Method for preparing a catalyst mediating H2 evolution, said catalyst and uses thereof
10137435 ยท 2018-11-27
Assignee
- Commissariat A L'energie Atomique Et Aux Energies Alternatives (Paris, FR)
- Universite Joseph Fourier (Grenoble, FR)
Inventors
- Vincent ARTERO (Quaix en Chartreuse, FR)
- Marc Fontecave (Saint Ismier, FR)
- Saioa Cobo (San Sebastian, ES)
- Pierre-Andre Jacques (Sainte Consorce, FR)
- Holger Dau (Berlin, DE)
- Jonathan Heidkamp (Mohorn, DE)
Cpc classification
C25B11/091
CHEMISTRY; METALLURGY
Y02P20/133
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
B01J31/182
PERFORMING OPERATIONS; TRANSPORTING
B01J2540/10
PERFORMING OPERATIONS; TRANSPORTING
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
B01J37/348
PERFORMING OPERATIONS; TRANSPORTING
Y02E60/50
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
B01J31/1835
PERFORMING OPERATIONS; TRANSPORTING
B01J31/1805
PERFORMING OPERATIONS; TRANSPORTING
C25B11/073
CHEMISTRY; METALLURGY
C25D5/011
CHEMISTRY; METALLURGY
B01J31/16
PERFORMING OPERATIONS; TRANSPORTING
B01J2531/0247
PERFORMING OPERATIONS; TRANSPORTING
B01J2531/0244
PERFORMING OPERATIONS; TRANSPORTING
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
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J31/16
PERFORMING OPERATIONS; TRANSPORTING
H01M4/86
ELECTRICITY
C25D5/00
CHEMISTRY; METALLURGY
Abstract
The present invention concerns a method for the preparation of a catalyst onto a solid support of a (semi-)conductive material consisting in depositing said catalyst onto said support from a near-neutral aqueous solution containing at least one nickel or cobalt organic complex and at least one basic oxoanion, by a method selected in the group consisting of reductive electrodeposition, photochemical electrodeposition and photoelectrochemical deposition. The present invention also concerns said catalyst and uses thereof.
Claims
1. A method for the preparation of a catalyst onto a solid support of a conductive or semiconductive material, the method comprising: depositing said catalyst onto said solid support from a near-neutral aqueous solution containing at least one nickel or cobalt organic complex and at least one basic oxoanion, using a method selected from the group consisting of reductive electrodeposition, photochemical electrodeposition, and photoelectrochemical deposition, wherein the catalyst consists of elemental cobalt/nickel covered or coated by a cobalt/nickel oxo/hydroxo-oxoanion layer.
2. The method according to claim 1, wherein the conductive or semiconductive material of said solid support is selected from the group consisting of a metallic material, a carbon material, a semiconductor or conductor metal oxide, nitride, and chalcogenide.
3. The method according to claim 1, wherein the conductive or semiconductive material of said solid support is selected from the group consisting of silicon, brass, stainless steel, iron, copper, nickel, cobalt, aluminium, silver, gold, titanium, carbon black, single or multi-walled carbon nanotubes (CNT), fullerenic nanoparticles, graphite, glassy carbon, graphene, reduced graphene oxide, doped diamond, TiO.sub.2, NiO, ZnO, ZrO.sub.2, ITO, SnO.sub.2, WO.sub.3, Fe.sub.2O.sub.3, BiVO.sub.4, Ta.sub.2O.sub.5, Ta.sub.3N.sub.5, TaON, ZnS, ZnSe, CdS, CdSe, CdTe, ZnTe, and composites of these materials, possibly doped with other elements.
4. The method according to claim 1, wherein the near-neutral aqueous solution has a pH of between 5 and 9.
5. The method according to claim 1, wherein the near-neutral aqueous solution has a pH of between 6 and 8.
6. The method according to claim 1, wherein the near-neutral aqueous solution has a pH of between 6.3 and 7.7.
7. The method according to claim 1, wherein the near-neutral aqueous solution has a pH of between 6.5 and 7.5.
8. The method according to claim 1, wherein the near-neutral aqueous solution has a pH of between 6.7 and 7.3.
9. The method according to claim 1, wherein the near-neutral solution is an aqueous solution having a pH of 7.
10. The method according to claim 1, wherein said cobalt or nickel organic complex is selected from the group consisting of cobalt or nickel dioxime/diimine complex; and cobalt or nickel amine/imine/pyridine complex.
