The present invention relates to aptamer sensors, and to devices and methods including aptamer sensors.
This section is intended to introduce the reader to various aspects of art that may be related to various aspects of the present invention, which are described and/or claimed below.
This discussion is believed to be helpful in providing the reader with background information to facilitate a better understanding of various aspects of the present invention. Accordingly, it should be understood that these statements are to be read in this light, and not as admissions of prior art.
Electrochemical sensors such as enzymatic and aptamer-based sensors promise single-step and continuous sensing capabilities that are reagent-free and label-free, but inherent to this same promise is susceptibility to interference and degradation due to fouling, uncontrolled pH or salinity, or other solutes in the sample fluid. For at least pH and salinity, some sample fluids are inherently buffered, such as blood, but other emerging biofluids, such as human sweat or environmental fluids, can have widely ranging pH and salinity. A need exists for improved methods of (1) protecting electrochemical sensors from damaging pH and/or salinity levels (or damaging fluctuations in pH and/or salinity), and (2) protecting electrochemical sensors from other degradation mechanisms as well, such as oxidants, nucleases, or other solutes that can hinder or damage a sensor.
Certain exemplary aspects of the invention are set forth below. It should be understood that these aspects are presented merely to provide the reader with a brief summary of certain forms the invention might take and that these aspects are not intended to limit the scope of the invention. Indeed, the invention may encompass a variety of aspects that may not be explicitly set forth below.
Many of the drawbacks and limitations stated above can be resolved by creating novel and advanced interplays of chemicals, materials, sensors, electronics, microfluidics, algorithms, computing, software, systems, and other features or designs, in a manner that affordably, effectively, conveniently, intelligently, or reliably brings sensing technology into proximity with biofluid and analytes.
Various aspects of the disclosed invention are directed to aptamer sensors that overcome the drawbacks described above—such as by providing a device that protects aptamer sensors from damage or degradation due to harmful solutes in fluid. To that end, in one embodiment, such a device may be used for detecting the presence of, or measuring the concentration of, a target analyte in a sample fluid. The device includes a housing defining a plurality of chambers including at least a first chamber and a second chamber. The first chamber includes a sensor fluid therein, and the second chamber includes a reservoir fluid therein. A sample fluid area is also defined by the housing. This sample fluid area is capable of receiving a sample fluid to be tested for the presence or concentration of a target analyte. A first element separates the first chamber from the sample fluid area and restricts diffusion of solutes between the sensor fluid and sample fluid. A second element separates the first chamber from the second chamber and restricts diffusion of solutes between the sensor fluid and the reservoir fluid. The device also includes at least one sensing electrode that is positioned in the sensor fluid.
In various embodiments, the first and second elements (that restrict diffusion of solutes between the various fluids) may be chosen from membranes, encasements, and combinations thereof. Further, the reservoir fluid may include enhancing solutes. In this and alternate embodiments, the reservoir fluid may remove at least one harmful solute from the fluid sample.
The objects and advantages of the disclosed invention will be further appreciated in light of the following detailed descriptions and drawings in which:
As used herein, “continuous sensing” with a “continuous sensor” means a sensor that changes in response to changing concentration of at least one solute in a solution such as an analyte. Similarly, as used herein, “continuous monitoring” means the capability of a device to provide multiple measurements of an analyte over time.
As used herein, the term “about,” when referring to a value or to an amount of mass, weight, time, volume, pH, size, concentration or percentage is meant to encompass variations of ±20% in some embodiments, ±10% in some embodiments, ±5% in some embodiments, ±1% in some embodiments, ±0.5% in some embodiments, and ±0.1% in some embodiments from the specified amount, as such variations are appropriate to perform the disclosed method.
As used herein, the term “electrode” means any material that is electrically conductive such as gold, platinum, nickel, silicon, conductive liquid infused materials such as ionic liquids, PEDOT:PSS, conductive oxides, carbon, boron-doped diamond, nanotubes or nanowire meshes, or other suitable electrically conducting materials.
As used herein, the term “blocking layer” or “passivating layer” means a homogeneous or heterogeneous layer of molecules on an electrode which alter the electrochemical behavior of the electrode. Examples include a monolayer of mercaptohexanol on a gold electrode or as another example natural small-molecule solutes in serum that form a layer on a carbon electrode.
As used herein, the term “aptamer” means a molecule that undergoes a conformation or binding change as an analyte binds to the molecule, and which satisfies the general operating principles of the sensing method as described herein. Such molecules are, e.g., natural or modified DNA, RNA, or XNA oligonucleotide sequences, spiegelmers, peptide aptamers, and affimers. Modifications may include substituting unnatural nucleic acid bases for natural bases within the aptamer sequence, replacing natural sequences with unnatural sequences, or other suitable modifications that improve sensor function but which behave analogous to traditional aptamers.
