CN106824190B - WO (WO) 3-x Nanometer catalyst and its preparation and application - Google Patents

WO (WO) 3-x Nanometer catalyst and its preparation and application Download PDF

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CN106824190B
CN106824190B CN201710124940.5A CN201710124940A CN106824190B CN 106824190 B CN106824190 B CN 106824190B CN 201710124940 A CN201710124940 A CN 201710124940A CN 106824190 B CN106824190 B CN 106824190B
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CN106824190A (en
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李涛
黄瑞杰
郑婷婷
曾杰
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Institute of Advanced Technology University of Science and Technology of China
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652Chromium, molybdenum or tungsten
    • B01J23/6527Tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • B01J37/341Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation
    • B01J37/343Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation of ultrasonic wave energy
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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

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Abstract

The invention discloses a WO 3‑x The nano catalyst has a flake structure, wherein x is the number of oxygen defects, and x is more than or equal to 0.08 and less than or equal to 0.18. The invention also discloses the WO 3‑x A preparation method of a nano catalyst. The invention also discloses the WO 3‑x Application of the nano catalyst. The invention obtains WO by liquid phase ultrasonic stripping 3‑x The nanometer catalyst is used for preparing the nanometer catalyst,the high conductivity is good for the transmission of electrons in the catalytic process; the catalyst has moderate free energy of hydrogen adsorption, can effectively improve the catalytic activity of hydrogen production, has the performance close to that of the current commercial Pt/C catalyst, is low in price, has better stability, and is suitable for commercial application.

