The present application claims priority to Korean Patent Application No. 10-2023-0146956, filed on Oct. 30, 2023, the entire contents of which are incorporated herein for all purposes by this reference.
The present disclosure relates to a MoS2—Ni electrode and, in more detail, to a method for manufacturing an alkaline electrolysis electrode through co-sputtering.
As methods of forming a 1T structure of MoS2 in the related art, there are electrochemical and physical delamination, surface treatment, physical deformation (strain effect), transition metal doping, etc.
The method using electrochemical and physical delamination, which is a well known method, is to perform delamination on MoS2 using lithium (Li) atoms and can ensure a high 1T yield, but has a problem that it is difficult to be applied for a area and large has difficulty in commercialization of actual electrodes as a nano-scale process. The method using surface treatment involves techniques such as plasma and Ar gas treatment to induce deformation of Mo—S bond, thereby forming a 1T structure, but has a problem that the 1T yield is low as 15 to 50%.
The method using physical deformation ensures a 1T structure through structural deformation by applying physical force to a target material ((2H MOS2 sheets) and has a high 1T structure yield, but can ensure excellent performance only when applying deformation of 10 to 11% to generate structural deformation. However, there is only a result by calculation and it is practically difficult to maintain a structure by applying strain over 10% to a molecular structure and there is a limitation in application to a bulky electrode.
The method using transition metal doping, which ensures a 1T structure by generating a gliding effect on the S atomic plane by doping 2H MOS2 with transition metal, can ensure various 1T yields, depending on transition metal and uses hydrothermal synthesis for such doping, but has a problem that multiple steps are required and the cost is increased in electrodeionization back from a powder type.
An objective of the present disclosure is to improve a 1T structure yield through a single process and provide an electrolysis electrode with high activity in alkaline water electrolysis.
In order to achieve the objectives, a method for manufacturing an electrode using co-sputtering according to an embodiment of the present disclosure includes: preparing a substrate in a chamber; preparing MoS2 and Ni as sputter targets in the chamber; pre-sputtering the sputter targets; and simultaneously depositing the sputter targets on the substrate.
The substrate may be Ni foam or Ni coin.
The sputter target MoS2 and the sputter target Ni may be different in power supply type.
Power may be supplied in an RF type for the sputter target MOS2.
Power may be supplied in a DC type for the sputter target Ni
Power of the sputter target MoS2 may be 100 to 300 W.
Power of the sputter target Ni may be 5 to 50 W.
Time for the simultaneous deposition may be 1 to 5 hours (hr).
The present disclosure has effects of being able to provide an alkaline electrolysis electrode having a 1T structure through Ni doping and improve hydrogen evolution reaction activity and dynamic operation responsiveness in alkaline water electrolysis.
Further, the present disclosure has effects of being able to manufacture an electrode through a single process using co-sputtering, easily control the doping amount of elements, and achieve a large-area electrode.
The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee.
Hereafter, embodiments of the present disclosure will be described in detail so that those skilled in the art can easily achieve the present disclosure. However, the present disclosure may be modified in various different ways and is not limited to the embodiments described herein.
A method for manufacturing an electrode through co-sputtering according to an embodiment of the present preparing a substrate in a chamber; disclosure includes: preparing MoS2 and Ni as sputter targets in the chamber; pre-sputtering the sputter targets; and simultaneously the sputter targets on the substrate.
The substrate may be washed through sonication to remove an oxide film and impurities on the substrate before it is put (prepared) into the chamber and the washing may use KOH, HCL, or DI water. In this case, a KOH solution, DI water, and an HCl solution may be sequentially used and the sonication may be simultaneously performed.
The substrate may be a Ni base material and the Ni base material may be a Ni foam or Ni coin type.
As the sputter targets MoS2 and Ni may be used. The sputter target MoS2 may be a main structure material constituting an electrode and the sputter target Ni may be a doping material for forming a 1T structure with respect to the MoS2 structure.
The sputter target Ni can ensure a 1T structure of an electrode through Ni doping and can improve adsorption with a Ni base material (Ni foam or Ni coin) that is usually used in alkaline water electrolysis, which can improve hydrogen adsorption energy for high hydrogen evolution reaction activity through the 1T structure and can activate an electrochemically inactive basal plane through Ni doping.
The sputter target MoS2 and the sputter target Ni may be different in power supply type. For example, power may be supplied in an RF type for the sputter target MoS2 and power may be supplied in a DC type for the sputter target Ni.
Further, power of the sputter target MoS2 may be 100 to 300 W. Power of the sputter target Ni may be 5 to 50 W. Accordingly, the sputter target MoS2 may form the main structure of an electrode and the sputter target Ni may be configured as a doping material.