As used herein, the term “redox tag” or “redox molecule” means any species such as small or large molecules with a redox active portion that when brought adjacent to an electrode can reversibly transfer at least one electron with the electrode. Redox tag or molecule examples include methylene blue, ferrocene, quinones, or other suitable species that satisfy the definition of a redox tag or molecule. In some cases, a redox tag or molecule is referred to as a redox mediator. Redox tags or molecules may also exchange electrons with other redox tags or molecules.
As used herein, the term “optical tag” or “fluorescent tag” means any species that fluoresces in response to an optical source such as LED and whose fluorescence is detectable by a photodetector such as a photodiode. Example fluorescent tags include fluorescein and may be used in combination with other fluorescent tags or optical quenchers such a black-hole quencher dyes to change the fluorescence of the optical tag.
As used herein, the term “analyte” means any solute in a solution or fluid which can be measured using a sensor. Analytes can be small molecules, proteins, peptides, electrolytes, acids, bases, antibodies, molecules with small molecules bound to them, DNA, RNA, drugs, chemicals, pollutants, or other solutes in a solution or fluid.
As used herein, the term “membrane” means a polymer film, plug of hydrogel, liquid-infused film, tiny pore, or other suitable material which is permiselective to transport of a solute through the membrane by solute parameters such as size, charge state, hydrophobicity, physical structure, or other solute parameters than can enable permiselectivity. For example, a dialysis membrane is permselective by passing small solutes but not large solutes such as proteins. Membranes as understood herein need not be multiporous, for example, a nanotube or nanopore can act as a permiselective filter and is therefore considered part of a membrane as understood for the present invention.
As used herein, the term “sample fluid” means any solution or fluid that contains at least one analyte to be measured, or any solution or fluid that is tested to determine the presence of at least one analyte therein.
As used herein, the term “sensor fluid” means a solution or fluid that differs from a sample fluid by at least one property, and through which the sensor solution and the sample fluid are therefore separated but are in fluidic connection through at least one pathway such as a membrane. The sensor solution may comprise at least one aptamer as a solute.
As used herein, the term “reservoir fluid” means solution or fluid that differs from sample fluid by at least one property, and through which the sensor solution and the reservoir solution are in fluidic connection through at least one pathway such as a membrane or a pin-hole connection. A reservoir fluid may have multiple function in a device, for example, by introducing a solute continuously or as needed by diffusion equilibrium into the sensor fluid, or for example removing unwanted solutes from a sensor fluid and acting as a “waste removal element”.
As used herein, a “device” comprises at least one sensor based on at least one aptamer, at least one sensor solution, and at least one sample fluid. Devices can sense multiple samples and be in multiple configurations such as a device to measure a pin-prick of blood, or a microneedle or in-dwelling sensor needle to measure interstitial fluid, or a device to measure saliva, tears, sweat, or urine sensor, or a device to measure water pollutants or food processing solutes, or other devices which measure at least one analyte found in a sample fluid.
One or more specific embodiments of the present invention will be described below. In an effort to provide a concise description of these embodiments, all features of an actual implementation may not be described in the specification. It should be appreciated that in the development of any such actual implementation, as in any engineering or design project, numerous implementation-specific decisions must be made to achieve the developers' specific goals, such as compliance with system-related and business-related constraints, which may vary from one implementation to another. Moreover, it should be appreciated that such a development effort might be complex and time consuming, but would nevertheless be a routine undertaking of design, fabrication, and manufacture for those of ordinary skill having the benefit of this disclosure. All ranges of parameters disclosed herein include the endpoints of the ranges.
Certain embodiments of the disclosed invention show sensors as simple individual elements. It is understood that many sensors require two or more electrodes, reference electrodes, or additional supporting technology or features which are not captured in the description herein. Sensors measure a characteristic of an analyte. Sensors are preferably electrical in nature, but may also include optical, chemical, mechanical, or other known biosensing mechanisms. Sensors can be in duplicate, triplicate, or more, to provide improved data and readings. Sensors may provide continuous or discrete data and/or readings. Certain embodiments of the disclosed invention show sub-components of what would be sensing devices with more sub-components needed for use of the device in various applications, which are known (e.g., a battery, antenna, adhesive), and for purposes of brevity and focus on inventive aspects, such components may not be explicitly shown in the diagrams or described in the embodiments of the disclosed invention.
