CN114524489A - Co with 2D/3D hybrid structure2P-CeOxPreparation method and application of integrated electrode - Google Patents

Co with 2D/3D hybrid structure2P-CeOxPreparation method and application of integrated electrode Download PDF

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CN114524489A
CN114524489A CN202210092904.6A CN202210092904A CN114524489A CN 114524489 A CN114524489 A CN 114524489A CN 202210092904 A CN202210092904 A CN 202210092904A CN 114524489 A CN114524489 A CN 114524489A
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ceo
urea
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杨丽君
于洋
张蕾
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Liaoning University
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
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    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/073Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
    • C25B11/091Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F2101/30Organic compounds
    • C02F2101/38Organic compounds containing nitrogen
    • YGENERAL 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
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Abstract

The invention relates to Co with a 2D/3D hybrid structure2P‑CeOxA preparation method and application of an integrated electrode belong to the technical field of catalysis. The preparation method comprises the following steps: soaking foam Nickel (NF) in Co (NO) solution3)26H2O、Ce(NO3)36H2Performing multi-potential deposition reaction in a mixed solution of O and NaCl, repeatedly washing with deionized water after reaction, and dryingDrying to obtain Co (OH)2‑CeOxa/NF electrode; mixing Co (OH)2‑CeOx/NF electrode in NaH2PO2Phosphorization under existence to obtain a target product Co2P‑CeOxa/NF electrode. The method has the characteristics of simplicity, convenience, high efficiency, low cost and low decomposition voltage required by electrocatalysis, and can be applied to the fields of electrocatalysis hydrogen production, urea degradation, small molecule catalytic oxidation and the like.

