CN115763845B - Preparation method of chromium-based inorganic matter coupled transition metal nitrogen-doped carbon catalyst - Google Patents

Preparation method of chromium-based inorganic matter coupled transition metal nitrogen-doped carbon catalyst Download PDF

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CN115763845B
CN115763845B CN202211456797.7A CN202211456797A CN115763845B CN 115763845 B CN115763845 B CN 115763845B CN 202211456797 A CN202211456797 A CN 202211456797A CN 115763845 B CN115763845 B CN 115763845B
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salt
doped carbon
transition metal
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CN115763845A (en
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张云龙
赵磊
夏云飞
沈力晓
戴昀昆
郭盼
刘博�
王振波
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Harbin Institute of Technology
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Abstract

A preparation method of a chromium-based inorganic matter coupled transition metal nitrogen doped carbon catalyst, belonging to the field of electrocatalysis. The method takes a prepared metal M-bipyridine solution as a starting point, then sodium chloride, chromium salt and organic ammonium salt are sequentially added into the solution, and the solution is stirred to dissolve solids and evaporated to dryness to obtain mixed powder; and then annealing, template removing, acid washing, suction filtering and drying are carried out to obtain the catalyst. Has the following advantages: introducing a chromium salt inorganic carrier into an M-N-C atomic-level dispersion catalyst to replace a conventional carbon carrier by a molten salt template method, wherein the method is applicable to various metal-nitrogen co-doped carbon catalysts (such as Fe, cu, ni and the like); the catalyst is ultrathin two-dimensional sheet-shaped formed by interconnecting nanocrystals, so that the mass transfer capacity can be effectively improved; the introduction of the chromium-based inorganic salt can improve Faraday efficiency, catalytic activity and durability under high-current and long-time working conditions, and is obviously superior to commercial platinum carbon catalysts and transition metal nitrogen doped carbon.

Description

Preparation method of chromium-based inorganic matter coupled transition metal nitrogen-doped carbon catalyst
Technical Field
The invention belongs to the field of new energy materials, and particularly relates to a composite catalyst prepared by using a two-dimensional flaky chromium-based inorganic substance as a carrier and coupling a transition metal nitrogen-doped carbon-type atomic distribution material (M-N-C, M is one or more of Fe, co, cu and Ni), which is applied to places such as fuel cells, metal-air cell cathode Oxygen Reduction Reaction (ORR), electrolytic water oxygen precipitation reaction (OER) and the like.
Background
The electrocatalyst is one of the core components of many novel energy conversion devices such as fuel cells, metal-air cells, water electrolysis engineering and the like. Currently, electrocatalysts are still based on noble metal catalytic materials, such as Pt, pd, ru and Ir, and are the most advanced oxygen electrode catalysts. However, their high price and limited reserves have greatly limited the development of the new energy industry. Therefore, it is necessary to develop a non-noble metal catalyst having high catalytic performance in place of the noble metal catalyst.
In a platinum group metal-free catalyst, a transition metal nitrogen-doped carbon-atom-dispersed material (M-N-C), i.e., MN with intercalation of atomic dispersion and nitrogen coordination in the carbon plane x Sites for oxygen reduction, oxygen Evolution (OER) and carbon dioxide reduction (CO) 2 RR) and the like, and shows good performance and good application prospect. The extremely high surface-to-volume ratio of M-N-C improves the catalysis of each atomEfficiency, improved uniformity of active sites, and the ability to tailor the guest environment, all of which are not only attractive for industrial applications, but also attractive for in-depth understanding of atomic-scale catalytic mechanisms. Despite their great progress in terms of activity and site structure, there is an urgent need to improve durability due to insufficient knowledge of their degradation mechanism during operation. Further research and improvement of M-N-C catalysts is still needed to facilitate practical use, particularly at high currents, and long term stability of the catalysts in severe battery testing.
