ELECTROCATALYSTS FOR HYDROGEN EVOLUTION REACTIONS (HER) WITH DELAFOSSITE OXIDES ABO2
20210388516 · 2021-12-16
Assignee
Inventors
- Claudia FELSER (Halle, DE)
- Guowei LI (Dresden, DE)
- Andrew MACKENZIE (Dresden, DE)
- Seunghyun KHIM (Dresden, DE)
Cpc classification
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
C01P2002/76
CHEMISTRY; METALLURGY
C01G51/40
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
B01J23/652
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
The present invention refers to material comprising a compound of the formula ABOx wherein x is >1.5 and ≤2.5, A is independently selected from a transition metal of IUPAC groups 10 and 11, and B is independently selected from a transition metal of IUPAC group 6, 7, 8 or 9 or a main group element of IUPAC group 13, as highly active catalyst for hydrogen evolution reaction (HER).
Claims
1. A hydrogen evolution reaction (HER) catalytic material comprising a compound of the formula (I):
ABOx (I) wherein x is >1.5 and ≤2.5, A is independently selected from a transition metal of IUPAC groups 10 and 11, and B is independently selected from a transition metal of IUPAC group 6, 7, 8 or 9 or a main group element of IUPAC group 13.
2. The catalytic material according to claim 1, wherein x is 2, and A is independently selected from: Pt, Pd, or Ag, and B is independently selected from: Co, Al, Cr, Fe, In, Nd or Rh.
3. The catalytic material according to claim 1, wherein the compound is PdCoO.sub.2 or PtCoO.sub.2.
4. A process for the manufacture of a compound according to claim 1, having the formula (I):
ABOx (I) wherein x is >1.5 and ≤2.5, A is independently selected from a transition metal of IUPAC groups 10 and 11, and B is independently selected from a transition metal of IUPAC group 6, 7, 8 or 9 or a main group element of IUPAC group 13; said process comprising mixing an “A”-halide with a “B”-oxide and heating the mixture to 600-1000° C.
5. An electrode in a photo/electrochemical cell comprising a compound according to formula (I):
ABOx (I) wherein x is >1.5 and ≤2.5, A is independently selected from a transition metal of IUPAC groups 10 and 11, and B is independently selected from a transition metal of IUPAC group 6, 7, 8 or 9 or a main group element of IUPAC group 13.
6. The electrode as claimed in claim 5, wherein the electrode is a hydrogen reduction electrode.
7. A process for producing hydrogen comprising reducing hydrogen in a photo/electrochemical cell having an electrode comprising a HER catalytic material as claimed in claim 1.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0016]
[0017]
[0018]
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
DETAILED DESCRIPTION OF THE INVENTION
[0026] The present invention is directed to HER catalytic material comprising compounds of delafossite structure of the formula (I)
ABOx (I)
wherein
x is >1.5 and ≤2.5,
A is independently selected from a transition metal of IUPAC groups 10 and 11, and
B is independently selected from a transition metal of IUPAC group 6, 7, 8 or 9 or a main group element of IUPAC group 13.
[0027] In a preferred embodiment
X is 2, and
[0028] A is independently selected from: Pt, Pd, or Ag, and
B is independently selected from: Co, Al, Cr, Fe, In, Nd or Rh.
[0029] Most preferred are the delafossite oxide compounds PdCoO.sub.2 and PtCoO.sub.2. PdCoO.sub.2 and PtCoO.sub.2 have a layered structure and crystallize in a rhombohedral space group, which is built by an alternating stacking of [A] layers and [BO.sub.2] slabs along the c-axis. Most delafossite oxides are insulators, but some, e.g. PdCoO.sub.2, PdCrO.sub.2, or PtCoO.sub.2, are good metals. The in-plane conductivities at room temperature are only about 3 μΩ cm, which is even higher than that of pure metals such as Pd, Cu, and Au. However, their carrier density is approximately 1.6*10.sup.22 cm.sup.−3. This is a factor of three lower than that of a 3d transition metal. This results in a long mean free path length of up to 0.6 nm, which is the longest of any known large carrier density metal. Considering that the “B”-elements are much cheaper than Platinum, and oxygen is free, the cost of catalysts can be decreased by as much as 75%. Yet, the HER activity is even higher than that of pure Platinum at high working current densities of >10 mA cm.sup.−2.
[0030] The delafossite oxide catalysts according to the present invention can be manufactured e.g. by mixing an “A”-halide such as a chloride, bromide or iodide with a “B”-oxide preferably by co-grinding the two compounds, preferably in an inert gas (e.g. N.sub.2, Ar) atmosphere for 10 to 60 minutes. The mixed powder is then heated to 600-1000° C., preferably 700-900° C., most preferred to about 800° C. for 3-8 hours, preferably 4-7 hours, most preferred for about 5 hours and then cooled down to 20-100° C., preferably 40-80° C., most preferred to 50-70° C. below the highest heating temperature at a cooling rate of 5-10° C./hour, preferably 6-8° C./hour, most preferred about 7° C./hour and then kept at this temperature for 10-50 hours, preferably 20-40 hours, most preferred about 30 hours. Finally, the composition is cooled to room temperature at a rate of 70-120° C./hour, preferably 80-100° C./hour, most preferred at about 90° C./hour. This reaction is preferably performed in a sealed tube, e.g. a quartz tube, preferably under reduced pressure of between 10-3 and 10-4 Pa.