As described above, various aspects of the disclosed invention are directed to aptamer sensors that overcome the drawbacks described in the Background section—such as by providing a device that protects aptamer sensors from damage or degradation due to harmful solutes in fluid. In one embodiment, such a device may be used for detecting the presence of, or measuring the concentration of, a target analyte in a sample fluid. To that end, and with reference to
Additionally, a plurality of aptamers (not shown in
With further reference to
The first element/protecting membrane 140, of this embodiment, may also enhance the operation of the device 100 by at least partially retaining at least one sensor enhancing solute in the sensor solution 132. One example of a sensor enhancing solute is a buffer. The reservoir fluid 134, in certain embodiments, can also assist in this by including at least one sensor enhancing solute in the reservoir fluid 134, which can be introduced into sensor fluid 132 by passing through second element 142. Reservoir fluid 134 may provide additional functions as well, such as (1) removing at least one harmful solute from sensor fluid 132, and/or (2) removing analyte from sensor fluid 132 (e.g., if analyte easily travels through first element 140 (e.g., membrane) toward sensor fluid 132 but not back into the sample fluid 130, which is the case, for example, when the analyte is a hydrophobic analyte such as cortisol and the first element 140 is an oil-infused membrane). Second element 142 can also be a membrane such as polyethersulfone (PES) or hydrogel, such as an agar hydrogel, that slows diffusion between sensor and reservoir fluids 132, 134. Alternatively, second element 142 may be a long and/or narrow channel which achieves the same effect of slowing diffusion.
Generally, a device as described herein may operate such that a solute that is potentially harmful to the sensing electrode 120 will have lower total mass transport through first element (e.g., membrane) 140 than through second element (e.g., membrane) 142 such that if the harmful solute enters the sensor fluid 132 it will be subsequently removed from sensor fluid 132 by moving into the reservoir fluid 134. Further, any harmful solutes that may be generated by sensing electrode 120 itself, such as an oxidative species that is electrochemically created, can also diffuse through second element (e.g., membrane) 142 to be removed from the sensor fluid 132. While harmful solutes in sensor fluid 132 can move via second element into reservoir fluid 134, the device 100 also operates such that analyte present in sample fluid 130 moves (e.g., diffuses) through first element (e.g., membrane) 140 easily enough such that the concentration of analyte in fluid sample 130 and the concentration of analyte in the sensor fluid 132 are comparable (e.g., differing by less than 50%, or by less than 10%, or by less than 5%). In other words, unlike the harmful solute example discussed above, the analyte does not easily move (e.g., diffuse) through second element (e.g., membrane) 142.
Further, enhancing solutes that are introduced from reservoir fluid 134 via second element 142 should have an adequate enhancing effect on the sensing electrode 120; and, in embodiments, this may be accomplished by ensuring that the enhancing solutes not easily transverse through first element 140. In other words, any restriction on the diffusion of at least one enhancing solute from the reservoir fluid 134 to the sensor fluid 132 provided by the second element (e.g., membrane) 142 is less than any restriction on the diffusion of the at least one enhancing solute from the sensor fluid 132 to the sample fluid 130 provided by the first element (e.g., membrane) 140 Enhancing solutes may include but are not limited to salts, buffers, anti-oxidants, nuclease inhibitors, and molecules that help passivate the sensor electrode such as albumin or peptides. All or a subset of the above features may form an embodiment of the present invention. In one embodiment, wherein the first element and/or second element are membranes, each membrane may be chosen from liquid filled membranes (such as oil-membranes), hydrogels, channels or porous networks, filtration or size-selective membranes, and other suitable materials that achieve the above stated functionality.
With reference now to
Electrochemical sensors such as enzymatic and aptamer based sensors promise single-step and continuous sensing capabilities that are reagent- and label-free; but, inherent to this same promise is susceptibility to interference and degradation due to fouling and uncontrolled pH or salinity in the sample fluid. With regard to pH and salinity, some sample fluids are inherently buffered, such as blood. But other emerging biofluids, such as human sweat or environmental fluids, can have widely ranging pH and salinity. This Example presents an oil-membrane sensor protection technique which allows for permeation of hydrophobic (lipophilic) analytes into a sealed sensor compartment containing ideal salinity and pH conditions, while simultaneously blocking common hydrophilic interferents (proteins, acids, bases, etc.) Herein, the oil-membrane sensor protection technique is validated by demonstrating continuous cortisol detection via electrochemical aptamer based sensors. The encapsulated electrochemical aptamer cortisol sensor of this Example exhibits a 5-minute concentration-on rise time and maintains measurement signal of at least 7 hours even in the extreme condition of an acidic solution of pH 3.