Disclosure of Invention
Aiming at the defects of the catalytic activity and stability of the traditional transition metal nitrogen doped carbon catalyst M-N-C (M is one or more of Fe, co, cu and Ni), a two-dimensional flaky chromium-based inorganic substance is used as a carrier to couple the M-N-C as a catalyst, and the catalytic durability of the obtained catalyst is obviously higher than that of the traditional M-N-C catalyst and the latest commercial 20% Pt/C catalyst.
In order to achieve the above purpose, the technical scheme adopted by the invention is as follows:
a preparation method of a chromium-based inorganic matter coupled transition metal nitrogen doped carbon catalyst comprises the following steps:
step one: preparing a metal M-bipyridine solution:
weighing metal M salt and bipyridine, respectively dissolving in ultrapure water at room temperature, mixing the two solutions after complete dissolution to obtain orange-yellow solution, and stirring at room temperature to enable M ions and bipyridine to fully coordinate and grow;
step two: preparation of M-Cr-organic ammonium salt mixed precursor:
sequentially adding sodium chloride, chromium salt and organic ammonium salt into the orange-yellow solution obtained in the step one, and stirring to completely dissolve the solid; placing the solution on a heating platform, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and placing the solid mixture in a vacuum oven for vacuum heating and drying to remove residual water to obtain an M-Cr-organic ammonium salt mixed precursor;
step three: preparation of chromium-based inorganic matter coupled M-N-C composite catalyst:
putting the precursor obtained in the second step into a mortar for full grinding, and then putting the mortar into a tube furnace for calcination treatment under a protective atmosphere; dispersing the calcined product into an aqueous solution, and removing a sodium chloride template through multiple times of water washing; to remove metal M clusters that may be present, the template-removed product is dispersed into dilute H 2 SO 4 And (3) in the aqueous solution, continuously stirring at 80 ℃ for 5 hours, and performing water washing, suction filtration and vacuum drying to obtain the chromium-based inorganic matter coupling transition metal nitrogen doped carbon catalyst.
Further, in the first step, the molar ratio of the metal M salt to the bipyridine is 1:1 to 4.
In the first step, the metal M salt is one or more of ferric nitrate, ferric chloride, ferric acetate, ferrous nitrate, ferrous chloride, ferrous acetate, cobalt nitrate, cobalt chloride, cobalt acetate, copper nitrate, copper chloride, copper acetate, nickel nitrate, nickel chloride and nickel acetate, and the bipyridine is 2,2 '-bipyridine or 4,4' -bipyridine.
In the second step, the input amount of the sodium chloride is determined according to the volume of the M-bipyridine solution, 0.5g of sodium chloride is corresponding to each milliliter of solution, and the molar ratio of the chromium salt to the metal M salt is 1-8: 1, the mass ratio of the organic ammonium salt to the chromium salt is 3:1.
in the second step, the chromium salt is one of chromium chloride, chromium sulfate and chromium nitrate, and the organic ammonium salt is one of urea, melamine, dicyandiamide and ammonium citrate.
Further, in the third step, the protective atmosphere is Ar or N 2 The calcining temperature is 650-800 ℃, the time is 1-3h, and the heating rate is 2-10 ℃/min.
The chromium-based inorganic matter coupled transition metal nitrogen doped carbon catalyst prepared by the method.
The chromium-based inorganic matter coupling transition metal nitrogen doped carbon catalyst prepared by the method is applied to a fuel cell, a metal-air cell cathode Oxygen Reduction Reaction (ORR) and an electrolytic water oxygen precipitation reaction (OER).
Compared with the prior art, the invention has the beneficial effects that:
(1) The invention can introduce the chromium-based inorganic carrier into the M-N-C atomic level dispersion catalyst to replace the conventional carbon carrier by a simple and effective molten salt template method, so as to synthesize various ultra-stable catalysts with different components and structures, can control the form of the chromium-based inorganic carrier by changing the selection of organic nitrogen ammonium salt, can control the nano-scale of the catalyst by changing the input amount of a sodium chloride template, and has the advantages of green color temperature, simplicity and great universality.
