Platinum oxide nanoparticles for electrochemical hydrogen evolution and methods for making and using the same
11767602 · 2023-09-26
Assignee
Inventors
Cpc classification
C25B11/067
CHEMISTRY; METALLURGY
C25B11/052
CHEMISTRY; METALLURGY
C25B11/075
CHEMISTRY; METALLURGY
Y02E60/36
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C25B11/054
CHEMISTRY; METALLURGY
International classification
C25B11/052
CHEMISTRY; METALLURGY
C25B11/067
CHEMISTRY; METALLURGY
Abstract
The catalyst composition includes graphitic carbon nitride and a plurality of platinum oxide nanoparticles disposed on the graphitic carbon nitride.
Claims
1. A catalyst composition comprising: graphitic carbon nitride; and a plurality of platinum oxide nanoparticles disposed on the graphitic carbon nitride, having a platinum loading from about 25% to about 35% by weight of the catalyst composition.
2. The catalyst composition according to claim 1, wherein each of the plurality of platinum oxide nanoparticles is from about 1.0 nm to about 4.4 nm.
3. The catalyst composition according to claim 1, wherein the plurality of platinum oxide nanoparticles have an average particle diameter from about 1.0 nm to about 3.0 nm.
4. A catalyst composition comprising: graphitic carbon nitride; and a plurality of platinum oxide nanoparticles disposed on the graphitic carbon nitride, wherein the plurality of platinum oxide nanoparticles includes platinum 4+ species and platinum 2+ species.
5. The catalyst composition according to claim 4, wherein the platinum 4+ species and the platinum 2+ species are present at a ratio from about 1.5:1 to about 1.75:1.
6. A catalyst composition comprising: graphitic carbon nitride; and a plurality of platinum oxide nanoparticles disposed on the graphitic carbon nitride, having an overpotential for reaching a current density of about 10 mA cm.sup.−2 from about −5 mV to about −10 mV.
Description
BRIEF DESCRIPTION OF DRAWINGS
(1) Various embodiments of the present disclosure are described herein below with reference to the figures wherein:
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DETAILED DESCRIPTION
(24) The present disclosure is directed to a catalyst composition including a plurality of metallic nanoparticles disposed on a nanosheet. As used herein, the term “nanosheet” denotes a nanoscale sheet having a thickness from about 10 nm to about 1,000 nm and any suitable width and length larger than then thickness. As used herein, the term “nanoparticle” denotes a particle having any shape and size from about 1 nm to about 100 nm.
(25) The nanosheet may be formed from carbon nitride (C3N4) by thermal treatment, namely, pyrolysis, of urea. Urea may be placed in a covered reaction vessel and heated to a first temperature from about 200° C. to about 400° C., which in embodiments may be about 300° C. Urea may be heated at a rate from about 1° C. per minute to about 5° C. per minute, and in embodiments may be heated at a rate of about 2° C. per minute. The first temperature may be held from about 1 hour to about 4 hours, and in embodiments may be held for about 3 hours. The resulting solid following the first heating step may then be collected and heated again in open atmosphere, e.g., air, to a second temperature, which is higher than the first temperature and may be from about 500° C. to about 600° C., and in embodiments may be about 520° C. The temperature may be held from about 3 hours to about 5 hours, and in embodiments may be about 4 hours. The resulting solid following the second heating step may then be washed, filtered, and dried to obtain the C3N4 nanosheet material.
(26) Thereafter, nanoparticles may be formed and deposited on C3N4 to form the catalyst composition. Suitable nanoparticles may be formed from copper (Cu), silver (Ag), gold (Au), platinum (Pt), oxides or alloys thereof. C3N4 nanosheet materials may be dispersed or suspended in water, to which a metal halide salt may be added. The suspension may be heated to a temperature from about 80° C. to about 95° C. and in embodiments may be about 90° C. Suitable metal halides may include metal chlorides, such as platinum chloride (PtCl.sub.2), platinum tetrachloride (PtCl.sub.4), silver chloride (AgCl.sub.2), silver tetrachloride (AgCl.sub.4), gold chloride (AuCl.sub.3), copper chloride (CuCl.sub.2), and the like. In embodiments, combinations of different metal halide salts may be mixed. Metal halide may be mixed with the suspension from about 24 hours to about 72 hours, and in embodiments may be about 48 hours. Prior to mixing metal halide, the metal halide may be dissolved in hydrochloric acid (HCl) and the solution may then be neutralized by using an acid neutralizing agent, such as anhydrous sodium bicarbonate (NaHC.sub.3), to achieve a pH of about 7. The dissolved metal from the metal halide forms metal oxide nanoparticles, which are then deposited on the nanosheet, thereby forming the catalyst composition.
