CHROMIUM AND NICKEL CO-DOPED RUTHENIUM OXIDE CATALYST FOR OXYGEN EVOLUTION REACTION IN ACIDIC MEDIA
20260085437 ยท 2026-03-26
Assignee
- Toyota Motor Engineering & Manufacturing North America, Inc. (Plano, TX, US)
- Toyota Jidosha Kabushiki Kaisha (Aichi-ken, JP)
Inventors
- Li Qin ZHOU (Okemos, MI, US)
- Siwen Wang (Ann Arbor, MI, US)
- Charles A. Roberts (Farmington Hills, MI, US)
- Chen Ling (Troy, MI, US)
Cpc classification
C25B11/093
CHEMISTRY; METALLURGY
C25B9/23
CHEMISTRY; METALLURGY
International classification
C25B11/093
CHEMISTRY; METALLURGY
Abstract
An oxygen evolution reaction (OER) catalyst for reaction in acidic media comprising: a chromium (Cr) and nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst, and wherein the chromium (Cr) and nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Cr and a Ni co-doped in a ruthenium oxide (RuO.sub.2). Methods of preparing the OER catalyst are disclosed.
Claims
1. An oxygen evolution reaction (OER) catalyst comprising: a chromium (Cr) and a nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst, and wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Ni and a Cr co-doped in a ruthenium oxide (RuO.sub.2).
2. The OER catalyst of claim 1, wherein Ru (ruthenium) ranges from about 75.0 at % to about 33.3 at %, chromium ranges from about 12.5 at % to about 33.3 at %, and nickel ranges from about 12.5% to about 33.3 at %.
3. The OER catalyst of claim 1, wherein the OER catalyst is Ru.sub.0.75Cr.sub.0.125Ni.sub.0.125O.sub.2.
4. The OER catalyst of claim 1, wherein the chromium for doping the ruthenium oxide (RuO.sub.2) is from chromium (II) chloride (CrCl.sub.2) precursor.
5. The OER catalyst of claim 1, wherein the nickel for doping the ruthenium oxide (RuO.sub.2) is from nickel(II) chloride hexahydrate (NiCl.sub.2.Math.6H.sub.2O) precursor.
6. The OER catalyst of claim 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is a solid solution metal oxide.
7. The OER catalyst of claim 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises nanoparticles of the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst.
8. The OER catalyst of claim 1, wherein the OER catalyst has a particle size of less than about 10 nm.
9. The OER catalyst of claim 1, wherein the OER catalyst comprises a tetragonal rutile-type structure.
10. The OER catalyst of claim 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is at an anode of a proton exchange membrane (PEM) water electrolyzer.
11. The OER catalyst of claim 1, wherein the OER catalyst is applicable for an acidic OER.
12. The OER catalyst of claim 1, wherein OER activity is performed in an acidic media, wherein the acidic media is perchloric acid.
13. The OER catalyst of claim 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst increased OER activity as indicated by a decrease in overpotential by about 89 mV at 10 mA/cm.sup.2 as compared to OER activity of a RuO.sub.2 catalyst not co-doped with the chromium and nickel.
14. The OER catalyst of claim 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is durable for about 2.5 to about 100 hours.
15. A proton exchange membrane (PEM) water electrolyzer comprising the OER catalyst of claim 1.
16. A method of performing OER catalysis in acidic media, the method comprising an OER catalysis reaction in acidic media, the acidic media comprising an OER catalyst, the OER catalyst comprising: a nickel (Ni) and chromium (Cr) co-doped ruthenium oxide (RuO.sub.2) catalyst, and wherein the nickel (Ni) chromium (Cr) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Ni and a Cr co-doped in a ruthenium oxide (RuO.sub.2).
Description
BRIEF DESCRIPTION OF DRAWINGS
[0023] The present teachings will become more fully understood from the detailed description and the accompanying drawings wherein:
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[0035]
[0036] It should be noted that the figures set forth herein are intended to exemplify the general characteristics of the methods, algorithms, and devices among those of the present technology, for the purpose of the description of certain aspects. These figures may not precisely reflect the characteristics of any given aspect and are not necessarily intended to define or limit specific examples within the scope of this technology. Further, certain aspects may incorporate features from a combination of figures.
