric field in inducing particulate movement or sedimentation. In some cases, sedimentation rates are too low to be useful for applications, such as blood cell separation from plasma, or separation of particulate impurities from water. Thus, separation of particulates using the ambient gravitational field or natural particle buoyancy at useful rates has remained an objective.
In the device of
v is the sedimentation rate, d is the diameter of the particle, ρp is the density of the particle, ρ1 is the density of the DGM, η is the viscosity of the DGM, and gc is the centrifugal force. In the case where the centrifugal force is simply equal to gravity, sedimentation of blood components is slow with erythrocytes settling at ˜1 micron/s. Previously, this has limited the utility of the earth's gravitational field (g) for high speed, sedimentation-based cell separation, and necessitated the equipment intensive centrifugation approach. As an example, centrifugal forces of 10-800×g are typically applied to blood to separate out specific cell types, which are stratified across the DGM. With the application of the excess centrifugal force, separation can take place on the order of minutes. A simpler and automated separation is enabled by the claimed device that can use only the earth's gravitational field to achieve similar separation rates. It should be noted that other forces would follow a similar relationship where centrifugal, or gravitational force fields could be substituted without limitation for magnetic, electric, or dielectric fields.
As noted, the sample loaded to the device may be processed in the microchannel, as the particles or cells from a fluidic sample or oil from a water sample may be separated and sediment through the microporous surface and enter into the collection chamber. The particles, cells or other materials present in the fluidic sample may be of interest, which are collected or captured in the collection chamber and described herein as “captured particles” or “captured cells”. The captured particles or captured cells may be recovered from the collection chamber of the device, which are described at times herein as “recovered particles” or “recovered cells”. In some embodiments, the recovery of particles or cells is less than 100%, wherein the number of captured particles or captured cells in the collection chamber is different than the number of recovered particles or recovered cells.
The fluid that flows through the microchannel and emerges at the fluid outlet after removal of at least a portion of the particulates in the unprocessed fluid (at times herein referred to as the “loaded sample”) may be recovered from the device's fluid outlet. The fluid recovered from the fluid outlet may be referred to herein as “processed sample” and/or “processed fluid”. In some embodiments, the processed sample may be a sample of interest. For example, the processed water sample recovered after removal of the particles is purified water, which is a sample of interest. In some other embodiments, the processed sample may be a waste product. For example, in case of a purification of cells from a whole blood sample, the plasma generated as “processed sample” is collected to a waste chamber and the sample of interest may be the recovered blood cells. In some other examples, the processed plasma may be a sample of interest, depending on the user requirement. In one or more embodiments, the processed sample is collected from the device outlet, wherein the outlet is coupled to a pump to drive out the processed sample.
As noted, the device is configured such that the microporous surface operationally generates a fluid flow regime comprising a high flow rate portion flowing through the microchannel and a low flow rate portion flowing through the collection chamber. The microporous surface effectively generates a resultant force derived from a fluid drag force in the direction of fluid flow across the length l of the microchannel and a force for particle sedimentation across the height h of the microchannel. In some embodiments, the resultant force favors sedimentation and captures the particles in the collection chamber. The fluid flow rate above the microporous surface may be high, which allows processing of larger sample volume using the device compared to the sample volume typically used for known devices.
The device may be configured, such that the time required for the particles to sediment through the microporous surface is less than the time required for the particles to transit across the length l of the microchannel. The particle capture efficiency and/or volumetric throughput may be improved by either increasing the length l or decreasing the height h of the microchannel. An increase in length l of the microchannel increases the time available for the particles to interact with the microporous surface. As noted, “capture efficiency” refers to a probability function, dependent on the average number of particles interacting with the pores during transit through the device and the probability of particle passage through a pore for each such interaction. The probability of particle passage through the pore for each interaction may depend on the ratio of particle/pore diameters.
In addition to particle collection, the device may be configured to distinguish particles with respect to size, sedimentation velocity, or density. The particles with different size may be separated using the device. The particles having different sedimentation velocity may also be separated using the device. In some embodiments, the particle has an average diameter between 1 and 250 μm. As the microporous surface comprises pores with an average diameter in a range of 1 to 500 μm, the particles that are smaller than the pore size pass through the microporous surface. The particles, which are passed through the pores of the microporous surface, are captured in the collection chamber.