(2) The chromium-based inorganic matter coupled M-N-C catalyst of the invention is an ultrathin two-dimensional sheet structure composed of a plurality of interconnected nanocrystals. The two-dimensional structure is beneficial to the full contact between the active site and the reactant in the catalytic process, and the open structure at the two sides of the nano sheet can also effectively promote the efficiency of the mass transfer process and simplify the transportation path of reaction intermediate products and products. This also greatly improves the mass transfer capacity of the catalyst, due to the large number of pores between the crystals, allowing electrolyte and ions to be transported through the sheet.
(3) The chromium-based inorganic carrier introduced by the invention can improve the graphitization degree of M-N-C and enhance the conductivity of the catalyst. The introduction of the chromium-based inorganic matters can also induce electron spin polarization in the carbon layer where M-N-C is located, so that the catalytic selectivity and Faraday efficiency are improved, and the generation of byproducts is reduced. The chromium-based inorganic material has better thermodynamic and corrosion resistance capabilities relative to the carbon support, ensuring long-term stability of the catalyst at high currents and in severe battery testing.
In summary, the catalysts of the present invention are ultrathin, two-dimensional platelets composed of a plurality of interconnected nanocrystals. The chromium-based inorganic carrier is introduced into the M-N-C atomic-level dispersion catalyst to replace a conventional carbon carrier, so that the graphitization degree of the M-N-C is improved, the catalytic selectivity and Faraday efficiency are improved, and the durability of the catalyst under the conditions of high current and long-time working is improved.
Drawings
FIG. 1 is a flow chart of the preparation of examples 1-3 of the present invention;
FIG. 2 is the present inventionCoCN@Cr prepared in example 1 2 O 3 SEM images of (a);
FIG. 3 is FeCN@Cr prepared in example 2 of the present invention 2 O 3 SEM images of (a);
FIG. 4 is an SEM image of NiCN@CrN prepared in example 3 of the invention;
FIG. 5 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 A TEM image of (a);
FIG. 6 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 HRTEM images of (a);
FIG. 7 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 XPS profile of N1s in CoCN prepared in comparative example 3;
FIG. 8 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 XPS profile of Co 2p in CoCN prepared in comparative example 3;
FIG. 9 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 Raman spectrum of CoCN prepared in comparative example 3;
FIG. 10 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 Pt/C of comparative example 1, coCN prepared in comparative example 3, cr prepared in comparative example 4 2 O 3 Is a polar diagram of ORR (fuel cell);
FIG. 11 is a CoCN@Cr prepared in example 1 of the present invention 2 O 3 Catalytic efficiency test patterns of CoCN prepared in comparative example 3, including electron transfer number and byproduct H 2 O 2 Yield (fuel cell field);
FIG. 12 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 The Pt/C of comparative example 1, the half cell of CoCN prepared in comparative example 3, was tested for i-t stability for 10 hours in succession (fuel cell and zinc-air cell fields);
FIG. 13 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 I-t stability test patterns (fuel cell and zinc-air cell fields) for 50 hours in succession;
FIG. 14 is a CoCN@Cr prepared in example 1 of the invention 2 O 3 10000 cycles of aging of half cellTest patterns (fuel cell and zinc-air cell fields);
FIG. 15 is a CoCN@Cr prepared in example 1 of the present invention 2 O 3 Long-term charge-discharge cycle performance graphs (zinc-air battery field) of the Pt/c+ir/C mixtures of comparative examples 1 and 2 applied in ZABs;
FIG. 16 is FeCN@Cr prepared in example 2 of the present invention 2 O 3 ORR polarization diagram of Pt/C of comparative example 1 (fuel cell field);
FIG. 17 is an OER polarization diagram (electrolyzed water field) of NiCN@CrN prepared in example 3 of the present invention, ir/C of comparative example 2;
FIG. 18 is a chart of the stability test (electrolyzed water field) of the NiCN@CrN electrocatalytic OER prepared in example 3 of the present invention.
