A HIGHLY ACTIVE AND DURABLE NON-NOBLE METAL-SULPHIDE BASED HER CATALYST AND THE PREPARATION THEREOF
20230061774 · 2023-03-02
Inventors
Cpc classification
C25B11/091
CHEMISTRY; METALLURGY
C25B11/052
CHEMISTRY; METALLURGY
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
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
International classification
C25B11/091
CHEMISTRY; METALLURGY
Abstract
A highly active and exceptionally durable non-noble metal-sulphide based Hydrogen Evolution Reaction (HER) catalyst and the preparation thereof. More particularly, provided is a highly active earth abundant metal-sulphide based HER catalyst with exceptionally durable hydrogen evolution activity even after 100 hrs.
Claims
1. A Hydrogen Evolution Reaction (HER) catalyst comprising a 3R-MoS.sub.2-Ni.sub.xS.sub.y catalyst; wherein x=1,3 and y=1,2,4.
2. The HER catalyst as claimed in claim 1, wherein said catalyst shows a stability in alkaline media even after 100 hrs.
3. The HER catalyst as claimed in claim 1, wherein said catalyst needs overpotentials of (η20) 21 mV and (η100) 85 mV to reach the current densities of 20 and 100 mA cm.sup.−2, respectively in 1M KOH at the scan rate of 2 mVs.sup.−1.
4. The HER catalyst as claimed in claim 1, wherein said catalyst shows an exchange current density of 2.04 mA cm.sup.−2 at 0V.
5. The HER catalyst as claimed in claim 1, wherein said catalyst requires over potential of (η100) 450 mV to reach the current density of 100 mA cm' in OER (oxygen evolution reaction).
6. A method of synthesizing a HER catalyst comprising 3R-MoS.sub.2-Ni.sub.xS.sub.y catalyst; wherein x=1,3 and y=1,2,4, wherein said catalyst is synthesized by a hydrothermal process comprising the steps of: (a) dissolving (NH.sub.4).sub.6Mo.sub.7O.sub.24.4H.sub.2O (Ammonium molybdate tetrahydrate), Ni (NO.sub.3).sub.2.6H.sub.2O (Nickel nitrate hexahydrate) and (NH.sub.4).sub.2CS (Thiourea) in water; and (b) maintaining the reaction mixture at a temperature in the range of 150-250° C. for the period of 8-16 hrs in an autoclave reactor to afford black colored product of 3R-MoS.sub.2-Ni.sub.xS.sub.y catalyst; wherein x=1,3 and y=1,2,4.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0031]
[0032]
[0033]
[0034]
DETAILED DESCRIPTION OF THE INVENTION
[0035] The invention will now be described in detail in connection with certain preferred and optional embodiments, so that various aspects thereof may be more fully understood and appreciated.
[0036] The present invention provides a highly active metal-sulphide based catalyst for HER. The catalyst is based on unique combination of earth abundant metal-sulphides system, which is exceptionally stable and durable with negligible loss of activity even after 100 hrs.
[0037] In an embodiment the present invention provides an extremely active electrocatalysts for producing the Hydrogen (H.sub.2) through water alkali electrolyser; wherein said catalyst is composed of 3R-MoS.sub.2 with different polymorphs of Ni.sub.xS.sub.y (wherein x=1,3 and y=1,2,4 for HER and OER in alkaline media. The efficient electrocatalysts require very less over potential to reach the current density of 100 mA cm.sup.−2 (η.sub.100) 85 mV for HER and (η.sub.100)+450 mV for OER.
[0038] Mo exists as 1T, 2H and 3R polymorphs. 2H MoS.sub.2 is bulk layered, similar to graphene, and has low activity. 1T MoS.sub.2 is converted to 2H MoS.sub.2 at high temperature 3R has few layers, a large surface area and is difficult to synthesize. However, 3R is more stable in comparison to other two polymorphs and is therefore difficult to form. The 3R polymorph of MoS.sub.2 is in conjunction with NiS, NiS.sub.2 and Ni.sub.3S.sub.4.
[0039] Another embodiment of the present invention provides a process for the preparation of a highly active earth abundant metal-sulphides based catalyst for HER; wherein said process comprises of dissolving (NH.sub.4).sub.6 Mo.sub.7O.sub.24.4H.sub.2O (Ammonium molybdate tetrahydrate), Ni (NO.sub.3).sub.2.6H.sub.2O (Nickel nitrate hexahydrate) and (NH.sub.4).sub.2CS (Thio urea) in water and maintaining the reaction mixture at a temperature in the range of 150-250° C. for the period of 8-16 hrs in an autoclave reactor to afford black coloured product of 3R-MoS.sub.4-Ni.sub.xS.sub.y catalyst; wherein x=1,3 and y=1,2,4.
[0040] Yet another embodiment of the present invention provides a highly active metal-sulphide based catalyst for HER; wherein said catalyst shows a notable stability in alkaline media with a negligible loss of the activity even after 100 hrs. Thus, the heterostructure of 3R-MoS.sub.2-Ni.sub.xS.sub.y catalyst becomes very stable and durable for producing the large-scale hydrogen in water alkali electrolysers for industrial application.
