ELECTROCHEMICAL CELL CONTAINING NANOSTRUCTURED MATERIAL-BASED WORKING ELECTRODE
20190331629 ยท 2019-10-31
Assignee
Inventors
Cpc classification
C01B32/05
CHEMISTRY; METALLURGY
G01N27/4168
PHYSICS
International classification
C01B32/05
CHEMISTRY; METALLURGY
G01N27/413
PHYSICS
Abstract
An electrode that comprises a nanostructured material that comprises pyrolyzed date palm leaves that are obtained from a pyrolysis of an agro-waste containing date palm leaves in an inert gas and in a temperature range of 800 to 1600 C., an electrochemical cell thereof, and a method of determining a hydroquinone concentration in a hydroquinone-containing solution with the electrochemical cell. Various combinations of embodiments are also provided.
Claims
1-9.
10. An electrochemical cell, comprising: a working electrode comprising a nanostructured material comprising pyrolyzed date palm leaves, wherein the nanostructured material has a thickness in the range of 10 to 1,000 m and wherein the pyrolyzed date palm leaves are obtained from a pyrolysis of an agro-waste comprising date palm leaves in an inert gas and in a temperature range of 800 to 1600 C.; a conductive metallic substrate; and an insulating material; wherein the nanostructured material is disposed on the conductive metallic substrate; wherein the insulating material at least partially covers the nanostructured material disposed on the conductive metallic substrate; a reference electrode; and a counter electrode, wherein the reference electrode and the counter electrode are in ionic communication with the working electrode via an electrolyte.
11. The electrochemical cell of claim 10, wherein the electrolyte comprises hydroquinone.
12. The electrochemical cell of claim 10, wherein the reference electrode comprises silver-silver chloride.
13. The electrochemical cell of claim 10, wherein the counter electrode comprises platinum.
14. A method of determining a hydroquinone concentration in a hydroquinone-containing solution with the electrochemical cell of claim 10, comprising: contacting the hydroquinone-containing solution with the working electrode, the counter electrode, and the reference electrode of the electrochemical cell; applying a voltage to the working electrode relative to the reference electrode to oxidize at least a portion of hydroquinone in the hydroquinone-containing solution thereby generating an electric current in the electrochemical cell; and determining the hydroquinone concentration in the hydroquinone-containing solution based on the electric current.
15. The method of claim 14, wherein a detection limit of the electrochemical cell is in the range of 1.0 to 10.0 M of hydroquinone.
16. The method of claim 14, wherein the hydroquinone concentration in the hydroquinone-containing solution is in the range of 1.0 M to 1.0 M.
17. The method of claim 14, wherein the hydroquinone concentration is determined at a temperature in the range of 10 to 40 C.
18. The method of claim 14, wherein the hydroquinone-containing solution comprises hydroquinone and at least one of a halide, a sulfate, a nitrate, a phosphate, an acetate of an alkali metal, and nitrophenol, and wherein a hydroquinone selectivity of the electrochemical cell is at least 95% by mole.
19. The method of claim 14, wherein the voltage is in the range of 0.05 to 0.5 volts relative to the reference electrode.
20. The method of claim 14, wherein the hydroquinone concentration is determined from a calibration curve that linearly relates the electric current to the hydroquinone concentration.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0032] A more complete appreciation of the disclosure and many of the attendant advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:
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DETAILED DESCRIPTION OF THE EMBODIMENTS
[0061] Referring now to the drawings, wherein like reference numerals designate identical or corresponding parts throughout the several views.
[0062] According to a first aspect, the present disclosure relates to an electrode 100 comprising a nanostructured material 102. The term nanostructured material as used in this disclosure relates to a carbonaceous (carbon-containing) material that includes carbon walls that are arranged in a stacked configuration (as shown in
[0063] In some preferred embodiments, the nanostructured material contains pores with an average pore size in the range of 1 to 10 nm, preferably 1.5 to 5.0 nm, preferably 1.8 to 4.0 nm, preferably 2.0 to 2.5 nm; a specific pore volume in the range from about 0.1 to about 1.0 cm.sup.3/g, preferably from about 0.3 to about 0.9 cm.sup.3/g, preferably from about 0.5 to about 0.8 cm.sup.3/g; and a BET surface area in the range from about 150 to about 300 m.sup.2/g, preferably from about 160 to about 280 m.sup.2/g, preferably from about 180 to about 250 m.sup.2/g, preferably from about 190 to about 220 m.sup.2/g.
[0064] In a preferred embodiment, the nanostructured material 102 has a thickness in the range of 10 to 1,000 m, preferably 50 to 800 m, preferably 100 to 600 m, preferably 150 to 500 m, preferably 180 to 400 m, preferably about 200 m, as shown in
[0065] The pores present in the nanostructured material 102 may be three-dimensionally interconnected via the carbon walls (as shown in
[0066] The nanostructured material 102 may be utilized in various applications due to light weight, mechanical stability, and relatively high electrical and thermal conductivities. Accordingly, the nanostructured material 102 may be utilized as an electrode in fuel cells, photovoltaic cells, electrochemical cell, and solar cells; as a drug carrier for drug-delivery applications, as an adsorbing material, as a catalyst carrier, as a heat-insulating material, as a buffer material, as a filter, as a tool in ceramic sintering, etc.
