The present disclosure relates to a sensor and method for detecting arsenic in water.
Arsenic is considered as one of the most toxic elements in the natural environment. The Environmental Protection Agency (EPA) regulates the arsenic standard for drinking water at 10 ppb. In natural water, arsenic generally exists in the form of arsenite (As(III)) and arsenate (As(V)), enhancing its toxicity and mobility. Traditional instrumental analytical methods to identify arsenic in water are complicated and expensive, due to the requirements of high-cost instruments, agent preparation, and well-trained technicians. Therefore, there is a need for high-efficiency, low-cost, and rapid-response sensors for real-time monitoring of the arsenic level in natural water.
In one embodiment, the disclosure provides a working electrode comprising carbon nanotubes functionalized with a metal oxide, and metal nanoparticles on the carbon nanotubes, on the metal oxide, or on both of the carbon nanotubes and the metal oxide.
In another embodiment, a sensor is provided, with the sensor comprising a working electrode, where the working electrode comprises carbon nanotubes functionalized with a metal oxide, and metal nanoparticles on the carbon nanotubes, on the metal oxide, or on both of the carbon nanotubes and the metal oxide.
In a further embodiment, the disclosure provides a method of monitoring for the presence of an analyte in water, where the method comprises contacting a device comprising a working electrode with the water to be monitored. The working electrode comprises carbon nanotubes functionalized with a metal oxide, and metal nanoparticles on the carbon nanotubes, on the metal oxide, or on both of the carbon nanotubes and the metal oxide.
The present disclosure is concerned with working electrodes, sensors, and methods of detecting the presence of analytes (e.g., arsenic) in water, preferably in a continuous manner.
Referring to
Referring to (i) of
The substrate 12 preferably has a low water absorbency and low moisture permeability. Preferably, the water absorbency is less than about 3%, more preferably less than about 2%, and even more preferably less than about 1% according to ASTM method D570. It is also preferred that the substrate 12 does not experience hygroscopic expansion or similar deformation, which can generally be determined visually.
The substrate 12 generally has a thickness of about 50 μm to about 5 mm, preferably about 50 μm to about 2.5 mm, more preferably about 75 μm to about 1,000 μm, and even more preferably about 100 μm to about 300 μm. The substrate 12 is preferably planar, or at least presents a planar surface on which current collector 10 is deposited. The substrate may be flexible, but should be rigid enough to enable the appropriate printing and deposition processes. Additionally, substrate 12 is generally rectangular in shape, but could also be configured to be square, circular, etc., as may be desired for the particular application. Substrate 12 is preferably sized and shaped such that the entire current collector 10 can fit on the substrate surface and within the outer perimeter of substrate 12.
The substrate 12 provides a build surface 13 (i.e., a surface on which components of the sensor can be supported during and after sensor construction). The current collector 10 may be deposited on the substrate 12 by any number of conventional techniques, including sputtering, electron beam evaporation, ion-assisted electron beam evaporation, thermal evaporation, inkjet printing, screen printing, gravure printing, or flexography. As illustrated in
The size and shape of the electrode templates can vary. In the embodiment illustrated in
Regardless of the material chosen, the average thickness (as measured by an interferometer or stylus profilometer) of the current collector 10 is preferably about 10 nm to about 1,000 nm, more preferably about 50 nm to about 200 nm, and even more preferably about 100 nm.
As shown in (ii) of
As shown in
The protective conductive layer 32 should be chemically inert and exhibit low resistance. That is, protective conductive layer 32 preferably has a sheet resistance of about 1Ω/square/mil to about 5 kΩ/square/mil, more preferably about 1Ω/square/mil to about 1,000Ω/square/mil, and even more preferably from about 1Ω/square/mil to about 500Ω/square/mil.
The protective conductive layer 32 may be formed of any conductive material that is not oxidized or reduced during device operation, including, but not limited to, carbonaceous materials (e.g., carbon, amorphous carbon, carbon nanotubes, graphite, graphene, carbon nanobuds, glassy carbon, carbon nanofibers), gold, platinum, silver, and combinations thereof, with conductive carbon being a particularly preferred material for forming protective conductive layer 32. Oxidation of a material can be tested using Tafel analysis, EIS, or cyclic voltammetry in inert electrolyte solution or other electrochemical methods using inert electrolyte solution, for example. The protective conductive layer 32 may be deposited by any appropriate method, including sputtering, electron beam evaporation, ion-assisted electron beam evaporation, thermal evaporation, inkjet printing, screen printing, gravure printing, or flexography.