(27) In embodiments where the metal halide is a platinum halide, such as PtCl.sub.2 or PtCl.sub.4, the resulting nanoparticles may be platinum oxide nanoparticles being from about 1.0 nm to about 4.0 nm, with the average particle diameter from about 1.0 nm to about 3.0 nm. Platinum loading may be from about 25% to about 35% by weight of the catalyst composition, in embodiments from about 28% to about 32% by weight of the catalyst composition. The atomic ratio of platinum species in the nanoparticles, Pt4+:Pt2+, may be from about 0.4:1 to about 2.00:1, in embodiments the ratio may be from about 1.5:1 to about 1.75:1. In further embodiments, PtCl.sub.2 and PtCl.sub.4 may be mixed at different ratios to vary the ratio of Pt4+:Pt2+ in order to tailor HER activity of the catalyst composition. The HER activity of the catalyst composition according to the present disclosure may be expressed as an overpotential needed to reach a current density of about 10 mA cm.sup.−2, η10, which may be from about −5 mV to about −10 mV.
(28) The catalyst composition according to the present disclosure may be used in HER, a water splitting electrolysis reaction. The rate of hydrogen generation from the HER according to present disclosure may be affected by the pH and temperature at which HER is carried out. Accordingly, the HER may be carried out at a pH from about 1 to about 14, in embodiments, from about 9 to about 13, and in further embodiments, from about 10 to about 12. The HER may also be carried at a temperature from about 22° C. and 100° C., in embodiments from about 30° C. to about 80° C., and in further embodiments, from about 40° C. to about 60° C. HER may be carried with any suitable water, however, certain impurities present in the water may affect the rate of hydrogen generation.
(29) The method for hydrogen generation according to the present disclosure includes providing the catalyst composition according to the present disclosure and exposing the catalyst composition to a hydrogen containing compound, such as water or an aqueous solution. Exposure to the compound may be carried by placing the catalyst composition in a liquid container.
(30) The hydrogen containing compound may be an aqueous alkaline medium, which may be prepared by dissolving an alkaline compound including alkali metal hydroxides such as lithium hydroxide, sodium hydroxide and potassium hydroxide, and tetraalkylammonium hydroxides such as tetramethylammonium hydroxide and tetraethylammonium hydroxide. Suitable solvents include pure water or water that is mixed with various water-miscible solvents including alcohols such as methyl and ethyl alcohols, dimethylformamide, dimethylacetamide, ethyleneglycol, diethyleneglycol and the like. The aqueous alkaline medium may include from about 1% by to about 30% by weight of the alkaline compound dissolved therein. The generated hydrogen may be collected or syphoned for later use. In further embodiments, the generated hydrogen may be used directly with any system and or apparatus that utilizes hydrogen as a source of fuel, such as a fuel cell.
(31) The following Examples illustrate embodiments of the present disclosure. These Examples are intended to be illustrative only and are not intended to limit the scope of the present disclosure. Also, parts and percentages are by weight unless otherwise indicated. As used herein, “room temperature” or “ambient temperature” refers to a temperature from about 20° C. to about 25° C.
EXAMPLES
Example 1
(32) This example describes synthesis of C3N4, which is used as a substrate for forming a catalyst composition.
(33) C3N4 was prepared by thermal treatment of urea. About 15 g of urea was placed in a crucible, covered, heated in air to 300° C. at a rate of 2° C. min.sup.−1 and held for 3 h. The resulting white solid was ground to a fine powder, heated again in air to 520° C. at a rate of about 20° C. min.sup.−1 and held for about 4 hours. The resulting light-yellow solid was collected and washed with water purified using NANOPURE™ water, filtered, and dried in a vacuum furnace for about 24 hours at approximately 60° C., providing C3N4 nanosheets. C3N4 nanosheets were imaged, which are shown in
Example 2
(34) This example describes deposition of platinum oxide nanoparticles on C3N4 to form the catalyst composition according to the present disclosure.
(35) Platinum oxide deposition was performed by dispersing about 50 mg of C3N4 of Example 1 in about 50 mL of NANOPURE™ water under ultrasonication for about 1 hour. The resulting dispersion was then placed onto a hot plate under stirring. Two samples were prepared, a first sample of about 0.27 mmol of PtCl.sub.2 and a second sample of about 0.27 mmol of PtCl.sub.4. Each sample was slowly added to the stirring suspension and allowed to mix at about 90° C. for about 48 hours. In the case of PtCl.sub.2, the salt was first dissolved in HCl and neutralized with anhydrous sodium carbonate to achieve a neutral pH before addition. The products were collected by centrifugation at about 4500 rpm for about 10 minutes, washed with NANOPURE™ water and acetone, and dried in a vacuum oven overnight.
