US20160296944A1 - Systems and methods for three-dimensional extraction of target particles ferrofluids - Google Patents
Systems and methods for three-dimensional extraction of target particles ferrofluids Download PDFInfo
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- US20160296944A1 US20160296944A1 US14/777,504 US201414777504A US2016296944A1 US 20160296944 A1 US20160296944 A1 US 20160296944A1 US 201414777504 A US201414777504 A US 201414777504A US 2016296944 A1 US2016296944 A1 US 2016296944A1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/28—Magnetic plugs and dipsticks
- B03C1/288—Magnetic plugs and dipsticks disposed at the outer circumference of a recipient
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- 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
- B01L3/50273—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 means or forces applied to move the fluids
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- 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
- B01L3/502761—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 specially adapted for handling suspended solids or molecules independently from the bulk fluid flow, e.g. for trapping or sorting beads, for physically stretching molecules
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/033—Component parts; Auxiliary operations characterised by the magnetic circuit
- B03C1/0332—Component parts; Auxiliary operations characterised by the magnetic circuit using permanent magnets
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/033—Component parts; Auxiliary operations characterised by the magnetic circuit
- B03C1/0335—Component parts; Auxiliary operations characterised by the magnetic circuit using coils
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- 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
- B01L2200/0647—Handling flowable solids, e.g. microscopic beads, cells, particles
- B01L2200/0668—Trapping microscopic beads
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- 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
- B01L2400/043—Moving fluids with specific forces or mechanical means specific forces magnetic forces
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/18—Magnetic separation whereby the particles are suspended in a liquid
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/26—Details of magnetic or electrostatic separation for use in medical applications
Definitions
- the present disclosure relates to extraction in biocompatible ferrofluids and in particular, to systems and methods for separating a cells and/or other target particles suspended in a ferrofluid (e.g., a biocompatible ferrofluid).
- a ferrofluid e.g., a biocompatible ferrofluid
- concentrating and extracting target moieties within microfluidics may be accomplished two-dimensionally, by placing a ferrofluid containing the target moieties within at least one micro/flow channel, and applying a magnetic field.
- the magnetic field is configured to effect an indirect force on the target moieties such that they are focused/separated into different streamlines of particles across the width of the flow channel.
- the streamlines that carry the target moieties are then extracted at the end of the channel via multiple outlets in the plane of the flow channel.
- Such approaches may be limited by the resolution with which the width of the streamlines carrying the focused moieties are aligned with a particular outlet channel for extracting those streamlines.
- Pulsations, or other non-steady pressure effects originating from, for example, pumps, geometry/elasticity of liquid channels/connectors, trapped air bubbles, partial blockages due to particles flowing through narrow geometries, and the like, can all add to time-dependent deviations in the ultimate trajectories of the target moieties.
- Embodiments of this disclosure correspond to further developments and applications of the inventor's previous series of disclosures, including, for example PCT publication no. WO2011/071912 and WO2012/057878, the noted disclosures of which are all herein incorporated by reference in their entireties.
- a method for extracting particles within a ferrofluid medium may comprise flowing a mix comprising a ferrofluid medium containing one or more types of target particles through at least one microfluidic channel.
- the at least one channel having a first inlet portion for receiving the flow and a second portion spaced downstream from the first portion, a first side spaced away from a second side and comprising to a width of the channel, and a third side spaced away from a fourth side and comprising a height of the channel, wherein the mix flows through the channel in a first direction from the first portion to the second portion.
- the method may also include applying a magnetic field adjacent at least one of the sides of the channel, the magnetic field configured to concentrate at least one type of target particle contained in the mix medium within a width region comprising a portion of the width and a height region comprising a portion of the height, the height region being located at or adjacent to the third side, such that the at least one first type of target particles from the flow are concentrated within the width region and the height region creating a concentrated flow of target particles.
- the method may also include extracting a flow of concentrated target particles of the first type from the mix via an extraction opening arranged on the third side at or near the second portion, where the flow of target particles of the first type from the extraction opening includes an exit velocity.
