CN114497574B - Self-supporting transition metal phosphide doped porous carbon film hydrogen evolution electrocatalytic material - Google Patents

Self-supporting transition metal phosphide doped porous carbon film hydrogen evolution electrocatalytic material Download PDF

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CN114497574B
CN114497574B CN202111457789.XA CN202111457789A CN114497574B CN 114497574 B CN114497574 B CN 114497574B CN 202111457789 A CN202111457789 A CN 202111457789A CN 114497574 B CN114497574 B CN 114497574B
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carbon film
transition metal
film
hydrogen evolution
self
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CN114497574A (en
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段东红
周娴娴
张庆杰
刘世斌
张鼎
卫国强
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Taiyuan University of Technology
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9075Catalytic material supported on carriers, e.g. powder carriers
    • H01M4/9083Catalytic material supported on carriers, e.g. powder carriers on carbon or graphite
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/8605Porous electrodes
    • 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

Abstract

The invention belongs to the technical field of electrocatalytic hydrogen evolution, and provides a self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material. The electrocatalytic material prepared by the invention has excellent electrocatalytic hydrogen evolution performance under alkaline and acidic conditions, and the catalyst is not easy to fall off.

Description

Self-supporting transition metal phosphide doped porous carbon film hydrogen evolution electrocatalytic material
Technical Field
The invention belongs to the technical field of electrocatalytic hydrogen evolution, and particularly relates to a self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material.
Technical Field
The technology for producing hydrogen by electrolyzing water provides a convenient and sustainable way for high-efficiency conversion and effective storage of electric energy, and is also an important way for preparing high-purity hydrogen. Although noble metals such as Pt have excellent hydrogen evolution catalytic performance, the noble metals have rare reserves in the crust, are expensive, and are not suitable for large-scale commercial application. Therefore, the development of efficient, low-cost and widely available non-noble metal hydrogen evolution electrocatalysts is an urgent need for solution.
Among the current non-noble metal hydrogen evolution electrocatalysts, transition Metal Phosphides (TMPs) have been widely used for hydrogen evolution reactions due to their good mechanical strength, electrochemical conductivity and chemical stability. However, the hydrogen evolution electrocatalyst is usually powder, and a binder is required to be added to prepare the electrode into suspension for coating, or the electrode is grown on various conductive matrixes such as glassy carbon, foam nickel mesh, foam copper mesh, foam nickel iron mesh, titanium sheet, copper sheet, carbon cloth and the like in situ. The addition of the polymer binder will greatly increase the electrical resistance of the electrocatalyst and reduce the electrochemical performance of the catalyst. And the catalyst is loaded on the conductive matrix, so that the electrocatalyst is easy to fall off from the surface of the electrode under high current density in the hydrogen evolution reaction process, and the stability is poor. Therefore, the loading of the high-activity metal phosphide hydrogen evolution catalyst on a proper conductive matrix is a key to improving the hydrogen evolution performance.
Disclosure of Invention
Aiming at the situation, the invention aims to provide a self-supporting hydrogen evolution electro-catalytic material which can effectively solve the problems of few active sites, low catalytic efficiency and poor stability of the existing hydrogen evolution electro-catalytic material.
In order to achieve the above purpose, the invention provides a self-supporting transition metal phosphide doped porous carbon film hydrogen evolution electrocatalytic material, which is prepared by calcining a transition metal doped carbon film and sodium phosphite in an argon atmosphere, and comprises the following specific operations:
taking a certain amount of transition metal doped carbon film and sodium hypophosphite according to the mass ratio of 1:5-1:10, and respectively placing the carbon film and the sodium hypophosphitePutting into two porcelain boats; transferring the mixture into a tube furnace, wherein sodium hypophosphite is arranged at the upstream side, and an MCNT@C carbon film is arranged at the downstream side; calcining at 350 deg.C for 2 hr under argon atmosphere, and raising temp. rate to 2 deg.C min -1 The method comprises the steps of carrying out a first treatment on the surface of the After naturally cooling to room temperature, a transition metal phosphide-doped carbon film was obtained and represented as an mpcnt@c carbon film.
