Patent Application
20130137108
The instant application contains a Sequence Listing which has been submitted in ASCII format via EFS-Web and is hereby incorporated by reference in its entirety. Said ASCII copy, created on Dec. 5, 2012, is named B19729US.txt and is 2,307 bytes in size.
Disclosed herein is a diffusion-limiting reactor having a first element and a closure element, said reactor having at least two interconnected reservoirs said interconnection being by non-impinging microchannel, and at least one said reservoir and said microchannel being magnetic accessible. Further disclosed is a method of sample separation.
The target-probe or sample microbead diagnostic field has long sought a technology capable of the rapidly moving beads by other than relying on flow. An ideal system would be capable of taking less than 1 min to move thousands of beads in a microfluidic environment. Such technology would largely avoid diffusional mixing. This can be expressed as channel length (L) which will be is long so that time of diffusion=(L*L)/2D is more than 60 min. D is the diffusivity of molecule.
Available separatory chips employ reservoirs with a channel connecting said two reservoirs. The channel contains the same solution as one of the reservoirs. The reservoirs contain different solutions.
Particular reference is made to U.S. Pat. No. 7,708,881 to Yu. In Yu, the separation scheme requires multiple washes and elusion by a series of reaction chambers connected by round microfluidics channels. Yu discloses 50 um-500 um diameter channel connection with openings but does not provide any length. Their large diameter connections and short lengths permits significant molecular diffusion or mixing. Thus, the mixing solution, buffer solution and elusion solution, having mixed, ineffectively wash the beads. There is no optimal design of microtube connector between reservoir for magnetic movement in Yu. The beads bunch up and likely to clog channel. Large number of beads would lead to clogs and loss of beads in reservoir. Also, magnetic beads are pulled to the top limiting washing
Yu discloses a PMMA and Teflon device. The bonding between PMMA and Teflon will not provide perfect sealing. Both PMMA and Teflon are hydrophobic. This fosters bubble traps which are hard to exclude. Also PMMA and Teflon present surfaces which are hard to functionalize. Silicon based materials lend themselves to non specific binding of bio molecules.
Yu does not disclose employing different viscosity fluids in channels. The disclosed designs are not suitable for small electric field or gravity driven opposing flow, and offer no teaching or suggestion by which to temperature control reservoirs fluid by metal coating based methodologies. U.S. Pat. No. 7,708,881 and all publications cited herein are incorporated by reference in their entirety.
Reference is made to European Patent Application No.10800660.2 (PCT/US2010/042426) entitled DETECTION OF SHORT RNA SEQUENCES (Tripathi, et al,) published on Jun. 13, 2012 under Publication No. 2462236 disclosing an assay termed a SMART assay.
The disclosed microfluidic sample enrichment and target detection technology provides the following attributes to the problem at hand:
(a) It is not a standard round tube based separation technique nor does it require repeated washing/rinsing steps or excessive reagents. It does not use lateral flow.
(b) The rapid travel of magnetic beads (at least about 0.5 mm/sec and preferably at least about 0.7 mm/sec) through microchannel fluids provides limited carry-over of target or sample molecules not bound to microbeads.
(c) It does not require flow of sample solution containing target molecules. The capture/binding of spores occurs in the output reservoir, so that the method uniquely processes large amount of sample for rapid separation;
(d) It separates at high efficiency without membrane or pumps; Thus, it is quite useful for resource limited settings;
(e) To reduce the carry over or diffusion of unbound molecules, a counter flow of clean high viscosity buffer from output reservoir to input reservoir is optionally created by fluid volume differential;
(f) Multiple washes are be generated by fabricating a microchannel from output reservoir to an additional output reservoir and so on (
(g) The method can be fully automated using motion control hardware;
(h) The method can be integrated to a downstream microfluidic process; and,
(i) A magnetic stirrer can be used inside the reservoirs for mixing.
As to high viscosity reaction fluids or buffers, particular reference is made to viscosities of from 10× to 400× (10 times to 400 times) the viscosity of water with particular reference to the 20× to 200× range (dynamic viscosity). As to viscosity enhancers, specific reference is made to methylcellulose, hydroxypropylmethylcellulose, poly(vinlypyrrolidone) and poly(vinly alcohol). In some embodiments water is viscosity enhanced by addition of said viscosity enhancers.