Introduction
Electrochemical sensor demonstrations are highly prevalent for testing in (1) buffer fluid or (2) blood. This should not be surprising because these two fluids are highly relevant testing standards and because both fluids are well-buffered in their pH and salinity. Being well-buffered is important to electrochemical sensor operation because pH and salinity can significantly confound sensor response. This challenge can be particularly acute for continuous biosensors because unlike a single-use point-of-care sensor, pH and salinity are much more difficult to control over the longer time period associated with continuous sensing.
Enzymatic sensors are most commonly deployed for both real-time and point-of-care assays because of their ability to couple a biochemical reaction to a change in redox state of a co-factor (e.g., NADH and FADH2) that can be measured directly or indirectly. However, enzymatic sensors are particularly sensitive to changes in pH and salinity, as they are composed of amino acids. Enzymes, as well as other proteins, are inherently pH sensitive because of their labile side-chain protonation sites, and are salinity sensitive because of their charged functional groups. Therefore, any change in salinity and/or pH must be accounted for with regards to converting enzymatic activity to analyte concentration. Changes in salinity and/or pH— and/or failing to account for such changes—increases the risk of inaccurate measurement of analyte concentration when using enzymatic sensors.
Other biosensors that utilize biorecognition elements suffer from similar constraints, including electrochemical aptamer sensors invented by Plaxco and colleagues [Dauphin-Ducharme, P.; Yang, K.; Arroyo-Curras, N.; Ploense, K. L.; Zhang, Y.; Gerson, J.; Kurnik, M.; Kippin, T. E.; Stojanovic, M. N.; Plaxco, K. W. Electrochemical Aptamer-Based Sensors for Improved Therapeutic Drug Monitoring and High-Precision, Feedback-Controlled Drug Delivery. ACS sensors 2019, 4 (10), 2832-2837. https://doi.org/10.1021/acssensors.9b01616]. These sensors rely on the high binding affinity of the analyte to the aptamer. Aptamers are known to be sensitive to both salinity and pH, thus impacting sensor performance and analyte response. Additionally, electrochemical aptamer sensors often use redox couples that are pH sensitive, such as an immobilized methylene blue redox couple.
In biofluids, the majority of the most problematic solutes are hydrophilic, including salts, acids, bases, and larger molecules (such as proteins) that must have a hydrophilic shell to maintain their water solubility. Generalizing the problematic solutes as hydrophilic presents a significant opportunity for more robust sensing of hydrophobic solutes since hydrophilic/hydrophobic selective protection could theoretically be added to sensors. Implementing such a hydrophilic/hydrophobic filter would provide protection even beyond the widely deployed size-selective protective membranes such as those used for in-vivo glucose sensors and other electrochemical aptamer sensors. Furthermore, this hydrophilic/hydrophobic membrane could be adapted to filter out redox-active interfering agents such as the negatively charged FAD/FADH2 and NAD+/NADH coenzymes.
And so, in this Example (and in accordance with the principles of the disclosed invention), the present inventors present a novel approach of oil-membrane sensor protection, which allows for permeation of hydrophobic (lipophilic) analytes into a sealed compartment containing the sensor in desirable pH conditions, while the same oil-membrane simultaneously blocks protein foulants and pH interferents (acids/bases). In this Example, the present inventors specifically validate an oil-membrane sensor protection technique by demonstrating continuous cortisol detection via electrochemical aptamer sensors. The oil-membrane encapsulated electrochemical aptamer cortisol sensor described herein exhibits a 5-minute concentration-on rise time and a measurement signal over at least 7 hours, even under extremely acidic conditions of pH 3. Also discussed are novel methods for rapidly optimizing the oil-membrane technique for each new analyte and application.
From an application perspective, the novel oil-membrane approach presented here is important for numerous applications, including those with hydrophobic analytes, such as orally administered drugs (hydrophobic by design for gut permeation), and steroid hormones (cortisol, testosterone, estrogen, melatonin, etc.). Improved robustness to variable pH also satisfies an acute and immediate need for sweat biosensing, where pH can vary significantly Further, the present inventors believe that having sensor protection even more robust than size-selective membranes could be valuable, especially if the sensor is preserved in optimal buffer conditions. In addition, oil-membrane protection may prove important as biosensing moves into areas that require alternative fluids with non-ideal pH and salinity, such as environmental sensing or food processing. Many emerging potent bio-toxins are hydrophobic because of the need to rapidly permeate biological tissue, and therefore are ideal candidates for oil-membrane protection. Lastly, oil-membrane protection may also be useful because many hydrophobic analytes in biofluids tend to bind to transport proteins, such as albumin, thus greatly reducing the unbound drug concentration for detection by electrochemical sensors. Oil-membrane protection could allow for protein denaturation by using salts or pH outside the membrane barrier to release the hydrophobic analytes such that they are increased to measurable concentrations, while still preserving the sensor environment. Simply, oil-membrane sensor protection has the potential to open up numerous biosensing applications that are currently challenged or even unobtainable with electrochemical sensors.