Detailed Description
The following description of the present invention refers to the accompanying drawings and examples, but is not limited to the same, and modifications and equivalents of the present invention can be made without departing from the spirit and scope of the present invention.
Preparing a metal M-bipyridine solution at room temperature, and stirring at room temperature to enable M ions and bipyridine to fully coordinate and grow; then adding sodium chloride solid, chromium salt solid and organic ammonium salt into the solution respectively, and stirring to completely dissolve the solid; placing the solution on a heating platform, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and then placing the collected solid mixture in a vacuum oven for drying to obtain mixed powder; and finally, annealing the mixed powder in a protective atmosphere, washing to remove the sodium chloride template, and carrying out acid washing, suction filtration and drying procedures to obtain the chromium-based inorganic matter coupling transition metal nitrogen-doped carbon ultrastable catalyst.
The catalyst designed by the invention takes ultrathin two-dimensional sheet chromium-based inorganic matters formed by a plurality of interconnected nanocrystals as carriers, the two-dimensional structure is favorable for the full contact between active sites and reactants in the catalytic process, and the open structures on the two sides of the nanosheets can also effectively promote the mass transfer processThe efficiency of the reaction intermediate and the transportation route of the product are simplified. The presence of a large number of pores between the crystals allows the electrolyte and ions to be transported through the sheet, which can also greatly improve the mass transfer capacity of the catalyst. In addition, the introduced chromium-based inorganic carrier can improve the graphitization degree of M-N-C, enhance the conductivity of the catalyst, induce the spin polarization of electrons in a carbon layer where the M-N-C is positioned, improve the catalytic selectivity and Faraday efficiency, reduce the generation of byproducts and effectively inhibit the damage of active oxygen species to the active sites of the catalyst. Compared with the traditional carbon material, the chromium-based inorganic carrier has higher thermodynamic stability and corrosion resistance, so that the M-N-C coupled with the chromium-based inorganic carrier not only has higher catalytic activities such as ORR, OER and the like, but also has ultrahigh durability under high current and long-time circulation. In addition, the invention can introduce inorganic carrier into different types of M-N-C (M= Co, fe, cu, ni and the like) atomic fraction separation catalysts by a green and easy sodium chloride molten salt template method, and is widely applied to ORR, OER and carbon dioxide reduction (CO) 2 RR) and the like, and the energy conversion devices, further improves the practical value of the invention.
Example 1:
this example provides CoCN@Cr 2 O 3 The preparation method of the catalyst comprises the following steps:
1. preparing Co-bipyridine solution: weigh 24mg CoCl 2 ·6H 2 O and 48mg of 2,2 '-bipyridine are respectively dissolved into 20mL of ultrapure water, after the O and the 2' -bipyridine are completely dissolved, the two solutions are mixed to obtain orange-yellow solution, and the orange-yellow solution is stirred for 24 hours at normal temperature to enable Co ions and the bipyridine to fully coordinate and grow;
2. preparation of Co-Cr-organic ammonium salt mixed precursor: 20g of NaCl and 24mg of CrCl are respectively added into the solution prepared in the step one 2 And 72mg of organic ammonium salt and stirring to completely dissolve the solid. Then, placing the solution on a heating platform at 65 ℃, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and then placing the collected solid mixture in a vacuum oven for heating and drying to remove residual water;