[0041] The electrochemical HER performance of the MNS catalyst is carried out in 1M KOH at the scan rate of 2 mVs.sup.−1. The MNS catalyst (3R-MoS.sub.2-Ni.sub.3S.sub.4-NiS.sub.2-NiS) needs overpotentials of as low as 21 and 85 mV to reach the current densities of 20 and 100 mA cm.sup.−2 respectively. This is three times lower than that of NS (Ni.sub.3S.sub.4-NiS.sub.2) catalyst. The Tafel plots are used to understand the kinetics of the catalysts. The Tafel slope of MNS i.e. 82 mV dec.sup.−1 is much lower than that of NS i.e., 112 mV dec.sup.−1. The MNS catalysts are following the Volmer-Heyrovsky mechanism, i.e., electrochemical desorption reaction. MNS catalyst demonstrates an exchange current density of 2.04 mA cm-2 at OV vs RHE which is better than that of Pt/C, the benchmark catalyst. Higher the exchange current density, better is the intrinsic activity of the catalysts. The comparison of HER data for the MNS catalysts with standard is summarized below in Table-1.
[0042] The MNS catalyst of the present invention is tried for oxygen evolution reaction (OER) in same electrolyte solution in 1M KOH. MNS catalysts possess better activity than standard Ru/C. MNS catalyst requires an overpotential of as low as 450mV to reach a current density of 100 mA cm.sup.−2, whereas the standard Ru/C needs 510 mV to reach the same current density (100 mA cm.sup.−2) as seen in
TABLE-US-00001 TABLE 1 Mass η.sub.20 η.sub.100 J.sub.200 Tafel J.sub.0 loading (mV) @ (mV) @ (mA cm.sup.−2) (mV (mA Catalyst (mg) mA cm.sup.−2 mA cm.sup.−2 @ mV dec.sup.−1) cm.sup.−2) NF — 127 248 56 102 1.14 Pt/C 9.3 — 76 363 85 1.16 NS 9.5 85 187 120 112 1.47 MNS 9.3 21 85 437 82 2.04
TABLE-US-00002 TABLE 2 Mass loading η.sub.50 (mV)@ η.sub.100 (mV)@ Catalyst (mg) mA cm.sup.−2 mA cm.sup.−2 NF — 510 560 Ru/C 9.3 470 510 NS 9.5 420 480 MNS 9.3 390 450
[0043]
[0044] PXRD pattern is studied to understand the phase composition of MS and NS. In
[0045]
[0046] The MNS catalyst is tested for long term stability test in 1M KOH for 100 h. It is remarkable to observe a high activity retention of around 95% even after 100 h. (
[0047]
[0048] Table 3 below summarizes the data of comparison for HER performance of 3R-MoS.sub.2-Ni.sub.3S.sub.4-NiS.sub.2-NiS with other reported substrate independent catalyst based on Mo-Ni.sub.xS.sub.y (wherein x=1,3 and y=1,2,4).
TABLE-US-00003 TABLE 3 η.sub.x (mV)@ Tafel J.sub.0 Catalyst Synthesis mA cm.sup.−2 (mV dec.sup.−1) (mA cm.sup.−2) Electrolyte V doped NiS Hydrothermal/ 10@110 90 — 1M KOH Calcination rGo-MoS.sub.2 Hydrothermal 10@210 46 — 0.5M H.sub.2SO.sub.4 NiS.sub.2 Hydrothermal/ 1@79 63 1.47 1M KOH Calcination 10@174 82 0.5M H.sub.2SO.sub.4 50@ 283 1@50 10@148 50 @ 243 NiS.sub.2 Electrospining/ 10@450 83.5 — 0.5M H.sub.2SO.sub.4 Surfuriation N-rGO-Ni.sub.3S.sub.4—MoS.sub.2 Hydrothermal 10@94 56 — 0.5M H.sub.2SO.sub.4 Mo.sub.1—x—NiS.sub.2 Hydrothermal 10@297 94 8.5 × 10.sup.−3 0.5M H.sub.2SO.sub.4 Pt@NiS.sub.2—MoS.sub.2 Hydrothermal/CVD 10@34 40 — 0.5M H.sub.2SO.sub.4 3R—MoS.sub.2—Ni.sub.3S.sub.4—NiS.sub.2—NiS Hydrothermal 20@21 82 2.04 1M KOH 100@85
[0049] Table 4 below summarizes the data of comparison for HER performance of 3R-MoS.sub.2-Ni.sub.3S.sub.4-NiS.sub.2-NiS with other reported Phosphide based catalysts.
