SEPARATION METHOD AND APPARATUS FOR MICROVESICLES
20220347687 · 2022-11-03
Inventors
Cpc classification
B01D21/28
PERFORMING OPERATIONS; TRANSPORTING
B01L2200/0652
PERFORMING OPERATIONS; TRANSPORTING
C12N15/1003
CHEMISTRY; METALLURGY
B01L2400/082
PERFORMING OPERATIONS; TRANSPORTING
B01L3/502753
PERFORMING OPERATIONS; TRANSPORTING
C12N15/1006
CHEMISTRY; METALLURGY
B01L2300/0864
PERFORMING OPERATIONS; TRANSPORTING
C12M1/42
CHEMISTRY; METALLURGY
B01D43/00
PERFORMING OPERATIONS; TRANSPORTING
B01L2300/0816
PERFORMING OPERATIONS; TRANSPORTING
B01L2400/0436
PERFORMING OPERATIONS; TRANSPORTING
B01L3/502761
PERFORMING OPERATIONS; TRANSPORTING
H03H9/15
ELECTRICITY
International classification
B01L3/00
PERFORMING OPERATIONS; TRANSPORTING
C12N15/10
CHEMISTRY; METALLURGY
Abstract
A microfluidic control system and method for separating flexible particles such as cell vesicles or biomacromolecules such as exosomes in a sample. The system of the present invention comprises one or more ultrahigh frequency acoustic resonators. The ultrahigh frequency acoustic resonators are capable of generating in a fluid channel an acoustic wave of which the frequency is about 0.5-50 GHz and propagated towards a wall opposite the fluid channel. By adjusting the power of the generated acoustic wave and/or the speed at which a conditioning solution flows through an acoustic wave area, flexible particles in a specified range are pushed to and remain at the top part of the flow channel in the acoustic wave area, while flexible particles outside of the specified range go downstream via the acoustic wave area to be collected, thus capturing or releasing the flexible particles in a solution such as cell vesicles or biomacromolecules, particularly exosomes.
Claims
1. A method for separating flexible particles comprising. (1) allowing a solution sample containing flexible particles such as cellular microvesicles or biomolecular particles such as nucleic acids and proteins to flow through a microfluidic device, said device comprising a fluid channel; one or more ultra-high frequency (UHF) bulk acoustic wave resonators disposed at the bottom of said fluid channel, said ultra-high frequency bulk acoustic wave resonators being capable of generating bulk acoustic waves in said fluid channel with a frequency of about 0.5-50 GHz and transmitted to the top of said fluid channel; (2) said UHF resonator emitting bulk acoustic waves transmitted to the top of said fluid channel; (3) adjusting the power of the bulk acoustic waves and/or adjusting the velocity of said solution flow so that the designated flexible particles are pushed to the top of the fluid channel and remain thereat when they are flowing through the region of influence of the bulk acoustic waves, and (4) optionally, obtaining the fluid downstream of the bulk acoustic wave region; and/or varying the parameters of step (3) such that the designated flexible particles that are pushed to the top of the fluid channel and remain there are released.
2. (canceled)
3. The method of claim 1, wherein said flexible particles are cellular microvesicles, including exosomes, vesicles, membrane vesicles, prostatic vesicles, microparticles, intraluminal vesicles, intranuclear body-like vesicles, or cytosolic vesicles, wherein said flexible particles have a diameter of about 0.02-1 um.
4. The method of claim 3, wherein said UHF resonator has a distance to the top of the fluid channel of about 10-60 um.
5. The method of claim 1, wherein said flexible particle is a nucleic acid, wherein said nucleic acid is about 50 bp-50 kbp in length.
6. The method of claim 5, wherein said UHF resonator has a distance to the top of the fluid channel of about 5-25 um.
7. The method of claim 1, wherein the power of the bulk acoustic wave generated by said UHF resonator is adjusted to be about 0.5-2000 mW.
8. The method of claim 1 wherein the velocity of flow of said solution through the bulk acoustic region is regulated to be about 0.1-100 μL/min.