One embodiment of a device for separating one or more cells of average diameter (d) from a blood sample, comprises a microchannel of length l and height h comprising an inlet and an outlet; a microporous surface with an average pore diameter (p) and porosity (q), on one or more walls of the microchannel; a collection chamber on the opposing side of the microporous surface; and an applied gravitational field across the height h of the microchannel to sediment the cells through the microporous surface into the collection chamber. In this embodiment, as noted before, the microporous surface operationally generates a fluid flow regime comprising a high flow rate portion that flows through the microchannel and a low flow rate portion that flows through the collection chamber. In this embodiment, an average time required for the cells to sediment through the microporous surface is less than the average time required for the cells to transit across the length l of the microchannel.
As illustrated in
As shown in
In some embodiments, a top view of the device 10 comprises a microporous surface 32, as shown in
The device enables high speed separation without using a centrifuge or additional equipment. In an exemplary embodiment of the device 10, a high velocity flow-stream flows across a wide sedimentation area of the microchannel 16 over the microporous surface 32. For example, the microchannel comprises a sedimentation area of 10 mm×400 mm over the microporous surface. In one embodiment, the flow-stream within the microchannel 16 extends across the microporous surface 32, which covers the collection chamber 22. Unlike a filtration device, a pressure drop across the microporous surface 32 is significantly minimized as the fluid stream enters into the microchannel 16 through the opening 18 and spreads over the wide area of the microporous surface 32. The majority of the fluid-flow occurs over the microporous surface 32. The device is configured such that the fluid sample is entered into the microchannel 16, spread over the microporous surface 32. The particles or cells of the fluid sample are sediment through the pores of the microporous surface, and are trapped into the collection chamber 22 underneath the microporous surface 32.
In an example of a method for separating one or more particles from a fluidic sample, the method comprises loading the sample to a device, wherein the device comprises a microchannel of length l and height h, comprising an inlet and an outlet; a microporous surface constitutes one or more walls of the microchannel; a collection chamber on an opposing side of the microporous surface, and an applied force field across the height h of the microchannel to sediment the particles through the microporous surface and capture into the collection chamber. The method further comprises contacting the sample with the microporous surface; generating a fluid flow regime comprising a high velocity portion flowing through the microchannel and a low velocity portion flowing within the collection chamber; sedimenting the particles through the microporous surface into the collection chamber; collecting the particles in the collection chamber under the applied force field and retaining a fluid in the microchannel; and driving out the retained fluid through the outlet of the microchannel. An average time required for the particles to sediment through the microporous surface is less than the average time required for the particles to transit across the length l of the microchannel. The fluid recovered after sedimentation of the particles or cells from the sample comprises a reduced number of particles or cells compared to the number of particles or cells initially present during loading of the sample.
In one embodiment, the sample is a whole blood sample, wherein the method is employed to separate one or more cell types from the blood sample. In this embodiment, the method comprises loading the blood sample to the device comprising a microchannel with a microporous surface and a collection chamber, contacting the blood sample to the microporous surface; generating a fluid flow regime comprising a high velocity portion flowing through the microchannel and a low velocity portion flowing through the collection chamber; sedimenting the cells through the microporous surface and capturing into the collection chamber under the applied force field and retaining a plasma fluid in the microchannel. The retained fluid, here plasma, is driven out through the outlet of the microchannel, wherein a time required for the cells to sediment through the microporous surface is less than the time required for the cells to transit across the length l of the microchannel.