[0067] The nanostructured material 102 of this disclosure is obtained from a pyrolysis of an agro-waste containing date palm leaves in an inert gas, e.g. nitrogen, helium, neon, and/or argon, and in a temperature range of 800 to 1600 C., preferably 900 to 1,550 C., preferably 1,000 to 1,500 C., preferably 1,100 to 1,450 C., preferably 1,200 to 1,400 C. In a preferred embodiment, the nanostructured material 102 is obtained from a pyrolysis of an agro-waste containing date palm leaves in the presence of nitrogen gas and in a temperature in the range of 1,300 to 1,600 C., preferably about 1,500 C. In another embodiment, the nanostructured material 102 is obtained from a pyrolysis of an agro-waste containing date palm leaves in the presence of nitrogen gas and in a temperature in the range of 800 to 1,000 C., preferably about 850 C.
[0068] The term inert gas as used herein refers to a gaseous mixture that does not chemically react with the agro-waste during the pyrolysis. In a preferred embodiment, the inert gas is at least one selected from the group consisting of nitrogen, helium, neon, and argon. However, the inert gas is not limited to nitrogen, helium, neon, and/or argon; and other gaseous mixtures that do not react with the agro-waste during the pyrolysis may also be utilized.
[0069] The term agro-waste as used in this disclosure relates to any leftover or waste materials obtained from an agricultural product or process. Examples of agro-waste may include, but are not limited to residual plant materials such as husks, shells, stems, roots, leaves, leaflets, or cores. For example, in some embodiments, the agro-waste includes palm leaves (e.g. date palm leaves), soybean hulls, cellulosic fibers, cellulose, grass, coconut shells, rice husks, corn stalks, wheat straw, wood chips, and wood pulp that remains after wood processes (e.g., sawmills or lumber yards). Preferably, the agro-waste contains date palm wastes, e.g. trunks, pits, roots, stems, leaves, and/or leaflets of date palm trees. However, in a preferred embodiment, the agro-waste consists of date palm leaflets. According to this embedment, less than 1.0 vol %, preferably less than 0.5 vol %, preferably less than 0.1 vol % of the agro-waste that is utilized to form the nanostructured material contains trunks, pits, roots, and/or stems of date palm trees.
[0070] The nanostructured material 102 may have various compositions depending on the type of the agro-waste that is pyrolyzed. In some embodiments, the date palm leaves (or preferably date palm leaflets) comprises cellulose, hemicellulose, and lignin, wherein the amount of cellulose is at least 50 wt %, preferably in the range of 50 wt % to 70 wt %, preferably 55 wt % to 65 wt %, relative to the total weight of the date palm leaves. In addition, the date palm leaves (or preferably date palm leaflets) includes minerals such as iron, magnesium, silicon, potassium, and calcium. The composition of the date palm leaves may be different than the composition of other agro-waste, e.g. date palm trunk, date palm fronds, rice husk, etc. wherein the amount of cellulose is no more than 40 wt %, preferably no more than 30 wt %. In addition, the amount of minerals such as iron, magnesium, silicon, potassium, and calcium in these agro-wastes is at least 20%, preferably at least 40%, preferably at least 60% lower than that of the date palm leaves. According to the compositional difference, the nanostructured material, which is obtained from the pyrolysis of date palm leaves, may have a different composition than the composition of a material which is obtained from the pyrolysis of an agro-waste other than date palm leaves. For example, in one embodiment, the nanostructured material, which is obtained from date palm leaves (or preferably date palm leaflets) includes at least 90 wt %, preferably at least 95 wt % carbon as well as at least at least 5 wt %, preferably about 8 wt % to about 10 wt % (relative to the total weight of the nanostructured material) of a mineral selected from the group consisting of oxygen, nitrogen, iron, silicon, potassium, manganese, magnesium, and calcium; whereas a material that is obtained from the pyrolysis of date palm trunks, includes at least 95 wt %, or preferably at least 98 wt % carbon as well as about 2 wt %, preferably about 3 wt % to about 5 wt % of a mineral selected from the group consisting of oxygen, nitrogen, iron, silicon, and calcium. Said compositional differences may affect electrical properties, e.g. electrical conductivity, particular when the nanostructured material is used in an electrochemical cell.
[0071] The term pyrolysis as used in this disclosure refers to a process of thermochemical decomposition of an agro-waste at elevated temperatures and in the absence of an oxidizing agent such as oxygen, hydrogen peroxide, and/or a halogen-containing gas, e.g. a chlorine-containing gas. The agro-waste may have a polymeric structure consisting of carbohydrates (cellulose and hemicellulose) and lignin with small amounts of extraneous organic chemicals and minerals. The pyrolysis of the agro-waste may form a solid, for example in a form of ash, that mainly contains carbon atoms, heteroatoms (e.g. nitrogen, oxygen, and hydrogen), and minerals. The pyrolysis of the agro-waste may also form char, tar, and volatile compounds, which may evaporate during the pyrolysis thus leaving behind the nanostructured material 102.