- a system for extracting particles within a ferrofluid medium may include at least one microfluidic channel having a first inlet portion and a second portion spaced downstream from the first portion for receiving a flow of a mix comprising a ferrofluid medium containing one or more types of target particle, a first side spaced away from a second side and comprising a width of the fluidic channel, and a third side spaced away from a fourth side and comprising a height of the fluidic channel.
- the fluid flows through the fluidic channel in a first direction from the first end to the second end.
- the system may also include magnetic field means arranged adjacent at least one of the sides of the fluidic channel, the magnetic field configured to focus at least one type of target particles contained in the ferrofluid medium flow within a width region comprising a portion of the width and a height region comprising a portion of the height.
- the height region being located at or adjacent to the third side, such that the target particles from the flow are concentrated within the width region and the height region creating a concentrated flow of particles.
- the system may further include an extraction opening arranged on the third side at or near the second end, the extraction opening configured to receive and direct the concentrated flow of target particles from the fluidic channel at an exit velocity.
- FIG. 1 is the illustrative structures of a microfluidic platform that performs concentration/enrichment of a target moiety.
- FIG. 2 is a schematic illustration of a system for extracting target particles from a ferrofluid medium according to some embodiments of the present disclosure.
- FIG. 3 is a schematic illustrating a flow simulation depicting flow streamlines in close proximity to the exit opening of a microfluidic channel according to some embodiments of the present disclosure.
- FIG. 1 shows a top view of a microfluidic channel 10 configured to perform concentration/enrichment of target particles 12 (e.g., moieties) from a ferrofluid flow 11 (e.g., comprising a mix of target particles and a ferrofluid medium).
- target particles 12 e.g., moieties
- ferrofluid flow 11 e.g., comprising a mix of target particles and a ferrofluid medium.
- magnetic field means 8 which may comprise at least one of an electrode, a permanent magnet, and an electromagnet
- applies a magnet field which is configured to focus target particles of the mix in a stream (e.g., see focusing boundaries 6 ). Misalignments due to device construction or pressure variations may limit the effective enrichment factor.
- magnetic field means are shown simply as two bars above/below the schematic of the channel, it is understood that the magnetic field means may be positioned anywhere relative to the flow which would affect the functionality of focusing/separating target particles (see, e.g., WO2011/071912 and WO2012/057878)
- FIG. 2 illustrates concepts according to some embodiments, which may be referred to as “blow-hole” extraction.
- target particles 22 are suspended in a magnetic liquid medium 21 (e.g., a ferrofluid medium) forming a mix, where the target particles may comprise one or more types of particles (e.g., one more types of biological particles—e.g., cells, moieties, and the like), and flowed through one or more microfluidic channels 20 of an extraction and/or microfluidic system.
- Types of target particles also may be (and may be in addition to being a biological particle) based on at least one of size, shape, features, mass and charge.
- the fluidic channel(s) 20 may be provided for in a cartridge configured to be removable from a general system for each new particle extraction.
- Magnetic field applying means 26 which may comprise any one or more of electrodes and magnets, may be positioned adjacent at least one side of the fluidic channel, and are simply shown adjacent the channel in FIG. 2 ; however, it will be understood that the magnetic field means is positioned relative to the channel(s) to effect the separation functionality of at least some of the embodiments taught by this disclosure.
- the magnetic fields are configured to act upon the mix/ferrofluid 21 such that target particles 22 are concentrated, focused, or otherwise separated (these terms used interchangeably throughout), along a portion of the flow.
- a fluidic cartridge having for example parallel microfluidic channels 20 , is arranged adjacent (e.g., on top of) one or more current-carrying electrodes and/or magnets.
- the target particles 22 Upon activation of the magnetic field, the target particles 22 become concentrated, for example, along a central portion of the fluid flow from an inlet 24 end/portion to an outlet end/portion 25 (e.g., an end/portion of the channel which is spaced apart from the inlet end), and, in some embodiments, the magnetic field also is configured to concentrate the target particles along one side of the fluidic channel.