Examples of methods for separation of cells from a whole blood sample are illustrated in
The spreading of the fluid flow stream across the wide separation surface provides a significant opportunity for interaction of the particles with the surface. The addition of a static collection chamber 22 allowed sedimentation of the particles into the collection chamber, without traversing the particles across entire length l of the microchannel, unlike standard centrifuge tubes or large sedimentation tanks. The pressure drop across the microporous surface is minimized enough such that re-entry of the particles into the high speed flow-stream and loss of particles into the waste chamber is minimized, which is demonstrated by showing clear plasma in
Another embodiment of the device 90 is shown in
As noted, the sample loaded to the device is a fluidic sample. In some embodiments, the fluid may include a biological sample, water sample, aqueous slurry, oil slurry, oil-water emulsion or combinations thereof. As noted, the biological materials used in the embodiments may comprise a physiological body fluid, a pathological body fluid, a cell extract, a tissue sample, a cell suspension, a forensic sample and combinations thereof. In some embodiments, the biological material is a physiological body fluid or a pathological body fluid, such as the fluid generated from secretions, excretions, exudates, and transudates, or cell suspensions such as, blood, lymph, synovial fluid, semen, saliva containing buccal swab or sputum, skin scrapings or hair root cells, cell extracts or cell suspensions of humans or animals. In some embodiments, the physiological/pathological liquids or cell suspensions may be extracted from plants. In one or more embodiments, the extracts or suspensions of parasites, bacteria, fungi, plasmids, or viruses, human or animal body tissues such as bone, liver or kidney. In some embodiments, the sample fluid is a biological sample selected from whole blood, cell extract, tissue extract or combinations thereof. In one embodiment, the sample fluid comprises whole blood.
In one or more embodiments, the particle comprises red blood cells, white blood cells, platelets, biological cells, tissue fragments, metals, minerals, polymers or combinations thereof.
In some embodiments, the device 10 (
The applications for the device 10 (
In one or more embodiments, the device 10 (
In some embodiments, the device is configured to integrate with another device or system, more specifically with an analytical device. As noted, the device may have one or more coupling means through which the device may integrate with another device depending on the requirement. The coupling means may include but is not limited to, an adapter, or a connector. In some embodiments, the device itself is configured to have one or more holders, connecting ports or combination thereof, which mechanically couples the device to another device. The device may be electronically or mechanically coupled to another device for downstream applications.
In one or more embodiments, the device further comprises one or more containers for collecting waste or fluid after separation of the particles or cells. In embodiments, where blood is a sample, the plasma generated after separation of the cells may be collected to a waste chamber. In some other embodiments, when the sample is water or oil, after separation of the particles, the purified fluid is collected to a collection chamber coupled to the outlet. This collection chamber is different than the collection chamber for particles present opposing side of the microporous surface. In one or more embodiments, the non-limiting examples of containers are bag, chamber and vessels. The containers may be disposable or reusable. Various components of the device may be operationally connected to each other using conduits, holder, adapter, or valves. The device may further comprise one or more sensors, such as temperature sensor, pressure sensor, flow sensor or pH sensor, depending on the requirement.
A microfluidic separation device housing was created using a commercially available rapid prototyping instrument and an ABS-like photopolymer (DSM Somos WaterShed XC 11122). The microfluidic separation device was assembled from three parts, created on the rapid prototyping instrument together with a porous KAPTON film which served as the microporous body or microporous surface, and a set of pressure sensitive adhesive films which joined the parts together and served to create the microchannel. Useful reference may be made to
The first part 101 (
Two different types of microporous bodies were used in the devices. As mentioned, the first type of microporous body was formed from a KAPTON sheet with laser-machined pore arrays having average pore diameter of about 21.7 microns with a 50 micron center-to-center pore spacing. The second type of microporous body employed was a medical grade polyamide woven mesh having 40 micron pores and 40% porosity (SEFAR MEDIFAB, 07-40/40).
The collection chamber 22 defined by second part 102 had dimensions of 40 millimeters by 10 millimeters by 2 millimeters, resulting in a 750 microliter (μL) holding volume. As configured, the microfluidic separation device could process a total volume of about 0.5 milliliters of blood before the collection chamber reached its maximum cell holding capacity.
The microfluidic separation device was equipped with two ports 123 and 124 (
Once primed, a sample fluid comprising particulates dispersed with a base fluid (such as whole blood comprising blood cells are the particulates) dispersed within blood plasma (the base fluid) was introduced into fluid inlet 12 and was made to flow through the microchannel 16 contact the upper surface of the microporous body by the application of a vacuum on the fluid outlet 14 side of the device. Owing to the gravitational forces present, particulates within the sample fluid flowing within the microchannel tended to sediment downwardly through the pores of the microporous body and into the underlying water-filled collection chamber, wherein the downward motion of the particulates continued. Operation of the microfluidic separation device typically effected at least a substantial separation of particulates and base fluid. The processed fluid, a mixture of the base fluid and water exchanged with the collection chamber was collected in the fluid outlet.