[0072] In some embodiments, the agro-waste is pyrolyzed according to the following procedure. First, the agro-waste is placed in a ceramic crucible 110, e.g. an alumina crucible, and is heated to a temperature of 100 to 120 C., preferably about 105 C., for at least 24 hours, preferably at least 36 hours, but no more than 48 hours, to remove water from the agro-waste. Then, the agro-waste is heated with a heating rate in the range of 5 to 20 C./min, preferably 8 to 15 C./min, preferably about 10 C./min to an elevated temperature in the range of 800 to 1600 C., preferably 900 to 1,550 C., preferably 1,000 to 1,500 C., preferably 1,100 to 1,450 C., preferably 1,200 to 1,400 C., in an inert gas, preferably nitrogen. The agro-waste is isothermally heated at the elevated temperature for at least 2 hours, preferably at least 4 hours, but no more than 12 hours. All heating steps may be performed in a furnace 108 having a temperature control system, which may provide a heating rate of up to 50 C./min, or preferably up to 40 C./min, or preferably up to 30 C./min. The furnace 108 may also be equipped with a cooling accessory, which may provide a cooling rate of up to 20 C./min, or preferably up to 15 C./min, or preferably up to 10 C./min. Accordingly, the furnace 108 may be cooled with a cooling air stream, a liquid nitrogen stream, or a combination thereof.
[0073] In one embodiment, the agro-waste is heated in a multi-step heating protocol, e.g. a two-step heating protocol, wherein the agro-waste is heated to a first elevated temperature in a range of 400 to 600 C., preferably 450 to 550 C., with a first heating rate in the range of 5 to 20 C./min, preferably about 10 C./min. The agro-waste may be isothermally heated at the first elevated temperature for at least 1 hour, but no more than 4 hours. Then, the agro-waste is heated to a second elevated temperature in a range of 800 to 1,600 C., preferably 1,200 to 1,400 C., with a second heating rate in the range of 1 to 6 C./min, preferably 2 to 5 C./min. The agro-waste may be isothermally heated at the second elevated temperature for at least 2 hours, preferably at least 4 hours, but no more than 12 hours. After that, the agro-waste is cooled to room temperature (i.e. a temperature in the range of 20 to 30 C., preferably about 25 C.) with a cooling rate in the range of 2 to 10 C./min, preferably about 5 C./min. The multi-step heating protocol, i.e. the first and the second heating rates, the first and the second elevated temperatures, the cooling rate, etc., may determine the carbon wall thickness and also the number of carbon walls in each stack as well as the average pore size and the BET surface area of the nanostructured material 102 and the carbon walls. For example, the multi-step heating protocol, as described, may form a nanostructured material with an average pore size in the range of 1 to 10 nm, preferably 1.5 to 5.0 nm, preferably 1.8 to 4.0 nm, preferably 2.0 to 2.5 nm; and a BET surface area in the range from about 150 to about 300 m.sup.2/g, preferably from about 160 to about 280 m.sup.2/g, preferably from about 180 to about 250 m.sup.2/g, preferably from about 190 to about 220 m.sup.2/g. In addition, said multi-step heating protocol may form stacks of carbon walls, wherein each stack contains at least 5 carbon walls, preferably at least 8 carbon walls, preferably at least 10 carbon walls, preferably 15 to 25 carbon walls. The multi-step heating protocol may form carbon walls with a thickness ranging from about 1.0 to about 50 m, preferably from about 2.0 to about 40 m, preferably from about 5.0 to about 30 m, preferably from about 10 to about 25 m, and channels between the carbon walls, wherein the width of the channels may range from about 10 to about 500 m, preferably from about 20 to about 200 m, preferably from about 40 to about 100 m, and a depth of the channels may range from about 10 m to about 1,000 m, preferably from about 20 to about 800 m, preferably from about 50 to about 500 m, preferably from about 100 to about 400 m.
[0074] The term electrode as used in this disclosure relates to an electrical conductive material that brings into contact with a non-metallic element, e.g. an electrolyte, of a circuit, e.g. an electrochemical cell. Preferably, the term electrode in this disclosure refers to a working electrode of an electrochemical cell.