9. The method of claim 1, wherein said UHF bulk acoustic wave resonator has a bulk acoustic wave generation area of about 500-200000 μm.sup.2, preferably about 5000-50000 μm.sup.2, and most preferably about 10000-25000 μm.sup.2.
10. The method of claim 1, wherein said fluid channel comprises a sample inlet, and auxiliary solution inlet provided on one or both sides of said sample inlet.
11. The method of claim 1, wherein said solution sample contains different flexible particles, said method comprising obtaining the flexible particles that are pushed to the top of the fluid channel and remain thereat, and obtaining flexible particles that are not pushed to the top of the fluid channel and collected downstream of the bulk acoustic wave affected region or said method comprising controlling a gradually release of different flexible particles after they are all pushed to the top of the fluid channel and remain thereat.
12. The method of claim 11, wherein the control includes one of the following or any combination thereof: (a) adjusting the distance of said UHF resonator to the top of the fluid channel; (b) adjusting the power of the bulk acoustic wave; or (c) adjusting the velocity of said solution flow through the bulk acoustic wave region.
13. A microfluidic device for separating flexible particles, comprising a fluid channel having an inlet and an outlet; one or more UHF bulk acoustic wave resonators provided on one wall of said fluid channel, said UHF bulk acoustic wave resonators being capable of generating bulk acoustic waves in said fluid channel with a frequency of about 0.5-50 GHz and transmitted to the top of said fluid channel; a power adjusting device which adjusts the power of said bulk acoustic waves generated by said UHF resonator; a flow rate adjusting device which adjusts the velocity of said solution flowing through the region of the bulk acoustic wave, said UHF resonators are being able to emit bulk acoustic waves transmitted to the top of said fluid channel and cause the solution flowing through the bulk acoustic wave region to become an acoustic current, said microfluidic device set to adjust the power of the bulk acoustic waves by said power regulator and/or to adjust the velocity of said solution flowing through the bulk acoustic wave influence region by said flow rate adjustment device, such that the designated flexible particles are pushed to the top of the fluid channel in the bulk acoustic wave influence region.
14. The microfluidic device of claim 13, wherein said flexible particles are cellular microvesicles, including exosomes, vesicles, membrane vesicles, prostatic vesicles, microparticles, intraluminal vesicles, intranuclear body-like vesicles, or cytosolic vesicles, said flexible particles have a diameter of about 0.02-1 μm, and wherein said UHF resonator has a distance to the top of the fluid channel of about 10-60 um.
15. (canceled)
16. The microfluidic device of claim 13, wherein said flexible particle is a nucleic acid, said nucleic acid is about 50 bp-50 kbp in length, and wherein said UHF resonator has a distance to the top of the fluid channel of about 5-25 μm.
17. (canceled)
18. The microfluidic device of claim 13, wherein said a power adjusting device outputs power of about 0.5-2000 mW.
19. The microfluidic device of claim 13, wherein said flow rate adjusting device adjusts the velocity of flow of said solution through the bulk acoustic region to be about 0.1-10 mm/s.
20. The microfluidic device of claim 13 any one of claims 13-17, wherein said UHF bulk acoustic wave resonator has a bulk acoustic wave generation area of about 500-200000 μm.sup.2.
22. The microfluidic device of claim 13, wherein said ultra-high frequency bulk acoustic wave resonator is a thin film bulk acoustic wave resonator or a solid state assembled resonator.
23. The microfluidic device of claim 13, wherein said fluidic channel is divided into different regions, wherein UHF resonators for separating different flexible particles are provided in the different regions, said UHF resonators for separating different flexible particles may have differently shaped acoustic wave generating regions, or apply bulk acoustic waves of different power, or have different flow rates, or have different flow channel heights, or any combinations thereof.
24. A kit comprising a microfluidic device as defined in claim 13 and reagents for analysis of microvesicles.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0088] In order to more clearly illustrate the technical solutions in the embodiments or prior art of the present invention, the following is a brief description of the accompanying drawings for use in the description of the embodiments or prior art. It will be apparent that the accompanying drawings in the following description are some embodiments of the present invention, and that other drawings of the present invention are available to a person of ordinary skill in the art.