Cell Separation-Whole blood or cell-suspensions were used to test collection efficiencies of mammalian cells using the microfluidic separation device. Typical white blood cell dimensions are 10 to 12 microns, and thus the microporous body having 21.7 micron pore diameters provided an about a 2 to 1 ratio of pore diameter to cell dimension. A syringe pump was attached to the fluid outlet used to create a flow of the cell-containing sample in the fluid inlet through the microchannel and into the fluid outlet at defined rates (PicoPlus syringe pump, Harvard Apparatus) from 50 to 1000 microliters per minute (μL/min). Phosphate buffered saline (PBS), deionized water or cell culture medium were used as priming fluids. Separated base fluid was collected by pipetting from the fluid outlet. Separated cells were recovered from the collection chamber using a syringe. In all cell separation examples disclosed herein, the external force field which caused the cells to traverse the microporous body from the microchannel to the collection chamber was gravity and the microfluidic separation device was oriented such that the passage of cells from the microchannel to the collection chamber was in a downward direction.
Cell collection efficiency was assessed on a SysMex XE2100 Hematology Analyzer and provided red and white blood cell counts from whole blood samples. White blood cell viability and collection efficiency were assessed on a NucleoCounter® *(chemometec) Live/Dead Analyzer. Collection efficiencies were recorded as the ratio of the number of cells introduced through the device fluid inlet 12 (
Computational Fluid Dynamics: A finite element method analysis solution to the full Navier-Stokes equation was also performed using Comsol® multiphysics. Velocity fields were extracted for scaled devices (large enough to model ten pores across the microporous surface) with and without the microporous surface. This allowed visualization of the effect of the microporous surface on flow conditions within the collection chamber. The output boundary condition was set to pressure at 0 Pa, inflow velocities were set to match the 50 uL/min experimental conditions. Collection efficiencies over a range of particle/fluid density ratios were estimated using the particle tracing function in Comsol®, and counting the number of particles that entered the pore array. Additional simulations were then run to investigate the effect of changing the particle/pore size ratio for densities that match those reported for white blood cells and plasma in the literature.
Whole blood (0.5 mL) was introduced into to the fluid inlet of a primed microfluidic separation device and caused to flow through the device at a flow rate of 1000 μl/min A microfluidic separation device without a microporous body that separate the collection chamber from a microchannel was used as a control. This device had an idealized configuration and fluid dynamics is shown in
Whole blood (0.5 mL) was introduced into to the fluid inlet of a primed microfluidic separation device and caused to flow through the device at a flow rate of 50, 250, 500 or 1000 μl/min The microfluidic separation device identical to that used in present Example with the exception that no microporous body to separate the collection chamber from a microchannel was used as a control. Data are gathered in
Red blood cell separation was carried out with a flow rate of 1000 μl/min on a sample consisting of 0.5 mL of whole blood using a primed microfluidic separation device disclosed herein. Separation of red blood cells from the processed fluid collected in the fluid outlet was essentially quantitative. The relative performance of the device was compared with a representative device without a microporous body. Whole blood (0.5 mL) was introduced into to the fluid inlet of a primed microfluidic separation device. The microfluidic separation device identical to that used in present Example with the exception that no microporous body to separate the collection chamber from a microchannel was used as a control. The plasma recovered from the outlet of the device is transparent and clear fluid without contamination of red blood cells, as shown in
The role of the microporous body is evident in
A whole blood sample (0.5 mL) was introduced into the primed microfluidic separation device configured as in
Additional experiments were carried out at higher and lower flow rates using the microfluidic separation device configured as in
While only certain features of the invention have been illustrated and described herein, many modifications and changes will occur to those skilled in the art. It is, therefore, to be understood that the appended embodiments are intended to cover all such modifications and changes as fall within the scope of the invention.
This application claims the benefit of U.S. Provisional Application No. 61/916379, entitled “System for separation of particulates and associated methods and devices”, filed on Dec. 16, 2013, which is herein incorporated by reference.
| Number | Date | Country | |
|---|---|---|---|
| 61916379 | Dec 2013 | US |