When one or more metals are used as the material for the protective conductive layer 32, the protective conductive layer preferably has a sheet resistance of about 1Ω/square/mil to about 5 kΩ/square/mil, more preferably about 1Ω/square/mil to about 500Ω/square/mil. When one or more non-metals, including carbon allotropes or carbon-filled polymers, are used as the material for the protective conductive layer 32, the protective conductive layer preferably has a sheet resistance of about 1Ω/square/mil to about 5 kΩ/square/mil, more preferably about 1Ω/square/mil to about 500Ω/square/mil. Regardless of the material utilized, the average thickness (as measured by a stylus profilometer or four-point probe) of the protective conductive layer 32 is preferably about 1 μm to about 100 μm, more preferably about 5 μm to about 25 μm, and even more preferably about 13 μm.
Referring to
The reference electrode material may be deposited by any conventional means, including stencil printing, screen printing, sputtering, electron beam evaporation, ion-assisted electron beam evaporation, thermal evaporation, inkjet printing, screen printing, gravure printing, or flexography. The average thickness of the reference electrode 48 is preferably about 1 μm to about 100 μm, more preferably about 5 μm to about 25 μm, and even more preferably about 13 μm.
In the embodiment illustrated in
Referring to
The encapsulant layer 50 should be a dielectric material and preferably has an ionic impedance (measured by electrochemical impedance spectroscopy) of at least about 1 MΩ, preferably at least about 5 MΩ, and more preferably at least about 10 MΩ. The encapsulant layer 50 should have a resistance of at least about 1M Ω, preferably at least about 5 MΩ, and more preferably at least about 10 MΩ. The encapsulant layer 50 must exhibit sufficient adhesion to adjacent layers (including substrate 12) to prevent leakage and/or diffusion of the analyte solution around and/or through the encapsulant layer 50.
The encapsulant layer 50 can be formed from a material chosen from one or more of poly(cycloolefins), polyesters, polyimides, silicones, polyacrylates, polysulfones, and combinations thereof. In one embodiment, the encapsulant is DuPont 5018 dielectric material. In another embodiment, the encapsulant is Zeonex® 790R material. The encapsulant layer 50 may be deposited by any appropriate means, including screen printing, inkjet printing, gravure printing, and flexography. An additional UV cure or baking step may be used to cure the encapsulant layer 50. The average thickness of the encapsulant layer 50 is preferably about 1 μm to about 100 μm, more preferably about 5 μm to about 25 μm, and even more preferably about 13 μm.
Referring to
The metal oxide-functionalized CNTs can be purchased already functionalized with the desired metal oxide. Alternatively, the functionalized CNTs can be fabricated prior to deposition, with one exemplary process being a two-step process that involves first taking the raw CNTs and polymer wrapping in a pyrene dispersant for non-covalent functionalization. This is an enthalpy-driven interaction forming π-π0 stacking between aromatic rings of CNTs, which when compared to entropic reactions that rely solely on surfactants (such as SDBS), have less aggregation and higher stability. The CNTs are reacted and wrapped with pyrene after placing in chlorosulfonic acid. This mixture is then quenched in water and neutralized with ammonium hydroxide. Next, the solution is filtered leaving the final oxidized CNT paste containing approximately 0.15 wt. % CNTs and 99 wt. % solvent. The remaining mass is residual water and functionalized 1-pyrenemethylamine HCl The CNT paste is then diluted with 2-methyl-1,3-propanediol to prevent the CNTs from drying out as allowing the CNT material to fully dry during filtration or storage will result in the inability to redisperse.
The second step in the CNT fabrication process is the metal oxide functionalization. There are several methods for achieving this including hot pressing of composite powder, pressure-less sintering technique, direct in-situ growth, in situ CVD synthesis, high-intensity ultrasonic radiation, assembling pre-synthesized metal oxide nanoparticles as building blocks on CNTs, spontaneous formation of metal oxide nanoparticles on CNTs, thermal decomposition of metal oxides precursor directly onto the surface of carbon nanotube, hydrothermal crystallization, sol-gel followed by spark plasma sintering, surfactant wrapping sol-gel, chemical precipitation, and controlled heteroaggregation.
Regardless of the functionalization process or if the CNTs are purchased already functionalized, suitable CNTs include single-walled, double-walled, and/or multi-walled CNTs (SWCNTs, DWCNTs, and MWCNTs, respectively).