The co-sputtering is performed as a process of single step, so it is possible to expect reduction of costs in manufacturing of an electrode, and simultaneously, it is possible to easily control the Ni doping amount by controlling power of a sputter target gun and it is possible to manufacture a large-area electrode.
Time for the simultaneous deposition may be 1 to 5 hours (hr).
Hereafter, the present disclosure is described in more detail through embodiments. The following embodiments are only examples for helping understand the present disclosure without limiting the present disclosure.
A nickel substrate (Ni foam) is prepared into a chamber, sonication is performed on the nickel substrate in 1 mole of KOH solution for 2 minutes (min) to remove an oxide film and impurities on the prepared substrate, the substrate is washed in DI water through sonication, the substrate is immersed in an HCl solution of 20 wt %, and then washed again in DI water through sonication (washing of substrate). The washed substrate is moved into a main chamber from the load lock chamber, pressure is set at ˜10−3 torr using a rotary chamber, and then a vacuum is produced at 5×10−6 torr using a turbo molecular pump (chamber vacummized). The inside of the chamber is set at a work pressure of 5×10−3 torr using a Baratron gauge by sending Ar gas at 50 sccm (chamber pressure set). Thereafter, MoSz (diameter: 4 inch, thickness: 14 inch, purity: 99.9%) and Ni (diameter: 4 inch, thickness: 2 mm, purity: 99.99%) are prepared as sputter targets, and then pre-sputtering is performed on the sputter targets at 100 W for MoS2 and 10 W for Ni for 5 minutes (min) to remove impurities on the surfaces of the sputter targets and check production of plasma with the shield of the substrate closed (pre-sputtering). Thereafter, co-sputtering is performed at a pressure condition of 5×10−3 torr while maintaining the temperature of the substrate at 200° C. using a heater, a rotator is operated so that an electrode is uniformly deposited on the substrate, and MoS2 and Ni are simultaneously deposited through RF output and DC output, respectively, under the sputtering conditions in the following Table 1, whereby a MOS2/Ni electrode was manufactured (deposition of electrode).
An electrode was manufactured under the conditions of the following Table 1 using only MOS2 (diameter: 4 inch, thickness: ¼ inch, purity: 99.9%) by performing the same process as the above embodiment.
The weight ratios and molar ratios of the electrodes manufactured in the embodiment and the comparative example were shown in the following Table 1.
In Table 2, the weight ratio is the mass of each of MOS2 and Ni deposited on the electrode manufactured in the embodiment using a Soda Limed Glass (SLG) substrate, and the molar ratio was calculated on the basis of 160.07 g/mo for MoS2 and 58.69 g/mol for Ni.
Surface SEM images of electrodes manufactured under the output conditions of the sputter target Ni in the comparative example, embodiment 1, embodiment 2, and embodiment 3 are shown in
Referring
On the other hand, it can be seen that the electrodes manufactured by simultaneously doping MoS2 and Ni in the embodiments 1 to 3 have a surface structure in which the edge plan decreases and the basal plane is further exposed. However, it can be seen that higher power for the sputter target Ni collapses the MoS2 structure, as in the embodiment 3. Accordingly, it can be seen that when the power for the sputter target Ni increases, the function of doping is substantially not achieved.
Expression SEM images of the electrodes manufactured under the output condition and the deposition time for a sputter target MoS2 in the embodiment and embodiments 4 to 7 are shown in
Further, an X-ray Diffraction (XRD) analysis result of the electrodes manufactured in the embodiments 5 to 7 is shown in
Referring to the electrodes manufactured in the embodiments 2, 4, and 5 in
Referring to
X-ray Photoelectron Spectroscopy (XPS) analysis was performed on the electrodes manufactured in the comparative example and the embodiments 1, 2, 4, and 5, and the analysis result is shown in
In
Referring to
X-ray Photoelectron Spectroscopy (XPS) analysis was performed on the electrodes manufactured in the embodiments 5 to 7, and the analysis result is shown in
Referring to
HR-TEM image analysis was performed on the electrodes manufactured in the comparative example and the embodiments 5 and 7, and the analyzed TEM image results are shown in
Referring to
Selected Area Electron Diffraction (SAED) pattern images of the electrode manufactured in the comparative example and the embodiments 5 and 7 were analyzed and are shown in
Referring to
Electrochemical surface area (ECSA) analysis was performed through a three-electrode system, and in more detail, graphite was used for a counter electrode (CE), Hg/HgO was used for a reference electrode (RE), and the electrode manufactured in the above embodiment was used for a WE (work electrode, electrode reaction area 0.785 cm2). Electrolyte was 1M of KOH solution, an ECSA was measured at scan rates of 20, 40, 60, 80, 100 mV/s through cyclic voltammetry (CV) in a non-Faraday region ((−0.65 to −0.55 V vs Hg/Hg0, 0.273˜0.373 V VS RHE), the halves of the sum of redox current density at medium voltage (−0.6 V vs Hg/Hg0, 0.32 V vs RHE) of CV at respective scan rates were plotted in a scan rate vs current density graph, and then a slope was obtained through linear fitting (slope value was ECSA, mF/cm2).