Device Design
1. Electrochemical Aptamer Sensor for Cortisol Sensing
Electrochemical aptamer sensors are affinity-based biosensors which equilibrate their signal to the analyte concentration. Electrochemical aptamer sensors used in this Example were provided by Eccrine Systems, Inc., Cincinnati, Ohio. In these electrochemical aptamer sensors (
2. Adding Oil-Membrane Protection onto the electrochemical aptamer Sensor
The oil-membrane encapsulation (see
3. Physics Behind Oil-Membrane Operation and Resulting Design
The permeability of the oil membrane affects sensor response time. An oil membrane will reduce the permeability (diffusion) of analytes to the sensor according to Eq. 1:
where the partition coefficient (K) is defined as the ratio of the concentrations at equilibrium of the analyte molecules in the oil vs. in the water; D is the diffusion coefficient for the analyte in the oil; and z is the thickness of the oil layer. Equation 1 is informative to oil membrane design.
The permeability equation (Eq. 1) clearly shows that a thinner membrane and, therefore, thinner oil thickness (z) will increase the membrane permeability (P). For this reason, the present inventors chose to use 11 μm thick polycarbonate track-etch membranes instead of thicker hydrophobic membranes such as conventional porous Teflon films (z=10s to 100s of μm). The oil wicks into and remains in the track-etch membrane pores because of its lower interfacial surface tension with the polycarbonate than the water has with polycarbonate. The membrane permeability equation (Eq. 1) also clearly reveals that a high diffusion coefficient (D) matters as well. The diffusion coefficient of an analyte is dependent on the viscosity of the fluid it is diffusing through. Therefore, an important design element for the oil is to have a low viscosity (diffusion coefficient is inversely proportional to the viscosity of the oil [Walter, A.; Gutknecht, J. Permeability of Small Nonelectrolytes through Lipid Bilayer Membranes. J. Membr. Biol. 1986, 90 (3), 207-217. https://doi.org/10.1007/BF01870127]. Consider an informative example related to the materials used here. The optimal track-etch membranes for this work (see Table 1-below) have an 11 μm membrane thickness and 15.7% porosity, which is equivalent to the analyte having to diffuse through a uniform 70 μm of oil (11 μm/0.157). Now consider castor oil, with a viscosity about 730 times greater than that of water (see Table 2-below). An 11 μm thick castor oil membrane would then be equivalent to a 51,170 μm thick water diffusion distance (11 μum/0.157*730). Alternatively, using a low viscosity oil, such as 1-decanol, the 11 μm thick oil-membrane would have an equivalent thickness of only 945 μm diffusion distance through water (see Table 2).
Now turning to the oil/water partition coefficient K: Although Equation 1 suggests that a high K is advantageous, it is actually misleading. In a static case, where concentration gradients are held constant on both sides of the oil membrane and the analyte is constantly diffusing through a membrane, Eq. 1 states that the highest possible K is beneficial. However, a very high K can be problematic in dynamic cases. An electrochemical aptamer sensor has to dynamically equilibrate to an often-changing analyte concentration in the biofluid; therefore, it is more important to understand the specific impact of a high K with rising or falling analyte concentrations on the biofluid side of the oil membrane.
Referring to
A high K is problematic for two reasons. First, the oil can become a huge sink for the analyte. Consider a K-value of 10,000 using the 11 μm track-etch membrane discussed above with 15.7% porosity. With the concentration of the analyte in the oil being 10,000 times higher than that in the water, the “effective volume” of the oil in terms of analyte capacity is equivalent to 11 μM* 0.157*10,000=17.27 cm of water. Clearly, K cannot be too large for this reason. A second reason why a high K is problematic is the oil retention of the analyte (lower free energy in the oil than in the water). A higher K can cause the oil to retain the analyte and induce an additional lag time as the analyte attempts to leave the oil and partition back into water. For the concentration-on process, this oil-to-water lag-time is not a major concern for the device because the volume of the buffer solution 532 is small, which reduces the total amount of analyte that must partition into the buffer solution (short lag time). For the concentration-off process, however, it is difficult for the analyte concentration in the buffer solution to decrease quickly, because the analyte concentration in the oil must first decrease, which is limited by the high K value of the oil (inherently a very high concentration of the analyte). Therefore, the oil-to-water lag time as the analyte goes from the oil back into the biofluid can create a major bottleneck for the concentration-off process, because the oil has acquired such a high concentration of the analyte. This much slower concentration-off response time will be observable later in the experimental results.