11. The method according to claim 1, wherein said cobalt or nickel organic complex is selected from the group consisting of [Co(DO)(DOH)pnCl.sub.2] with (DOH)(DOH)pn representing N.sup.2,N.sup.2-propanediylbis(2,3-butandione 2-imine 3-oxime); [Co(DO)(DOH)pnBr.sub.2]; [Co((DO).sub.2BF.sub.2)pnBr.sub.2] with ((DO).sub.2BF.sub.2)pn representing N.sup.2,N.sup.2-propanediylbis(2,3-butandione 2-imine 3-oximato)-N.sup.1,N.sup.1-difluoroboryl [Co(MO)(MOH)pnCl.sub.2] with (MOH)(MOH)pn representing N.sup.2,N.sup.2-propanediylbis(1,2-propandione 2-imine 1-oxime); [Ni((CO).sub.2BF.sub.2)pn](ClO.sub.4); [Co(dmgBF.sub.2).sub.2(H.sub.2O).sub.2] with dmgH.sub.2 representing dimethylglyoxime; [Co(dmgH).sub.2pyCl]; [Co(dmgH).sub.2(OH.sub.2).sub.2]; [Co(dmgBF.sub.2).sub.2(DMF).sub.2]; [Co(dmgBF.sub.2).sub.2(CH.sub.3CN).sub.2]; [Co(dpgBF.sub.2).sub.2(H.sub.2O).sub.2] with dpgH.sub.2 representing diphenylglyoxime; [Co(dpgBF.sub.2).sub.2(DMF).sub.2]; [Co(dpgBF.sub.2).sub.2(CH.sub.3CN).sub.2]; [Ni(dmgBF.sub.2).sub.2]; [Ni(dmgH).sub.2] [Ni(DO)(DOH)pn](ClO.sub.4); [Ni(MO)(MOH)pnCl]; [Ni((DO).sub.2BF.sub.2)pn](ClO.sub.4); [Co(DO)(DOH)pnBr(PPh.sub.3)]; [Co(DO)(DOH)pn(PPh.sub.3)]; [Co(dmg).sub.3(BF).sub.2].sup.+; [Co(dpg).sub.3(BF).sub.2].sup.+; [Co(dmg).sub.3(BPh).sub.2].sup.0/1+ and [Co(dpg).sub.3(BPh).sub.2].sup.0/1+.
12. The method according to claim 1, wherein said basic oxoanion is selected from the group consisting of a phosphate, carbonate, arsenate, borate, vanadate, chromate, phosphonate, phosphite, nitrate, nitrite, sulphate, sulphonate, molybdate, and tungstate.
13. The method according to claim 1, wherein the reductive electrodeposition comprises applying to said solid support a potential below ?0.4 V versus Ag/AgCl.
14. The method according to claim 1, wherein the reductive electrodeposition comprises applying to said solid support a potential below ?0.6 V versus Ag/AgCl.
15. The method according to claim 1, wherein the reductive electrodeposition comprises applying to said solid support a potential below ?0.8 V versus Ag/AgCl.
16. The method according to claim 1, wherein the reductive electrodeposition comprises applying to said solid support a potential of about ?1 V versus Ag/AgCl.
17. A method for mediating hydrogen evolution comprising implementing the catalyst obtained by the preparation method according to claim 1.
18. The method according to claim 3, wherein the conductive or semiconductive material is doped with one or n ore elements other than said selected material.
Description
SHORT DESCRIPTION OF THE DRAWINGS
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DETAILED DISCUSSION OF PARTICULAR EMBODIMENTS
I. Experimental Section
(14) I.1. Materials.