3.Cr 2 O 3 preparation of coupled Co-N-C composite catalyst: and (3) putting the precursor obtained in the step (II) into a mortar for full grinding, and then putting into a tube furnace for calcination treatment under inert atmosphere. The protective atmosphere is Ar or N 2 Inert gas, carbonization temperature of 700 ℃, carbonization time of 2h and heating rate of 2 ℃/min. Subsequently, the calcined product was dispersed in an aqueous solution, and the sodium chloride template was removed by washing with water a plurality of times. To remove Co clusters which may be present, the template-removed product is dispersed to 0.5mol L -1 Is a dilute H of (2) 2 SO 4 In the aqueous solution, stirring continuously at 80 ℃ for 5 hours, and obtaining the final flaky Cr by a water washing, suction filtration and vacuum drying mode 2 O 3 Co-N-C coupled composite ultra-stable catalyst (CoCN@Cr) 2 O 3 );
The flow of this embodiment is shown in fig. 1. The prepared CoCN@Cr under the process 2 O 3 The SEM, TEM and HRTEM morphologies of (1) are shown in FIG. 2, FIG. 5 and FIG. 6, the content of Co in ICP test is 1.02wt.%, and the CoCN@Cr morphology is shown in FIG. 7 and FIG. 8 2 O 3 XPS spectrum of Co 2p and N1s in the catalyst shows that Co in the catalyst is single-atom Co-N x FIG. 9 shows Raman spectra before and after the introduction of inorganic carrier, cr 2 O 3 The introduction of (3) increases the graphitization degree of the CoCN. CoCN@Cr 2 O 3 Catalyst ORR polarization test and catalytic efficiency test as shown in fig. 10 and 11, respectively, electron transfer and byproduct H 2 O 2 The yield indicates that Cr is introduced 2 O 3 The stability test of the catalyst in RDE is shown in FIG. 12, FIG. 13 and FIG. 14, the stability of the catalyst is greatly improved by the inorganic chromium salt, the current retention rate of the catalyst in the i-t test for 10 hours is 100%, the stability of the catalyst in ZABS battery is shown in FIG. 15 after long-time circulation, and the catalyst can be continuously and stably charged and discharged for more than 1500 hours.
Example 2:
this example provides FeCN@Cr 2 O 3 The preparation method of the catalyst comprises the following steps:
1. preparing Fe-bipyridine solution: weigh 28mg FeCl 3 ·6H 2 O and 48mg of 2,2 '-bipyridine are respectively dissolved into 20mL of ultrapure water, after the O and the 2' -bipyridine are completely dissolved, the two solutions are mixed to obtain orange-yellow solution, and the orange-yellow solution is stirred for 24 hours at normal temperature to enable iron ions and the bipyridine to fully coordinate and grow;
2. preparing Fe-Cr-organic ammonium salt mixed precursor: 20g of NaCl and 24mg of CrCl are respectively added into the solution prepared in the step one 2 And 72mg urea and stirring to completely dissolve the solid. Then, placing the solution on a heating platform at 65 ℃, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and then placing the collected solid mixture in a vacuum oven for heating and drying to remove residual water;
3. cr (Cr) 2 O 3 Preparation of coupled Fe-N-C composite catalyst: and (3) putting the precursor obtained in the step (II) into a mortar for full grinding, and then putting into a tube furnace for calcination treatment under inert atmosphere. The protective atmosphere is Ar inert gas, the carbonization temperature is 700 ℃, the carbonization time is 2 hours, and the heating rate is 2 ℃/min. Subsequently, the calcined product was dispersed in an aqueous solution, and the sodium chloride template was removed by washing with water a plurality of times. To remove Fe clusters which may be present, the template-removed product is dispersed to 0.5mol L -1 Is a dilute H of (2) 2 SO 4 In the aqueous solution, stirring continuously at 80 ℃ for 5 hours, and obtaining the final flaky Cr by a water washing, suction filtration and vacuum drying mode 2 O 3 Coupled Fe-N-C composite ultra-stable catalyst (FeCN@Cr) 2 O 3 );
The flow of this embodiment is shown in fig. 1. FeCN@Cr prepared by the process 2 O 3 The SEM morphology of (2) is shown in FIG. 3, and the content of Fe is 1.52wt.% in ICP test, feCN@Cr 2 O 3 The ORR polarization test of the catalyst is shown in fig. 16, and the catalytic performance of the catalyst is obviously higher than that of the noble metal catalyst of comparative example 1, which represents a broad practical prospect in the field of fuel cells.