Description

WO (WO) 3-x Nanometer catalyst and its preparation and application
Technical Field
The invention relates to the technical field of catalysts, in particular to a WO (WO) 3-x Nano catalyst, its preparation and application.
Background
Since the seventies of the twentieth century, humans began to consider hydrogen as a carrier of energy. Since hydrogen molecules not only have the highest energy density, but also burn in the engine or are converted into electric energy in the fuel cell, by-products thereof are produced only with water and no other harmful substances. In contrast, fossil energy containing carbon generates harmful substances such as water and carbon dioxide after combustion, which causes great harm to the environment. It is well known that hydrogen is one of the most abundant elements in the crust, but under most conditions it does not exist in the form of molecular hydrogen, so we have to develop efficient and sustainable hydrogen production technology. However, most of the hydrogen has been obtained by reforming natural gas so far, and this process is not only required to consume fossil energy, but also inevitably generates carbon dioxide gas. Electrocatalytic production of hydrogen using renewable energy sources (e.g., solar energy) is a clean and sustainable method. As early as 1789, j.r.deiman has begun to study electrocatalytic water decomposition. The traditional commercial catalyst used for electrocatalytic aquatic hydrogen is Pt/C, and the catalyst has high catalytic performance, but the platinum element has little earth reserves and great extraction and synthesis difficulty. This results in an expensive catalyst, which severely limits its large-scale use.
The transition metal oxide elements are rich in total class, and the earth reserves are rich, can be used as a catalyst and is cheaper; the sheet sample with the two-dimensional crystal structure has larger specific surface area, more surface defects and more exposed active sites, and is favorable for the adsorption of hydrogen atoms. Oxygen defects are beneficial to increase the density of states of the sample near the fermi level, the conductivity of the oxide is improved, which facilitates electron transport during electrocatalysis. The oxygen defect provides proper free energy for hydrogen adsorption for the catalyst, and accelerates the catalytic reaction.
Disclosure of Invention
Based on the technical problems existing in the background technology, the invention provides a WO 3-x The nano catalyst has larger specific surface area, more defects and more exposed active sites, effectively improves the utilization rate of atoms, increases the conductivity due to oxygen defects, accelerates the electron transfer in the electrocatalytic process, provides moderate free energy of hydrogen adsorption, and favorably improves the electrocatalytic efficiency, thereby exerting the catalytic advantage of the nano catalyst in the electrolytic aquatic hydrogen reaction and developing wider application potential.
The invention provides a WO 3-x A nanocatalyst having a sheet structure wherein x is the number of oxygen defects.
Preferably, 0.08.ltoreq.x.ltoreq.0.18.
Preferably, the flake thickness is 5 to 6nm.
The invention also proposes the above WO 3-x The preparation method of the nano catalyst comprises the following steps: will W 18 O 49 Adding the precursor into a mixed solution of absolute ethyl alcohol and deionized water, then carrying out ultrasonic crushing and peeling, then cleaning, and freeze-drying to obtain WO 3-x A nano catalyst.
Preferably, the volume ratio of the absolute ethyl alcohol to the deionized water is 0.8-1.2: 0.8 to 1.2, W 18 O 49 The mass volume ratio (g/L) of the precursor to the mixed solution is 0.8-1.2: 0.8 to 1.2.
Preferably, the ultrasonic pulverization and peeling time is 4 to 6 hours.
Preferably, the freeze-drying temperature is-38 to-40 ℃ and the freeze-drying time is 22 to 26 hours.
Preferably, the specific operation of the washing is as follows: and (3) centrifugally separating the materials after ultrasonic crushing and stripping, and then ultrasonically washing the product obtained by centrifugation by using a polar solvent.
Preferably, the method comprises the steps of, the specific operation of cleaning is as follows: centrifuging the materials after ultrasonic crushing and stripping for 18-20 min at a rotation speed of 2000 rpm, ultrasonically washing for 1-2 min, adding deionized water, and centrifuging for 8-10 min at a rotation speed of 11000-13000 rpm.
Preferably, W 18 O 49 The precursor is prepared by the following process: adding tungsten hexachloride into absolute ethanol solution at normal temperature, stirring uniformly, performing hydrothermal reaction, cooling to room temperature, cleaning, and vacuum drying to obtain W 18 O 49 A precursor.
Preferably, the method comprises the steps of, the mass volume ratio (mg/mL) of the tungsten hexachloride to the absolute ethyl alcohol is 18-22: 0.8 to 1.2.
Preferably, the temperature of the hydrothermal reaction is 160-180 ℃, and the time of the hydrothermal reaction is 20-24 hours.
Preferably, the specific operation of the washing is as follows: centrifuging the cooled material at a rotation speed of 11000-13000 r/min for 8-10 min, then ultrasonically washing the centrifugate with absolute ethyl alcohol, centrifuging at a rotation speed of 11000-13000 r/min for 8-10 min, and then ultrasonically washing the centrifugate with absolute ethyl alcohol.
Preferably, the temperature of the vacuum drying is 50 to 60 ℃.
The invention also proposes the above WO 3-x The nano catalyst is applied to the reaction of hydrogen production by electrolysis of water.
The invention adopts a liquid phase ultrasonic crushing and stripping method to obtain WO 3-x The nano catalyst has the advantages that the thin sheet structure improves the atom utilization rate in the catalytic process, the oxygen defect improves the electrical conductivity of the catalyst, and moderate free energy of hydrogen adsorption is provided, so that the catalytic efficiency of the electrocatalytic process is facilitated. Compared with the traditional crystal material synthesis method, the method has the advantages of mild condition, simple procedure, greatly reduced synthesis cost and environmental protection in the synthesis process. The invention has great advantages in the aspect of electrocatalytic electrode reaction, and the activity of the invention is close to that of commercial PtAnd (3) the catalyst is good in stability.
WO obtained by the invention 3-x The nano catalyst is compared with a commercial Pt/C catalyst, and the current density of the nano catalyst is 10mA/cm in the process of electrolyzing aquatic hydrogen 2 The overpotential required was 38.8mV, and in equivalent cases, 23.1mV for a commercial catalyst Pt/C, indicating that the electrocatalytic performance of the present invention is close to that of a commercial catalyst. And after 1000 circles of cyclic voltammetry scanning, the performance of the catalyst is basically free from obvious attenuation, and further shows that the catalyst has good stability.
Drawings
FIG. 1 is a diagram of W obtained in example 5 of the present invention 18 O 49 Transmission electron microscopy of the precursor.
FIG. 2 shows WO obtained in example 5 of the present invention 3-x Transmission electron microscopy of nanocatalysts.
FIG. 3 is a diagram of WO obtained in example 5 of the present invention 3-x X-ray electron diffraction image of nanocatalyst.
FIG. 4 shows WO obtained in example 5 of the present invention 3-x The scanning transmission electron microscope of the nano catalyst is provided with a high-angle annular dark field image.
FIG. 5 is a diagram of WO obtained in example 5 of the present invention 3-x Of nano-catalysts an atomic force scan image.