DETAILED DESCRIPTION
[0037] The present teachings relate to lattice doping to stabilize RuO.sub.2 crystal structure, therefore improving activity and durability of RuO.sub.2 based catalysts for oxygen evolution reaction in acidic media.
[0038] In various aspects, the present teachings provide oxygen evolution reaction (OER) catalyst comprising: [0039] a chromium (Cr) and a nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst, and [0040] wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Ni and a Cr co-doped in a ruthenium oxide (RuO.sub.2).
[0041] In some aspects, the chromium used for doping can be from chromium (II) chloride CrCl.sub.2 precursor.
[0042] In some aspects the nickel can be from nickel(II) chloride hexahydrate NiCl.sub.2.Math.6H.sub.2O precursor.
[0043] In some aspects of the OER catalyst, Ru (ruthenium) ranges from about 75.0 at % (atomic percent) to about 33.3 at %, chromium ranges from about 12.5 at % to about 33.3 at %, and nickel ranges from about 12.5% to about 33.3 at %.
[0044] In some aspects, the OER catalyst is Ru.sub.0.75Cr.sub.0.125 Ni.sub.0.125O.sub.2.
[0045] In yet another aspect of the OER catalyst, the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst increased OER activity as indicated by a decrease in overpotential by about 89 mV at 10 mA/cm.sup.2 as compared to OER activity of a RuO.sub.2 catalyst not co-doped with the chromium and the nickel.
[0046] In yet another aspect of the OER catalyst, the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is durable for about 100 hours. In some aspects, the disclosed OER catalysts are durable for about 2.5 to about 100 hours.
[0047] In yet another aspect, a proton exchange membrane (PEM) water electrolyzer comprises the OER catalyst.
[0048] In these different aspects of the OER catalyst, the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is a solid solution metal oxide.
[0049] In these different aspects of the OER catalyst, the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises nanoparticles of the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst having a particle size of less than about 10 nm, about 8 nm, about 6 nm, about 5 nm, or less than about 5 nm.
[0050] The OER catalyst comprises a tetragonal rutile-type structure.
[0051] The OER catalyst is at an anode in a PEM water electrolyzer. The OER catalyst is applicable for OER reaction in an acidic medium. In some aspects, the acidic media comprises perchloric acid (HClO.sub.4).
[0052] The disclosed OER catalysts can increase OER activity by a decrease in overpotential by about 89 mV at 10 mA/cm.sup.2 as compared to OER activity of catalyst of an RuO.sub.2 not co-doped with the chromium and nickel.
[0053] Yet another aspect is a method of performing OER catalysis in acidic media, the acidic media comprising an OER catalyst, the OER catalyst comprising: [0054] a nickel (Ni) and chromium (Cr) co-doped ruthenium oxide (RuO.sub.2) catalyst, and [0055] wherein the nickel (Ni) chromium (Cr) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Ni and a Cr co-doped in a ruthenium oxide (RuO.sub.2). The acidic media can be perchloric acid (HClO.sub.4).
[0056]
[0057] The half reaction taking place on the anode side of a PEM water electrolyzer is referred to as the Oxygen Evolution Reaction (OER). Here the liquid water reactant is supplied to catalyst where the supplied water is oxidized to oxygen, protons and electrons:
##STR00001##
[0058] The half reaction taking place on the cathode side of a PEM water electrolyzer is the Hydrogen Evolution Reaction (HER), wherein the supplied electrons and the protons that have conducted through the membrane are combined to create gaseous hydrogen:
##STR00002##
[0059] The total reaction is: H.sub.2O(liquid).fwdarw.H.sub.2(gas)+O.sub.2(gas).
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[0065] Scanning transmission electron microscope (STEM) images in
[0066] Chemical mapping using energy dispersive X-ray spectroscopy (EDS) in STEM showed a uniform distribution of Cr, Ni and Ru in the nanoparticles (
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[0072] Rotating disk electrode (RDE) evaluation results are shown in
[0073]
EXAMPLE
[0074] Various aspects of the present disclosure are further illustrated with respect to the following example. It is to be understood that this example is provided to illustrate specific examples of the present disclosure and should not be construed as limiting the scope of the present disclosure in or to any particular aspect.