- the magnetic field means may be configured to direct the target particles in a concentrated stream within the center of the fluid flow, and may also (or in place of) concentrate the target particles along the “ceiling” (e.g., a side) of the channel (relative to the “floor” of the channel, in, for example, a vertical direction).
- an extraction opening/orifice/hole 23 is arranged downstream from the inlet end 24 of the channel 20 , on the “ceiling” side, from which the concentrated flow of target particles (e.g., the target particles themselves) may be extracted therefrom ( FIG. 2 ).
- the velocity or speed of the flow of concentrated target particles from the extraction opening 23 may be adjusted either passively, by controlling flow resistance of the extraction orifice or main ferrofluid flow, and/or actively via the incorporation of a pressure of flow sink downstream of the extraction orifice (e.g., an outlet to the microfluidic channel).
- the magnetic field may be configured to effect the velocity, in some embodiments, of particles being extracted via the extraction opening.
- the extraction opening 23 is downstream of the inlet 24 , in some embodiments, sufficiently far from the inlet 24 that the particles 22 being manipulated have had time to be pushed up to the channel ceiling and concentrated into a tight stream.
- the distance configured is based on at least one of flow rate, magnetic field intensity and size of the particles being manipulated. In some embodiments, the distances may be in range of between about 0.5-5 cm. As for the size of the extraction opening size, in some embodiments, the size may be between about 100 to about 1000 ⁇ m.
- the focusing resolution achieved in the plane of the fluidic channel 10 may be supplemented by the localization field/power achieved in the normal direction (i.e., the z-axis in FIGS. 1 and 2 ).
- target particles 12 e.g., cells and/or other microscale moieties
- a wall of the fluidic channel 10 e.g., externally applied magnetic fields via the magnetic field means
- the average distance from the specific wall and the target particles may effectively become their corresponding average radii as the particles interact (e.g., roll) on the wall—and thus, become flow streamlines of such particles.
- the exit flow rate through the extraction channel (relative to the main channel's flow rate) may be engineered to be sufficient enough to attract flow streamlines having distances from the wall slightly larger than the average radius of the focused target particles. According to such embodiments, these focused target particles may then be extracted through the extraction orifice.
- the wall height is configured to be greater than the largest particle within the ferrofluid mix, and may be, for example, between about 10-1000 ⁇ m.
- FIG. 3 shows a flow simulation depicting flow streamlines for target particle 31 extraction which are in close proximity to the extraction opening 32 .
- target particles 31 e.g., cells of about 2 microns in diameter
- the extraction orifice/geometry may be configured to yield a predetermined extraction margin, which in some embodiments may be near or equal to 100%, less than 100% or between about 75% and 100%, or a majority.
- streamlines that are about 2 microns below the channel ceiling, and (in some embodiments) co-linear with the location of the extraction opening 32 may be attracted to the extraction opening 32 for extraction ( FIG. 3 ).
- a flow channel 30 that is 50 microns deep which may yield a boost of about 25 times (50/2) the concentration factor already achieved along the x-y plane.
- concentration factors on the order of between about 250-500 may be realized.
- embodiments of the devices, systems and methods have been described herein. As noted elsewhere, these embodiments have been described for illustrative purposes only and are not limiting. Other embodiments are possible and are covered by the disclosure, which will be apparent from the teachings contained herein. Thus, the breadth and scope of the disclosure should not be limited by any of the above-described embodiments but should be defined only in accordance with claims supported by the present disclosure and their equivalents.
- embodiments of the subject disclosure may include methods, systems and devices which may further include any and all elements from any other disclosed methods, systems, and devices, including any and all elements corresponding to target particle separation, focusing/concentration. In other words, elements from one or another disclosed embodiments may be interchangeable with elements from other disclosed embodiments.
- one or more features/elements of disclosed embodiments may be removed and still result in patentable subject matter (and thus, resulting in yet more embodiments of the subject disclosure).
- some embodiments of the present disclosure may be patentably distinct from one and/or another reference by specifically lacking one or more elements/features.
- claims to certain embodiments may contain negative limitation to specifically exclude one or more elements/features resulting in embodiments which are patentably distinct from the prior art which include such features/elements.