(36) The PtCl.sub.2 sample was named Pt2+90C and formed the first plurality of platinum oxide nanoparticles and the PtCl.sub.4 sample was named Pt4+90C and formed the second plurality of platinum oxide nanoparticles. The supernatant exhibited an orange color, indicative of an excess of platinum chloride in the solution, and became clear after washing, signifying effective removal of excess metal salts.
Example 3
(37) This Example describes chemical analysis of the catalyst compositions of Example 2.
(38) With reference to
(39) With reference to
(40) Furthermore, high resolution TEM images reveal clearly-defined lattice fringes of the nanoparticles (insets to
(41) Further structural insights were obtained in X-ray diffraction (XRD) measurements. With reference to
(42) XPS measurements were then carried out to determine the chemical composition and electronic environment of the material. X-ray photoelectron spectroscopy (XPS) measurements were performed with a Phi 5400/XPS instrument equipped with an Al K.sub.α source operated at about 350 W and 10.sup.−9 Torr. As shown in the survey spectra of
(43) With reference to
(44) Similar behavior was observed in the Pt4+90C sample, where the two doublets occurred at about 76.2 eV and about 72.9 eV as well as about 78.0 eV and about 74.7 eV, respectively. However, the ratio of Pt4+:Pt2+ was significantly higher at about 1.66:1, more than approximately 3.5 times that in Pt2+90C. Thus, the plots of
(45) The high-resolution scans of the C 1s and N 1s electrons are depicted in
(46) Upon thermal refluxing with platinum salts, the nitrogen and carbon peaks associated with the C3N4 matrix exhibited an increase in binding energy. The primary carbon peak shifted to 287.97 eV and 288.04 eV (C—N═C), and the defect carbon shifted to 284.53 eV and 284.57 eV (C—C) for Pt2+90C and Pt4+90C, respectively. The N 1s electrons also experienced a similar increase in binding energy with the three primary peaks centered at approximately 398.47 eV and 398.54 eV (C—N═C), 399.92 eV and 399.88 eV (N—(C).sub.3), 401.10 eV and 401.18 eV (C—N—H), corresponding to Pt2+90C and Pt4+90C, respectively. This slight increase in binding energy was attributed to electron donation from the C3N4 support to the Pt centers suggesting a strong interaction between the nanoparticles and C3N4.
(47) Further structural insights were obtained in X-ray absorption spectroscopic (XAS) measurements, where data was collected at the Pt L3 edge to probe the Pt electronic states and investigate the local structures. X-ray absorption spectroscopy (XAS) measurements were performed at 10 K on beamline 4-1 at the Stanford Synchrotron Radiation Lightsource (SSRL) using an Oxford liquid helium cryostat.
(48) The data were reduced and analyzed using the r-space X-ray absorption package (RSXAP). In
(49) EXAFS plots for Pt2+90C and Pt4+90C were then compared to that for α-PtO.sub.2 in
(50) The reference α-PtO.sub.2 has a hexagonal structure; and the environment about Pt consists of 6 nearest-neighbor O atoms, six second-neighbor Pt atoms and six third-neighbor O atoms. To fit the data, theoretical Pt—O and Pt—Pt functions were calculated for α-PtO.sub.2 using FEFF7, plus a weak multiscattering peak, as shown in
(51) TABLE-US-00001 TABLE 1 Sample Pt—O (Å) Pt—Pt (Å) Pt2 + 90C 2.071 ± 0.01 3.204 ± 0.02 Pt4 + 90C 2.034 ± 0.01 3.154 ± 0.02
Example 4
(52) This example describes analysis of electrocatalytic performance of catalyst compositions of Example 2.
(53) Electrochemical measurements were performed with a CHI710 workstation, and electrochemical impedance measurements were carried out with a Gamry Reference 600 instrument. A glassy carbon electrode (5.60 mm in diameter, 0.246 cm.sup.2) was used as the working electrode, while an Ag/AgCl (1.0 M potassium chloride (KCl)) electrode and graphite rod were used as the reference and counter electrodes, respectively. The Ag/AgCl electrode was calibrated versus a reversible hydrogen electrode (RHE) and all potentials in the present study were referenced to this RHE. In a typical experiment, about 2 mg of dry samples of catalyst compositions of Example 2 were mixed with about 3 mg of carbon black and sonicated for about 20 minutes in approximately 1 mL of isopropanol followed by an addition of about 40 μL NAFION™ (a sulfonated tetrafluoroethylene based fluoropolymer-copolymer) and sonicated for an additional 10 minutes. About 30 μL of the prepared ink was dropped onto the surface of the glassy carbon electrode and dried at room temperature, corresponding to a catalyst mass loading of about 0.244 mg cm.sup.−2.
(54) To assess the electrocatalytic performance of these materials toward HER, linear sweep voltammetry was performed under a nitrogen atmosphere in 0.5 M H.sub.2SO.sub.4 at the potential scan rate of about 10 mV s.sup.−1.