TABLE-US-00004 TABLE 4 η.sub.x (mV)@ Tafel J.sub.0 Catalyst Synthesis mA cm.sup.−2 (mV dec.sup.−1) (mA cm.sup.−2) Electrolyte N—CoP Hydrothermal/ 10@39 58 — 1M KOH Phosporiatiomn Mo—CoP Electrodepostion/ 10@76 52 — 1M KOH Phospodiation MoPS Electrodeposition 10@200 36 — 0.5M H.sub.2SO.sub.4 iP-CoP Hydrothermal/ 10@76 93 — 1M KOH Phosphoriation 50@ 135 CoFeP Electrodeposition/ 10@ 58 46 — 1M KOH Phosphoriation Co3S4—CoP Hydrothermal/ Onset@ 38 45 — 0.5M H.sub.2SO.sub.4 Phosphoriation/ 10@ 86 Sulfuriation
[0050] Table 5 below summarizes the data of comparison for HER performance of 3R-MoS.sub.2-Ni.sub.3S.sub.4-NiS.sub.2-NiS with other reported other polymorphs of MoS.sub.2 based catalysts.
TABLE-US-00005 TABLE 5 η.sub.x (mV)@ Tafel J.sub.0 Catalyst Synthesis mA cm.sup.−2 (mV dec.sup.−1) (mA cm.sup.−2) Electrolyte NiO@1T—MoS.sub.2 Hydrothermal Onset@ 0 52 0.44 1M KOH 10@46 1T′ MoS.sub.2 Hydrothermal 10@170 38 — 0.5M H.sub.2SO.sub.4 1T/2H MoS.sub.2 Hydrothermal 10@234 46 — 0.5M H.sub.2SO.sub.4 1T/2H MoS.sub.2 Hydrothermal 10@156 47.9 — 0.5M H.sub.2SO.sub.4 1T—MoS.sub.2-G/NF Solvothermal 10@117 38 0.056 0.5M H.sub.2SO.sub.4 1T/2H MoS.sub.2 Microwave 10@240 43.1 — 0.5M H.sub.2SO.sub.4 1T/2H MoS.sub.2 Pyrolysis 10@130 77 0.014 0.5M H.sub.2SO.sub.4
EXAMPLES
[0051] Following examples are given by way of illustration and therefore should not be construed to limit the scope of the invention.
Example 1: Synthesis of 3R-MoS.SUB.2.-Ni.SUB.x.S.SUB.y .(wherein x=1,3 and y=1,2,4) Catalyst
[0052] Prior to the synthesis procedure, a piece of Ni Foam (NF) 1×3 cm was cleaned with Distilled Water, 3M HCl solution, Distilled water and finally with ethanol for 10 mins each, then vacuum dried at a temperature range between 60° C. and 100° C. for 8-14 h. 10 mm (NH.sub.4).sub.6 Mo.sub.7O.sub.24.4H.sub.2O (Ammonium molybdate tetrahydrate), 50 mM of Ni (NO.sub.3).sub.2.6H.sub.2O (Nickel nitrate hexahydrate) and 500 mM of (NH.sub.4).sub.2CS (Thio urea) are dissolved in 80 mL milliQ water. The above solution is stirred at constant rotation speed of 500 RPM for complete dissolution of metal precursor in water. After complete dissolution, the above solution was transferred into the 100 mL Teflon lined stainless steel autoclave, the reaction was kept for4-16 h at the temperature of 150-250° C., after the reaction the temp was reduced to a temperature ranging between 25° C-35° C. Finally, black color product of 3R-MoS.sub.2-Ni.sub.xS.sub.y (wherein x=1,3 and y=1,2,4) material was filtered through vacuum suction filtration by milliQ water. The filtration process was continuously followed 3-5 times and used ethanol to remove the unreacted metal precursor during the reaction. After completion of the filtration process, the final product was dried the temperature ranging between 60° C-100 ° C. in oven for 8-14 h.
Example 2: Preparation of Electrodes
[0053] 70-90% of as synthesised catalyst (MNS, NS), 5-25% carbon black and 1-7% PVDF binder were added to the pestle mortar and ground for 3-5 mins clockwise and anticlockwise in the both directions. Then, 60μL -100μL of NMP (N-methyl Pyrrolidone) solvent is added to the above powder and grinding process was followed for again 3-5 mins in both directions. After grinding it was formed as a slurry. After making the slurry, it was loaded on washed 1 cm.sup.2 NF (Like a painting). It was coated three times. After each coating, NF was dried by hand drier for 1-2 mins with 15 cm gap between the NF and hand drier. After coating, the loaded NF was dried the temperature ranging between 60 ° C. -120° C. for 8-14 h.
Example 3: Electrochemical Hydrogen Evolution Reaction
[0054] The electrochemical HER and OER performance of the as prepared electrocatalyst is carried out in 1M KOH solution at the scan rate of 2 mV/s is to collect the LSV polarization curve in a three-electrode system. The as prepared catalysts as a working electrode, graphite rod and Saturated Calomel Electrode (SCE) are used as the counter and reference electrode respectively. All the potentials are converted into RHE.
ADVANTAGES OF THE INVENTION
[0055] One-pot synthesis [0056] Aqueous medium synthesis [0057] Highly surface-active unique microstructure and morphology [0058] Usage of highly active 3R polymorph of -MoS.sub.2 with Ni.sub.xS.sub.y [0059] Unique composition [0060] Substrate independent catalyst. [0061] Highly active and stable electrocatalysts in alkaline media. [0062] Scalable synthesis method.