Description

Co with 2D/3D hybrid structure2P-CeOxPreparation method and application of integrated electrode
Technical Field
The invention relates to Co with a 2D/3D hybrid structure2P-CeOxA preparation method and application of an integrated electrode belong to the technical field of catalysis.
Background
Along with the social development and the improvement of the industrialization degree, the accompanying environmental pollution and the energy crisis are increasingly intensified, and researchers are promoted to explore and develop a high-efficiency sustainable green energy system. As a green and sustainable 'carbon-free' energy source, the hydrogen energy source has the characteristics of high energy, no pollution, good combustion performance and the like. The hydrogen production by electrocatalysis water splitting has the advantages of high product purity, zero emission and the like, and is considered to be an attractive hydrogen production technology. The urea is an ideal hydrogen storage material with application prospect due to low price, stability, relative innocuity, easy storage and transportation and higher energy density (16.9MJ/L) than liquid hydrogen. Electrocatalytic Urea Oxidation (UOR) is also recognized as an effective way to produce hydrogen from urea-rich wastewater. Compared with anodic oxidation reaction (OER, 1.23V vs standard hydrogen electrode potential (RHE)) for water decomposition, the theoretical potential (0.37V vs RHE) required by the UOR is lower, and the potential is greater to replace the OER to realize high-efficiency hydrogen production. However, UOR is essentially a slow kinetic process involving six electron transfer, requiring a suitable electrocatalyst to accelerate the slow reaction process of UOR, lowering the reaction energy barrier and thus achieving efficient urea electrolysis. To date, precious metal materials (such as platinum, rhodium, etc.) have outstanding electrocatalytic activity on UOR, but their rarity, high price, etc. limit their development in practical large-scale applications. Therefore, the research and development of the non-noble metal-based electrocatalyst with high efficiency, energy conservation and environmental protection, particularly the application of the bifunctional electrocatalyst in Hydrogen Evolution Reaction (HER) and UOR, has more important practical significance.
The transition metal phosphide is used as a novel bifunctional electrocatalyst, has the advantages of high conductivity of metalloid, low preparation cost, controllable central metal valence state and the like, and is widely applied in the fields of electrocatalysis of HER, UOR and the like. The cobalt phosphide has good corrosion resistance and good electrocatalytic activity in both acidic and alkaline systems. But business of businessThe industrialized cobalt phosphide is limited in wide application in the field of electrocatalysis due to the characteristics of high overpotential, low oxidation efficiency and the like. Recent researches show that the electronic structure of the transition metal phosphide can be effectively adjusted by introducing other metal elements or constructing a unique heterostructure, so that the conductivity of the transition metal phosphide is improved, and the intrinsic catalytic activity of the catalyst is further improved. Since CeOxHaving two stable and reversible oxidation states (Ce)4+/Ce3+) The reversible surface oxygen ion exchange capacity, good electron/ion conduction efficiency and excellent oxygen storage/release capacity, and oxygen vacancies are easily generated on a heterogeneous interface to improve the ionic conductivity, so the method has wide application prospect in the energy-related field. In view of cobalt phosphide and CeOxExcellent physical and chemical properties by constructing cobalt phosphide and CeOxThe heterostructure not only can form an optimized electronic structure on the surface of the catalyst by utilizing metal-phosphorus and metal-oxygen bonds, but also can adjust the proportion of metals with different valence states in the catalytic material to generate more vacancies or defects so as to promote the catalytic reaction.
Disclosure of Invention
One of the purposes of the invention is to provide Co with a 2D/3D hybrid structure2P-CeOxA preparation method of an integrated electrode.
Another object of the present invention is to provide a Co utilizing 2D/3D hybrid structure2P-CeOxAn application method for electrocatalytic hydrogen production by an integrated electrode and urea degradation.
In order to achieve the purpose, the invention adopts the technical scheme that:
co with 2D/3D hybrid structure2P-CeOxThe preparation method of the integrated electrode comprises the following steps: soaking foam Nickel (NF) in Co (NO) solution3)2 6H2O、Ce(NO3)3 6H2Performing multi-potential deposition reaction in a mixed solution of O and NaCl, repeatedly washing with deionized water after the reaction, and drying to obtain Co (OH)2-CeOxa/NF electrode; mixing Co (OH)2-CeOx/NF electrode in NaH2PO2Phosphating the mixture in the presence of oxygen to obtain a target product Co2P-CeOxa/NF electrode.