Although discussion herein on the oil-membrane physics remains focused on analyte transport, it also affects device design for blocking foulants and interferents. K will always have some finite value, even for hydrophilic acids, bases, and salts (it is never zero), and K depends on the charge state of the solute, which can further depend on the pH of the biofluid (solute ionization constants pKa and pKb). For example, a solute might be found primarily in its charged state (98%) within a biofluid of a specific pH. The remaining 2% remains in an uncharged state and may diffuse through the protective oil membrane barrier. For this reason, it is important to understand the effects of pH on analyte properties. Therefore, as the experimental data will show, the oil membrane provides limited protection over time.
Lastly, oil viscosity and oil partition coefficient (K) are not the only relevant materials parameters for oil optimization (See Table 3-below). For most sensor applications the oil must remain liquid at room temperature, while also having low vapor pressure, such that it is not rapidly lost during assembly or potential dry storage. Solubility of the oil in water is also critical because eventual oil loss into water could cause failure in the oil-membrane protection of the sensor. A simple example calculation is as follows. Consider a device that is brought into contact with 0.3 μL of biofluid per minute and a sensor and membrane area of 0.1 cm2 with the membrane containing 0.0173 μL of oil. Assuming that all the oil that could partition into the water does so at any given time (an unrealistic but instructive assumption), if the device were to operate continuously for 24 hours without losing all the oil to the biofluid, the water solubility of the oil would need to be less than 36 mg/L.
Methods
1. Materials
All oils, reagents and cortisol solution were purchased from Sigma-Aldrich (St. Louis, MO). The 96 transwell plate was purchased from Sigma-Aldrich (St. Louis, MO). The polycarbonate track-etch membrane with 1 μm diameter pore size was obtained from Sterlitech Corporation (Kent, WA). The cortisol aptamer solution and Synthetic Sweat Solution were obtained from Eccrine Systems, Inc (Cincinnati, OH). The titration curve for the cortisol aptamer is shown in
2. Sensor Functionalization
The gold planar electrodes were manufactured using a Temescal FC-1800 E-Beam Evaporator from Ferrotec (CA, USA). Ti (40 nm thick) was deposited on the glass slide as an adhesion promoting layer prior to the 200 nm gold layer. A layer of Kapton® polyimide film, laser cut to size (geometric design shown in
For cleaning, the electrode array was first sonicated for 5 minutes. Then it was connected to a CHI E600 electrochemical analyzer through 5252 SOIC clips from Pomona Electronics (CA, USA). Each foot was connected to an individual working channel A Pt wire electrode and a Ag/AgCl electrode were wired as a common counter electrode and common reference electrode, respectively, shared by six channels. The electrode array was immersed in 0.5 M H2SO4 solution. Cyclic voltammetry was applied to a 1-V/s scan rate from 0 to 1.6 V to electrochemically clean the surface of the electrode. The surface was rinsed with DI water and dried under an air gun. This was followed by O2 plasma cleaning for 2 minutes.
A 400 nM cortisol aptamer solution was drop casted onto the surface of the working electrodes and allowed to incubate in the dark for an hour. The cortisol aptamer was obtained from Eccrine Systems, Inc (Cincinnati, OH). The remaining solution was shaken off after incubation. Then 5 mM mercaptohexanol (MCH) solution from Sigma-Aldrich (St. Louis, MO) was used to further passivate the surfaces of the working, counter, and reference electrodes. The functionalized electrodes were stored in a dry hood for 2 hours and protected from the light. When this process was completed, the surface was rinsed with DI water to get rid of extra MCH.
The gold rod electrode was purchased from CH Instruments, Inc (Austin, TX). The cleaning and functionalization process were same as those of the planar electrodes.
3. Integration for Device without Buffer Reservoir
The oil-membrane device shown in
For assembly, the functionalized sensor was first placed into a 100 mm diameter petri dish filled with PBS solution. With the oil-membrane and bottom- and top-adhesive assemblies all attached to each other, they were then placed onto the sensor electrode array. Once assembled, the device was removed from the solution, the extra solution on its outside was dried, and the device was quickly sealed with Brampton marine epoxy from Brampton Technology LTD. (CT, USA) along the perimeter of the device. After 30 minutes, and once the epoxy was cured, the sensor was ready for testing.