[0075] In some preferred embodiments, the agro-waste consists of date palm leaves having date palm leaflets. The date palm leaflets may preferably be separated from the date palm leaves and are cut into pieces having different sizes and shapes. For example, the date palm leaflets may cut into rounded pieces, circular pieces, elliptical pieces, and rectangular pieces, etc. Preferably, the date palm leaflets are cut into rectangular pieces (as shown in
[0076] In a preferred embodiment, the nanostructured material 102 preserves its shape and stability at standard temperatures and pressures (i.e. a temperature in the range of 20 to 30 C., preferably 22 to 28 C., preferably about 25 C., and a pressure in the range of 0.8 to 1.2 atm, preferably 0.9 to 1.1 atm, and preferably about 1.0 atm). In view of that, the nanostructured material 102 may not be disposed on a substrate in applications that involves standard temperatures and pressures. For example, in one embodiment, the nanostructured material is utilized in an electrochemical cell that operates at standard temperatures and pressures, wherein the nanostructured material is not disposed on a substrate or a substrate electrode. The term substrate as used herein refers to a rigid material that provides stability to a material that is disposed thereon. Alternatively, the term substrate as used herein may refer to a carrier that carries a material that is disposed (or deposited) thereon. Accordingly, the nanostructured material is preferably not disposed (or secured) on a substrate such as glassy carbon, silicon wafer, glass, quartz, glass wafer, etc. However, the term substrate as used herein does not refer to a conductive material that is electrically in contact with the nanostructured material, wherein the conductive material is utilized as a junction to electrically connect the nanostructured material to a power source. In view of that, in one embodiment, the nanostructured material 102 is utilized in an electrochemical cell as an electrode, wherein the nanostructured material 102 is disposed on a conductive material 104 with an adhesive (not shown in
[0077] In a preferred embodiment, the cost of manufacturing the electrode 100 is substantially lower than the cost of manufacturing an electrode that includes carbon nanoparticles, e.g. carbon nanotubes, graphene sheets, fullerene, glassy carbon nano/microspheres, etc. deposited onto a conductive substrate, e.g. gold, platinum, palladium, glassy carbon, etc. Accordingly, the cost of manufacturing the electrode 100 may be at least two times, preferably at least three times, preferably at least five times lower than the cost of manufacturing an electrode that includes carbon nanoparticles deposited onto a conductive substrate.
[0078] Referring now to
[0079] The electrochemical cell 200 provided in this disclosure may be utilized as an indicative tool to detect and/or determine a concentration of organic molecules such as hydroquinone and ferrocyanide, as well as bis-phenolic compounds such as bisphenol-A, bisphenol-F, bisphenol-S, bisphenol-C, bisphenol-E, bisphenol-P, bisphenol-Z, etc. In a preferred embodiment, the electrochemical cell 200 is utilized to detect and/or determine a concentration of hydroquinone in a solution. The electrochemical cell 200 provided herein may also be used to detect environmental pollutants or organic pesticides such as organophosphate.
[0080] The term working electrode as used in the second aspect refers to the term electrode as described in the first aspect. The term working electrode refers to the electrode when describing the specification of the electrochemical cell. Other than that, the term electrode and the term working electrode are identical and may be used interchangeably in this disclosure.
[0081] In some embodiments, the working electrode 100 includes the nanostructured material, which is obtained from the pyrolysis of the agro-waste. The working electrode 100 may further include the conductive material that is adhered to the nanostructured material from one side preferably with the adhesive. The conductive material may cover at least 10%, preferably at least 20%, preferably at least 30%, preferably at least 40%, preferably at least 50%, preferably at least 60%, preferably at least 70%, preferably at least 80%, preferably at least 90%, preferably at least 95%, preferably at least 99% of the surface area of one side of the nanostructured material. The conductive material may have a thickness in the range of 0.1 to 5 mm, preferably 0.5 to 3 mm, preferably 1 to 2 mm, whereas the adhesive may have a thickness of no more than 0.5 mm, preferably no more than 0.4 mm, preferably 0.1 to 0.3 mm. The working electrode 100 may or may not include the conductive material and/or the adhesive. The conductive material may only be used to electrically connect the nanostructured material to a power source, and is preferably not meant to take part in oxidizing the electrolyte. Accordingly, a volume ratio of the nanostructured material to the conductive material, when present, may be in the range of 1:1 to 1:20, preferably 1:1.5 to 1:15, preferably 1:2 to 1:12, preferably 1:2.5 to 1:10, preferably 1:3 to 1:8.
[0082] An electrical conductivity of the working electrode 100 may be within the range of 10.sup.3 to 3.010.sup.3 s/m, preferably 1.210.sup.3 to 2.510.sup.3 s/m, preferably 1.510.sup.3 to 2.010.sup.3 s/m, at a temperature in the range of 20 to 30 C., preferably 22 to 28 C., preferably about 25 C.
[0083] In some embodiments, the working electrode 100 may further include an insulating material 106 which covers at least a portion of the nanostructured material (as shown in
[0084] In some embodiments, the nanostructured material 102 is coated with metallic nanoparticles before being used as the working electrode in the electrochemical cell. Preferably, the nanostructured material 102 is coated with metallic nanoparticles via deposition methods known to those skilled in the art, such as, e.g., sputtering, ion bombardment, etc. Preferably both sides of the nanostructured material are coated, although in some embodiments, only one side of the nanostructured material may be coated. Accordingly, in some embodiments, at least 10%, preferably at least 20%, preferably 50% to 100%, preferably 60% to 99.9%, preferably 80% to 99.5% of the surface area of the nanostructured material is coated with the metallic nanoparticles. The nanostructured material may be acid treated before being coated with the metallic nanoparticles thereon. Treating the nanostructured material with an acid, e.g., sulfuric acid and/or nitric acid may form carboxylic acid functional groups in the nanostructured material that may stabilize the metallic nanoparticles on the nanostructured material after coating, due to the presence of strong interactions between the metallic nanoparticles and carbon atoms that is provided via carboxylate groups.