Further, in the above preparation method, the mixed solution contains 0.9mol/L Co (NO)3)2 6H2O、0.09mol/L Ce(NO3)3 6H2A mixed solution of O and 0.1mol/L NaCl in a volume of 70 mL.
Further, in the preparation method, the multi-potential deposition reaction takes a platinum wire as a counter electrode, an Ag/AgCl electrode as a reference electrode and NF as a working electrode.
Furthermore, in the above preparation method, the multi-potential deposition reaction is performed by depositing the Ag/AgCl material at-1.2V vs. 400s, then depositing the Ag/AgCl material at 0.5V vs. 50s, and the electrodeposition area is 10X 10mm2
Further, in the preparation method, the drying condition is drying at 60 ℃ for 12 hours.
Further, in the preparation method, the phosphorization is to prepare Co (OH)2-CeOxthe/NF electrode was placed in an alumina porcelain boat and placed in the middle of a tube furnace while the other was charged with 0.6g NaH2PO2The porcelain boat is placed in a pot containing Co (OH)2-CeOxThe porcelain boat of the/NF electrode keeps a distance of 10cm and is positioned at the upstream position of the gas path at N2The temperature was raised to 350 ℃ under the atmosphere and maintained for 2 hours.
Furthermore, in the preparation method, the temperature rise rate is 2 ℃/min.
The Co with 2D/3D hybrid structure prepared by the preparation method provided by the invention2P-CeOxThe integrated electrode is applied to electrocatalytic hydrogen production and urea degradation.
Further, the application and the method are as follows: co of 2D/3D hybrid structure2P-CeOxAn integrated electrode as a working electrode, a platinum wire as a counter electrode and Hg/HgO as a reference electrode are placed in a quartz reaction container to form a three-electrode system, and N is introduced into a KOH solution containing urea2And (3) the reaction is carried out for 20min until the reaction is saturated, and the rotating speed of 1600rpm is always kept in the process.
Further, in the above application, the KOH solution containing urea is a KOH solution containing 0.33mol/L urea and 1mol/L with pH of 13.7.
The invention has the beneficial effects that:
1. the Co2P-CeOx integrated electrode with a 2D/3D hybrid structure is constructed in a multi-potential deposition and low-temperature phosphorization mode, so that the conductivity is further improved, more active sites are exposed, the mass/charge transmission is promoted, the electronic structure is optimized, and the electrocatalytic activity and stability are improved.
2. By adopting the method of the invention, the urea is degraded while the electrocatalytic hydrogen production is carried out by adopting a two-electrode system in the alkaline medium containing the urea, and the potential of only 1.42V can reach 30mA/cm2The current density is reduced by 0.17V compared with the potential required by full water decomposition, the degradation efficiency of the electro-catalysis urea after 10 hours reaches 76.4 percent, and a new thought is provided for designing a novel multi-level hybrid structure integrated electrode.
3. The method has the characteristics of simplicity, convenience, high efficiency, low cost and low decomposition voltage required by electrocatalysis, and can be applied to the fields of electrocatalysis hydrogen production, urea degradation, small molecule catalytic oxidation and the like.
Drawings
FIG. 1 is Co2P-CeOxScanning Electron Micrograph (SEM) of/NF electrode.
FIG. 2 is Co2P-CeOx/NF、Co2P/NF and CeOxX-ray diffraction (XRD) spectrum of/NF electrode.
FIG. 3 is a graph showing the performance of electrocatalytic hydrogen evolution of different catalytic electrodes, wherein (a) is a polarization curve and (b) is a Tafel curve.
FIG. 4 is a graph of the performance of different catalytic electrodes for electrocatalytic urea oxidation, where (a) is the polarization curve and (b) is the Tafel curve.
FIG. 5 shows Co under a two-electrode system2P-CeOxA polarization curve diagram of the NF electrocatalytic hydrogen production and urea degradation.
FIG. 6 is a graph of urea degradation efficiency for a two-electrode system.
Detailed Description
Example 1
1) Foamed nickel (N)F,10×20×1mm3) The pretreatment of (1): sequentially performing ultrasonic treatment in 3mol/L HCl, ethanol and water for 15min to clean the surface, and drying for later use;
2) soaking NF in 70mL of 0.9mol/L Co (NO)3)2 6H2O、0.09mol/L Ce(NO3)3 6H2In the mixed solution of O and 0.1mol/L NaCl, a platinum wire is taken as a counter electrode, an Ag/AgCl electrode is taken as a reference electrode, NF is taken as a working electrode, a multi-potential step method is adopted to deposit for 400s by-1.2V vs. Ag/AgCl, then 0.5V vs. Ag/AgCl is adopted to deposit for 50s, and the electrodeposition area is 10 multiplied by 10mm2Repeatedly washing with deionized water, drying at 60 deg.C for 12h to obtain Co (OH)2-CeOxa/NF electrode;