Electrochemical surface area (ECSA) analysis was performed on the electrodes manufactured in the embodiments 2, 4, and 5, and the analysis results are shown in
Referring to
Electrochemical surface area (ECSA) analysis was performed on the electrodes manufactured in the embodiments 5 to 7, and the analysis results are shown in
Referring to
Hydrogen evolution reaction (HER) analysis was performed through a three-electrode system, and in more detail, graphite was used for a counter electrode (CE), Hg/HgO was used for a reference electrode (RE), and the electrode manufactured in the above embodiment was used for a WE (work electrode, electrode reaction area 0.785 cm2). Electrolyte was 1M of KOH solution and a polarization curve was plotted to current density of ˜−64 mA/cm2 after measurement was performed at a scan rate of 5 mV/s in the ranges of −0.924 to −1.6 V vs Hg/HgO and 0 to 0.676 V vs RHE. In Tafel, a measured polarization curve was plotted for a log value of current density vs and overvoltage (a value of a polarization voltage in HER, ideal voltage of hydrogen evolution reaction was 0 V) and then Tafel slope was obtained using linear fitting. EIS was performed at −1.1 V vs Hg/Hg. and 0.176 V vs RHE to minimize the influence by hydrogen bubbles and measurement was performed within the range of 100 kHz˜0.1 Hz.
(1) HER Analysis According to Sputter Target Ni Power
Hydrogen evolution reaction (HER) analysis was performed on the electrodes manufactured in the embodiments 1 to 3 and the analysis results are shown in
Values of overvoltage η and charge transfer resistance Rct are shown in the following Table 3 on the basis of the analysis results shown in
Referring to
(2) HER Analysis According to Sputter Target MoS2 Power
Hydrogen evolution reaction (HER) analysis was performed on the electrodes manufactured in the embodiments 2, 4, and 5 and the analysis results are shown in
Values of overvoltage η and charge transfer resistance Rct are shown in the following Table 4 on the basis of the analysis results shown in
Referring to
(3) HER Analysis According to Deposition Time
Hydrogen evolution reaction (HER) analysis was performed on the electrodes manufactured in the embodiments 5 to 7 and the analysis results are shown in
Values of overvoltage η and charge transfer resistance Rct are shown in the following Table 5 on the basis of the analysis results shown in
Referring to
The overvoltages of the electrodes manufactured in the embodiments 2 to 7 according to the analysis shown in FIGS. 13A to 15C are shown in
The 1T yield, Cal, and overvoltage (current density of 10 mA/cm2) of the electrodes manufactured in the comparative example and the embodiments 1, 2, and 4 to 7 according to the analysis shown in
The electrode (base material Ni foam) manufactured in the embodiment 7 and having a size of 4.4×4.8 cm2 was configured as a cathode, an Ni foam (4.4×4.8 cm2) as configured as an anode, Zirfon UPT 500 was used as a diaphragm, 400 kgf was applied as load cell pressure, electrolyte was 30 wt % of KOH, an electrolyte flow rate was 500 sccm, and electrolyte temperature was 80° C., whereby a single cell was manufactured.
The same configuration as the application example 2 was applied and Ni—Fe LDH (4.4×4.8 cm2) was configured as an anode.
Comparative Group. Manufacturing of Single Cell
The same configuration as the application example 2 was applied and Ni foam (4.4×4.8 cm2) was configured as a cathode.
The configurations of the single cells according to the application example 1, the application example 2, and the comparative group are shown in the following Table 6.
Cell voltages according to current density of the single cells manufactured in the application example 1, the application example 2, and the comparative group were measure and the measured results are shown in
Referring to
Cell voltage over time of the single cell manufactured in the application example 1 was measured while applying constant current of 0.4 A/cm2, and the result is shown in
Dynamic operation performance evaluation according to on/off (start/stop) was performed on the single cell manufactured in the application example 1 and the result is shown in
Although embodiments of the present disclosure were described above in detail, the spirit of the present disclosure is not limited thereto and the present disclosure may be changed and modified in various ways on the basis of the basic concept without departing from the scope of the present disclosure described in the following claims.
Number | Date | Country | Kind |
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10-2023-0146956 | Oct 2023 | KR | national |