Preparing the transition metal doped carbon film, namely placing the porous CNT@PAN film containing transition metal ions into a muffle furnace at 260 ℃ for pre-oxidation for 2 hours, wherein the heating rate is 2 ℃/min; pre-oxidizing, transferring to a tube furnace filled with a mixed gas of hydrogen and argon, carbonizing at 700-900 ℃ for 1 h, and heating at a speed of 5 ℃/min; finally, a transition metal doped carbon film is obtained and is marked as MCNT@C film, and M is Co, fe or Ni.
The preparation of the porous CNT@PAN film containing transition metal ions mainly comprises the steps of dissolving 0.5g of transition metal chloride in 10ml of ethylene glycol to form a solution A containing transition metal ions; 2g of carbon nano tube and 2g of polyacrylonitrile (PAN, MW=40000, > 99%) are dissolved in an organic solvent and magnetically stirred for 12 hours at 60-80 ℃ to form a uniform black solution B; mixing the solution A and the solution B, magnetically stirring for 5 hours to obtain uniform black casting solution, pouring the cooled solution on a glass plate, and scraping the solution into a liquid film with the thickness of 200+/-10 mu m by using a film coater; then the glass plate carrying the film layer is soaked in ultrapure water rapidly, after 24 hours of stabilization, the film is taken out of the water and naturally dried in the air, and then the vacuum drying is carried out for 4 hours at 90 ℃ to obtain the glass plate.
The transition metal chloride is CoCl 2 ·6H 2 O、FeCl 3 ·6H 2 O or NiCl.6H 2 O。
The organic solvent is N, N-dimethylformamide, dimethyl sulfoxide or N, N-dimethylacetamide.
The volume ratio of the mixed gas is 1:5 of hydrogen to argon, and the flow rate is 20-40 mL/min.
The beneficial effects of the invention are as follows: uniformly mixing a transition metal precursor, a carbon nano tube and a high polymer compound, coating the mixture into a high polymer film with a certain thickness, and carbonizing and phosphating the high polymer film to prepare the self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material; the metal phosphide is uniformly distributed in the carbon film, is tightly combined with the conductive matrix, is not easy to fall off, and can form a high conductive network by adding the carbon nano tube, meanwhile, the carbon film generated by carbonizing the high polymer compound is used as a supporting matrix of the catalyst, can generate a synergistic effect with the metal phosphide, reduces hydrogen evolution overpotential, and simultaneously has better hydrogen evolution catalytic performance in acidic and alkaline media.
Drawings
FIG. 1 is an X-ray diffraction pattern of the CoPCNT@C carbon film prepared in example 1;
FIG. 2 is a detailed scan of electrocatalytic hydrogen evolution under acidic conditions for an example;
FIG. 3 is a detailed scan of electrocatalytic hydrogen evolution under alkaline conditions for an example;
FIG. 4 is a graph showing the hydrogen evolution stability under alkaline conditions of example 1.
Detailed Description
The self-supporting hydrogen evolution electrocatalytic material prepared by different transition metal precursors is shown in the examples, and the electrocatalytic hydrogen evolution capability is effectively demonstrated by analyzing the scanning curve of the examples under the acid and alkali conditions.
Example 1
Weigh 0.5g CoCl 2 ·6H 2 O is dissolved in 10ml glycol to form Co-containing solution 2+ Is a solution A of (2); weigh 2g carbon nanotubes and 2g polyacrylonitrile (PAN, mw=40000),>99%) was dissolved in 21g of N, N-dimethylformamide and magnetically stirred at 70℃for 12 hours to form a uniformly black solution B. Mixing the solution A and the solution B, magnetically stirring 5h to obtain uniform black casting solution, pouring the cooled solution on a glass plate, and scraping the solution into a liquid film with the thickness of 200+/-10 mu m by using a film coater. Then the glass plate carrying the film layer is soaked in ultrapure water rapidly, after 24h is stabilized, the film is taken out of the water and naturally dried in the air, and then the vacuum drying is carried out at 90 ℃ for 4h, thus obtaining the porous Co-containing film 2+ Cnt@pan film.