4. Integration for Device with Buffer Reservoir
In the device, the sensor electrode array 720 was connected to 5252 SOIC clips from Pomona Electronics (CA, USA) and placed flat. A 10 cm diameter petri dish was filled with lx PBS solution and placed right next to the sensor as a buffer reservoir (with reservoir fluid 734). A 5 mm wide L-shape cut-out of a single layer of Kimtech Science™ Kimwipes™ Delicate Task Wipe was fully saturated with PBS solution. One 5 mm long leg 760 of the L-shape Kimwipes™ tissue was applied onto the sensor. The other leg 762 was connected to the buffer reservoir. A layer of polycarbonate track-etch membrane saturated with oil 764 was applied on top of the Kimwipes™ tissue. A 5 mm wide strip was cut out from a single layer of Kimtech Science™ Kimwipes™ Delicate Task Wipe, wetted with buffer solution, and applied on top to pass sample fluid from a syringe pump 766 over the oil membrane to waste pump. The sample fluid 730 was pumped at 4 μL/min. A 5 mm×5 mm×3 mm acrylic block was then placed on top of the strip as a weight to hold all the layers compressed against each other. This device is shown in the drawing of
5. Data Generation and Analysis
During the test, the sensor was connected to a CHI E600 (CH Instruments, Inc, Austin, TX) through 5252 SOIC clips. Square wave voltammetry was used within a scanning window of 0 to -0.5 V, with amplitude of 0.035 V and frequency of 500 Hz (for rod electrodes) or 120 Hz (for planar electrodes). The raw data was exported from a saved text file from the CH Instrument (Austin, TX) Software. The signals were processed by a customized model in MATLAB (available at https://www.mathworks.com/products/matlab.html). The signal gain was measured by reading the highest current within two manually set potential points and then subtracting the baseline linearly matched by these two set points.
Experiments and Results
1. Initial Oil Screening Test
As noted in the Device Design section (above), oil choice is a consideration for the successful realization of the oil-membrane technique. The nine different oils listed in Table 3 were initially selected and tested. Initial selection parameters are based on low water solubility and low vapor pressure, to ensure long-term oil integrity within the membrane pores. In addition, oils with positive octanol/water K values are favored because of the hydrophobic nature of the test analyte (cortisol) while achieving a low permeability for hydrophilic interferents (pH and salinity).
In order to rapidly screen the oil candidates, a commercially available transwell setup was modified to measure the concentration of diffused cortisol through transwell membranes with different oils.
2. Directly Testing Oils Against Salt and pH Permeability
Before testing the integrated devices, the top three-performing oils (1-decanol, tetradecane, castor oil) were tested directly against high salt solution and extreme acidic solution. A U-boat setup was employed to measure salt diffusion from one buffer solution compartment to another separated by an oil membrane. For the salt diffusion test, a 10 mL buffer solution containing 0.15 M NaCl was placed in a right (control) chamber and 10 mL distilled (DI) water was placed in a left (monitored) chamber. The two chambers were separated by an oil-impregnated membrane secured by two rubber washers. The electrical resistance of the solution was measured in 60 seconds increments using a CHI 600E potentiostat, as shown in
As shown in
3. Initial Sensor Tests as Control Experiments
The sensors were first characterized directly for the effects of pH on sensor response in order to aid in the interpretation of electrochemical aptamer sensor data. To initially find the optimal pH environment for the specific cortisol-binding aptamer, a three-electrode system was tested: an aptamer-functionalized gold disk electrode, a Pt wire counter electrode, and an Ag/AgCl reference electrode. The sensor system was tested for 5 minutes in each solution—with and without cortisol—to measure the on/off signal performance The pH of the sensor solution was varied from pH 8.5 to 5.5. The activity of methylene blue was demonstrated by the signal gain as a function of time pre- and post-cortisol exposure (
As an additional control experiment to further reveal the negative impact of pH and the positive impact of oil-membrane protection, another U-boat test setup in a similar manner to that described above was implemented but using a cortisol electrochemical aptamer sensor to monitor sensor functionality. The monitor side was filled with 10 mL of synthetic sweat solution (SSS) at pH 7.5 without cortisol, while the control side was filled with SSS containing 10 μM cortisol concentration at pH 3. Castor oil was used as the oil in the oil membrane. The sensor with the oil-membrane protection responded to cortisol by an increase in redox-couple peak current, and the redox-couple peak position (potential) remained stable over time. Conversely, the same experiment but without oil in the membrane (water-filled) showed that the signal gain response decreased, and the redox peak rapidly shifted in potential. With these results in hand, the next set of experiments pursued the testing of fully integrated devices.