FIG. 6 shows WO obtained in example 5 of the present invention 3-x Image of the resistivity of the nanocatalyst as a function of temperature.
FIG. 7 shows the present invention WO obtained in example 5 3-x Linear sweep voltammetric images of nanocatalysts and Pt/C catalysts.
FIG. 8 shows WO obtained in example 5 of the present invention 3-x Image of electrocatalyst electrocatalytic stability.
Detailed Description
The technical scheme of the invention is described in detail through specific embodiments.
Example 1
The invention proposes the above WO of 3-x The preparation method of the nano catalyst comprises the following steps: will W 18 O 49 Adding the precursor into a mixed solution of absolute ethyl alcohol and deionized water, then carrying out ultrasonic crushing and peeling, then cleaning, and freeze-drying to obtain WO 3-x Nanometer scale a catalyst.
Example 2
The invention proposes the above WO 3-x The preparation method of the nano catalyst comprises the following steps: will W 18 O 49 The precursor is added into a mixed solution of absolute ethyl alcohol and deionized water, and the volume ratio of the absolute ethyl alcohol to deionized water is 1:1, W 18 O 49 The mass volume ratio (g/L) of the precursor to the mixed solution is 1:1, then ultrasonic crushing and peeling, then cleaning, freeze drying to obtain WO 3-x A nano catalyst.
W 18 O 49 The precursor is prepared by the following process: adding tungsten hexachloride into absolute ethanol solution at normal temperature, stirring uniformly, performing hydrothermal reaction, cooling to room temperature, cleaning, and vacuum drying to obtain W 18 O 49 A precursor.
Implementation of the embodiments example 3
The invention proposes the above WO 3-x The preparation method of the nano catalyst comprises the following steps: will W 18 O 49 The precursor is added into a mixed solution of absolute ethyl alcohol and deionized water, and the volume ratio of the absolute ethyl alcohol to deionized water is 1:1, W 18 O 49 The mass volume ratio (g/L) of the precursor to the mixed solution is 1:1, then carrying out ultrasonic crushing and stripping for 6 hours, centrifuging the material after ultrasonic crushing and stripping for 18 minutes at a rotation speed of 2000 rpm, ultrasonically washing for 1 minute, adding deionized water, centrifuging for 10 minutes at a rotation speed of 11000 rpm, and freeze-drying at-40 ℃ to obtain WO 3-x A nano catalyst.
W 18 O 49 The precursor is prepared by the following process: adding tungsten hexachloride into absolute ethyl alcohol solution at normal temperature, and uniformly stirring, wherein the mass volume ratio (mg/mL) of the tungsten hexachloride to the absolute ethyl alcohol is 20:1, then carrying out a hydrothermal reaction at 180 ℃ for 20 hours, cooling to room temperature, centrifuging the cooled material at 11000 rpm for 10min, and then using the centrifuged productUltrasonic washing with absolute ethanol for 1min, centrifuging at 11000 rpm for 10min, ultrasonic washing the centrifugate with absolute ethanol, and vacuum drying at 60deg.C to obtain W 18 O 49 A precursor.
Example 4
The invention proposes the above WO 3-x The preparation method of the nano catalyst comprises the following steps: will W 18 O 49 The precursor is added into a mixed solution of absolute ethyl alcohol and deionized water, and the volume ratio of the absolute ethyl alcohol to deionized water is 1:1, W 18 O 49 The mass volume ratio (g/L) of the precursor to the mixed solution is 1:1, then carrying out ultrasonic crushing and stripping for 5 hours, centrifuging the material after ultrasonic crushing and stripping for 19 minutes at a rotation speed of 2000 rpm, ultrasonically washing for 2 minutes, adding deionized water, centrifuging for 9 minutes at a rotation speed of 12000 rpm, and freeze-drying at-40 ℃ to obtain WO 3-x A nano catalyst.
W 18 O 49 The precursor is prepared by the following process: adding tungsten hexachloride into absolute ethyl alcohol solution at normal temperature, and uniformly stirring, wherein the mass volume ratio (mg/mL) of the tungsten hexachloride to the absolute ethyl alcohol is 20:1, then carrying out hydrothermal reaction at 190 ℃ for 22 hours, cooling to room temperature, centrifuging the cooled material at 12000 rpm for 9min, then carrying out ultrasonic washing on the centrifuged product with absolute ethyl alcohol for 1.5min, centrifuging at 12000 rpm for 9min, then carrying out ultrasonic washing on the centrifuged product with absolute ethyl alcohol, and carrying out vacuum drying at 55 ℃ to obtain W 18 O 49 A precursor.
Example 5
The invention proposes the above WO 3-x The preparation method of the nano catalyst comprises the following steps:
adding tungsten hexachloride into absolute ethyl alcohol solution at normal temperature, and uniformly stirring, wherein the mass volume ratio (mg/mL) of the tungsten hexachloride to the absolute ethyl alcohol is 20:1, then carrying out a hydrothermal reaction at 160 ℃ for 24 hours, cooling to room temperature, centrifuging the cooled material at 13000 rpm for 8min, and then carrying out ultrasonic washing on the centrifuged product with absolute ethanol for 2min, centrifuging at 13000 rpm for 8min, ultrasonic washing the centrifugate with absolute ethanol, and vacuum drying at 50deg.C to obtain W 18 O 49 A precursor;
will be 20mgW 18 O 49 The precursor is added into a mixed solution of 10mL of absolute ethyl alcohol and 10mL of deionized water, and the volume ratio of the absolute ethyl alcohol to the deionized water is 1:1, W 18 O 49 The mass volume ratio (g/L) of the precursor to the mixed solution is 1:1, then carrying out ultrasonic crushing and stripping for 5 hours, centrifuging the material after ultrasonic crushing and stripping for 20 minutes at a rotation speed of 2000 rpm, ultrasonically washing for 2 minutes, adding deionized water, centrifuging for 8 minutes at a rotation speed of 13000 rpm, and freeze-drying at-40 ℃ for 24 hours to obtain WO 3-x Nanometer scale catalytic reaction and (3) an agent.
According to the detection, WO obtained in this example 3-x The stoichiometric ratio of tungsten to oxygen in the nano catalyst is 1:2.82, the thickness of the lamellar structure is 5nm.
Experimental example 6
5mg of WO obtained in example 5 3-x Adding the nano catalyst into a mixed solution of 0.5mL of absolute ethyl alcohol, 0.46mL of deionized water and 0.04mL of perfluorosulfonic acid, carrying out ultrasonic treatment for 0.5H, then dripping 10 mu L of the solution onto a glassy carbon electrode with the diameter of 5mm, drying, and taking the solution as a working electrode and adding 0.5mol/L H 2 SO 4 The activity of the catalyst as hydrogen for electrolysis of water was measured in the solution. The potential sweep speed was 2mV/s, the electrode rotation speed was 1600 rpm, the resulting linear scan curve is shown in fig. 7. The current density in the hydrogen production process is 10mA/cm 2 The overpotential required was 38.8mV, whereas the overpotential required for Pt/C as a commercial catalyst was 23.1mV in the same case, indicating the WO of the invention 3-x Nanocatalyst performance has been approximated to commercial catalysts. In addition, WO of the invention 3-x After 1000 circles of cyclic voltammetry scanning, the current density of the nano catalyst is 10mA/cm 2 The overpotential required is 40.2mV, which indicates that the activity of the catalyst is not obviously attenuated, i.e. the stability of the catalyst is good.
The foregoing is only a preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art, who is within the scope of the present invention, should make equivalent substitutions or modifications according to the technical scheme of the present invention and the inventive concept thereof, and should be covered by the scope of the present invention.