(15) The cobalt complexes used hereinafter to prepare H.sub.2CoCat are [Co(DO)(DOH)pnCl.sub.2] [15] and [Co(dmgBF.sub.2).sub.2(H.sub.2O).sub.2] with dmgH.sub.2 representing dimethylglyoxime [27] were prepared according to previously described procedure.
(16) Fluorine doped tin oxide (FTO) coated glass slides with 7-10 ?/sq surface resistivity and a thickness of 6000 ? were purchased from Solems (France).
(17) KH.sub.2PO.sub.4 (98-100.5%) and K.sub.2HPO.sub.4 (99%) were purchased from Carlo Erba and Acros Organics respectively. ZnCl.sub.2 (Fluka, purity >98%)) and KCl (Fluka, purity 99.5%) analytical reagent grade were used for ZnO preparation without further purification.
(18) A three-electrode electrochemical cell was used for ZnO nanorods deposition on FTO substrates. The electrochemical growth was done at E=?1.0 V vs SCE, passed charge density 10 and 30 C.Math.cm.sup.?2 and T=80? C.
(19) Further details can be found in [28].
(20) I.2. Methods.
(21) X-ray photoemission spectroscopy (XPS) analyses were performed with a Kratos Axis Ultra DLD using a high-resolution monochromatic AlK? line X-ray source at 1486.6 eV. Fixed analyzer pass energy of 20 eV was used for core level scans. Survey spectra were captured at pass energy of 160 eV. The photoelectron take-off angle was normal to the surface, which provided an integrated sampling depth of approximately 15 nm. All spectra were referenced with an external gold substrate with a binding energy of 84.0 eV for Au 4f. For quantification, relative sensitivity factors issued from Wagner's publication were used [29]. The amount of carbon varies from samples and corresponds to carbon contamination from the atmosphere and/or ethanol washing after electrodeposition.
(22) SEM images and EDX spectra were recorded with a FEG-SEM (Leo 1530) operating at 5 kV and equipped with a Princeton Gamma-Tech EDX system operating at 15 kV.
(23) Electrochemical analysis was done using a Bio-logic SP300 potentiostat. FTO was preferred to graphite and ITO (indium-tin oxide) as the electrode material to minimize background H.sub.2 evolution and avoid reductive degradation of the ITO substrate [30,31] respectively.
(24) Cyclic voltammograms are shown using two different potential scales: first, potential is quoted against the Ag/AgCl reference electrode. Second, to ease reading the graphs in terms of overpotentials, potentials are also quoted against the Reversible Hydrogen Electrode (ie the apparent standard potential of the H.sup.+/H.sub.2 couple at the given pH).
(25) The potential of the Reversible Hydrogen Electrode (RHE) is defined as E.sup.RHE=?0.059 pH. Thus potentials measured versus the Ag/AgCl electrode can be converted versus the RHE by using the following formula: E.sub.vs RHE=E.sub.vs Ag/AgCl+E.sup.o Ag/AgCl+0.059 pH. The [Fe(CN).sub.6].sup.3?/[Fe(CN).sub.6].sup.4? couple (E.sup.0=0.20 V vs Ag/AgCl in phosphate buffer at pH=7) has then been used for the standardisation of the measurements.
(26) The electrochemical experiments were carried out in a three electrode cell consisting of two compartments separated by a glass frit. The catalyst was assembled on a working electrode of FTO-coated glass of 1 cm.sup.2 and rinsed with acetone and deionized water prior to use. Connection of the FTO to the potentiostat was made via an alligator clip. The platinum-grid counter electrode was placed in a separate compartment connected by a glass-frit and filled with the electrolytic solution. The potential has been calibrated after each experiment by adding potassium ferrocyanide in the solution and measuring its half-wave potential.
(27) During controlled-potential coulometry and linear sweep voltammetry experiments, the cell was flushed with nitrogen (5 ml.Math.min.sup.?1) and the output gas was sampled (100 ?l) every 2 min and analysed in a Perkin-Elmer Clarus 500 gas chromatograph equipped with a porapack Q 80/100 column (6?) thermostated at 40? C. and a TCD detector thermostated at 100? C.