3) mixing the prepared Co (OH)2-CeOxthe/NF electrode was placed in an alumina porcelain boat and placed in the middle of a tube furnace while the other was charged with 0.6g NaH2PO2The porcelain boat is placed in a pot containing Co (OH)2-CeOxThe porcelain boat of the/NF electrode keeps a distance of 10cm and is positioned at the upstream position of the gas path at N2Heating to 350 ℃ at the heating rate of 2 ℃/min in the atmosphere, and keeping for 2h to obtain the target product Co2P-CeOxa/NF electrode.
4) For comparison, Co (OH)2/NF electrode and CeOxthe/NF electrode was placed in an alumina porcelain boat and placed in the middle of a tube furnace while the other was charged with 0.6g NaH2PO2Is placed at a distance of 10cm from the porcelain boat and is located at the upstream position of the gas path at N2Raising the temperature to 350 ℃ at the temperature rise rate of 2 ℃/min in the atmosphere, and keeping the temperature for 2 hours to respectively obtain Co2P/NF electrode and CeOxa/NF electrode.
As can be seen from FIG. 1, the composite Co2P-CeOxIs a hybrid structure of a 2D nano sheet and a 3D nano flower. The XRD spectrum of figure 2 confirms that the composite material is Co2P and CeOxThe complex of (1).
Example 2
In a standard three-electrode system, a platinum wire is taken as a counter electrode, Hg/HgO is taken as a reference electrode, and the synthesized composite electrode is taken as a working electrodeIn a 1mol/L KOH solution (pH 13.7), according to ERHE=EHg/HgO+0.098+0.059pH converts the potential vs. hg/HgO to a potential vs. standard hydrogen electrode (RHE). Before each test, N is2The solution was pumped in for at least 20min until saturation and the rotation speed of 1600rpm was maintained throughout the test to facilitate surface bubble release. The overpotential (η) is based on η ═ ERHE-0. The test for Linear Sweep Voltammograms (LSV) (97% iR correction) was performed at a sweep rate of 5mV/s over a potential interval of 0 to-0.4V vs. RHE. Tafel slopes are obtained from η ═ a + blogJ, where η is the overpotential, b is the tafel slope, and J is the current density. The results are shown in FIG. 3.
As shown in FIG. 3 (a), Co2P-CeOxthe/NF electrode shows higher electrocatalytic HER performance and the current density is 10mA/cm2Only needs lower over potential 84mV which is lower than that of other electrode materials Co2P/NF(106mV)、CeOxNF (203mV) and NF (268 mV). The slope of the Tafel plot is shown in FIG. 3 (b), Co2P-CeOx/NF、Co2P/NF、CeOxTafel slopes of/NF and NF were 53.2, 55.5, 127.2 and 151.8mV/dec, Co2P-CeOxThe Tafel slope of/NF is minimum, which shows that the electrode has faster electron transfer efficiency and is more beneficial to electrocatalysis of HER.
Example 3
In a standard three-electrode system, a platinum wire is used as a counter electrode, Hg/HgO is used as a reference electrode, and the synthesized composite electrode is used as a working electrode. In a 1mol/L KOH solution (pH 13.7) containing 0.33mol/L urea, according to ERHE=EHg/HgO+0.098+0.059pH converts the potential vs. hg/HgO to a potential vs. standard hydrogen electrode (RHE). Before each test, N is2The solution was pumped in for at least 20min until saturation and the rotation speed of 1600rpm was maintained throughout the test to facilitate surface bubble release. And carrying out LSV test at a scanning speed of 5mV/s within a potential interval of 1.2-1.6V vs. Tafel slopes are obtained from E ═ a + blogJ, where E is the potential, b is the tafel slope, and J is the current density. The results are shown in FIG. 4.
As shown in FIG. 4 (a), Co2P-CeOxthe/NF shows the highest electrocatalytic activity, and the current density reaches 30mA/cm2The time overpotential only needs 1.37V, and Co2P/NF(1.38V)、CeOxThe potentials required by/NF (1.40V) and NF (1.48V) are both larger than that of Co2P-CeOxof/NF and with increasing current density, Co2P-CeOxThe performance of the/NF catalytic UOR is obviously superior to that of other materials. FIG. 4 (b) shows Tafel curves for different catalysts, Co2P-CeOxTaffel slopes of/NF (106mV/dec) are all lower than Co2P/NF(138mV/dec)、CeOxNF (162mV/dec) and NF (158mV/dec) indicate that they have more favorable UOR catalytic kinetics.
Example 4
A standard two-electrode system is adopted, and Co is used in an electrolytic cell containing 0.33mol/L urea and 1mol/L KOH solution respectively2P-CeOxThe results of the full hydrolysis test conducted with/NF as both cathode and anode are shown in FIG. 5.
The current density reaches 30mA/cm2The hydrogen production process only needs 1.42V potential for driving, and the full water decomposition (HER II OER) needs 1.59V for reaching the current intensity and is 0.17V higher than the HER II UOR, so that the high-efficiency energy-saving hydrogen production is realized. Cathode (H) in the electrolytic process2) And an anode (O)2) A large amount of bubbles are generated.
The two-electrode system is adopted to maintain the current density at 70mA/cm2Continuously electro-catalyzing urea oxidation, and monitoring the degradation content of urea in real time by adopting a dimethylaminobenzaldehyde-assisted ultraviolet-visible spectrum detection method. As shown in FIG. 6, after 10h of continuous electrolysis, the degradation efficiency of urea reaches 76.4%, and finally, the urea is degraded while the hydrogen is produced by electrocatalysis.