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DETAILED DESCRIPTION
[0094] The nature and benefits of the present disclosure are further described with reference to the following examples, which are intended to illustrate the invention provided herein and not to limit the scope of the present disclosure.
EXAMPLE 1
Experimental Method and Materials
[0095] Microfluidic channel and UHF bulk acoustic resonator preparation:
[0096] Microfluidic channels made of polydimethylsiloxane (PDMS) were prepared by soft lithography.
[0097] The bulk acoustic wave resonator devices are prepared by chemical vapor deposition, metal sputtering, and lithography on a silicon wafer. The specific methods are as follows.
[0098] 1. The surface of the silicon wafer is thoroughly cleaned using a solution with a 3:1 volume ratio of concentrated sulfuric acid to hydrogen peroxide, which effectively removes organic and inorganic materials from the wafer.
[0099] 2. On the cleaned silicon wafer, an aluminum nitride film is formed by surface sputtering, and then a silicon dioxide film is deposited using an ion-enhanced chemical vapor deposition method. Then, using the same method, the aluminum nitride film and the silicon dioxide film are deposited alternately to form a Bragg acoustic reflection structure with alternating layers of aluminum nitride and silicon dioxide.
[0100] 3. On top of the Bragg reflector structure, a 600 nm molybdenum film is sputtered as the bottom electrode. Next, the molybdenum electrode film is photolithographed using standard photolithography techniques, including glue coating, exposure, and development, followed by etching to form a bottom electrode with a target pattern.
[0101] 4. Another layer of aluminum nitride film is sputtered on the molybdenum electrode as a piezoelectric layer. The pattern is defined on the aluminum nitride film using dry etching.
[0102] 5. The pattern on the mask plate is transferred using negative photoresist and then a 50 nm thick layer of titanium tungsten alloy is sputtered, which acts as an adhesion layer to increase the adhesion of the gold electrode. After that, a 300 nm thick layer of gold thin film of the upper electrode is formed by using vapor deposition. Finally, acetone is used to remove the gold film around the target pattern to form the gold electrode with the target pattern.
[0103] Finally, the bulk acoustic wave resonator device is integrated with the PDMS microchannel chip. The bulk acoustic wave resonator device is set in the middle of the channel.
[0104] The bulk acoustic wave resonator device is connected to a network analyzer using a standard SMA interface, and the frequency of the bulk acoustic wave emitted by the resonator device in the microchannel can be measured by testing the spectrum to find the resonance peak.
[0105] Instruments and Materials
[0106] Signal generator: MXG Analog Signal Generator, Agilent, N5181A 100 kHz-3 GHz
[0107] Power amplifier: Mini-Circuits, with 35 dBm enhancement of the original RF source power
[0108] Syringe Pump: New Era Pump Systems, Inc., NE-1000
EXAMPLE 2
[0109] In this embodiment of the present invention, a microfluidic device is provided which can be used to separate and capture flexible particles in solution. The flexible particles may be artificial or natural. The flexible particles may be biomolecular particles such as nucleic acids. The flexible particles may also be microclusters with a membrane structure, in particular microclusters with a lipid bilayer or a lipid-like bilayer. In one aspect of the present invention, the flexible particles are nature, such as cellular vesicles that are released by cells into the extracellular environment, including exosomes, microvesicles, vesicles, membrane vesicles, prostatic vesicles, microparticles, intraluminal vesicles, intranuclear body-like vesicles, or cytosolic vesicles.
[0110] The method and devices of the present invention can be used to separate and capture flexible particles in solution, for example to separate and obtain microvesicles in blood.
[0111] As shown in
[0112] The microfluidic device provided by the present invention may be provided independently or may be part of a microfluidic system, for example in the form of a loadable chip. Microfluidic systems or devices can be used to contain and transport fluidic materials such as liquids with flow channel sizes in the micron or even nanometer range. Typical microfluidic systems and devices typically include structures and functional units of millimeter or smaller size.