Preferably, the CNTs are pristine, that is, CNTs having little or no sidewall defects, existing functionalization (other than metal oxide functionalization as described herein, in embodiments where already-functionalized CNTs are purchased), or doping. Suitable CNTs have an onset temperature or initial decomposition temperature when measured by thermogravimetric analysis (TGA) or at least about 400° C. Although the number of walls affects the outer diameter of the CNTs, it is generally preferred that the CNTs used as described herein have an outer diameter of about 0.5 nm to about 20 nm, preferably about 0.6 nm to about 10 nm, and more preferably about 0.7 nm to about 5 nm.
Suitable metal oxides for use in metal-oxide-functionalized CNT layer 52 have a high affinity for As(III) and are excellent localizers for concentrating As(III) near the working electrode, thus improving reduction and oxidation during the stripping process, leading to higher current levels flowing from the working electrode to the counter electrode. Examples of suitable metal oxides for use herein include Fe3O4, FeO2, MnO, CoOx, SnO2, TiOx, IrO2, RuOx, and mixtures thereof In one embodiment, oxides of titanium (TiO1-2) are used to functionalize CNT layer 52. The amount of metal oxide utilized is adjusted to optimize the sensitivity of the final device. Too much metal will result in aggregation and loss of surface area/electrical signal, and too little metal will result in less adsorption/electrical signal. The ratio of CNTs to metal oxide is preferably from about 1:300 to about 2:1 by weight, more preferably from about 1:10 to about 1:1 by weight, and even more preferably about 1:2 by weight.
In one embodiment, the metal oxide can be provided as metal oxide nanoparticles. In that instance, the average particle size of the metal oxide nanoparticles will be about 10 nm to about 10 μm, more preferably about 10 nm to about 1 μm, even more preferably about 10 nm to 500 nm, as determined by scanning electron microscope
The use of the functionalized CNTs effectively increases the surface area of the working electrode 56. In this case, the electrochemical surface area (ESA) is preferably greater than the geometrical surface area (GSA). The ESA can be determined experimentally by using well-known electrochemical reactions with a known redox mediator electrolyte solution, such as ferrocene methanol. Using the Anson equation,
Q=nFACD
1/2π−1/2t1/2
where Q is the charge in coulombs, n is the number of electrons for oxidation or reduction of one molecule of redox mediator, F is Faraday's constant, A is the electrochemical surface area, C is the concentration of the redox mediator, D is the diffusion coefficient of the solution, typically in cm2/s, and t is time in seconds, the electrochemical surface area, A, can be determined.
The ratio of the ESA to GSA is defined as ρ, the roughness factor. Preferably, the roughness factor of the metal oxide-functionalized CNT layer is at least 1, more preferably at least 1.05, and even more preferably at least 1.1.
Finally, and referring to
Regardless of the preparation method, noble metals are preferred as the nanoparticles because of their high conductivities and chemical inertness. Preferred metal nanoparticles include those chosen from Au, Ag, Pd, Pt, Ru, Ir, and combinations thereof, with Au being particularly preferred.
Additionally, the metal nanoparticles 54 utilized preferably have an average particle size of about 10 nm to about 10 μm, more preferably about 10 nm to about 1 μm, even more preferably about 10 nm to 500 nm as determined by scanning electron microscope. In one preferred embodiment, the ESA of the working electrode 56 with metal nanoparticles 54 will be equal to or greater than the ESA of the working electrode prior to the addition of metal nanoparticles.
The above process forms the final sensor 58, as shown schematically in
Importantly, the sensor 58 formed herein is a transducer, which is different from a transistor or electronic switch. It will be appreciated that a transducer, in its simplest definition transforms a signal from one energy form to another energy form, while a transistor in its simplest definition controls the flow of electricity. The latter would include a source (input) and a drain (output), neither of which are present in a transducer.
Advantageously, the sensor 58 can be used for detection of various analytes (e.g., arsenic, and particularly As3+). In one embodiment, the sensor 58 can be used as part of the voltammetry system. In another embodiment, the sensor 58 can be used in other devices, and particularly in electrochemical sensor systems. Preferred such systems generally comprise precision microcontroller, a multiplexer array, temperature detector electronics, and a data acquisition system. Additionally, two or more of the sensors 58 can be used in the same system, depending on the user's needs.