[0085] The metallic nanoparticles may include, without limitation, copper, gold, titanium, platinum, silver, palladium, ruthenium, rhenium, iron, nickel, indium, lead, tin, zinc, or combinations thereof. The metallic nanoparticles may have an average particle size of less than 100 nm, preferably 10 to 80 nm, preferably 15 to 50 nm, more preferably 20 to 40 nm. In some embodiments, the metallic nanoparticles include bimetallic composite particles such as PtRu, PtNi, etc. The metallic nanoparticles may have similar rounded shapes, or may have various shapes including, without limitation, spherical, elliptical, cubical, hexagonal, pyramidal, conical, and/or irregular shapes. A coating layer may be formed after coating the nanostructured material with the metallic nanoparticles. A thickness of the coating layer may preferably be in the range from about 1 nm to 1 m, preferably 2 to 500 nm, preferably 5 to 200 nm, preferably 10 to 100 nm, preferably 15 to 50 nm. The presence of the metallic nanoparticles in a form of the coating layer may enhance stability and may prolong an effective life span of the working electrode. In a preferred embodiment, an electrical conductivity of the working electrode, after coating with the metallic nanoparticles, is increased by at least 10%, preferably at least 20%, preferably at least 50%, preferably at least 80%, preferably at least 100%, preferably 120% to about 150%, relative to the electrical conductivity of the working electrode that is not coated with the metallic nanoparticles. In one embodiment, the counter electrode 202 of the electrochemical cell 200 includes platinum. The counter electrode 202 may be made of platinum, or alternatively may be made of a platinum alloy including at least 50 wt %, preferably at least 60 wt %, preferably at least 70 wt %, preferably at least 80 wt %, preferably 85 wt % to 95 wt % relative to the total weight of the counter electrode. The counter electrode 202 may also include at least one metallic element selected from the group consisting of copper, gold, titanium, silver, palladium, ruthenium, rhenium, iron, nickel, indium, lead, tin, zinc. A weight ratio of the at least one metallic element to platinum in the counter electrode 202 is in the range from about 1:1 to about 1:20, preferably 1:2 to about 1:15, preferably 1:3 to about 1:12, preferably 1:5 to about 1:10. An electrical conductivity of the counter electrode 202 may be within the range of 3.010.sup.6 to 7.010.sup.7 s/m, preferably 5.010.sup.6 to 5.010.sup.7 s/m, preferably 10.sup.7 to 2.010.sup.7 s/m, at a temperature in the range of 20 to 30 C., preferably 22 to 28 C., preferably about 25 C.
[0086] The reference electrode 204 as used herein is preferably stable over time and in various temperatures, i.e. the reference electrode 204 has a fixed and a reproducible electrode potential. The reference electrode 204 may be a saturated calomel electrode or preferably a silver/silver-ion electrode. In a preferred embodiment, the reference electrode 204 is a silver/silver-chloride electrode. The electrochemical cell may not include a reference electrode, and therefore the counter electrode may serve as a combined counter/reference electrode.
[0087] The working electrode 100, the reference electrode 204, and the counter electrode 202 are disposed adjacent to one another in the electrochemical cell 200 (as shown in
[0088] In one embodiment, the working electrode 100, the reference electrode 204, and the counter electrode 202 are in ionic communication via the electrolyte 206. The electrolyte 206 is an aqueous solution that includes hydroquinone, and may further include a halide, a sulfate, a nitrate, a phosphate, and an acetate of an alkali metal, phenol, a nitro-phenol and an amino-phenol, a bis-phenolic compound such as bisphenol-A, bisphenol-F, bisphenol-S, bisphenol-C, bisphenol-E, bisphenol-P, bisphenol-Z, etc. For example, in one embodiment, the electrolyte 206 includes hydroquinone and also includes potassium chloride, sodium sulfate, sodium phosphate, potassium nitrate, 2-nitrophenol, and 4-nitrophenol. The electrolyte 206 may have a pH in the range of 5 to 9, preferably 6 to 8, preferably about 7. In a preferred embodiment, when a voltage is applied to the working electrode 100 relative to the reference electrode 204, at least a portion of hydroquinone present in the electrolyte 206 is oxidized thereby generating an electric current in the electrochemical cell.
[0089] According to a third aspect, the present disclosure relates to a method of determining a hydroquinone concentration in a hydroquinone-containing solution with the electrochemical cell.