[0113] The fluid channels, or microfluidic channels, of said microfluidic devices are generally closed except for openings for fluid entry and exit. The cross section of the fluid channel typically has dimensions of 0.1-500 m, which can be of various shapes including elliptical, rectangular, square, triangular, circular, etc. Fluid channels can be prepared using a variety of known micro-preparation techniques with materials including, but not limited to, silica, silicon, quartz, glass, or polymeric materials (e.g., PDMS, plastic, etc.). Said channels can be coated with a coating. The coating may modify the properties of the channel and may be patterned. For example, the coating may be hydrophilic, hydrophobic, magnetic, conductive, or biologically functionalized.
[0114] In one aspect of the present invention, wherein said fluid channel of the microfluidic device has a height of about 5-60 um, preferably about 8-45 um, more preferably about 10-30 um.
[0115] In one aspect of the present invention, the microfluidic device is for separating or capture vesicles such as exosome, said fluid channel of the microfluidic device has a height of about 10-60 um, preferably about 8-45 um, more preferably about 10-20 um.
[0116] In one aspect of the present invention, said fluid channel of the microfluidic device has a width of about 50-1000 μm, preferably about 100-500 μm, more preferably about 150-300 μm.
[0117] The microfluidic channel 100 in this embodiment has an inlet and an outlet for solution entry and exit. Said inlet is connected to a fluid injection device for receiving the solution. Said inlet in this embodiment comprises a sample inlet 101 and a buffer inlet 102, wherein said buffer inlet is two inlets provided on either side of said sample inlet. Said microfluidic inlet setting facilitates passive focusing of the sample solution when passing through the sample inlet in the middle by this setting (sample flow in the middle and buffer flow on both sides).
[0118] As shown in
[0119] The flow rate of the injected solution can be controlled by means of an external pressure source, an internal pressure source, electrodynamics, or magnetic field dynamics. The external pressure source and internal pressure source can be a pump, such as a peristaltic pump, a syringe pump, or a pneumatic pump. In this embodiment, a syringe pump fine-tuned by a computer is used to control the flow rate of the liquid injection.
[0120] In the present invention, the flow rate of the solution ranges from about 0.1-10 mm/s, preferably from about 0.3-5 mm/s, more preferably from about 0.5-3 mm/s. In another aspect of the present invention, the flow rate of said solution ranges from about 0.1-100 μL/min, preferably from about 0.1-50 μL/min, more preferably from about 0.5-30 μL/min.
[0121] Said channels may be a single channel, or a plurality of channels arranged in parallel, wherein the outflow and inflow of solution and the flow rate thereof of each channel may be controlled jointly or independently as desired.
[0122] The microfluidic device of the present invention has one or more UHF bulk acoustic resonators 200, which are provided on one of the walls of the fluid channel (typically provided at the bottom of the flow channel). Said UHF bulk acoustic wave resonators may generate bulk acoustic waves at a frequency of about 0.5-50 GHz in said fluid channel which transmit to a wall on the opposite side of said fluid channel (typically the top of the flow channel).
[0123] The UHF bulk acoustic wave resonator that may be used in the present invention may be a thin film bulk acoustic wave resonator or a solid state assembly type resonator, such as a thickness stretching vibration mode acoustic wave resonator.
[0124] As shown in
[0125] Said UHF bulk acoustic wave resonators are bulk acoustic wave generating components that can generate bulk acoustic waves in said fluid channel that are transmitted to the opposite side of said fluid channel's wall.
[0126] As shown in the cross-section on the right side of
[0127] In the present invention, said shape of the bulk acoustic wave action region includes at least, but is not limited to, one of the following: a circle, an ellipse, a semicircle, a parabola, a polygon with an acute or obtuse angle at the vertex, a polygon with the vertex replaced by a circular arc, a polygon with any combination of an acute angle, a semicircle or a parabola at the vertex, or a repeatedly arranged square or circular array of the same shape. The present application provides the acoustic action area of the above-mentioned shapes, but other acoustic action areas of any shape are also within the scope of protection of the present application.