Abstract
Description
- This application claims benefit under 35 USC 119(e) of U.S. provisional patent application No. 61/794,607, filed Mar. 15, 2013, and entitled, “3D Extraction in Biocompatible Ferrofluids,” the entire disclosure of which is herein incorporated by reference in its entirety.
- The present disclosure relates to extraction in biocompatible ferrofluids and in particular, to systems and methods for separating a cells and/or other target particles suspended in a ferrofluid (e.g., a biocompatible ferrofluid).
- As shown in
FIG. 1 , as the inventor's prior disclosures describe, i.e., WO2011/071912 and WO2012/057878, concentrating and extracting target moieties within microfluidics may be accomplished two-dimensionally, by placing a ferrofluid containing the target moieties within at least one micro/flow channel, and applying a magnetic field. The magnetic field is configured to effect an indirect force on the target moieties such that they are focused/separated into different streamlines of particles across the width of the flow channel. The streamlines that carry the target moieties are then extracted at the end of the channel via multiple outlets in the plane of the flow channel. - To that end, such approaches may be limited by the resolution with which the width of the streamlines carrying the focused moieties are aligned with a particular outlet channel for extracting those streamlines. Pulsations, or other non-steady pressure effects originating from, for example, pumps, geometry/elasticity of liquid channels/connectors, trapped air bubbles, partial blockages due to particles flowing through narrow geometries, and the like, can all add to time-dependent deviations in the ultimate trajectories of the target moieties.
- Embodiments of this disclosure correspond to further developments and applications of the inventor's previous series of disclosures, including, for example PCT publication no. WO2011/071912 and WO2012/057878, the noted disclosures of which are all herein incorporated by reference in their entireties.
- Accordingly, in some embodiments, a method for extracting particles within a ferrofluid medium is provided. The method may comprise flowing a mix comprising a ferrofluid medium containing one or more types of target particles through at least one microfluidic channel. The at least one channel having a first inlet portion for receiving the flow and a second portion spaced downstream from the first portion, a first side spaced away from a second side and comprising to a width of the channel, and a third side spaced away from a fourth side and comprising a height of the channel, wherein the mix flows through the channel in a first direction from the first portion to the second portion. The method may also include applying a magnetic field adjacent at least one of the sides of the channel, the magnetic field configured to concentrate at least one type of target particle contained in the mix medium within a width region comprising a portion of the width and a height region comprising a portion of the height, the height region being located at or adjacent to the third side, such that the at least one first type of target particles from the flow are concentrated within the width region and the height region creating a concentrated flow of target particles. The method may also include extracting a flow of concentrated target particles of the first type from the mix via an extraction opening arranged on the third side at or near the second portion, where the flow of target particles of the first type from the extraction opening includes an exit velocity.
- In some embodiments, a system for extracting particles within a ferrofluid medium is provided. Such embodiments may include at least one microfluidic channel having a first inlet portion and a second portion spaced downstream from the first portion for receiving a flow of a mix comprising a ferrofluid medium containing one or more types of target particle, a first side spaced away from a second side and comprising a width of the fluidic channel, and a third side spaced away from a fourth side and comprising a height of the fluidic channel. The fluid flows through the fluidic channel in a first direction from the first end to the second end. The system may also include magnetic field means arranged adjacent at least one of the sides of the fluidic channel, the magnetic field configured to focus at least one type of target particles contained in the ferrofluid medium flow within a width region comprising a portion of the width and a height region comprising a portion of the height. The height region being located at or adjacent to the third side, such that the target particles from the flow are concentrated within the width region and the height region creating a concentrated flow of particles. The system may further include an extraction opening arranged on the third side at or near the second end, the extraction opening configured to receive and direct the concentrated flow of target particles from the fluidic channel at an exit velocity.