[0090] The hydroquinone-containing solution as used herein refers to an aqueous solution that contains hydroquinone (1,4-hydroquinone) and may further contain one or more of a halide, a sulfate, a nitrate, a phosphate, and/or an acetate of an alkali metal or an alkaline earth metal such as, e.g., potassium chloride, sodium sulfate, sodium phosphate, and potassium nitrate, phenol, a nitro phenol, e.g., 2-nitrophenol and 4-nitrophenol, an amino phenol, a bis-phenolic compound such as bisphenol-A, bisphenol-F, bisphenol-S, bisphenol-C, bisphenol-E, bisphenol-P, and bisphenol-Z, an alkoxy phenol compound such as methoxy phenol and ethoxy phenol, and an alcohol compound such as methanol, ethanol, propanol, isobutanol, n-butanol, and n-pentanol. In one embodiment, the hydroquinone-containing solution may be tap water, seawater, wastewater, bottled water, or water from a river, a lake, a pond, etc. In another embodiment, the hydroquinone-containing solution may be a blood sample. Preferably, the hydroquinone concentration in the hydroquinone-containing solution is within the range of 1.0 M to 1.0 M, preferably 10 M to 10 mM, preferably 20 M to 10 mM, preferably 30 M to 1.0 mM, preferably 40 M to 500 M. The preferable ranges of the hydroquinone concentration are not limited, and the method may determine the hydroquinone concentration when falls outside these preferable ranges. Also, the hydroquinone-containing solution may have a pH in the range of 5 to 9, preferably 6 to 8, preferably about 7.
[0091] The method may detect the presence of hydroquinone in a solution. The term detect as used herein refers to a qualitative measurement whereby the presence of hydroquinone in a solution is indicated. Also, the term determine as used in this disclosure relates to a quantitative measurement whereby a hydroquinone concentration is measured. In one embodiment, a detection limit of the electrochemical cell is in the range of 1.0 to 10.0 M, preferably 2.0 to 8.0 M, preferably 3.0 to 7.0 M, preferably 4.0 to 6.0 M of hydroquinone. The term detection limit as used herein refers to the smallest hydroquinone concentration that is detectable by the electrochemical cell. In another embodiment, the detection limit of the electrochemical cell is less than 1.0 M, preferably in the range of 10 to 500 nM, preferably 50 to 200 nM.
[0092] According to the method, the hydroquinone-containing solution is first contacted with the working electrode, the counter electrode, and the reference electrode of the electrochemical cell. The hydroquinone-containing solution may preferably be contacted with the working electrode, the counter electrode, and the reference electrode for example by submerging (or partially submerging) said electrodes into the hydroquinone-containing solution (as shown in
[0093] When the hydroquinone-containing solution is brought into contact with the working electrode, the counter electrode, and the reference electrode, a voltage is applied to the working electrode. The voltage is measured relative to the reference electrode 204 or a combined counter/reference electrode, e.g. in the embodiments where the electrochemical cell does not include reference electrode, with a voltmeter 210. In a preferred embodiment, the voltage is applied by a power source 208 that provides a DC current and the voltage is in the range of 0.05 to 0.5 volts, preferably 0.1 to 0.45 volts, preferably 0.2 to 0.4 volts, preferably about 0.3 volts, relative to the reference electrode, when the reference electrode is a silver/silver-chloride electrode. The voltage may also be outside of the above preferred ranges, e.g., in the range of 0.5 to 5.0 volts, or 1.0 to 4.0 volts, relative to the reference electrode. Accordingly, at least a portion of hydroquinone present in the hydroquinone-containing solution is oxidized on the working electrode. As a result, an electric current is generated in the electrochemical cell, which may be measured with an ammeter 212. The hydroquinone concentration may further be determined from the electric current via a calibration curve that correlates the electric current to the hydroquinone concentration.
[0094] For example, in some embodiments, the electric current is linearly correlated to the hydroquinone concentration (as shown in
[HQ]=a*I+b(I)
wherein [HQ] represents a molar concentration of hydroquinone (in M), I represents the electric current (in A), a represents a constant value in the range of 2 to 10 A.sup.1, preferably 4 to 9 M. A.sup.1, preferably 6 to 8 A.sup.1, preferably about 7.3 M. and b represents a constant value in the range of 1 to 5 preferably 2 to 4 preferably about 3.1 M.
[0095] The calibration curve may depend on several characteristics of the electrochemical cell, for example, the electrical conductivity of each of the working electrode and the counter electrode, the pore size and the BET surface area of the working electrode, the pH of the electrolyte, a dielectric constant of the electrolyte, a temperature at which the hydroquinone concentration is determined, etc. In one embodiment, the hydroquinone concentration is determined at a temperature in the range of 10 to 40 C., preferably 15 to 35 C., preferably 20 to 30 C., preferably about 25 C.
[0096] In one embodiment, a response time of the electrochemical cell to determine the hydroquinone concentration is in the range of 5 to 60 seconds, preferably 10 to 30 seconds, preferably 12 to 20 seconds. The term response time as used herein refers to the time duration that is measured from contacting the hydroquinone-containing solution with the working electrode, the counter electrode, and the reference electrode until the hydroquinone concentration is determined.