(28) I.3. Deposition Procedure.
(29) Before starting the deposition, the FTO substrate is cycled hundreds of times between ?1 V and +1 V in 0.5 M potassium phosphate buffer (KPi), pH 7.0 to ensure the stability and reproducibility of experiments.
(30) Catalyst films were grown by controlled potential electrolysis of freshly prepared 0.1 mM Co(DO)(DOH)pnCl.sub.2 solution and in 0.5 M KPi, pH 7.0. Performing the electrolysis at ?1 V (vs Ag/AgCl) gives rise to a catalyst film of several micrometer thickness formed by nanoparticles after a course of around three hours.
(31) During this time, a film is formed on the working electrode surface. After the film formation is completed, the substrate is transferred to a cobalt-free 0.5 M KPi, pH 7.0, with potential set to reductive conditions (?1 V vs Ag/AgCl).
(32) Photodeposition was carried out by immersing ZnO electrode in a UV cell of freshly prepared 0.5 mM or 0.1 mM Co(DO)(DOH)pnCl.sub.2 solution and in 0.1 M KPi, pH 7.0 and illuminating the samples using a UV-handlamp for 3 h (VL-6LC, ?=254 nm).
(33) I.4. XAS Sample Preparation and Data Collection.
(34) The glassy carbon substrates (SIGRADUR K, thickness 100 ?m) had a surface resistivity of 2-15 ?/sq and were from HTW Hochtemperatur-Werkstoffe GmbH. KH.sub.2PO.sub.4 (99.5%) and K.sub.2HPO.sub.4 (99.5%) were purchased from AppliChem.
(35) For preparing the XAS samples, the inventors employed a single compartment, three electrode setup driven by an SP-200 potentiostat from BioLogic. The electrochemical cell consisted of a sample frame for XAS measurements glued (Momentive, SCNC silicone glue) on a glassy carbon substrate (working electrode) and a Pt wire (counter electrode) attached on the inner side of the frame. An Hg/HgSO.sub.4 reference electrode (?440 mV vs Ag/AgCl) was approached close to the center of the frame.
(36) Aqueous solutions of KH.sub.2PO.sub.4 (0.5 M) and K.sub.2HPO.sub.4 (0.5 M) were mixed until the KP.sub.i mixture reached a pH of 7.0. This electrolyte was pipetted into the sample frame until the liquid reached the reference electrode. The overall ohmic resistance of the electrochemical cell was determined by impedance spectroscopy and then used as set value for the applied IR compensation. The electrochemical background of the glassy carbon substrate was low, as verified by cyclic voltammetry.
(37) For the formation of the Co film, 0.5 mM Co(DO)(DOH)pnCl.sub.2 was added and a voltage of ?1.0 V vs Ag/AgCl was applied for 3 h. Then the cobalt solution was replaced by (cobalt-free) KP.sub.i via pipetting. Four CVs from ?1.21 V to ?0.56 V vs Ag/AgCl (scan rate: 20 mV/s) were performed to characterize the Co deposit.
(38) Finally, the Co film was equilibrated at ?1 V vs Ag/AgCl for 4 min and then rapidly frozen in a bath of liquid nitrogen. The reference electrode was removed before freezing to avoid any damage to the electrode by immersion in liquid nitrogen. However the potential between the working and the counter electrode was kept constant by applying the same voltage that had been present before removing the reference electrode (using a standard DC power supply connected to working and counter electrode). The power supply was disconnected after freezing in liquid nitrogen.
(39) X-ray absorption spectra were collected at beamline KMC1 of the BESSY, a synchrotron radiation source operated by the Helmholtz Zentrum Berlin (HZB). Spectra were collected at 20 K in absorption and fluorescence mode as described elsewhere [3].
II. Results
(40) II.1. Preparation of Catalytic Material.
(41) A. By Reductive Electrode Position.