Particular attention is drawn to the capacity for the disclosed fluid filled system to comprise distinct fluids at particular locations. This provides altered or reduced mixing or diffusion associated with differing fluid viscosities. In a particular embodiment it is contemplated that one reservoir have a solution of specific salinity, pH, rehology, temperature, etc as well as other components (e.g., proteins, nucleotides, epitopes, viral, ligands, or other molecules) while the microchannel leading to a next reservoir have the same or different fluid (or multiple fluids in specific sections), and the outflow reservoir have, perhaps, yet another fluid composition. And, of course, an elaborate system of multiple reservoirs and multiple microchannels, in line or branching, is also contemplated.
In a specific configuration the reactor process entails moving the magnetic beads between reservoirs by the use of an electrical field of <30 V/cm. A field of this density avoids significant non-specific binding. An optimized electric field is not strong enough to unbond target molecules but strong enough to unbond nonspecific molecules on the magnetic beads.
The invention further comprises a method of sample separation by fluid filled diffusion-limiting reactor having a first element and a closure element, wherein the reactor has at least two interconnected reservoirs. In this embodiment the interconnection is a non-impinging microchannel leading between at least two reservoirs. The microchannel is magnetic accessible. In this method of separating the samples the method comprises moving samples while the samples are affixed to magnetic beads. The method includes mixing a first solution at least incorporating a plurality of the magnetic beads under conditions wherein the sample binds with the magnetic beads in the first reservoir. The method next moves the magnetic beads using magnetic force. The magnetic beads are moved from one reservoir through said interconnecting micro channel add deposited in the next (or subsequent) reservoir. Particularly noted in this method is employing high viscosity fluid as part of the fluid fill. Note is made of viscosities of at least about 10× to about 400× the viscosity of water, and particularly from about 20× to about 200× the viscosity of water. Useful viscosity enhancers include, without limitation, methylcellulose, hydroxypropylmethylcellulose, poly(vinlypyrrolidone) and poly(vinly alcohol), alone or in combinations. Without being bound by any particular theory, faster bead movement reduces diffusion of material. It is also more efficient than fluid flow modalities to quickly conclude material separation Particular note is made of moving magnetic beads by magnetic force through said microchannel comprises moving at about at least about 0.5 mm/sec, and preferably at least about 0.7mm/sec.
a) and (b) are schematics of the SMART assay.
c) is a diagram of three phases of a separation process.
d) is a diagram of probe amplification.
a) is a diagram of a chip or reactor design of the present invention and
a)-(c) are graphs of probe amplification (fluorescence) data.
a)-(c) are graphs of probe sensitivity (fluorescence) data.
The present system provides rectangular or square microchannels of a taper design for efficient bead travel. The taper design also reduces the need for strong magnets. Further noted is the use of high viscosity liquids in channels. This avoids or reduces carryover of unwanted molecules. This is facilitated by the motive force being magnetic force or field and not (or only minimally) fluid flow. In the disclosed embodiments, individual reservoirs can be accurately temperature controlled. In one embodiment temperature control is by metal coating or film on a reactor glass cover and induction heating.
A significant aspect of this separation method is utilization of magnetic beads for bioassays, not as a static solid-support, but as a mobile platform on which multi-step microfluidic procedures are be performed. In one embodiment, magnetic beads bearing a capture antibody/nucleotide and detector antibodies/nucleotide probes are mixed in with a sample containing target molecules in the microfluidic reservoir 1 (
This invention will be better understood with reference to the following definitions:
A. Diffusion-limiting shall mean bead migration is accomplished in least than 60 minutes, and preferably less than 30, minutes and most preferably in less than about 1 minute. Since the diffusion time tdiff˜l2/2D in a l=30 mm long microchannel is much longer (hours) than the total time of bead transfer tBT˜1 min, the disclosed reactor and process exhibits limited or no diffusion of molecules.
B. Reactor shall mean a first element and a closure element applied to said first element so as to enclose fluid and beads used in the operation. The first element of the reactor contains at least two reservoirs and at least one channel interconnecting the reservoirs. In one embodiment, reservoirs and interconnecting channel(s) are located on the upper surface of the first element, to which the closure element may be applied. It is to be appreciated that “upper surface” references are for convenient description, Fluid and beads may be introduced into the reservoirs, and the cover element applied, while the reactor is held in inverted or any other orientation.