[0097] In some embodiments, the hydroquinone-containing solution includes hydroquinone and one or more of a halide, a sulfate, a nitrate, a phosphate, and/or an acetate of an alkali metal or an alkaline earth metal such as, e.g., potassium chloride, sodium sulfate, sodium phosphate, and potassium nitrate, phenol, a nitro-phenol, e.g., 2-nitrophenol and 4-nitrophenol, an amino-phenol, an alkoxy phenol compound, e.g., methoxy phenol and ethoxy phenol, and an alcohol compound, e.g., methanol, ethanol, propanol, isobutanol, n-butanol, and n-pentanol; however, the hydroquinone-containing solution does not include the bis-phenolic compounds such as bisphenol-A, bisphenol-F, bisphenol-S, bisphenol-C, bisphenol-E, bisphenol-P, and bisphenol-Z. According to these embodiments, a hydroquinone selectivity of the electrochemical cell is at least 95% by mole, preferably at least 96% by mole, preferably at least 97% by mole, preferably at least 98% by mole, preferably at least 99% by mole. In the embodiments wherein the bis-phenolic compounds are present in the hydroquinone-containing solution, the hydroquinone selectivity of the electrochemical cell may be related to a molar ratio of the bis-phenolic compounds to hydroquinone. For example, in one embodiment, a molar ratio of the bis-phenolic compounds to hydroquinone is in the range of 1:1 to 1:5, preferably 1:1.5 to 1:4, preferably 1:2 to 1:3, wherein the hydroquinone selectivity of the electrochemical cell is in the range of 50% to 85% by mole, preferably 60% to 80% by mole, preferably 70% to 75% by mole. As used herein, the term hydroquinone selectivity refers to a molar ratio of hydroquinone relative to other organic molecules present in the hydroquinone-containing solution that are oxidized in the working electrode. For example, when the hydroquinone selectivity of the electrochemical cell is 95% by mole it means 95% by mole of all molecules that are oxidized in the working electrode is hydroquinone. The hydroquinone selectivity of the electrochemical cell may be related to the BET surface area and the pore size of the working electrode. Further, the hydroquinone selectivity may be related to the kinetics of oxidation. For example, at a specified voltage, hydroquinone may be more readily adsorbed onto the working electrode than other organic molecules present in the electrolyte.
[0098] The examples below are intended to further illustrate protocols for the electrode, the electrochemical cell, and the method of determining the hydroquinone concentration with the electrochemical cell, and are not intended to limit the scope of the claims.
Example 1Materials and Preparation of a Nanostructured Carbon Electrode (NSCE) from Date Palm Leaflets (DPLs)
[0099] Dead date palm leaves were collected from the lake side of King Fand University of Petroleum and Minerals, Saudi Arabia. N.sub.2 gas with a purity of 99.99% was supplied by the SCG gas center, Jubail, Kingdom of Saudi Arabia. Copper tape (one-sided adhesive) and Scotch 898 premium-grade Filament Tape (one-sided adhesive) were obtained from 3M, United States. Potassium chloride (KCl), potassium nitrate (KNO.sub.3), sodium sulfate (Na.sub.2SO.sub.4), sodium phosphate monobasic monohydrate, sodium phosphate dibasic heptahydrate, acetic acid, sodium acetate, potassium ferrocyanide (K.sub.4[Fe(CN).sub.6]), potassium ferricyanide (K.sub.3[Fe(CN).sub.6]), and hydroquinone (HQ) were purchased from Sigma-Aldrich. 2-Nitrophenol and 4-nitrophenol were purchased from Fluka and Alfaser, respectively. De-ionized water was used throughout the experiments and was obtained by using a water purification system (Barnstead Nanopure, Thermo Scientific, USA).