In one embodiment, the sensor system comprises a sensing platform for a continuous water resource monitoring by electrochemical detection. Continuous monitoring can be provided for drinking water, fresh water, wastewater, and water produced by reverse osmosis. In one embodiment, the sensor system is placed in a flow path of water to be monitored, so that the water contacts the sensor 58. This device may be used as a standalone sensor in environments where the water parameters (pH temperature, ionic strength) are controlled, or in concert with compensation sensors where water parameters are not controlled. Compensation sensors may include electrical conductivity, temperature, pH, oxidation reduction potential, and/or mass flow. Advantageously, the sensing system is particularly advantageous in low ionic strength environments (<100 mM).
Voltammetry is one method for quantitative detection of analytes in water. In these systems, the potential is controlled, and current is measured at the working electrode and the counter electrode is the conductor that completes the circuit. The working electrode and counter electrode make up one of the half cells. The other half cell is the reference electrode, which has a constant electrochemical potential, allows no current to flow through it, and is used to measure the working electrode potential. Voltammetry may be implemented in many forms that are well-understood by those having skill in the art, including, but not limited to, linear sweep voltammetry, cyclic voltammetry, and pulse voltammetry techniques (including square wave voltammetry, normal pulse voltammetry, differential pulse voltammetry). The sensor described herein is especially suited for pulse voltammetry, and one especially preferred embodiment is square wave voltammetry.
Square wave voltammetry (SWV) is one of the fastest and most sensitive electrochemical technique for quantitative detection in comparison to the commonly used cyclic voltammetry any other voltametric techniques. Therefore, SWV is used for arsenite detection in water using a three-electrode system and two half-cell reactions. SWV is one of many pulse voltammetry electrochemical techniques. Other pulse voltammetry techniques such as differential pulse, may result in results similar to SWV. In these systems, the potential is controlled, current is measured at the working electrode 56, and the counter electrode 44 is the conductor that completes the circuit. The working electrode 56 and counter electrode 44 make up one of the half cells. The other half cell is the reference electrode 48, which has a constant electrochemical potential, allows no current to flow through it, and is used to measure the working electrode potential.
In order to perform SWV on these electrodes, a potentiostat or equivalent circuit shown in
The second step is the stripping process. In this process, the voltage on the working electrode 56 is increased slowly over increments, and preferably maintained substantially constant (i.e., +/−0.05 V) during each increment, to oxidize the As0 to As3+ off the working electrode 56, allowing ions to flow from the working electrode 56 to counter electrode 44 and generating current through the circuit. The As(III) oxidation peak is generated around 0.2 V. The current generated and measured from this step is the difference between the forward oxidation current and the reverse reduction current. In one cycle of square wave, forward current is measured when going from a negative to positive voltage. The reverse current is measured when going from positive to negative voltage. The difference (forward−reverse) is taken to increase signal and filter out any capacitive current that is generated from a double layer in the sensor 58. This current difference is then plotted on the y-axis against voltage on the x-axis in a line graph to generate a voltammogram with the As(III) oxidation peak around 0.2 V.
A resting step may be performed after each of the first step (the accumulation process) and the second step (the stripping process). This resting step is preferably at least about 1 nanosecond, more preferably about 1 nanosecond to about 1 second, even more preferably about 1 nanosecond to about 100 milliseconds.
There are several parameters in SWV that can be modified to produce better current signal and the most optimal voltammogram. First, the SWV electrochemical voltage window is preferably about −0.5 V to about 0.5 V vs an AgCl reference electrode. The voltage stepping increment is preferably about 0.001 V to about 0.05 V, more preferably about 0.005 V to about 0.025 V, and more preferably about 0.008 V. The frequency of the square wave is preferably about 1 Hz to about 50 Hz, more preferably about 10 Hz to about 40 HS, and more preferably about 25 Hz. Lower frequency allows full transport of the ions and maximum current generation.
Still referring to
The calibration curve plays an important role in the determination of sensitivity, linear range, and limit of detection (LOD). The calibration test is performed measuring known arsenic concentrations of 0 ppb on the blank cycle up to a predetermined level, such as 100 ppb, after a series of doses. The more doses that are performed, and the smaller the increments, the more data points that will be collected, and the more precise the calibration curve. The voltammograms produced are evaluated for their peak height (Ip) in μA and plotted against As(III) concentration in ppb to generate the calibration curve. An example of a calibration curve is shown in
The linear range can be fit using any suitable technique, such as using a Microsoft Excel software fitting technique to produce the sensitivity or the slope of the line, linear range, and LOD. For example, in one representative embodiment using titanium-oxide-modified CNTs with gold nanoparticles as the working electrode material, the sensitivity was 7e-7 A/ppb, with a linear range from 6.2 ppb to 94 ppb for As(III), and an LOD of 6.2 ppb for As(III).