It is a further condition of said reactor that of said at least two reservoirs, one is an input reservoir, and said input reservoir and associated interconnecting microchannel is magnetic accessible. The microchannels of this invention are necessarily rectangular or square.
C. Magnetic accessible shall mean that a magnet is capable of moving the microbeads of this invention from said input reservoir through said microchannel to an output reservoir.
D. In the present invention the microchannels are configured in a non-impinging taper. Non-impinging shall mean microchannel tapering from a transverse width of about 4:1. to about 3:1 with particular reference to 4:1, wherein the wider end of the microchannel is at the entry point for magnetic or ferromagnetic microbeads of from about 2 to about 3 microns-3 microns (collectively, “microbeads”) and the narrower end is the exit point for said beads. Typically the entry point of the a microchannel is from a input reservoir and the exit point of a microchannel is to an output reservoir. It is understood that in multiple reservoir reactions or schemes, magnetic beads are caused to enter an output reservoir as to a first step, but be moved from there into a further microchannel, thus rendering said output reservoir an input reservoir as to a further microchannel and reservoir.
In one embodiment the microchannel tapers from about 200-50 microns over length of about 2-3 cm. The depth of channel is from about 10 to about 120 um and is substantially the same for entire channel.
Typically microchannels of this invention employing magnetic or ferromagnetic beads of from about 2 to about 3 microms-3 microns. Attention is drawn to microchannels from about 2 to about 5 mm in length with particular reference to microchannels of about 3 to about 4 mm in length.
Note is made of microchannels rectangular in cross section with a depth of about 10 to about 120 microns, with particular reference to a depth of from about 95 to about 105 microns and particularly about 100 microns.
In one reactor embodiment the first element comprises polydimethylsiloxane (PDMS) and the closure element comprises glass. Reactors have two or more depressions or hollow areas being reservoirs and microchannels connecting at least two said reservoirs.
A polydimethylsiloxane (PDMS) microchip is usefully fabricated using soft lithography. PDMS is poured over the fabricated SU-8 structure on a silicon wafer and then incubated at 75° C. for two hours. The PDMS is removed from the mold, cleaned with ethanol and oxygen plasma (PDC-32G, Harrick Plasma Ithaca, N.Y.) and bonded to a Pyrex® slip (1.4 mm thick). The microchannel is a tapered lane of 400 μm wide down to 50 μm wide, 120 μm deep and 30 mm long. The depth of the channel is measured by surface profilometer (Dektak). 1 μL of 1 μg/μL (˜65,000 beads) magnetic beads progressing through the microchannel at 0.7±0.04 mm/s (images captured at 2× magnification). Beads are guided to the beginning of the channel (left, ˜400 μm width) just beyond the initial tapering from an input reservoir. Beads then are guided to the middle of the channel (middle, ˜200 μm width). Beads are finally guided the full duration of the channel (30 mm in total) and are located at the end of the channel (right, ˜50 μm width) about to enter an output reservoir.
E. Sample or target-probe as used herein shall be broadly construed as referencing proteins, nucleotides, epitopes, viral, ligands, or other molecules which are affixed or capable of being to magnet beads for separation in the process described herein. In the process of this invention, samples are separated from other materials, which may be proteins, nucleotides, epitopes, viral, ligands, or other molecules, but distinguished as not being the desired material to bind or affix to the magnetic beads. It is to be understood that the magnetic beads may be coated with a material (e.g., straptavidin) to facilitate the binding of a sample to a bead.
In
In
In the above embodiment, the microchannel connecting reservoirs are long. In one configuration the channel contains high viscosity fluid. In another embodiment, the channel contains a fluid that is not that of either connected reservoir. This, unlike known systems, provides a different flow environment for magnetic bead travel providing enhanced separation of sample from extraneous or unbound molecules.
In
In one embodiment, a magnet (bar magnet, 2.5×1.25×0.64 cm thick) is used, directly beneath the reactor and held approximately 1 mm in front of the main bead cluster during movement. The reactor is moved relative to the magnet moving beads through the microchannel toward the output reservoir at a specific velocity. Rare earth magnets (Grade N52) were purchased from K&J Magnetics (Jamison, Pa.). Spherical super-paramagnetic streptavidin coated Dynabeads® M-280 (Ø 0 2.8 μm, 10 mg/ml) were obtained from Invitrogen (Carlsbad, Calif.).