[0031] General Properties
[0032] The electrocatalysts of the present invention exhibits a very low resistivity at room temperature, which is in the range of 0.05-3 μΩ cm in the temperature range of 5-300 K. This facilitates easy electron transfer between the catalyst and electrolyte. Moreover, the present electrocatalysts show higher activity under acidic conditions than Pt foil. The overpotential to deliver a current density of 10 mA/cm.sup.2 is only 33 mV. The Tafel slope is as low as 30 mV/dec. in acidic (pH=0) medium. All these values are lower than that of Pt foil (71 mV @10 mA/cm.sup.2 with Tafel slope of 74 mV/dec.), and even comparable with nano Pt/C catalysts (28 mV @10 mA/cm.sup.2 with Tafel slope of 34 mV/dec.). The exchange current density is determined to be 0.795 mA/cm.sup.2, which is higher than that of Pt/C catalyst with a value of 0.518 mA/cm.sup.2. The high chemical stability and electrochemical activity of the electrocatalyst do not change even after the compounds have been exposed to air for 3 months.
[0033] The electrocatalyst of the present invention consists of a compound with delafossite structure of the ABOx, wherein x is >1.5 and ≤2.5, A is independently selected from a transition metal of IUPAC groups 10 and 11, and B is independently selected from a transition metal of IUPAC group 6, 7, 8 or 9 or a main group element of IUPAC group 13. For example, the ABOx, compound can be grown on a conductive substrate such as Ni foam, carbon cloth, or can be mixed with graphene to increase the mobility and conductivity. However, it has surprisingly been found that the present ABOx, compounds can be used in single crystal form directly as a working electrode. In this case the electrode has a size of about 0.5 to 1.5×0.5 to 3.0×0.05 to 1.0 mm.sup.3, preferably about 1×2×0.1 mm.sup.3. The single crystal electrode can then be attached to a wire, e.g. Cu wire, e.g. with silver paint.
Example
[0034] The invention is explained in more detail below with reference to examples.
[0035] Powders of reagent-grade PdCl.sub.2 (99.99+% purity; Alfa Aesar) and CoO (99.995% purity; Alfa Aesar) were ground together for about one hour under an inert gas atmosphere. The mixed powder was then sealed in a quartz tube under a vacuum of 5×10.sup.−4 Pa. The sealed quartz tube was heated in a vertical furnace to 800° C. for 5 hours and cooled down to 740° C. at a rate of 7.5° C./hour and kept at this temperature for 30 hours. Finally, the furnace was cooled from 740° C. to room temperature at a rate of 90° C./hour.
[0036] Analytical Methods
[0037] X-ray powder diffraction patterns were obtained from a D8 Advance X-ray diffractometer (Bruker, AXS) using Cu Kα, radiation. The microstructure of the samples was examined by scanning electron microscope (SEM, FEI Quanta 200 F) with capabilities for energy dispersive X-ray spectroscopy (EDX). Transport measurements were performed using standard four-probe ac techniques in 4He cryostats (Quantum Design).
[0038] HER catalytic measurements were performed on the Autolab PGSTAT302N with impedance module electrochemistry workstation with a conventional three electrode cell configuration. A Ag/AgCl (3 M KCl) electrode was used as the reference electrode, and a graphite rod was used as the counter electrode. The electrolyte was 0.5 M H.sub.2SO.sub.4 solution and purified by Ar before use. Linear sweep voltammograms were recorded using a PdCoO.sub.2 single crystal electrode with a scan rate of 1 mV/S. Stability tests were carried out at a current density of 50 mA/cm.sup.2 in the initial test for 24 hours. To check the chemical stability of the catalyst, the same measurement was repeated again after exposing the crystal to air for two weeks. All potentials were referenced to a reverse hydrogen electrode (RHE).
[0039] Composition and Structure
[0040] PdCoO.sub.2 single crystals were synthesized and separated from unreacted CoO and from CoCl.sub.2 powder by cleaning the product with boiling alcohol.
[0041]
[0042]
[0043] Physical Transport Properties
[0044]
[0045] Electrocatalytic Activity Assessment
[0046]
[0047] The HER polarization curves for Cu wire, commercial Pt/C, and PdCoO.sub.2 electrocatalysts are shown in
[0048] Tafel slope and exchange current density were obtained by fitting the experiment data with the Butler-Volmer equation (
[0049] The long-term chemical and electrochemical stability were tested and shown in