[0100] Initially, the dead date palm leaves were washed with water and dried at 40 C. The leaflets from the leaves were separated and cut into 2-cm-long pieces. These pieces were placed in a flat alumina crucible, which was then inserted in the glass tube of a tubular furnace. We confirmed the position of the crucible in the middle of the tubular furnace. Next, we locked the glass tube and flushed in copious amounts of N.sub.2 for five minutes to make an inert atmosphere. Next, we purged N.sub.2 through the tube drop by drop, and commenced heating at a rate of 10 C./min until the temperature reached 850 C. The temperature was then maintained at this value for five hours. Next we cooled the furnace to room temperature (at a cooling rate of 5 C./min) and took out the prepared nanostructured carbon electrode (NSCE). The prepared NSCE is referred to as NSCE.sub.850 in this disclosure. The prepared NSCE.sub.850 was made into a usable electrode by attaching copper tape to one side of it. Next, we covered NSCE.sub.850 and the copper tape with the Scotch tape except for a 0.2 cm.sup.2 area of the NSCE (working electrode area) and end of copper tape which were used to connect them with the potentiostat. The detailed procedure is described diagrammatically in
Example 2Characterization Methodology
[0101] All electrochemical measurements were taken using a CHI (760E) electrochemical workstation (http://www.chinstruments.com). The prepared NSCE (working electrode area 0.2 cm.sup.2) or a 3-mm-diameter glassy carbon electrode (GCE) (working electrode area 0.071 cm.sup.2) was used as the working electrode, Ag/AgCl was used as the reference electrode, and a platinum wire was used as the counter electrode. The working surface area of the NSCE was 2.82 times greater than that of the GCE in the electrochemical experiments. We therefore multiplied the current obtained at the GCE by 2.82 to compare it to the current obtained at the NSCE. All electrochemical experiments were carried out at RT without de-aeration. FE-SEM images were obtained using a field emission scanning electron microscope (TESCAN LYRA 3, Czech Republic). Energy dispersive X-ray spectra (EDS) were recorded using an Xmass detector, Oxford Instruments, equipped with the Lyra3 TESCAN FESEM. TGA-DSC analysis was performed using a Netzsch STA (Model STA 449 F3). A Raman spectrometer (iHR320 with CCD detector, HORIBA) with green laser (300 mW) excitation at .sub.0=532 nm was used to examine the graphite structure of the prepared NSCE. An XPS equipped with an Al-K micro-focusing X-ray monochromator (ESCALAB 250Xi XPS Microprobe, Thermo Scientific, USA) was applied for the chemical analysis of the prepared NSCE. Brauner-Emmet-Teller (BET) nitrogen adsorption-desorption isotherms, and Barrett-Joyner-Halenda (BJH) methods were followed for analyzing specific surface area and pore size distribution, respectively by using (BET, Micromeritics ASAP 2020) at 77 K.
Example 3Thermal Analysis of NSCE
[0102]
[0103] The TGA curve (
[0104] In addition, the TGA curve (
Example 4FESEM and EDS Analysis of NSCE
[0105] The NSCE.sub.1500 was planner type as the original sample of DPL.
[0106] The EDS analysis of NSCE.sub.850 confirmed the presence of C, O, N, Fe, Si, K, and Ca (data not shown). Generally, carbon prepared at around 850 C. from lingo-cellulose-type materials contains some oxygen as well as carbon. The other EDS-detected elements in NSCE.sub.850, i.e., N, Fe, Si, K and Ca, are also found in the date palm [Trabzuni D M, Ahmed S E B, Abu-Tarboush H M, (2014) Chemical Composition Minerals and Antioxidants of the Heart of Date Palm from Three Saudi Cultivars, Food and Nutrition Sciences, 5: 1379-1386].
[0107] To confirm the planar (nearly two-dimensional) type structure of the NSCE.sub.850, we recorded FESEM images (
Example 5Raman Analysis of NSCE
[0108]
[0109] The above results also indicated that carbon obtained by heating DPLs to 1500 C. is a good candidate to be used as a working electrode. However, due to the higher manufacturing cost, only the NSCE.sub.850 was used for further characterization.
Example 6XPS Analysis of NSCE
[0110]
Example 7BET Analysis of NSCE
[0111] Surface attributes, such as surface area, pore size, and pore volume of prepared samples were studied by BET surface area analysis.
Example 8Electrochemical Properties of NSCE with Respect to K.SUB.4.[Fe(CN).SUB.6.]
[0112]
[0113] Separately, the scan rate dependence of the CVs was measured for NSCE.sub.850 in an electrolyte solution containing 0.1 M KCl and 5 mM K.sub.4[Fe(CN).sub.6] (
Example 9Electrochemical Properties of NSCE with Respect to Hydroquinone
[0114] In our next trial, we investigated the electrocatalytic properties of NSCE.sub.850 and the GCE toward the electrochemical reaction of HQ.
Example 10Electrochemical Impedance Analysis of NSCE
[0115] In order to clarify the electrochemical performance of the electrode, electrochemical impedance spectroscopy (EIS) was also employed as a technique for the electrochemical characterization of NSCE.sub.850.
Example 11Amperometric Determination of Hydroquinone Concentration
[0116] The dependence of the current on HQ concentration and the limit of detection of HQ for NSCE.sub.850 were measured by using the amperometry method.
[0117]
[0118] Substrate-free carbon electrodes, each consisting of interconnected nanostructured carbon, were prepared by carrying out pyrolysis of date palm leaflets and were used for electrochemical applications. The elemental compositions of these electrodes were identified by EDS and XPS analysis. The electrocatalytic properties of these electrodes were evaluated by recording the corresponding CVs in the absence and the presence of K.sub.4[Fe(CN).sub.6] and HQ in solutions of 0.1 M supporting electrolyte. The voltammetry studies revealed the electrocatalytic properties of these electrodes to be superior to those of the GCE. The prepared nanostructured carbon electrodes showed a low detection limit for HQ with high analytical selectivity, sensitivity, and stability due to the electrocatalytic activities.