The calibration curve can then be used to identify the As(III) concentration in an unknown solution. First, the SWV voltammogram is generated using a calibrated sensor 58. Then, the height of the As(III) oxidation peak is measured and compared to the calibration curve. The point along the calibration curve with the same y-value of the peak height observed in the unknown solution is located, and the x-value of that point is the As(III) concentration of the unknown solution.
It will be appreciated that the composite comprising metal-oxide-functionalized CNTs 52 and metal nanoparticles 54 shows excellent catalytic activity for arsenite detection in water with high sensitivity, low limit of detection (LOD), and wide linear range, as described above. This composite can electrochemically reduce As3+ to As0 due to increased adsorption capability. Taking advantage of the low surface potential and work function, the metal nanoparticles 54 can facilitate the adsorption of As3+ on the sensing platform 46 of the working electrode 56 for further electrochemical reduction process.
Additional advantages of the various embodiments will be apparent to those skilled in the art upon review of the disclosure herein and the working examples below. It will be appreciated that the various embodiments described herein are not necessarily mutually exclusive unless otherwise indicated herein. For example, a feature described or depicted in one embodiment may also be included in other embodiments but is not necessarily included. Thus, the present disclosure encompasses a variety of combinations and/or integrations of the specific embodiments described herein.
As used herein, the phrase “and/or,” when used in a list of two or more items, means that any one of the listed items can be employed by itself or any combination of two or more of the listed items can be employed. For example, if a composition is described as containing or excluding components A, B, and/or C, the composition can contain or exclude A alone; B alone; C alone; A and B in combination; A and C in combination; B and C in combination; or A, B, and C in combination.
The following examples set forth methods in accordance with the disclosure. It is to be understood, however, that these examples are provided by way of illustration, and nothing therein should be taken as a limitation upon the overall scope.
A device was fabricated by using a sputter deposition system (Model SC450, Semicore, CA) to sputter a gold current collector onto a ZEONEX° ZF14-188 substrate (Zeon Europe GmbH, Germany). Deposition was carried out at a rate of 1.0 Å/s for 4 minutes and 20 seconds using a 150 μm molybdenum shadow mask for patterning to achieve a thickness of 100 nm. The patterned substrate was then plasma treated using an AST Products Inc. PS-350 plasma etcher (0.1 Torr chamber pressure, 50 sccm O2 flowrate, 50 W RF power, and 30 seconds RF time). A conductive carbon material, DuPont BQ242 (DuPont, Circleville, Ohio), was screen printed over the gold current collector using a stainless steel screen (mesh 230 cal with 0.0011″ wire diameter), on an ATMA OE 67 screen printer, fitted with a 70 durometer polyurethane squeegee. The squeegee speed was set to 250 mm/s, and off contact was set to 1.0 mm. Cure was done in a HIX Corporation NP-2410 IR cure oven with a belt speed of 28 inches per minute and temperature of 130° C. The reference electrode material, Sun Chemical-Gwent C2130809D5 (60:40 Ag:AgCl) (Gwent Electric Material Ltd, UK), was screen printed over the gold current collector to form the reference electrode. This screen printing was carried out using a stainless steel screen (mesh 230 cal with 0.0011″ wire diameter), on an ATMA OE 67 screen printer, fitted with a 70 durometer polyurethane squeegee. The squeegee speed was set to 250 mm/s, and off contact was set to 1 mm. Cure was conducted in a HIX Corporation NP-2410 IR cure oven with a belt speed of 28 inches per minute and temperature of 130° C. To define the working electrode area, the material sold under the name DuPont 5018A (DuPont, Circleville, Ohio) was screen printed over the gold current collector using a stainless steel screen (mesh 230 cal with 0.0011″ wire diameter), on an ATMA OE 67 screen printer, fitted with a 70 durometer polyurethane squeegee. The squeegee speed was set to 250 mm/s, and off contact was set to 1.0 mm. Cure was carried in a Heraeus DRS 10/12 UV belt oven with two passes at a belt speed of 4.0 feet per minute.