[0128] As shown in the right-hand section of
[0129] The UHF bulk acoustic wave resonator employed in this embodiment of the present invention is a thickness-stretching vibration mode in which a thin film layer of piezoelectric material is made by growing in the vertical direction and is excited by coupling the vertical electric field through the d33 piezoelectric coefficient. The UHF bulk acoustic resonator employed in the present invention can generate localized acoustic flow at the interface between the device and the liquid without a coupling medium or a coupling structure.
[0130] As shown in the right panel of
[0131] In the method of the present invention, the UHF resonator emits a bulk acoustic wave transmitted to the wall on the opposite side of said fluid channel (e.g., the top of the flow channel), and the volumetric force generated by the decay of the acoustic wave into the fluid causes an acoustic jet to appear in the solution and fluid moving downward surrounded the same flux and form a vortex. In the method of the present invention, when the solution containing the flexible particles flows through the region of influence of the bulk acoustic waves generated by the UHF resonator (there are the presence of acoustic jet and vortex), the particles in the vortex is subjected to forces including the fluid drag force (Stokes drag force) generated by the vortex, the acoustic radiation force (acoustic radiation force) caused by the decay of the acoustic waves, and the laminar flow generated by the inertial drag force (inertial lift force). Different flexible particles are influenced by different fluid drag force and acoustic radiation force. The fluid drag force is proportional to the particle radius; the acoustic radiation force is proportional to the particle radius cubic/quadratic (depending on the particle size and acoustic wavelength). Therefore, as the particle size decreases, the acoustic radiation force will decay faster than the drag force. After entering the vortex, the trajectory of the larger size particles is mainly controlled by the acoustic radiation force, and in the region where the acoustic radiation force is dominant, they move to the top of the flow channel under the upward acoustic radiation force; at the top of the flow channel, said flexible particles are subjected to the inertial drag force generated by the solution laminar flow, as well as to the drag force caused by the friction and adhesion between them and the top due to the pressure of the acoustic radiation force; when the drag force is greater than the inertial drag force, the said flexible particles stay at the top of the flow channel and do not go downstream with the liquid flow. While smaller size particles enter the vortex, the acoustic radiation force is not enough to push it away from the vortex motion trajectory, so its motion trajectory is dominated by the fluid drag force and moves with the vortex, or it can leave the bulk acoustic region under the inertial drag force generated by the solution laminar flow and enter the downstream with the liquid flow.
[0132] The applicant has unexpectedly found through experiments that in the method and device of the present invention, the flexible particles that are pushed to the top of the flow channel and stay (“blocked”) when the vesicles in the solution pass through the acoustic fluid region caused by the UHF bulk acoustic wave are related to the bulk acoustic wave power (related to the acoustic wave amplitude and intensity), the distance between the UHF resonator and the top of the flow channel, and the velocity of the solution flowing through the bulk acoustic wave region.
[0133] Without being constrained by the relevant theory, the Applicant believes that when the power of the UHF bulk acoustic wave tends to be nil, neither the acoustic radiation force nor the vortex is sufficient to act on the particles, so the action is dominated by the laminar drag force. As the power increases, the vortex force is not enough to change the particle motion dominated by the acoustic radiation force, so the particles start to be pushed to the top of the flow channel. As the power continues to increase, the acoustic fluid is strong enough to push the particles to the top where the acoustic radiation force is unable to push the particles to the center of the vortex, and thus the particles enter the vortex tunnel and move along it. As the power increases, the size of the particles that can be sent to the opposite side of the flow channel is decreasing, and the size of the particles that can be captured by the vortex is also decreasing. Within certain parameters, the size of the particles that can be pushed to the opposite side of the flow channel is smaller than that captured by the vortex at the same power.
[0134] Microvesicles of different sizes, especially those in the size range of 20-1000 nm, can be distinguished and separated by a suitable combination of bulk acoustic wave power (related to acoustic wave amplitude and intensity), the distance between the UHF resonator and the top of the flow channel, and the velocity of the solution flowing through the body acoustic wave region.
[0135] As a result, the present applicant's inventors have discovered and provided methods to more effectively separate cellular microvesicles.