Claims (10)

1. Co with 2D/3D hybrid structure2P-CeOxThe preparation method of the integrated electrode is characterized by comprising the following steps of: soaking foam Nickel (NF) in Co (NO) solution3)2 6H2O、Ce(NO3)3 6H2Performing multi-potential deposition reaction in a mixed solution of O and NaCl, and repeatedly washing with deionized water after reactionDrying to obtain Co (OH)2-CeOxa/NF electrode; mixing Co (OH)2-CeOx/NF electrode in NaH2PO2Phosphorization under existence to obtain a target product Co2P-CeOxa/NF electrode.
2. The method according to claim 1, wherein the mixed solution contains 0.9mol/LCo (NO)3)2 6H2O、0.09mol/L Ce(NO3)3 6H2A mixed solution of O and 0.1mol/L NaCl in a volume of 70 mL.
3. The method according to claim 1, wherein the multi-potential deposition reaction is carried out by using a platinum wire as a counter electrode, an Ag/AgCl electrode as a reference electrode, and NF as a working electrode.
4. The method of claim 3, wherein the multi-potential deposition reaction is performed by depositing the alloy at-1.2V vs. Ag/AgCl for 400s and then at 0.5V vs. Ag/AgCl for 50s, and the electrodeposition area is 10 x 10mm2
5. The method according to claim 1, wherein the drying condition is drying at 60 ℃ for 12 hours.
6. The method of claim 1, wherein said phosphating is performed using prepared Co (OH)2-CeOxthe/NF electrode was placed in an alumina porcelain boat and placed in the middle of a tube furnace while the other was charged with 0.6g of NaH2PO2The porcelain boat is placed in a pot containing Co (OH)2-CeOxThe porcelain boat of the/NF electrode keeps a distance of 10cm and is positioned at the upstream position of the gas path at N2Raising the temperature to 350 ℃ under the atmosphere, and keeping the temperature for 2 h.
7. The method according to claim 6, wherein the temperature is raised at a rate of 2 ℃/min.
8. Co of 2D/3D hybrid structure prepared by the preparation method of claim 12P-CeOxThe integrated electrode is applied to electrocatalytic hydrogen production and urea degradation.
9. Use according to claim 8, characterized in that the method is as follows: co of 2D/3D hybrid structure2P-CeOxAn integrated electrode as a working electrode, a platinum wire as a counter electrode and Hg/HgO as a reference electrode are placed in a quartz reaction container to form a three-electrode system, and N is introduced into a KOH solution containing urea2And the rotating speed of 1600rpm is always kept in the process until the saturation.
10. The use according to claim 9, wherein the KOH solution containing urea is a 1mol/L KOH solution containing 0.33mol/L urea and having a pH of 13.7.
CN202210092904.6A 2022-01-26 2022-01-26 Co with 2D/3D hybrid structure2P-CeOxPreparation method and application of integrated electrode Withdrawn CN114524489A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017168126A1 (en) * 2016-03-31 2017-10-05 University Of Sunderland Electrodes
CN109174162A (en) * 2018-10-26 2019-01-11 江苏大学 A kind of Fe2O3 doping double-metal phosphide elctro-catalyst and its preparation method and application
CN111545227A (en) * 2020-05-22 2020-08-18 辽宁大学 3D nanosheet network structure bimetallic phosphorus oxide electrocatalyst and preparation method and application thereof
US20210348284A1 (en) * 2018-08-16 2021-11-11 Newsouth Innovations Pty Limited Trimetallic layered double hydroxide composition
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017168126A1 (en) * 2016-03-31 2017-10-05 University Of Sunderland Electrodes
US20210348284A1 (en) * 2018-08-16 2021-11-11 Newsouth Innovations Pty Limited Trimetallic layered double hydroxide composition
CN109174162A (en) * 2018-10-26 2019-01-11 江苏大学 A kind of Fe2O3 doping double-metal phosphide elctro-catalyst and its preparation method and application
CN111545227A (en) * 2020-05-22 2020-08-18 辽宁大学 3D nanosheet network structure bimetallic phosphorus oxide electrocatalyst and preparation method and application thereof
CN113637997A (en) * 2021-08-11 2021-11-12 广西师范大学 Co2P/CuP2Preparation method of/NF hydrogen evolution and oxygen evolution electrocatalyst

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Title
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王云龙;郑科城;孙善善;陈旭;: "循环伏安法电沉积镍-钴-磷/泡沫镍电极及其析氢催化活性研究" *

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