a. Preparation of CNT Dispersion
A 1-liter reactor was loaded with 1.029 grams of Thin-Walled Carbon Nanotubes (Cheaptubes, SKU: 010109) tubes and 1.800 grams of 1-pyrenemethylamine HCl (Sigma Aldrich, St. Louis, Mo.), and the two were mixed thoroughly. A 1-kg bottle of chlorosulfonic acid (Sigma Aldrich, St. Louis, Mo.) was added to the reactor, and the lid was clamped on. The reactor was stoppered and equipped with overhead stirring. The stirring was set at 400 rpm and maintained for 3 days. A 4-liter jacketed quench vessel was equipped with an overhead stirrer and a recirculating chiller set to 5° C., with 1.5 liters of DI water being placed in the reactor. When the DI water reached 5° C., vacuum was used to slowly draw over the chlorosulfonic acid mixture. The temperature was kept between 10° C. and 20° C. by adjusting a release valve on the vacuum line to slow or speed the transfer rate. The temperature was set to 15° C., and a peristaltic pump was used to deliver 1.75 liters of 28-30% ammonium hydroxide (VWR, J. T. Baker®, Batavia, Ill.) at 4.9 mL/min. The resulting mixture was then filtered through an Advantec 3.0 PTFE filter (King Filtration Technologies, St. Louis, Mo.). The vacuum timer was set for 8 hours. The wet black solid was removed from the filter and mixed with a solution of 200 mL of 28-30% ammonium hydroxide in 1,800 mL of DI water. The filtration and addition of ammonium hydroxide were then repeated. The resulting solid was again filtered through an Advantec 3.0 μM, PTFE filter, and the black solid was then dispersed in 600 grams of 2-methyl-1,3-propanediol (Sigma Aldrich, St. Louis, Mo.). The final oxidized CNT paste contained 0.167 wt. % CNTs and 99% wt. % solvent, with the remainder being residual water and functionalized 1-pyrenemethylamine HCl. Next, 2.645 grams of this material were dispersed into 250 mL of DI water by sonication. The absorbance at 550 nm was measured. Multiplying the resulting number by the dilution factor gave an OD of 67.06.
b. Functionalizing CNTs with TiOx and Forming Ink
The dispersion in 2-methyl-1,3-propanediol was then diluted to an OD of 30 with 2-methyl 1,3-propanediol using a planetary mixer set at 1,350 rpm revolutions and 1,350 rpm rotation. Next, 200 grams of the OD=30 material and 50 grams of 2-methyl-1,3-propanediol were added to a 1-liter reactor equipped with overhead stirring and flushed with nitrogen. The stir rate was set to 450 rpm, and 100 grams of 2-methyl-1,3-propanediol and 3.62 mL of a 50% solution of titanium(IV) bis(ammonium lacto)dihydroxide in water (Sigma Aldrich, PN: 388165) were added to a 250-mL Schlenk flask connected to nitrogen. The contents of the flask were stirred with a magnetic stir bar and flushed for 5 minutes. Using an air-tight syringe, 50 mL of the solution were withdrawn from the flask, placed in a syringe pump, and added to the stirred reaction (in the 1-L reactor containing the OD=30 material) at 120 mL/hr. When solution addition was finished, the 1-L reactor was fitted with a reflux condenser and heated to 115° C. for 180 minutes. The reactor contents were then collected in a 300-gram planetary mixer jar.
An automated, programmable coating system (sold under the name ExactaCoat, Sono-Tek Corporation, Milton, N.Y.), was used to spray coat the TiOx/CNT ink from Example 2b onto the device from Example 1. While preheating the coating system tray to 125° C., the TiOx/CNT (further diluted to 0D=2 with 2-methyl 1,3-propanediol) dispersion was probe sonicated for 30 minutes after which the CNT dispersion was loaded into a 50-mL syringe and secured to the coating system's syringe pump, whose rate was set to 500 μL/min. The preheated tray was taken out, and a wafer was placed in the middle of the tray. The wafer was covered with a metal stencil cutout, so that only the working electrodes were visible, with magnets used to hold the stencil in place. The tray was placed back into the coating system and allowed to heat for 5 minutes. The spray coating parameters were set up by opening the PathMaster software and setting the syringe pump rate to 500 μL/min and the shaping air pressure to 0.6 kPa. The arm position/speed parameters were programmed, using the area command with 3 different sets of X, Y, and Z coordinates. These coordinates were set manually by moving the arm and teaching the coordinates for the bottom, top, and right side of the wafer. Z was constant at 57.0150 mm. The resulting XYZ coordinates were 48.5550, 38.600, 57.0150 for the bottom left corner of the wafer, 234.1150, 38.3600, 57.0150 for the top left corner, and 234.1150, 202.9100, 57.0150 for the top right corner. The Path Speed was set to 90 mm/s, and the Area Spacing set to 2. Once these parameters were set up, spray coating was initialized, and the working electrodes were coated with the ink, forming a TiOx/CNT composite layer on the working electrodes
A stock solution of 0.1M HAuCl4 and 0.1M K2SO4 was prepared by adding 33.979 grams of HAuCl4, 17.43 grams of K2SO4, and 200 mL of DI water to a 1-L volumetric flask. After the salts were totally dissolved, the flask was filled to the graduation marking of the volumetric flask with the DI water. After thoroughly stirring, the stock solution was ready to use.