Magnetic accessible is when the reactor is configured and adapted to move said magnetic beads between reservoirs by the use of an electrical field of about 20 to 40 V with particular reference to <30 V/cm. The non-specific binding usually contain weak interactions with bead surface. As such a small electric field breaks the interaction, likely by attracting the molecules towards positive electrode. Hence, the selected field is weak enough to unbond target molecules (while not breaking specific chemical bonds) but enough to unbond nonspecific molecules (as they are connected via weak bonds) on the magnetic beads.
The disclosed apparatus and method us useful in RNA amplification and detection using engineered amplification probes. The instant system amplifies and detects engineered ssDNA probes that hybridize to the target RNA. The amplifiable probe-target RNA complex is captured on magnetic beads using a sequence-specific capture probe and separated from unbound probe using the disclosed microfluidic technique. Hybridization sequences are not constrained as they are in target amplification reactions such as nucleic acid sequence amplification (NASBA). As disclosed herein, an ssDNA probe is amplified both off chip and in a microchip reservoir at the end of the separation microchannel using isothermal NASBA, and optimal solution conditions for ssDNA amplification Potassium and magnesium chloride are typically found in NASBA reactions. As disclosed herein, replacing the 70 mM of the 82 mM total chloride ions with acetate results in better reaction conditions in certain embodiments, particularly for low clinically relevant probe concentrations (≦100 fM). In particular embodiments of probe design and solution conditions, the initial heating step of NASBA was unnecessary, resulting in a true isothermal reaction proceeding at 41° C. for 90 minutes. The SMART assay using a synthetic model influenza DNA target sequence serves as a fundamental basis to show the efficacy of the capture and microfluidic separation system. The probes investigated here have been shown to successfully hybridize to full-length influenza A H5 vRNA, thus providing utility for addressing a clinically relevant detection problem.
Influenza is a widespread pathogen that results in approximately 36,000 annual deaths in the US. Influenza comprises variety of subtypes, which are classified by the antigenic subtype of hemagglutinin (H1-16) and neuraminidase (N1-9) proteins expressed on the viral particles. Seasonal influenza is generally caused by H1 N1, H3N2, and H1 N2 viruses, while highly pathogenic avian flu is caused by the H5N1 subtype. A swine-derived recombinant variant of H1 N1 virus has been reported in limiting a pandemic. A recurrent pandemic of influenza could result in millions of worldwide deaths. Such a catastrophic event may be avoided if rapid point-of-care diagnostics were available to health workers at the source of the infection, such that they could contain the infection before it spreads into the global community. Additionally, rapid diagnosis of influenza would prevent excessive antibiotic use, which leads to antibiotic resistant bacterial strains and is a large financial burden due to the extra cost of unnecessary treatment, hospitalization, and medication 9,10.
A number of approaches have been investigated for influenza diagnostics, but each of these has associated limitations. Viral culture is specific and provides viable virus for further testing, but it takes 3-14 days for a result, limiting its use for rapid diagnostics. Immuno-specific tests, such as rapid antigen tests and immuno-fluorescence microscopy, lack sensitivity and do not provide sequence specific information for subtyping. Viral nucleic acid amplification and detection can generate subtype or strain specific information, but these tests are also complex and expensive. Polymerase Chain Reaction (PCR) requires expensive benchtop thermal cyclers and trained technicians. Nucleic Acid Sequence Based Amplification (NASBA) is faster than PCR for RNA amplification and compares favorably with PCR for HIV RNA detection in clinical samples. It is limited by secondary structure of RNA, which makes primer design and multiplexing difficult. Hybridization sites on long, clinically relevant RNA strands require stringent oligonucleotide design, with only a small fraction of sequences hybridizing efficiently to RNA. Poor hybridization of ssDNA oligonucleotides complicates primer design, making many conserved regions unsuccessful as NASBA priming sites. To combat these issues, NASBA begins with a 65° C. heating step before the addition of enzymes to disrupt full-length RNA secondary structure, and primer sites for NASBA reactions are typically 100-250 nucleotides apart to avoid products with inhibitory secondary structure.