[0136] In the present invention, the frequency of the thin film bulk acoustic wave resonator is mainly determined by the thickness and material of the piezoelectric layer. The thickness of the piezoelectric layer of the thin film bulk acoustic resonator used in the present invention ranges from 1 nm to 2 um. The frequency of the UHF bulk acoustic resonator of the present invention is in the range of about 0.5-50 GHz, preferably greater than 1 GHz-about 10 GHz.
[0137] The bulk acoustic wave generated by said UHF bulk acoustic wave resonator is driven by a signal from a high frequency signal generator. The pulsed voltage signal driving the resonator can be driven with pulse width modulation, which can produce any desired waveform, such as a sine wave, square wave, sawtooth wave, or triangle wave. The pulsed voltage signal can also have an amplitude modulation or frequency modulation start/stop capability to start or eliminate bulk acoustic waves.
[0138] The microfluidic device of the present invention further comprises a power regulation device which regulates the power of the bulk acoustic waves generated by said UHF resonator. In this embodiment, said power regulating device is a power amplifier having a power regulation function. In one aspect of the present invention, said power adjusting device has an output power of about 0.5-2000 mW, preferably 5-1500 mW, more preferably 15-900 mW, for example 70-300 mW. Due to the high energy conversion efficiency of the thin film bulk acoustic wave resonator which essentially cause no energy loss, the output power of said power adjusting device can be considered essentially as the output power of the thin film bulk acoustic wave resonator generating bulk acoustic waves in fluid. In the microfluidic device of the present invention, said power adjusting device may be connected to a high frequency signal generator. The output circuit of said power amplifier is connected to the bottom electrode, piezoelectric layer, and top electrode of said ultra-high frequency bulk acoustic wave resonator, respectively.
[0139] The microfluidic devices of the present invention may also include detection devices for detecting signals of characteristics of cells or markers carried by them in the sample. These characteristics may include molecular size, molecular weight, molecular magnetic moment, refractive index, conductivity, charge, absorbance, fluorescence, polarity, and other physical properties. For example, detection devices include detecting electrical detection devices, such as Coulter counters, for cell counting. The detection apparatus may also be a photodetector, which includes an illumination source and optical detection components for detecting physical parameters such as charge, absorbance, fluorescence, polarity, etc.
[0140] In the microfluidic device of the present invention as shown in
[0141] The microfluidic devices provided by the present invention as described above can also be used to capture/isolate nucleic acids. The microfluidic devices and methods provided by the present invention are particularly suitable for the isolation of nucleic acids of small size. For example, the method of the present invention is suitable for isolating nucleic acids of length ≤1500 bp, preferably ≤500 bp, more preferably ≤200 bp, for example ≤100 bp. In this aspect of the present invention, the height of the fluid channel of said microfluidic device is typically about 5-25 um, preferably about 6-25 um, more preferably about 7-20 um.
EXAMPLE 3
Effect of Flow Channel Height on Acoustic Jets and Vortices Induced by Bulk Acoustic Waves
[0142] Observations were made on the acoustic jet and/or vortex currents generated by the UHF bulk acoustic wave resonator used in the present invention in microfluidic channels of different heights. The microfluidic channels of the present invention which are suitable for separating cellular microvesicles (20-800 nm) including exosomes (about 20-250 nm) have a suitable height of no more than 60 μm, e.g. 60 μm, 40 μm, 20 μm.
[0143] In this case, hollow glass beads (with a density close to water) were added to the fluid cavity to characterize the fluid velocity distribution by particle motion trajectories.
[0144] The results are shown in
[0145] The photos were taken by a high-speed camera at 5000 fps and combined with 100 frames. Each line segment in the figure represents the particle motion trajectory, because the time of 100 frames is the same (20 ms), and the length of the line segment represents the distance of the particle motion in this time period, the longer the line segment, the faster the particle motion is. It can be seen that with the same power, the speed of particle motion in the vortex increases as the height decreases. Since the drag force of the fluid is proportional to the flow velocity, the vortex will have a stronger drag force of the fluid when the height of the flow channel is lower. On the other hand, as the height decreases, the center of the vortex will also be closer to the UHF resonator, which means that the particles which enters the vortex enters above the UHF resonator has a trajectory closer to the surface, and the particles are subjected to greater acoustic radiation force and change trajectory into the center of the vortex. As can be seen, while the power conditions remain the same, reducing the height of the flow channel can increase the vortex fluid velocity, and therefore the drag force.