Will contain Co 2+ The CNT@PAN film is placed in a muffle furnace at 260 ℃ for pre-oxidation 2h (the heating rate is 2 ℃/min), and the pre-oxidation is carried outMoving the carbon film to a tube furnace filled with a mixed gas of hydrogen and argon with the volume ratio of 1:5 and the flow rate of 30mL/min, carbonizing the carbon film at the temperature of 800 ℃ for 1 h (the heating rate is 5 ℃/min), and finally obtaining the transition metal doped carbon film which is marked as CoCNT@C.
And (3) taking a certain amount of CoCNT@C carbon film and sodium hypophosphite according to the mass ratio of 1:10, and respectively putting the carbon film and the sodium hypophosphite into two porcelain boats. Then transferred to a tube furnace with sodium hypophosphite upstream and a cocnt@c carbon film downstream. Calcining at 350deg.C under argon atmosphere for 2h at a heating rate of 2deg.C/min -1 . After naturally cooling to room temperature, a cobalt phosphide-doped carbon film was obtained and represented as a CoPCNT@C carbon film.
The CoPCNT@C carbon film material prepared in the embodiment is directly used as a working electrode, a Saturated Calomel Electrode (SCE) is used as a reference electrode, and a graphite carbon rod is used as a counter electrode for electrochemical test by 0.5M H 2 SO 4 Or 1M KOH aqueous solution is used as electrolyte, and a three-electrode testing system is adopted to perform performance test on an electrochemical workstation. LSV curves were tested.
FIG. 1 is an X-ray diffraction pattern of a CoPCNT@C carbon film prepared in example 1 of the present invention, showing that the sample prepared in example 1 has characteristic X-ray diffraction peaks typical of CoP; FIGS. 2 and 3 show the linear polarization curves of the CoPCNT@C carbon film prepared in example 1 of the present invention in acidic and alkaline solutions when the current density reached-20 mA cm -2 When the CoPCNT@C carbon film electrode is in an acidic solution and an alkaline solution, the overpotential of the CoPCNT@C carbon film electrode is-77 mV and-102 mV respectively; the test result shows that the CoPCNT@C carbon film electrode prepared in the embodiment 1 of the invention has outstanding electrocatalytic hydrogen evolution performance.
Example 2
Weigh 0.5g NiCl 2 ·6H 2 O is dissolved in 10ml glycol to form Ni-containing 2+ Is a solution A of (2); 2g carbon nanotubes were weighed with 2g polyacrylonitrile (PAN, mw=40000,>99%) was dissolved in 21g N, N-dimethylacetamide and magnetically stirred at 60 ℃ for 12 hours to form a homogeneous black solution B. Mixing the solution A and the solution B, magnetically stirring 5h to obtain uniform black casting solution, pouring the cooled solution on a glass plate, and scraping the solution into a liquid film with the thickness of 200+/-10 mu m by using a film coater. Then rapidly putting the glass plate with the film layerSoaking in ultrapure water, stabilizing 24. 24h, taking out the membrane from water, naturally airing in air, and vacuum drying at 90deg.C for 4. 4h to obtain porous Ni-containing material 2+ Cnt@pan film.
Will contain Ni 2+ Pre-oxidizing the CNT@PAN film in a muffle furnace at 260 ℃ for 2h, wherein the heating rate is 2 ℃/min; transferring the mixture to a tubular furnace filled with hydrogen and argon in a volume ratio of 1:5 and a flow rate of 40mL/min, carbonizing 1 h at 900 ℃ and heating at a rate of 5 ℃/min; finally, a transition metal doped carbon film is obtained and is marked as NiCNT@C.