- Embodiments of the disclosure may further include one or more of the following features:
-
- the target particles comprise at least one of target moieties and target biological cells;
- the extraction opening having a shape comprising round, circular, square, a slit, rectangular, triangular and elliptical;
- the magnetic field means comprises at least one of one or more current-carrying electrodes and one or more magnets;
- velocity adjustment means;
- the velocity adjustment means comprises flow resistance means;
- the velocity adjustment means comprises at least one of: adjusting the magnetic field to effect forces on the flow affecting the exit velocity, the size of the extraction opening is configured to increase velocity, controlling the flow resistance from the extraction opening, and providing at least one of a pressure sink and a flow sink arranged downstream of the extraction opening.
- The above-noted embodiments, as well as other embodiments, will become even more evident with reference to the following detailed description and associated drawing, a brief description of which is provided below.
-
FIG. 1 is the illustrative structures of a microfluidic platform that performs concentration/enrichment of a target moiety. -
FIG. 2 is a schematic illustration of a system for extracting target particles from a ferrofluid medium according to some embodiments of the present disclosure. -
FIG. 3 is a schematic illustrating a flow simulation depicting flow streamlines in close proximity to the exit opening of a microfluidic channel according to some embodiments of the present disclosure. -
FIG. 1 shows a top view of amicrofluidic channel 10 configured to perform concentration/enrichment of target particles 12 (e.g., moieties) from a ferrofluid flow 11 (e.g., comprising a mix of target particles and a ferrofluid medium). In such cases, the alignment of the focused target particles with anoutlet 14 stream determines the concentration efficiency and loss. As is shown, magnetic field means 8 (which may comprise at least one of an electrode, a permanent magnet, and an electromagnet) applies a magnet field which is configured to focus target particles of the mix in a stream (e.g., see focusing boundaries 6). Misalignments due to device construction or pressure variations may limit the effective enrichment factor. While the magnetic field means are shown simply as two bars above/below the schematic of the channel, it is understood that the magnetic field means may be positioned anywhere relative to the flow which would affect the functionality of focusing/separating target particles (see, e.g., WO2011/071912 and WO2012/057878) -
FIG. 2 illustrates concepts according to some embodiments, which may be referred to as “blow-hole” extraction. In such embodiments, for example,target particles 22 are suspended in a magnetic liquid medium 21 (e.g., a ferrofluid medium) forming a mix, where the target particles may comprise one or more types of particles (e.g., one more types of biological particles—e.g., cells, moieties, and the like), and flowed through one or moremicrofluidic channels 20 of an extraction and/or microfluidic system. Types of target particles also may be (and may be in addition to being a biological particle) based on at least one of size, shape, features, mass and charge. The fluidic channel(s) 20 may be provided for in a cartridge configured to be removable from a general system for each new particle extraction. Magnetic field applying means 26, which may comprise any one or more of electrodes and magnets, may be positioned adjacent at least one side of the fluidic channel, and are simply shown adjacent the channel inFIG. 2 ; however, it will be understood that the magnetic field means is positioned relative to the channel(s) to effect the separation functionality of at least some of the embodiments taught by this disclosure. - In some embodiments, the magnetic fields are configured to act upon the mix/ferrofluid 21 such that
target particles 22 are concentrated, focused, or otherwise separated (these terms used interchangeably throughout), along a portion of the flow. For example, in some embodiments, a fluidic cartridge, having for example parallelmicrofluidic channels 20, is arranged adjacent (e.g., on top of) one or more current-carrying electrodes and/or magnets. Upon activation of the magnetic field, thetarget particles 22 become concentrated, for example, along a central portion of the fluid flow from aninlet 24 end/portion to an outlet end/portion 25 (e.g., an end/portion of the channel which is spaced apart from the inlet end), and, in some embodiments, the magnetic field also is configured to concentrate the target particles along one side of the fluidic channel. - For example, if the magnetic field means is placed below the cartridge, it may be configured to direct the target particles in a concentrated stream within the center of the fluid flow, and may also (or in place of) concentrate the target particles along the “ceiling” (e.g., a side) of the channel (relative to the “floor” of the channel, in, for example, a vertical direction).