Recently, diagnostic NASBA assays integrated with microfluidic systems have shown improvements over conventional benchtop techniques. These reactors decrease reagent use and further decrease energy consumption of the isothermal system by decreasing the reaction volume. Additionally, these small reaction volumes inherent in microfluidic chips (10 nL-2 μL) concentrate the target molecule of interest to improve primer binding and reaction kinetics. A reported study claimed the efficacy of small (10-50 nL) reaction volumes in silicon-glass reaction chamber, followed by a reactor containing 10 parallel 80 nL chambers that filled using capillary action. A particular reactor design contained 11 parallel channels with two separate chambers for each heating step separated by hydrophobic burst valves. The second chamber included dehydrated enzymes, which were shown to function in a real-time NASBA reaction upon the addition of off-chip heated reagents and primers. Although the full reaction was not run on chip, the sample was purified off-chip, and the capillary loading resulted in the loss of sample, this study shows several advantages of a microfluidic diagnostic system. The reactor was made to be simple, multiplexed, automated, shelf-stable, and consume fewer reagents and energy than its benchtop counterpart. Another reported assay integrated purification and amplification of RNA using a polydimethylsiloxane (PDMS) chamber reactor. Two reactors were contained on one chip, which would allow two RNA samples to be simultaneously purified from bacterial lysate, mixed with reaction mix, heated, mixed with enzyme, and detected real-time using sequence-specific molecular beacons. Both systems show the ability of microfluidics to create a closed, efficient, automated system that would decrease technician time, human error, and potential for contamination. These papers show the viability and advantages of incorporating a microfluidic platform with NASBA.
Disclosed herein is an amplification method, SMART, that both incorporates the advantages of microfluidics and avoids the limitations in NASBA, which include inhibitory secondary structure of the amplified RNA segment and constrained binding sites between 100 and 250 nucleotides apart. SMART achieves this by incorporating a microfluidic separation step, which allows the two binding sites to be anywhere along the RNA target. Additionally, the incorporation of an engineered ssDNA probe allows the user to choose amplifiable probe and primer sequences, which reduces secondary structure and enables the user to optimize reaction kinetics. Typically, the amplification step in SMART does not directly amplify the starting RNA.
To demonstrate this novel method, experiments were first performed off chip to verify that the amplification step created the expected nucleic acid products and to optimize solution conditions. Upon verification of an optimized amplifiable probe set and solution conditions, the optimized amplifiable probe set and solution conditions were then transferred to the microchip platform to investigate microfluidic separation and amplification. The technique achieved separation of bound probe from free probe by magnetically dragging beads through a microfluidic channel. Optimized real-time amplification and detection of the probe on-chip was also investigated.
The SMART method employs two probes that bind to specific sequences within the target RNA, allowing investigators to test for multiple characteristics of a pathogen such as subtype, drug resistance, and strain.
Amplification of the probe is performed via NASBA (
CCTATTGCTCTGATCTGATTAC
ATCTGATTAC
Table 1: Oligonucleotides used in the SMART method, shown 5′ to 3′. Probes, primers, and molecular beacon used in the NASBA reactions target H5 vRNA, but for proof-of-concept a short ssDNA synthetic target with H5 binding sites was used. The H3 ssDNA target contains binding sites specific for H3 vRNA, which serves as a negative control for H5 ssDNA target identification. The amplifiable probe sequence is conserved in 93.6% of all sequenced human H5 strains, and the capture probe is conserved in 89.3% of all sequenced human H5 strains. The lower-case region in the amplifiable probe corresponds to a binding site in H5 vRNA, the bold regions are the primer 1 binding sites, and the underlined region corresponds to the T7 RNA polymerase promoter. The beacon contains a FAM molecule on the 5′ end and a black hole quencher molecule on the 3′ end.
Design of Capture Probes, SMART Probes, Primers, and Molecular Beacons
Custom oligonucleotides given in Table 1 were purchased from either Integrated DNA Technologies, Inc. (Coralville, Iowa) or Eurofins MWG Operon (Huntsville, Ala.). The probe portion complementary to the H5 RNA target was chosen to be a sequence that has been previously shown to bind to viral RNA. Sequences of the nucleic acid arms flanking either side of the complementary portion were chosen to minimize secondary structure. This was done by first using an online folding tool (UNAFold on The DINAMelt Server, SUNY Albany) to reject sequences with predicted excessive secondary structure. The optimal probe and primer set was then chosen by finding the probe that gave the greatest product yield as shown via gel electrophoresis after a 90 minute amplification step.