And (3) taking a certain amount of NiCNT@C carbon film and sodium hypophosphite according to the mass ratio of 1:5, and respectively putting the NiCNT@C carbon film and the sodium hypophosphite into two porcelain boats. Then transferred to a tube furnace with sodium hypophosphite upstream and a NiCNT@C carbon film downstream. Calcining at 350deg.C under argon atmosphere for 2h at a heating rate of 2deg.C/min -1 . After naturally cooling to room temperature, a nickel phosphide-doped carbon film was obtained and represented as a NiPCNT@C carbon film.
The NiPCNT@C carbon film material prepared in the embodiment is directly used as a working electrode, a Saturated Calomel Electrode (SCE) is used as a reference electrode, and a graphite carbon rod is used as a counter electrode for electrochemical test by 0.5M H 2 SO 4 Or 1MKOH aqueous solution is used as electrolyte, and a three-electrode testing system is adopted to perform performance test on an electrochemical workstation. LSV curves were tested.
As shown in FIG. 2 and FIG. 3, the linear polarization curve of the NiPCNT@C carbon film prepared in example 2 of the present invention in an acidic and alkaline solution was measured when the current density reached-mA.cm -2 At this time, the overpotential of the NiPCNT@C carbon film electrode in acidic and alkaline solutions was-86 mV and-116 mV, respectively.
Example 3
Weigh 0.5g FeCl 3 ·6H 2 O is dissolved in 10ml glycol to form Fe-containing 3+ Is a solution A of (2); 2g carbon nanotubes were weighed with 2g polyacrylonitrile (PAN, mw=40000,>99%) was dissolved in 21g N, N-dimethylformamide and magnetically stirred at 80 ℃ for 12 hours to form a homogeneous black solution B. Mixing the solution A and the solution B, magnetically stirring 5h to obtain uniform black casting solution, pouring the cooled solution onto a glass plate, and scraping with a film coaterThe thickness of the liquid film is 200+/-10 mu m. Then the glass plate with the film layer is soaked in ultrapure water rapidly, after 24h is stabilized, the film is taken out of the water and naturally dried in the air, and then the porous Fe-containing film is prepared after 4h of vacuum drying at 90 DEG C 3+ Cnt@pan film.
Will contain Fe 3+ The CNT@PAN film is placed in a muffle furnace at 260 ℃ for pre-oxidation 2h (the heating rate is 2 ℃/min), the pre-oxidation is transferred into a tube furnace filled with hydrogen and argon mixed gas with the volume ratio of 1:5 and the flow rate of 20 mL/min, and 1 h (the heating rate is 5 ℃/min) is carbonized at 700 ℃ to finally obtain a transition metal doped carbon film which is marked as FeCNT@C.
And taking a certain amount of FeCNT@C carbon film and sodium hypophosphite according to the mass ratio of 1:10, and respectively putting the FeCNT@C carbon film and the sodium hypophosphite into two porcelain boats. Then transferred to a tube furnace with sodium hypophosphite upstream and FeCNT@C carbon film downstream. Calcining at 350deg.C under argon atmosphere for 2h at a heating rate of 2deg.C/min -1 . After naturally cooling to room temperature, an iron phosphide-doped carbon film was obtained and represented as FePCNT@C carbon film.
The FePCNT@C carbon film material prepared in the embodiment is directly used as a working electrode, a Saturated Calomel Electrode (SCE) is used as a reference electrode, and a graphite carbon rod is used as a counter electrode for electrochemical test by 0.5M H 2 SO 4 Or 1M KOH aqueous solution is used as electrolyte, and a three-electrode testing system is adopted to perform performance test on an electrochemical workstation. LSV curves were tested.