Claims (2)

1. WO (WO) 3-x A nanocatalyst, characterized in that it has a flake structure, wherein x is the number of oxygen defects;
the thickness of the flake is 5nm;
the oxygen defect provides a moderate free energy of hydrogen adsorption;
3-x=2.82;
said WO 3-x The preparation method of the nano catalyst comprises the following steps:
adding tungsten hexachloride into absolute ethanol solution at normal temperature, stirring uniformly, wherein the mass of tungsten hexachloride is 20mg, the volume of absolute ethanol is 1 mL, then carrying out hydrothermal reaction, the hydrothermal reaction temperature is 160 ℃, the hydrothermal reaction time is 24 hours, cooling to room temperature, centrifuging the cooled material at 13000 rpm for 8 minutes, then carrying out ultrasonic washing on the centrifuged product for 2 minutes by using absolute ethanol, centrifuging at 13000 rpm for 8 minutes, carrying out ultrasonic washing on the centrifuged product by using absolute ethanol, and carrying out vacuum drying at 50 ℃ to obtain W 18 O 49 Precursor(s) a body;
will be 20mgW 18 O 49 The precursor is added into a mixed solution of 10mL of absolute ethyl alcohol and 10mL of deionized water, and the volume ratio of the absolute ethyl alcohol to the deionized water is 1:1, W 18 O 49 Precursor quality is 1 g, the volume of the mixed solution is 1L, ultrasonic crushing and stripping are carried out for 5 hours, then ultrasonic crushing and stripping materials are centrifuged for 20 minutes at a rotation speed of 2000 rpm, ultrasonic washing is carried out for 2 minutes, deionized water is added, centrifugal separation is carried out for 8 minutes at a rotation speed of 13000 rpm, and freeze drying is carried out for 24 hours at-40 ℃ to obtain WO 3-x A nano catalyst.
2. A WO as claimed in claim 1 3-x The nano catalyst is applied to the reaction of hydrogen production by electrolysis of water.
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CN107715863B (en) * 2017-09-30 2020-04-28 五邑大学 Preparation method of anoxic tungsten oxide photocatalyst
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