Nucleic Acid Sequence-Based Amplification Reactions
The NASBA reaction was run in 200 μL polypropylene tubes, in transparent plastic cuvettes, and in 3 mm diameter PDMS microwells. Reaction volumes varied from 5-70 μL. The base NASBA mix contained 40 mM Tris pH 8.0, 12 mM MgCl2 or (CH3COO)2Mg (MgOAc), 70 mM KCl or CH3COOK (KOAc), 5 mM DTT, 1 mM dNTP, 2 mM rNTP, 0.2 μM each primer, and 15% DMSO at the final reaction concentrations. Real-time amplification reactions also included 50 nM final concentration of molecular beacon. The base enzyme mix contained 1.6 U/μL T7 RNA polymerase, 0.325 U/μL AMV-RT, 0.005 U/μL RNase-H, and 0.105 mg/mL bovine serum albumin (BSA) at the final reaction concentrations. To test optimized solution conditions, additional BSA and Tween-20 were added where indicated. Three different thermal scenarios were used to test optimized heating conditions: heating to 65° C. for 5 min and cooling to 41° C. for 5 min before the addition of enzymes, heating to 41° C. for 2 min before the addition of enzymes, and mixing the reaction mix and enzymes at room temperature. Off-chip heating was achieved using a MyCycler thermal cycler (Biorad, Hercules, Calif.) or a water bath housed within a fluorometer (Photon Technology International, Birmingham, N.J.). In-well heating was achieved using a Thermal-Clear 0.58×2.20 in. thin film heater (Minco, Minneapolis, Minn.) affixed to the bottom of the microreactor (
PDMS Reactor Fabrication
Masks were created in AutoCAD (Autodesk, San Rafael, Calif.) and negative masks were printed at 20,000 dpi (CAD/Art Services, Bandon, Oreg.). SU-8 100 (MicroChem Corp., Newton, Mass.) was spin coated at a thickness of 120 μm onto 2 inch silicon wafers, prebaked at 65° C., softbaked at 95° C., and exposed to UV light in the presence of the negative mask to selectively crosslink channels. The wafer was then baked again, placed in SU-8 developer to remove uncrosslinked SU-8, and cleaned using isopropanol. The resulting master mold was used to create PDMS microfluidic reactors (
Capture of Target Synthetic ssDNA
The short synthetic strand of ssDNA, amplifiable probe (Eurofins MWG Operon, Huntsville, Ala.), and a biotinylated H5 capture probe (Integrated DNA Technologies, Coralville, Iowa), shown in Table 1, were mixed in a hybridization buffer composed of 20 mM Tris pH 8.0, 20 mM MgCl2, 150 mM NaCl, 0.02% Tween-20, and 1 mg/mL BSA. A negative control sample contained an ssDNA target specific for H3 vRNA, and a bead control contained only the capture probe. The mixtures were heated to 70° C. for 2 minutes and cooled to 4° C. for 5 min before the addition of 2.8 μm diameter M-280 magnetic beads (Invitrogen, Carlsbad, Calif.) for a final volume of 20 μL. The samples were then incubated at room temperature for 35 min. Beads were collected at the bottom of the tube using cylindrical neodymium magnets (K&J Magnetics, Inc., Jamison, Pa.), and 18 μL of the supernatant was removed before transfer of the beads to the microfluidic separation platform.