(55) TABLE-US-00002 TABLE 2 Catalyst Platinum Loading Electrolyte η.sub.10 Catalyst Composition (mg/cm.sup.2) Solution (mV) Reference Pt oxide C.sub.3N.sub.4 Pt.sup.2+/Pt.sup.4+ 0.24 0.5M H.sub.2SO.sub.4 −7.7 Present application Pt/PtO2/Fe3O4 Pt.sup.0/Pt.sup.2+/Pt.sup.4+/Fe — 1.0M H.sub.2SO.sub.4 >−10 .sup.[1] PtO.sub.x/TiO.sub.2 Pt.sup.2+/Pt.sup.4+/Ti — 0.5M H.sub.2SO.sub.4 −150 .sup.[2] MoS.sub.x—O—PtO.sub.x Pt.sup.2+/Pt.sup.4+/MoS.sub.x 0.45 0.5M H.sub.2SO.sub.4 −25 .sup.[3] Pt—(PtO.sub.x)—NSs/ Pt.sup.0/Pt.sup.2+/Pt.sup.4+ 0.036 0.5M H.sub.2SO.sub.4 −5 .sup.[4] C .sup.[1]M. Sarno, E. Ponticorvo, Int J Hydrogen Energy 2017, 42, 23631-23638. .sup.[2]X. Cheng, Y. H. Li, L. R. Zheng, Y. Yan, Y. F. Zhang, G. Chen, S. R. Sun, J. J. Zhang, Energy Environ. Sci. 2017, 10, 2450-2458. .sup.[3]Y. X. Zhan, Y. Li, Z. Yang, X. W. Wu, M. Z. Ge, X. M. Zhou, J. J. Hou, X. N. Zheng, Y. C. Lai, R. R. Pang, H. Duan, X. A. Chen, H. G. Nie, S. M. Huang, Adv Sci 2019, 6, 1801663. .sup.[4]M. K. Kundu, T. Bhowmik, R. Mishra, S. Barman, Chemsuschem 2018, 11, 2388-2401.
(56) To further understand the reaction mechanisms of these materials, Tafel plots were derived from the polarization curves, as shown in
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(58) To further examine the influence of the Pt oxidation state on the HER performance, several additional electrochemical measurements were performed. In the first test, the Pt2+90C sample was found to show a marked improvement of the HER performance after 50 cycles at high potentials from about +0.9 V to about +1.2 V vs RHE at the potential rate of approximately 10 mV s.sup.−1 (where Pt.sup.2+ was electrochemically oxidized to Pt.sup.4+). In
(59) Additional tests were carried out with Pt4+90C. When the catalyst was subject to potential cycling between 0 and +0.02V vs RHE for 1000 cycles at 10 mV s.sup.−1 (where Pt.sup.4+ was electrochemically reduced to lower valence states), η.sub.10 in the subsequent HER measurement was found to deteriorate from about −7.7 mV to about −21.7 mV. However, after 50 potential cycles between +0.9 and +1.2 V, the HER performance was almost fully recovered, with η.sub.10 being about −9.8 mV. In contrast, electrochemical treatment (reduction or oxidation) of C3N4 alone did not lead to any change of the electrochemical response, suggesting that it is the Pt species that is responsible for the HER activity and Pt.sup.4+ is far more active than Pt.sup.2+. In fact, the HER activity increases markedly with increasing Pt.sup.4+ loading in the Pt4+90C sample as illustrated in
(60) As illustrated in the Examples above, PtOx nanoparticles were deposited onto C3N4 surfaces by thermal refluxing of C3N4 nanosheets and platinum chloride in water. The nanocomposites displayed similar platinum loading and particle size but with observable differences in the platinum valence states. It was shown that the platinum oxidation state greatly influenced the hydrogen evolution performance under electrochemical conditions, and platinum oxide nanoparticles in primarily a 4.sup.+ charge state exhibit HER performance superior to that of commercial platinum on carbon in acid media. The catalyst composition according to the present disclosure showed excellent stability and exceptional recoverability after recycling the material under oxidizing conditions. Accordingly, platinum oxide catalysts according to the present disclosure optimize the valence states of platinum by minimizing the formation of less oxidized, and less active species.
(61) It will be appreciated that of the above-disclosed and other features and functions, or alternatives thereof, may be desirably combined into many other different systems or applications. Also, that various presently unforeseen or unanticipated alternatives, modifications, variations or improvements therein may be subsequently made by those skilled in the art which are also intended to be encompassed by the following claims. Unless specifically recited in a claim, steps or components of claims should not be implied or imported from the specification or any other claims as to any particular order, number, position, size, shape, angle, or material.