For electrodeposition of Au nanoparticles, about 18 mL of the stock solution was transferred into a 20-mL PTFE vial, and the TiOx/CNT-coated device was properly connected with working electrode and counter electrode and placed into the solution. A homemade Ag/AgCl reference electrode made from a glass pipette, silver wire, and supersaturated KCl solution in agarose gel served as the reference electrode. The chronoamperometry was performed by a CHI660E potentiostat along with a CHI684 multiplexer (both from CH Instructions, Inc.).
A schematic illustration of this setup is shown in
Scanning electron microscope images were taken of the working electrode before voltage application commenced for comparison purposes.
A dispersion prepared as described in Example 2a was diluted to an OD of 30 with 2-methyl 1,3-propanediol using a planetary mixer set at revolution: 1,000 rpm, rotation: 300 rpm, time: 60 seconds, wave: on, vacuum: on. Next, 200 grams of the OD=30 material and 25 grams of 2-methyl-1,3-propanediol were added to a 1-liter reactor with an overhead mixer and reactor lid secured on the reactor. The reactor was lowered into an oil bath and stirred at 450 rpm. A ¼″ PFA tubing was attached to nitrogen through a 24/40 adapter, and the reaction mixture was flushed with nitrogen.
Next, 100 grams of 2-methyl-1,3-propanediol were added to a 250-mL Schlenk flask. A stir bar was added to this flask, and it was connected to the nitrogen line, with the nitrogen flow rate being set to 1 CFM. The nitrogen valve to the reactor was then closed and stoppered. The stir rate was set to 450 rpm, and Schlenk flask contents were stirred for 5 minutes to allow the flask to clear out humid air. After 5 minutes of stirring, 3.616 mL of a 50% solution of titanium(IV) bis(ammonium lactate)dihydroxide in water (Sigma Aldrich, PN: 388165) were added to the Schlenk flask. A piece of ¾″ PFA tubing was then attached to a 50-mL airtight syringe, and that syringe was used to remove 50 mL of the titanium mixture from the Schlenk flask. A Universal 24/40 to hose inlet with locking ring (Chemglass, CG-1047-05) was placed on the reactor. The syringe was placed in a syringe pump having a tube through the adapter, and the mixture was added to the 1-L reactor containing the OD=30 material at a pump rate of 120 mL/hr. When the addition was complete, the adapter was replaced with a condenser open to air. The temperature of the oil bath was set to 115° C., and the reaction was allowed to stir at 180 rpm for 180 minutes. After the reactor cooled back to room temperature, the condenser was removed, and 0.35 grams of gold(III) chloride hydrate (Sigma Aldrich, St. Louis, Mo.) were added to the reactor while it was stirring. Next, a solution was prepared by mixing 0.25 gram of tetrabutylammonium cyanoborohydride (Sigma Aldrich, St. Louis, Mo.) with 25 mL of 2-methyl-1,3-propanediol with a magnetic stirrer until the tetrabutylammonium cyanoborohydride was dissolved. The resulting solution was placed in a 25-mL syringe equipped with ¼″ PFA tubing and a Universal 24/40 to hose inlet with locking ring (Chemglass, CG-1047-05) and added to the reaction mixture in the 1-L reactor at a rate of 50 mL/hr through the 1/4″ tubing while stirring at 380 rpm. Stirring was continued overnight at 180 rpm and under nitrogen, after which the material was collected, and a UV-Vis spectrum was taken, which showed a titanium oxide peak. The reaction mixture was placed in a glass 1-liter wide-mouth bottle, which was filled with acetone (Sigma-Aldrich Inc., St. Louis, Mo.). This was processed using a high sheer mixer for 1 minute at 10,000 rpm and filtered using a 3.0-μm Advantec PTFE filter, not allowing the vessel to go completely dry. This resulting solid was again washed with 1 liter acetone, followed by 1 liter of 2-propanol, followed by 1 liter of water.