- Accordingly, in some embodiments, an extraction opening/orifice/
hole 23 is arranged downstream from theinlet end 24 of thechannel 20, on the “ceiling” side, from which the concentrated flow of target particles (e.g., the target particles themselves) may be extracted therefrom (FIG. 2 ). The velocity or speed of the flow of concentrated target particles from theextraction opening 23 may be adjusted either passively, by controlling flow resistance of the extraction orifice or main ferrofluid flow, and/or actively via the incorporation of a pressure of flow sink downstream of the extraction orifice (e.g., an outlet to the microfluidic channel). Likewise, the magnetic field may be configured to effect the velocity, in some embodiments, of particles being extracted via the extraction opening. The extraction opening 23 is downstream of theinlet 24, in some embodiments, sufficiently far from theinlet 24 that theparticles 22 being manipulated have had time to be pushed up to the channel ceiling and concentrated into a tight stream. Hence, the distance configured is based on at least one of flow rate, magnetic field intensity and size of the particles being manipulated. In some embodiments, the distances may be in range of between about 0.5-5 cm. As for the size of the extraction opening size, in some embodiments, the size may be between about 100 to about 1000 μm. - In some embodiment, the focusing resolution achieved in the plane of the fluidic channel 10 (e.g., the x-y plane in
FIGS. 1 and 2 ) may be supplemented by the localization field/power achieved in the normal direction (i.e., the z-axis inFIGS. 1 and 2 ). Since target particles 12 (e.g., cells and/or other microscale moieties) suspended in aferrofluid 11 may be directed towards a wall of the fluidic channel 10 (e.g., externally applied magnetic fields via the magnetic field means), the average distance from the specific wall and the target particles may effectively become their corresponding average radii as the particles interact (e.g., roll) on the wall—and thus, become flow streamlines of such particles. Accordingly, in some embodiments, the exit flow rate through the extraction channel (relative to the main channel's flow rate) may be engineered to be sufficient enough to attract flow streamlines having distances from the wall slightly larger than the average radius of the focused target particles. According to such embodiments, these focused target particles may then be extracted through the extraction orifice. In some embodiments, the wall height is configured to be greater than the largest particle within the ferrofluid mix, and may be, for example, between about 10-1000 μm. - For example,
FIG. 3 shows a flow simulation depicting flow streamlines fortarget particle 31 extraction which are in close proximity to theextraction opening 32. In such embodiments, and as an example, target particles 31 (e.g., cells of about 2 microns in diameter) are pushed via at least one of the ferrofluid flow and magnetic field, to within 1 micron of the upper channel (i.e., ceiling). Conservatively, the extraction orifice/geometry may be configured to yield a predetermined extraction margin, which in some embodiments may be near or equal to 100%, less than 100% or between about 75% and 100%, or a majority. Thus in a nearly 100% margin configuration, streamlines that are about 2 microns below the channel ceiling, and (in some embodiments) co-linear with the location of theextraction opening 32, may be attracted to theextraction opening 32 for extraction (FIG. 3 ). In another example, for aflow channel 30 that is 50 microns deep, which may yield a boost of about 25 times (50/2) the concentration factor already achieved along the x-y plane. Hence, in some embodiments, concentration factors on the order of between about 250-500 may be realized. - Any and all references to publications or other documents, including but not limited to, patents, patent applications, articles, webpages, books, etc., presented in the present application, are herein incorporated by reference in their entirety.
- Example embodiments of the devices, systems and methods have been described herein. As noted elsewhere, these embodiments have been described for illustrative purposes only and are not limiting. Other embodiments are possible and are covered by the disclosure, which will be apparent from the teachings contained herein. Thus, the breadth and scope of the disclosure should not be limited by any of the above-described embodiments but should be defined only in accordance with claims supported by the present disclosure and their equivalents. Moreover, embodiments of the subject disclosure may include methods, systems and devices which may further include any and all elements from any other disclosed methods, systems, and devices, including any and all elements corresponding to target particle separation, focusing/concentration. In other words, elements from one or another disclosed embodiments may be interchangeable with elements from other disclosed embodiments. In addition, one or more features/elements of disclosed embodiments may be removed and still result in patentable subject matter (and thus, resulting in yet more embodiments of the subject disclosure). Correspondingly, some embodiments of the present disclosure may be patentably distinct from one and/or another reference by specifically lacking one or more elements/features. In other words, claims to certain embodiments may contain negative limitation to specifically exclude one or more elements/features resulting in embodiments which are patentably distinct from the prior art which include such features/elements.