Example 3:
the embodiment provides a preparation method of a NiCN@CrN catalyst, which comprises the following steps:
1. preparing Ni-bipyridine solution: weigh 25mg NiCl 2 ·6H 2 O and 48mg of 2,2 '-bipyridine are respectively dissolved into 20mL of ultrapure water, after the O and the 2' -bipyridine are completely dissolved, the two solutions are mixed to obtain orange-yellow solution, and the orange-yellow solution is stirred for 24 hours at normal temperature to enable Co ions and the bipyridine to fully coordinate and grow;
2. preparation of Co-Cr-organic ammonium salt mixed precursor: 20g of NaCl and 24mg of CrCl are respectively added into the solution prepared in the step one 2 And 72mg melamine and stirring to completely dissolve the solid. Then, placing the solution on a heating platform at 65 ℃, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and then placing the collected solid mixture in a vacuum oven for heating and drying to remove residual water;
3. preparation of CrN coupled Ni-N-C composite catalyst: and (3) putting the precursor obtained in the step (II) into a mortar for full grinding, and then putting into a tube furnace for calcination treatment under inert atmosphere. The protective atmosphere is Ar inert gas, the carbonization temperature is 650 ℃, the carbonization time is 2 hours, and the heating rate is 5 ℃/min. Subsequently, the calcined product was dispersed in an aqueous solution, and the sodium chloride template was removed by washing with water a plurality of times. To remove Ni clusters which may be present, the template-removed product is dispersed to 0.5mol L -1 Is a dilute H of (2) 2 SO 4 In the aqueous solution, continuously stirring for 5 hours at the temperature of 80 ℃, and obtaining the final flaky CrN coupled Ni-N-C composite ultra-stable catalyst (NiCN@CrN) through a water washing, suction filtration and vacuum drying mode;
the flow of this embodiment is shown in fig. 1. The SEM morphology of nicn@crn prepared under this process is shown in fig. 4, with ICP test Ni content of 1.34wt.%. OER polarization test of nicn@crn catalyst as shown in fig. 17, catalytic performance far exceeds that of comparative example 2. In addition, the stability test of the catalyst in RDE is shown in FIG. 18, and the catalyst performance is still excellent after 10000 times of aging, which represents that the catalyst has wide practical prospect in the field of fuel cells.
Comparative example 1:
the latest commercial 20% Pt/C (Comm.20% Pt/C) of a certain enterprise was purchased and used for testing directly without any treatment.
ORR polarization test of this example Comm.20% Pt/C is shown in FIG. 7. RDE stability test As shown in FIG. 10, the catalytic stability was far less than that of CoCN@Cr 2 O 3
Comparative example 2:
the latest commercial Ir/C (Comm.20% Ir/C) of a certain enterprise is purchased and directly used for testing without any treatment.
The OER polarization test for this example Comm.20% Ir/C is shown in FIG. 17.
Comparative example 3:
the steps of the CoCN which is prepared by the sodium chloride molten salt template method and is not introduced with inorganic carrier are as follows:
1. preparing Co-bipyridine solution: weigh 24mg CoCl 2 ·6H 2 O and 48mg of 2,2 '-bipyridine are respectively dissolved into 20mL of ultrapure water, after the O and the 2' -bipyridine are completely dissolved, the two solutions are mixed to obtain orange-yellow solution, and the orange-yellow solution is stirred for 24 hours at normal temperature to enable Co ions and the bipyridine to fully coordinate and grow;
2. preparation of Co-organic ammonium salt mixed precursor: to the solution prepared in the first step, 20g of NaCl and 75mg of urea were added, respectively, and the solid was completely dissolved by stirring. Then, placing the solution on a heating platform at 65 ℃, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and then placing the collected solid mixture in a vacuum oven for heating and drying to remove residual water;