(42)
(43) To provide more insights into the reductive process at work at the onset of the wave, the inventors carried out an electrolysis experiment at ?0.9 V vs Ag/AgCl for 1 h (Q=0.1 C.Math.cm.sup.?2.sub.geometric), which resulted in a grey coating of the electrode. The catalytic material thus obtained is hereafter named H.sub.2CoCat.
(44) The scanning electronic micrograph (
(45) The modified electrode was then transferred to a Co-free KPi electrolyte and its electrocatalytic properties were quantified using gas chromatography (bold traces in
(46) H.sub.2CoCat appears to be stable as long as the electrode is kept at a potential more negative than about ?0.6 V vs Ag/AgCl. When poised at a more positive potential, or left at open-circuit potential, the catalytic film readily dissolves in the electrolyte yielding Co(II) species. By ICP-MS titration of Co(II) ions in the electrolyte after full redissolution, the inventors determine that 1.0 10.sup.?6 mol of cobalt are deposited per geometric cm.sup.?2, from which the inventors derive a H.sub.2 evolution turnover frequency of 80 h.sup.?1 per Co center at 385 mV overpotential.
(47) B. By a Photochemical Deposition.
(48) Finally the inventors observed that H.sub.2CoCat can also be deposited through a photochemical procedure.
(49) The inventors chose ZnO because the energy level of its conduction band is suitable for H.sub.2 evolution from neutral aqueous solutions. ZnO nanorods with high specific surface area (
(50) Gas chromatographic analysis of the headspace of the vial in the course of this experiment (
(51) II.1. Characterization of the Catalytic Material.
(52) The structure of the new material was characterized by X-ray photoelectron spectroscopy (XPS), Energy Dispersive X-ray (EDX) spectroscopy, X-ray absorption near-edge structure (XANES) and extended X-ray absorption fine-structure (EXAFS) spectroscopies.
(53) The XPS spectrum of freshly electro-deposited H.sub.2CoCat, recorded under limited air exposure conditions, shows the presence of cobalt, phosphorus and oxygen (
(54) As the Co.sub.2p and O.sub.1s core levels binding energies [34] of cobalt oxides and hydroxides are in the same range as those of cobalt phosphate, the inventors tentatively describe the surface of electrodeposited H.sub.2CoCat as a combination of cobalt(II) phosphate with a cobalt oxo/hydroxo species Co.sub.xO.sub.y(OH).sub.z, probably in the Co(II) state as observed for native cobalt oxide/hydroxide that forms at the surface of metallic cobalt.
(55) EDX spectra (
(56) The absence of crystalline features in the powder low-angle X-ray diffraction pattern recorded at low angles and in the electron diffraction patterns recorded in a transmission electron microscope indicates the amorphous nature of H.sub.2CoCat. For insight into the atomic structure, X-ray absorption spectra were collected at the Co K-edge after H.sub.2CoCat formation and fast freezing of the still-wet electrode in liquid nitrogen (quasi-in situ measurements) as described earlier [3]. When deposition (paralleled by catalytic H.sub.2 evolution) was achieved at ?1.0 V vs Ag/AgCl, XANES and EXAFS measurements suggest a dominating contribution of the hexagonal close-packed phase of metallic cobalt (
(57) All these data indicate that the new material is made of nanoparticles with a cobalt oxo/hydroxo phosphate component mostly located at the surface and metallic cobalt in the bulk.
(58) II.3. Transformation in Water Oxidation Catalyst.
(59) Poising the H.sub.2CoCat electrode at a fairly positive potential (+1.16 V vs Ag/AgCl) resulted in a stable anodic current density of 1 mA.Math.cm.sup.?2 (
(60) In order to characterize the electrocatalytic material after this redox shift a detailed analysis by EDX, XPS and X-ray absorption spectroscopy has been carried out. According to EDX spectra (
(61) On the other hand, the XANES and EXAFS spectra (
(62) This observation parallels the recent report by Nocera et al. regarding the anodic oxidation of a 800 nm sputtered cobalt film for the preparation of O.sub.2CoCat [35].