Example 1
Synthesis and Testing of Ru.sub.0.75Cr.sub.0.125Ni.sub.0.125O.sub.2
[0075] 0.1736 g of RuCl.sub.3, 0.0171 g of CrCl.sub.2 and 0.0331 g of NiCl.sub.2.Math.6H.sub.2O (Ru, Cr, and Ni at a molar ratio of 3:0.5:0.5) were added in 150 ml of 1 M HCl and sonicated for 2 hours. 0.4 g of Carbon black was then added and dispersed by stirring for 20 hours under room temperature. The mixture was dried by using a rotary evaporator and the remaining powder was collected. The powder was annealed in a flowing Ar/H.sub.2 (7% H.sub.2) atmosphere at 900 C. for 4 hours and then annealed in air at 550 C. for 4 hours.
Synthesis of RuO.SUB.2
[0076] For synthesis of RuO.sub.2 (referred to as synthesized RuO.sub.2), no CrCl.sub.2 and NiCl.sub.2.Math.6H.sub.2O were added as described above for the synthesis of Ru.sub.0.75Cr.sub.0.125 Ni.sub.0.125O.sub.2, and the rest of the procedure remained the same as described above.
Ink and Electrode Preparation for Electrochemical Measurements 20 mg of catalyst powder was added to a mixture of 1 ml of isopropyl alcohol, 4 ml of DI water, and 100 l of NAFION Dispersion D520 and sonicated for 1 h to obtain a well-dispersed catalyst ink. For electrode preparation, 20 l of catalyst ink was drop-cast on a 5.0-mm-diameter glassy carbon electrode, resulting in a catalyst loading of 400 g/cm.sup.2. The electrode was mounted to a rotator (Pine Instrument rotator upside down) and was rotated at a speed of 200 rpm and dried.
Electrochemical Measurement
[0077] The electrochemical experiments were conducted using a Pine Instrument rotating disk electrode (RDE) workstation. A three-electrode system, consisting of the catalyst film-coated glassy carbon working electrode, a platinum wire counter electrode, and a home-made Pt reference electrode (with fresh H.sub.2 from water electrolysis for each test), were used for all electrochemical measurements. The electrolyte used was 0.1 M HClO.sub.4.
[0078] Linear sweep voltammetry (LSV) test was performed at a scan rate of 1 mV/s; RDE rotating speed 1600 rpm; in O.sub.2 saturated 0.1 M HClO.sub.4. Results are provided in
[0079] Chronopotentiometry (CP) test was performed at 10 mV/cm.sup.2. Results are provided in
[0080] Further, the disclosure comprises additional notes and examples as detailed below.
Clauses
[0081] Clause 1. An oxygen evolution reaction (OER) catalyst comprising: [0082] a chromium (Cr) and a nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst, and [0083] wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Ni and a Cr co-doped in a ruthenium oxide (RuO.sub.2).
[0084] Clause 2. The OER catalyst of clause 1, wherein Ru (ruthenium) ranges from about 75.0 at % to about 33.3 at %, chromium ranges from about 12.5 at % to about 33.3 at %, nickel ranges from about 12.5% to about 33.3 at %.
[0085] Clause 3. The OER catalyst of clause 1, wherein the OER catalyst is Ru.sub.0.75Cr.sub.0.125 NiO.sub.0.125O.sub.2.
[0086] Clause 4. The OER catalyst of clause 1, wherein a chromium for doping the ruthenium oxide (RuO.sub.2) is from chromium (II) chloride CrCl.sub.2 precursor.
[0087] Clause 5. The OER catalyst of clause 1, wherein a nickel for doping the ruthenium oxide (RuO.sub.2) is from nickel(II) chloride hexahydrate NiCl.sub.2.Math.6H.sub.2O precursor.
[0088] Clause 6. The OER catalyst of clause 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is a solid solution metal oxide.
[0089] Clause 7. The OER catalyst of clause 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises nanoparticles of the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst.
[0090] Clause 8. The OER catalyst of clause 1, wherein the OER catalyst has a particle size of less than about 10 nm.
