TY - JOUR
T1 - Optimization of Ni−Co−Fe-Based Catalysts for Oxygen Evolution Reaction by Surface and Relaxation Phenomena Analysis
AU - Attias, Rinat
AU - Vijaya Sankar, Kalimuthu
AU - Dhaka, Kapil
AU - Moschkowitsch, Wenjamin
AU - Elbaz, Lior
AU - Caspary Toroker, Maytal
AU - Tsur, Yoed
N1 - Publisher Copyright:
© 2021 Wiley-VCH GmbH
PY - 2021/4/9
Y1 - 2021/4/9
N2 - Trimetallic double hydroxide NiFeCo−OH is prepared by coprecipitation, from which three different catalysts are fabricated by different heat treatments, all at 350 °C maximum temperature. Among the prepared catalysts, the one prepared at a heating and cooling rate of 2 °C min−1 in N2 atmosphere (designated NiFeCo−N2-2 °C) displays the best catalytic properties after stability testing, exhibiting a high current density (9.06 mA cm−2 at 320 mV), low Tafel slope (72.9 mV dec−1), good stability (over 20 h), high turnover frequency (0.304 s−1), and high mass activity (46.52 A g−1 at 320 mV). Stability tests reveal that the hydroxide phase is less suitable for long-term use than catalysts with an oxide phase. Two causes are identified for the loss of stability in the hydroxide phase: a) Modeling of the distribution function of relaxation times (DFRT) reveals the increase in resistance contributed by various relaxation processes; b) density functional theory (DFT) surface energy calculations reveal that the higher surface energy of the hydroxide-phase catalyst impairs the stability. These findings represent a new strategy to optimize catalysts for water splitting.
AB - Trimetallic double hydroxide NiFeCo−OH is prepared by coprecipitation, from which three different catalysts are fabricated by different heat treatments, all at 350 °C maximum temperature. Among the prepared catalysts, the one prepared at a heating and cooling rate of 2 °C min−1 in N2 atmosphere (designated NiFeCo−N2-2 °C) displays the best catalytic properties after stability testing, exhibiting a high current density (9.06 mA cm−2 at 320 mV), low Tafel slope (72.9 mV dec−1), good stability (over 20 h), high turnover frequency (0.304 s−1), and high mass activity (46.52 A g−1 at 320 mV). Stability tests reveal that the hydroxide phase is less suitable for long-term use than catalysts with an oxide phase. Two causes are identified for the loss of stability in the hydroxide phase: a) Modeling of the distribution function of relaxation times (DFRT) reveals the increase in resistance contributed by various relaxation processes; b) density functional theory (DFT) surface energy calculations reveal that the higher surface energy of the hydroxide-phase catalyst impairs the stability. These findings represent a new strategy to optimize catalysts for water splitting.
KW - density functional calculations
KW - electrocatalysis
KW - hydroxides
KW - porous materials
KW - relaxation processes
UR - http://www.scopus.com/inward/record.url?scp=85101399825&partnerID=8YFLogxK
U2 - 10.1002/cssc.202002946
DO - 10.1002/cssc.202002946
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C2 - 33561301
AN - SCOPUS:85101399825
SN - 1864-5631
VL - 14
SP - 1737
EP - 1746
JO - ChemSusChem
JF - ChemSusChem
IS - 7
ER -