Claims (12)
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Cited By (6)
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US20160370278A1 (en) * | 2013-07-04 | 2016-12-22 | Cytomos Limited | Biological sensing apparatus |
WO2016210348A3 (en) * | 2015-06-26 | 2017-02-02 | Ancera, Inc. | Background defocusing and clearing in ferrofluid-based capture assays |
US10350611B2 (en) * | 2017-06-27 | 2019-07-16 | General Electric Company | Apparatus and methods for particle separation by ferrofluid constriction |
US10928404B2 (en) | 2014-02-26 | 2021-02-23 | The Brigham And Women's Hospital, Inc. | System and method for cell levitation and monitoring |
US11204350B2 (en) | 2013-03-15 | 2021-12-21 | Ancera, Llc | Systems and methods for bead-based assays in ferrofluids |
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WO2022015845A2 (en) | 2020-07-14 | 2022-01-20 | Ancera Llc | Systems, devices and methods for analysis |
CA3206824A1 (en) | 2021-02-02 | 2022-08-11 | Mary K.H. Smith | Ferrofluid-based assay methods, and systems for parasite eggs or oocysts detection |
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JP2006010529A (en) * | 2004-06-25 | 2006-01-12 | Canon Inc | Separator and method for separating magnetic particle |
US8292083B2 (en) * | 2007-04-19 | 2012-10-23 | The Charles Stark Draper Laboratory, Inc. | Method and apparatus for separating particles, cells, molecules and particulates |
ATE554859T1 (en) * | 2007-05-24 | 2012-05-15 | Univ California | INTEGRATED FLUIDIC DEVICES WITH MAGNETIC SORTING |
WO2010117458A1 (en) * | 2009-04-10 | 2010-10-14 | President And Fellows Of Harvard College | Manipulation of particles in channels |
US20110262989A1 (en) * | 2010-04-21 | 2011-10-27 | Nanomr, Inc. | Isolating a target analyte from a body fluid |
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2014
- 2014-03-14 WO PCT/US2014/028705 patent/WO2014144340A1/en active Application Filing
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2018
- 2018-08-27 US US16/113,793 patent/US20190091699A1/en active Pending
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US11204350B2 (en) | 2013-03-15 | 2021-12-21 | Ancera, Llc | Systems and methods for bead-based assays in ferrofluids |
US11383247B2 (en) | 2013-03-15 | 2022-07-12 | Ancera, Llc | Systems and methods for active particle separation |
US20160370278A1 (en) * | 2013-07-04 | 2016-12-22 | Cytomos Limited | Biological sensing apparatus |
US10933418B2 (en) * | 2013-07-04 | 2021-03-02 | Cytomos Limited | Biological analysis apparatus |
US20210276013A1 (en) * | 2013-07-04 | 2021-09-09 | Cytomos Limited | Biological sensing apparatus |
US10928404B2 (en) | 2014-02-26 | 2021-02-23 | The Brigham And Women's Hospital, Inc. | System and method for cell levitation and monitoring |
WO2016210348A3 (en) * | 2015-06-26 | 2017-02-02 | Ancera, Inc. | Background defocusing and clearing in ferrofluid-based capture assays |
US11285490B2 (en) | 2015-06-26 | 2022-03-29 | Ancera, Llc | Background defocusing and clearing in ferrofluid-based capture assays |
US11833526B2 (en) | 2015-06-26 | 2023-12-05 | Ancera Inc. | Background defocusing and clearing in ferrofluid-based capture assays |
US10350611B2 (en) * | 2017-06-27 | 2019-07-16 | General Electric Company | Apparatus and methods for particle separation by ferrofluid constriction |
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US20190091699A1 (en) | 2019-03-28 |
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