[0091] Clause 9. The OER catalyst of clause 1, wherein the OER catalyst comprises a tetragonal rutile-type structure.
[0092] Clause 10. The OER catalyst of clause 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is at an anode of a proton exchange membrane (PEM) water electrolyzer.
[0093] Clause 11. The OER catalyst of clause 1, wherein the OER catalyst is applicable for an acidic OER.
[0094] Clause 12. The OER catalyst of clause 1, wherein OER activity is performed in an acidic media, wherein the acidic media is perchloric acid.
[0095] Clause 13. The OER catalyst of clause 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst increased OER activity as indicated by a decrease in overpotential by about 89 MV at 10 mA/cm.sup.2 as compared to OER activity of a RuO.sub.2 catalyst not co-doped with the chromium and nickel.
[0096] Clause 14. The OER catalyst of clause 1, wherein the chromium (Cr) and the nickel (Ni) co-doped ruthenium oxide (RuO.sub.2) catalyst is durable for about 2.5 to about 100 hours.
[0097] Clause 15. A proton exchange membrane (PEM) water electrolyzer comprising the OER catalyst of clause 1.
[0098] Clause 16. A method of performing OER catalysis in acidic media, the method comprising an OER catalysis reaction in acidic media, the acidic media comprising an OER catalyst, the OER catalyst comprising: [0099] a nickel (Ni) and chromium (Cr) co-doped ruthenium oxide (RuO.sub.2) catalyst, and [0100] wherein the nickel (Ni) chromium (Cr) co-doped ruthenium oxide (RuO.sub.2) catalyst comprises a Ni and a Cr co-doped in a ruthenium oxide (RuO.sub.2).
[0101] The preceding description is merely illustrative in nature and is in no way intended to limit the disclosure, its application, or uses. As used herein, the phrase at least one of A, B, and C should be construed to mean a logical (A or B or C), using a non-exclusive logical or. It should be understood that the various steps within a method may be executed in different order without altering the principles of the present disclosure. Disclosure of ranges includes disclosure of all ranges and subdivided ranges within the entire range.
[0102] The headings (such as Background and Summary) and sub-headings used herein are intended only for general organization of topics within the present disclosure and are not intended to limit the disclosure of the technology or any aspect thereof. The recitation of multiple examples having stated features is not intended to exclude other embodiments having additional features, or other examples incorporating different combinations of the stated features.
[0103] As used herein, the terms comprise and include and their variants are intended to be non-limiting, such that recitation of items in succession or a list is not to the exclusion of other like items that may also be useful in the devices and methods of this technology. Similarly, the terms can and may and their variants are intended to be non-limiting, such that recitation that an example can or may comprise certain elements or features does not exclude other examples of the present technology that do not contain those elements or features.
[0104] As used herein, the term about, in the context of concentrations of components of the formulations, typically means +/5% of the stated value, more typically +/4% of the stated value, more typically +/3% of the stated value, more typically, +/2% of the stated value, even more typically +/1% of the stated value, and even more typically +/0.5% of the stated value.
[0105] The broad teachings of the present disclosure can be implemented in a variety of forms. Therefore, while this disclosure includes particular examples, the true scope of the disclosure should not be so limited since other modifications will become apparent to the skilled practitioner upon a study of the specification and the following claims. Reference herein to one aspect, or various aspects means that a particular feature, structure, or characteristic described in connection with an embodiment or particular system is included in at least one embodiment or aspect. The appearances of the phrase in one aspect (or variations thereof) are not necessarily referring to the same aspect or embodiment. It should be also understood that the various method steps discussed herein do not have to be carried out in the same order as depicted, and not each method step is required in each aspect or embodiment.
[0106] The foregoing description of the embodiments has been provided for purposes of illustration and description. It is not intended to be exhaustive or to limit the disclosure. Individual elements or features of a particular embodiment are generally not limited to that particular embodiment, but, where applicable, are interchangeable and can be used in a selected embodiment, even if not specifically shown or described. The same may also be varied in many ways. Such variations should not be regarded as a departure from the disclosure, and all such modifications are intended to be included within the scope of the disclosure.