According to FIGS. 2 and 3, the linear polarization curves of FePCNT@C carbon films prepared in example 3 of the present invention in acidic and alkaline solutions are shown when the current density reaches-mA cm -2 The overpotential of the FePCNT@C carbon film electrode in the acidic and alkaline solutions is-99 mV and-136 mV respectively.
According to the embodiment, the metal phosphide is uniformly distributed in the carbon film, and is tightly combined with the conductive matrix and not easy to fall off by combining the embodiment with the attached drawing of the specification; the added carbon nano tube can form a high conductive network, and the carbon film generated by carbonizing the high molecular compound is used as a supporting matrix of the catalyst, can generate a synergistic effect with metal phosphide, reduces hydrogen evolution overpotential, and has good hydrogen evolution catalytic performance in acidic and alkaline media.

Claims (6)

1. A self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material is characterized in that metal phosphide is uniformly distributed in the carbon film, is tightly combined with a conductive matrix, forms a high-conductivity network by carbon nanotubes, and forms a porous carbon film hydrogen evolution electrocatalytic material by taking the carbon film generated by carbonizing a high-molecular compound as a supporting matrix of a catalyst and generating a synergistic effect with the metal phosphide;
the self-supporting transition metal phosphide doped porous carbon film hydrogen evolution electrocatalytic material is prepared by the following method, and the specific operation steps comprise:
taking a certain amount of transition metal doped carbon film and sodium hypophosphite according to the mass ratio of 1:5-1:10, and respectively putting the carbon film and the sodium hypophosphite into two porcelain boats; transferring the carbon film into a tube furnace, wherein sodium hypophosphite is arranged at the upstream side, and a transition metal doped carbon film is arranged at the downstream side; calcining at 350deg.C under argon atmosphere for 2h at a heating rate of 2deg.C/min -1 The method comprises the steps of carrying out a first treatment on the surface of the After naturally cooling to room temperature, a transition metal phosphide-doped carbon film was obtained and represented as an MPCNT@C carbon film.
2. A self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material as set forth in claim 1, wherein: preparing the transition metal doped carbon film, namely placing the porous CNT@PAN film containing transition metal ions into a muffle furnace at 260 ℃ for pre-oxidation for 2h, wherein the heating rate is 2 ℃/min; pre-oxidizing, transferring to a tube furnace filled with a mixed gas of hydrogen and argon, carbonizing at 700-900 ℃ for 1 h, and heating at a speed of 5 ℃/min; finally, a transition metal doped carbon film is obtained and is marked as MCNT@C film, and M is Co, fe or Ni.
3. A self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material as claimed in claim 2, wherein: the preparation of the porous CNT@PAN film containing transition metal ions mainly comprises the steps of dissolving 0.5g of transition metal chloride in 10ml of ethylene glycol to form a solution A containing transition metal ions; 2g of carbon nano tube and 2g of polyacrylonitrile are dissolved in an organic solvent and magnetically stirred for 12 hours at 60-80 ℃ to form a uniform black solution B; mixing the solution A and the solution B, magnetically stirring 5h to obtain uniform black casting solution, pouring the cooled solution on a glass plate, and scraping the solution into a liquid film with the thickness of 200+/-10 mu m by using a film coater; then the glass plate carrying the film layer is soaked in ultrapure water rapidly, after 24h is stabilized, the film is taken out of the water and naturally dried in the air, and then the film is dried in vacuum at 90 ℃ for 4h, thus obtaining the glass plate.
4. The self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material as set forth in claim 2, wherein the volume ratio of hydrogen to argon is 1:5 and the flow rate is 20-40 mL/min.
5. The self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material as set forth in claim 3, wherein said transition metal chloride is CoCl 2 ·6H 2 O、FeCl 3 ·6H 2 O or NiCl.6H 2 O。
6. A self-supporting transition metal phosphide-doped porous carbon film hydrogen evolution electrocatalytic material according to claim 3, wherein the organic solvent is selected from N, N-dimethylformamide, dimethyl sulfoxide or N, N-dimethylacetamide.
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