Separation of Probe Complex
Separation of the bead-probe complex (
In-Well Real-Time Probe Amplification
Real-time amplification of ssDNA probe was conducted in a microwell using NASBA mix without separation, such that the ssDNA probe was included in the NASBA mix and added directly to the microwell (W2,
Off-Chip Probe Amplification and Optimization
We first validated that the amplification reaction worked as designed, yielding expected products. To investigate this, combinations of starting material, including amplifiable probe, primers (primer 1 alternate and primer 2, as seen in Table 1) and dsDNA, were first characterized by small RNA gel electrophoresis to find their expected peaks and bands on an electropherogram plot. In addition, the dsDNA was transcribed in NASBA conditions with T7 RNA polymerase to find the expected band for the RNA product. Given this information, a series of tests varying the presence of enzymes with amplifiable probe and primers in NASBA conditions were performed to verify the full NASBA amplification. Three conditions (
A study to inspect the effect of replacing chloride ions with acetate ions was also performed to optimize NASBA for our application. To achieve this, an experiment was carried out by running 4 amplification conditions and adjusting the base NASBA mix: 1) a positive control; 2) replacing KCl with KOAc; 3) replacing MgCl2 with MgOAc; and 4) replacing both KCl and MgCl2 with acetate complements. Samples were subjected to 65° C./41° C. heating steps before amplification, and they were analyzed via gel electrophoresis. The data (
Since gel electrophoresis only allows for endpoint quantification, the previous result was investigated further to ensure that this leads to an improvement in real time detection. A positive control using KCl and an experimental sample replacing KCl with KOAc were prepared. After initial 65° C. followed by 41° C. heating steps were performed in a thermal cycler, each sample was run in a fluorometer for a 90 minute amplification reaction. The data show that the acetate sample has a faster initial rising time than the chloride sample even though the chloride sample has a faster exponential phase (
On-Chip Probe Amplification and Optimization
A microfluidic assay for the separation and amplification of bound probe molecules aims to simplify and streamline influenza detection, as well as save energy and reagents. The removal of the initial 65° C. heating step shortens the overall assay time, decreases the energy required to operate the device, and simplifies the heating implement necessary for the device. To determine the effects of removing this step, optimal H5 probe sequences were amplified under varied heating conditions. A full heat cycle before adding the mix to the well (65° C. for 5 min and 41° C. for 5 min before the addition of enzyme) was compared to adding the full NASBA mix to the well at room temperature and heating to 41° C. on chip for 1 pM of probe. A real-time in-well reaction that was exposed to a full heating cycle showed significantly faster exponential kinetics than the reaction that was brought to 41° C. from room temperature, although the time to positive did not appear to vary significantly between the two samples (
The addition of KCl was previously shown to increase the exponential phase of the NASBA reaction (
In-well kinetics may also differ from benchtop reactions due to the contact of the reaction to PDMS and paraffin oil. PDMS is the main component of the device shown in
Capture and Amplification of Probe: SMART Assay
After determining optimized reaction conditions for in-well probe amplification, we tested the ability of the system to operate from the capture step to the amplification/detection step. 1 pM of synthetic H5 ssDNA was captured with 2 pM each of amplifiable probe and capture probe. A negative control reaction contained synthetic H3 ssDNA, and a bead control contained only capture probe (Table 1). After microfluidic separation from free probe molecules, the beads were removed from W2 (
This work demonstrates a method for amplification and detection of RNA targets by using amplifiable probes, which are engineered to optimize reaction kinetics. The reaction products, kinetics, and chemical conditions were studied utilizing both off-chip and on-chip amplification and detection systems. An optimized amplification probe was chosen, and optimized ion concentrations were determined by replacing potassium chloride with potassium acetate. Furthermore, we showed that given these optimized conditions, the initial 65° C. step can be removed, making the amplification fully isothermal, thus providing significant advantages in field and other point of care setting. The hybridization of both a capture and amplifiable probe increases specificity of the assay, and the use of magnetic beads allows for separation of the target-bead complex from unbound amplifiable probe. A simple microfluidic reactor to facilitate the separation step was also presented. Amplification in well was shown to have rapid detection at 1 pM and 100 fM with reduced reagent use, requiring only 5 μL of reaction volume. Additionally, the small reaction volume concentrates the target and probe molecules, which may decrease the time to positive. Capture, on-chip separation, and off-chip amplification was also demonstrated. Although evidence existed for non-specific binding of amplification probe, there was a distinct decrease in signal with endpoint quantification, which corresponds to a large difference in time to positive in real-time quantification for on-chip amplification. This platform is clinically relevant, as the probes presented were based upon sequences that were shown to hybridize to full-length influenza A H5 vRNA. Additionally, due to the flexibility of the amplifiable probe sequence, this method is useful for detection of any number of RNA targets, and thus this work serves as a fundamental basis for a novel, general method for RNA detection.
Note is made of the following publications incorporated here by reference in their entirety:
Influenza during Seasonal Epidemics and Potential Pandemics. The Journal of Infectious Diseases, 2006. 194: p. S98-110.
This application claims priority to copending U.S. patent application Ser. No. 13/660,427 filed Oct. 25, 2012 and to U.S. Patent Application Ser. No. 61/551,087 filed Oct. 25, 2011.
| Number | Date | Country | |
|---|---|---|---|
| 61551087 | Oct 2011 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 13660427 | Oct 2012 | US |
| Child | 13731338 | US |