To evaluate the calibration curve of the TiOx/CNTs with Au-electrodeposited nanoparticles, a base solution of 100 mM phosphate buffer with pH 7 was prepared. This was done by adding 15.487 grams of K2HPO4·7H2O (Sigma-Aldrich Inc., St. Louis, Mo.) and 5.827 grams of K2HPO4·H2O (Sigma-Aldrich Inc., St. Louis, Mo.) into 800 mL of DI water. The solution was adjusted to pH 7 through titration using a 0.1M NaOH solution (Sigma-Aldrich Inc., St. Louis, Mo.) and then topped off to 1,000 mL with DI water. A stock solution of 0.02 mM NaAsO2 was prepared by first adding 2.5 mL of 0.05M NaAsO2 (Sigma-Aldrich, St. Louis, Mo.) solution using a Thermo Scientific Finnpipette into a 1.0-L volumetric flask and filled with phosphate buffer solution. This 0.02 mM NaAsO2 and 0.1M phosphate buffer pH 7 solution was used for dosing in the calibration test.
The calibration test was performed by dosing a pH 7, 100 mM phosphate buffer solution with small increments of 0.02mM NaAsO2 and 0.1M phosphate buffer solution via a pipette to give arsenic concentrations of 0 ppb on the blank cycle and up to 94 ppb after 16 doses. Five minutes were allowed between doses to stir and allow the solution in the vial to homogenize. The SWV was performed using a CHI660E potentiostat and parameters used were initial voltage: −0.5 V vs. 3M Ag/AgCl, final voltage: 0.5 V vs. 3M Ag/AgCl, step increment: 0.008 V, amplitude: 0.025 V, accumulation time: 300 s, frequency: 25 Hz, and sensitivity for current measurement: 1e-5. The voltammograms of every cycle were plotted together and are shown in
The calibration curves were obtained by plotting the arsenite oxidation peak height (Ip) or peak area (Ap) respectively, as shown in
To evaluate the long-term stability of the Au-functionalized TiOx/CNT composite towards arsenite detection in water, square wave voltammetry was performed using a sensor having Au-functionalized TiOx/CNTs on the working electrode in 100 mM phosphate buffer pH 7 with 50 ppb arsenite for 16 cycles with one SWV measured every 1.5 hours. The solution was stirred with a stir bar (10 mm length, 3 mm diameter) at 450 rpm. The SWV parameters were held constant as follows: initial voltage: −0.5 V vs. Ag/AgCl, final voltage: 0.5 V vs. Ag/AgCl, step increment: 0.008 V, amplitude: 0.025 V, accumulation time: 300 seconds, frequency: 25 Hz, and sensitivity for current measurement: 1e-5. All 20 SWVs were plotted together as shown in
In this Example, 1 mM ferrocene methanol in 100 mM KCl was used as the solution. Chronocoulometry was used with 0 mV and 500 mV vs. homemade Ag/AgCl (Sat. KCl) reference electrodes using 2-s pulse widths. The diffusion coefficient of the redox mediator solution was calculated using cyclic voltammetry and the Randles-Ševčík equation.
An example of an experimental Anson plot is shown in
The present application claims the priority benefit of U.S. Provisional Patent Application Ser. No. 63/217,339, filed Jul. 1, 2021, entitled PRINTED ELECTRONIC NANO-CARBON BASED DEVICES AND SYSTEMS TO IMPROVE REAL-TIME SURFACE WATER CONTAMINATION SENSING, and U.S. Provisional Patent Application Ser. No. 63/281,783, filed Nov. 22, 2021, entitled ARSENIC DETECTOR AND METHOD OF USE, each of which is incorporated by reference in their entireties.
This invention was made with Government support under W912HZ-18-2-0003 Modification P00001 entitled “PRINTED ELECTRONIC NANO CARBON-BASED DEVICES AND SYSTEMS TO IMPROVE REAL-TIME SURFACE WATER CONTAMINATION SENSING,” subaward 18004-001, and under W912HZ-21-2-0019 entitled “QUANTITATIVE WATER SENSING ARRAY FOR RAPID SENSING AND CONTINUOUS MONITORING,” subaward 20206-001, both awarded by the Department of the Army ERDC. The United States Government has certain rights in the invention.
Number | Date | Country | |
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63281783 | Nov 2021 | US | |
63217339 | Jul 2021 | US |