(63) After cathodic deposition, alternate switches between oxidative (+1.71 V vs RHE, bold traces in
(64) Importantly the inventors could not evidence any decrease in activity for both H.sub.2 and O.sub.2 evolution after several switches. The inventors conclude that the H.sub.2CoCat film rapidly, reversibly and reproducibly commute with the O.sub.2CoCat form.
(65) From the current densities and chromatographic measurements, the inventors derive turnover frequencies of 10 and 80 h.sup.?1 per Co center at 480 and 385 mV overpotential for O.sub.2 and H.sub.2 evolution respectively. In order to determine whether this reversible transformation proceeds through the complete dissolution of one form of the CoCat film followed by the electrodeposition of the other form, the inventors stopped the experiment before current stabilization after a switch from reductive to oxidative conditions.
(66) SEM analysis then reveals the coexistence of different domains at the surface of the electrode (
(67) This last observation finally provides a rationale for the fact that photochemically deposited H.sub.2CoCat on ZnO nanorods can be used as an electrocatalytic material for water oxidation, as previously described by Steinmiller and Choi [36]. Actually these authors initially interpreted the photodeposition of Co(II) salts on ZnO nanorods as the formation of O.sub.2CoCat. The inventors' results establish that O.sub.2 and not H.sub.2 evolved during the photochemical process which definitively demonstrates that the deposition of the material does not proceed through the oxidation of the Co(II) ions (equation 1) with concomitant O.sub.2 or water reduction as previously stated. Rather H.sub.2CoCat is formed through the reduction of the Co(II) ions (equations 2) thanks to photogenerated electrons in the conduction band paralleled by water oxidation (equation 3) by holes remaining in the valence band. Both the observed nanoparticle-based morphology and the similar Co/P ratio derived from EDX analysis support this conclusion. When no more Co(II) ions are present in the solution, light is used by the H.sub.2CoCat coated ZnO nanorods to split water and produce both O.sub.2 and H.sub.2 (
(68) However, if this material is electrochemically poised at an anodic potential and irradiated, as in the study by Steinmiller and Choi [36], H.sub.2CoCat equilibrates with the valence band potential of ZnO, transforms into O.sub.2CoCat and finally mediates water oxidation.
Co.sup.2+.fwdarw.O.sub.2CoCat+e.sup.?Eq. 1
Co.sup.2++2e.sup.?.fwdarw.H.sub.2CoCatEq. 2
2H.sub.2O.fwdarw.O.sub.2+4H.sup.++4e.sup.?Eq. 3
III. Conclusion
(69) The inventors have discovered that cobalt complexes can be used for the deposition of a new nanoparticulate cobalt-based material (H.sub.2CoCat) consisting of elemental cobalt covered by a cobalt oxo/hydroxo phosphate compound. The latter proves active as a catalyst material for hydrogen evolution under strictly neutral conditions, which bridges the gap between noble metal nanoparticles, active under highly acidic conditions, and classical Ni or Co-based metallic compounds [37] and catalysing H.sub.2 evolution under strongly alkaline conditions.
(70) H.sub.2CoCat can be reversibly transformed through anodic equilibration into a cobalt oxide material catalyzing water oxidation (O.sub.2CoCat). An important finding is that the switch between the two catalytic phasesH.sub.2 evolution and water oxidationis highly reversible and corresponds to a local interconversion between two morphologies at the surface of the electrode. After deposition, the coating thus functions as a robust, bifunctional and switchable catalyst.
(71) To the best of the inventors' knowledge, such a property is not found except for noble metal catalysts such as Pt. These results open new pathways for the deposition of cobalt oxide film onto materials, such as ZnO or quantum dots, that do not withstand harsh anodic conditions.
(72) Additionally, they now make it possible to design an electrocatalytic water-splitting cell working under neutral conditions and based on cobalt ions as the sole precursors. In such a device, the catalytic materials will spontaneously self-assemble on both electrodes from a cobalt or nickel organic complex upon switching on. In addition, it will be insensitive to material cross-transfers processes when the system is switched off and on.
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