4. Fully Integrated Device Tests
For the remainder of experiments, fully integrated devices were tested using components previously illustrated in
Initially, on the basis of the results in the previous sections, the three best-performing oils (1-decanol, castor oil, and tetradecane) were chosen for the fully integrated device tests. However, the tetradecane was not compatible with the epoxy used to assemble the sensor, nor does it remain stably wetted in the membrane pores (the interfacial tension being potentially too large with respect to the polycarbonate). As a result,
And so, the device concentration-on response time shown in
Next, the device concentration-off response time is discussed. As shown in
Lastly, to confirm that each test uses an oil membrane with high integrity (no leaks) and to test the ability of the oil-membrane to protect against pH, the final step in the experiments in
5. Stronger Buffer to Improve pH Protection
With 1-decanol as the highest-performing oil in terms of a fast concentration-on time, but also with reduced protection to pH, a simple solution to improve pH protection was next explored. Simply, the solution on the sensor side is more strongly buffered. The present inventors enhanced the buffer capacity of the SSS sensor solution by adding PBS powder to a final concentration of either lx PBS or 33×PBS. Results shown in
6. An Additional Buffer Reservoir Resolves Concentration-off Challenges and Buffering Capacity
The final design of the device pursued in this work is arguably the most compelling from an application perspective, as it resolves both the longevity concerns of the sensor system as well as the concentration-off response-time challenges discussed both theoretically and shown experimentally in previous sections. As shown in
Conclusions
In this Example, the efficacy of an oil-membrane sensor protection approach, including its design and operation with cortisol analyte both in the presence and absence of interferents is demonstrated. Although the cortisol aptamer sensors results can be highly variable from sensor-to-sensor in terms of signal-gain, the effects of oil-membrane protection are consistent and clear across all results and all figures. The results demonstrate the basic feasibility of the oil membrane approach for sensor protection and does so over time scales (>3 hours) and response time (1's to 10's of minutes) that are relevant for both point-of-care and continuous biosensing applications. The buffer-reservoir approach of
While the present invention has been disclosed by reference to the details of preferred embodiments of the invention, it is to be understood that the disclosure is intended as an illustrative rather than in a limiting sense, as it is contemplated that modifications will readily occur to those skilled in the art, within the spirit of the invention and the scope of the amended claims.
This application claims the benefit of the filing date of U.S. patent application Ser. No. 63/082,834, filed on Sep. 24, 2020; claims the benefit of the filing date of U.S. patent a Ser. No. 63/082,999, filed on Sep. 24, 2020; claims the benefit of the filing date of U.S. patent application Ser. No. 63/083,029, filed on Sep. 24, 2020; claims the benefit of the filing date of U.S. patent application Ser. No. 63/085,484, filed on Sep. 30, 2020; claims the benefit of the filing date of U.S. patent application Ser. No. 63/122,071, filed on Dec. 7, 2020; claims the benefit of the filing date of U.S. patent application Ser. No. 63/122,076, filed on Dec. 7, 2020; claims the benefit of the filing date of U.S. patent application Ser. No. 63/136,262, filed on Jan. 12, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,667, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,677, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,712, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,856, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,865, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,894, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,944, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,953, filed on Feb. 18, 2021; claims the benefit of the filing date of U.S. patent application Ser. No. 63/150,986, filed on Feb. 18, 2021; and claims the benefit of the filing date of U.S. patent application Ser. No. 63/197,674, filed on Jun. 7, 2021, the disclosures of which are incorporated by reference herein in their entireties.
Filing Document | Filing Date | Country | Kind |
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PCT/US2021/051919 | 9/24/2021 | WO |
Number | Date | Country | |
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63197674 | Jun 2021 | US | |
63150667 | Feb 2021 | US | |
63150677 | Feb 2021 | US | |
63150712 | Feb 2021 | US | |
63150856 | Feb 2021 | US | |
63150865 | Feb 2021 | US | |
63150894 | Feb 2021 | US | |
63150944 | Feb 2021 | US | |
63150953 | Feb 2021 | US | |
63150986 | Feb 2021 | US | |
63136262 | Jan 2021 | US | |
63122071 | Dec 2020 | US | |
63122076 | Dec 2020 | US | |
63085484 | Sep 2020 | US | |
63082834 | Sep 2020 | US | |
63082999 | Sep 2020 | US | |
63083029 | Sep 2020 | US |