EXAMPLE 4
Isolation of Exosomes from Plasma Samples
[0146] According to the method described in Examples 1 and 2, a microfluidic channel and a UHF resonator were prepared and set up as shown in
[0147] As shown in
[0148]
[0149] The first sample is a 10-fold dilution of plasma. The results of the experiment are shown in
[0150] Experimental parameters: flow rate Vpbs=Vplasma was 2 μL/min, which corresponds to V of 1.07 mm/s, the power applied to the UHF resonator was 209 mW, and the flow channel height was 20 um.
[0151] The second sample was undiluted plasma. The experimental results are shown in
[0152] The experimental parameters: the flow rate Vpbs was 2 μL/min, Vplasma was 3 μL/min, the power applied to the UHF resonator was 660 Mw, and the flow channel height was 20 um.
[0153] As can be seen, with the microfluidic device of the present invention, vesicles of different sizes, including exosomes, can be isolated as needed by adjusting the power and flow rate of the bulk acoustic waves generated by the UHF resonator.
EXAMPLE 5
Isolation of Nucleic Acids
[0154] According to the method described in Examples 1 and 2, a microfluidic channel and UHF resonator are prepared and set up as shown in the left side view of
[0155] Nucleic acid samples used herein are double-stranded nucleic acids obtained by PCR amplification reactions, which can be obtained by selecting (synthesizing) appropriate primers based on the sequence of the DNA template and then amplifying nucleic acids with the exact number of nucleotides. Nucleic acids are stained and quantified with the Qubit sDNA HS kit, dissolved in PBS solution and adjusted to approximately 85 ng/l.
[0156] The system setup and fluorescence observation phenomena are shown in
[0157] As shown in the figure, when the UHF resonator generates bulk acoustic waves after applying power (2100 mW), the nucleic acids of 76 bp, 151 bp, 200 bp, 500 bp, and 1000 bp are pushed onto the surface of the flow channel above the UHF resonator and captured by the acoustic radiation force as they pass through the bulk acoustic wave region. When the UHF resonator stops generating bulk acoustic waves, the captured nucleic acids are dislodged and flow in the direction of the liquid stream; where the dashed coil indicates the nucleic acids that move after being dislodged.
[0158] The results show that nucleic acids from about 50 bp to 1 kbp can be captured and released by the microfluidic device of the present invention.
[0159] As can be seen, the microfluidic device and method provided by the present invention can capture nucleic acids of different sizes by adjusting the power and flow rate of the bulk acoustic waves generated by the UHF resonator as needed, and then releasing them into solution for the purpose of isolating or purifying nucleic acids. Without being limited by this theory, the applicant believes that the microfluidic device provided by the present invention are suitable for being used to capture nucleic acids (especially small molecule nucleic acids) in the area affected by bulk acoustic wave, the effects are depending on the height of the flow channel and the frequency of the bulk acoustic wave; the nucleic acids are subjected to the acoustic radiation force caused by the acoustic wave attenuation.
[0160] The microfluidic apparatus and method provided by the present invention can, after capturing the nucleic acids of different sizes, release these nucleic acids of different sizes one by one in the order from smallest to largest as for further separation, by adjusting the power of the bulk acoustic waves generated by the UHF resonator and the flow rate of the solution passing through the bulk acoustic wave region.
[0161] In summary, the microfluidic devices and methods for separating flexible particles provided in this application enables selective and specific capture and release of flexible particles of different sizes, including cellular microvesicles or nucleic acids, thereby obtaining or purifying flexible particles for further analysis.
[0162] The above description is only an embodiment of the present invention and is not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principles of the present invention shall be included in the scope of protection of the present invention.