3. cr-free 2 O 3 Preparation of the coupled CoCN catalyst: and (3) putting the precursor obtained in the step (II) into a mortar for full grinding, and then putting into a tube furnace for calcination treatment under inert atmosphere. The protective atmosphere is Ar or N 2 Inert gas, carbonization temperature of 700 ℃, carbonization time of 2h and heating rate of 2 ℃/min. Subsequently, the calcined product was dispersed in an aqueous solution, and the sodium chloride template was removed by washing with water a plurality of times. To remove Co clusters which may be present, the template-removed product is dispersed to 0.5mol L -1 Is a dilute H of (2) 2 SO 4 In the aqueous solution, stirring continuously at 80 ℃ for 5 hours, and obtaining the final sheet-shaped Cr-free product by water washing, suction filtration and vacuum drying 2 O 3 Coupling ofCoCN;
The elemental valence analysis (XPS test) and graphitization degree (raman test) of CoCN prepared in this example are shown in fig. 7, 8 and 9, respectively; ORR polarization test, electron transfer number and H of CoCN 2 O 2 The yield test and the RDE stability test are shown in FIG. 10, FIG. 11 and FIG. 12, respectively. The ORR catalytic performance of CoCN is significantly lower than that of CoCN@Cr in example 1 2 O 3 Has higher by-product H 2 O 2 The yield proves that the catalytic efficiency is low, and the catalytic stability is far less than that of CoCN@Cr 2 O 3
Comparative example 4:
cr prepared by sodium chloride molten salt template method 2 O 3 The carrier comprises the following steps:
1. preparing a Cr-organic ammonium salt mixed precursor: 20g of NaCl and 24mg of CrCl were added to 40ml of ultrapure water, respectively 2 And 72mg urea and stirring to completely dissolve the solid. Then, placing the solution on a heating platform at 65 ℃, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and then placing the collected solid mixture in a vacuum oven for heating and drying to remove residual water;
2. cr (Cr) 2 O 3 Preparation of inorganic matters: and (3) putting the precursor obtained in the step (II) into a mortar for full grinding, and then putting into a tube furnace for calcination treatment under inert atmosphere. The protective atmosphere is Ar or N 2 Inert gas, carbonization temperature of 700 ℃, carbonization time of 2h and heating rate of 2 ℃/min. Then dispersing the calcined product into aqueous solution, washing for multiple times to remove sodium chloride template, and vacuum-drying to obtain final sheet Cr 2 O 3
Cr prepared in this example 2 O 3 The ORR polarization tests of (2) are shown in figure 7, respectively. Cr (Cr) 2 O 3 ORR catalysis of (C) is not performed by CoCN@Cr 2 O 3

Claims (8)

1. A preparation method of a chromium-based inorganic matter coupled transition metal nitrogen doped carbon catalyst is characterized by comprising the following steps of: the method comprises the following steps:
step one: preparing a metal M-bipyridine solution:
weighing metal M salt and bipyridine, respectively dissolving in ultrapure water at room temperature, mixing the two solutions after complete dissolution to obtain orange-yellow solution, and stirring at room temperature to enable M ions and bipyridine to fully coordinate and grow; the metal M salt is one or more of ferric nitrate, ferric chloride, ferric acetate, ferrous nitrate, ferrous chloride, ferrous acetate, cobalt nitrate, cobalt chloride, cobalt acetate, copper nitrate, copper chloride, copper acetate, nickel nitrate, nickel chloride and nickel acetate;
step two: preparation of M-Cr-organic ammonium salt mixed precursor:
sequentially adding sodium chloride, chromium salt and organic ammonium salt into the orange-yellow solution obtained in the step one, and stirring to completely dissolve the solid; placing the solution on a heating platform, removing water in the solution by a rotary evaporation method to obtain a solid mixture, and placing the solid mixture in a vacuum oven for vacuum heating and drying to remove residual water to obtain an M-Cr-organic ammonium salt mixed precursor; the input amount of the sodium chloride is determined according to the volume of the M-bipyridine solution, and each milliliter of the solution corresponds to 0.5g sodium chloride; the organic ammonium salt is one of urea, melamine, dicyandiamide and ammonium citrate;
step three: preparation of chromium-based inorganic matter coupled M-N-C composite catalyst:
putting the precursor obtained in the second step into a mortar for full grinding, and then putting the mortar into a tube furnace for calcination treatment under a protective atmosphere; dispersing the calcined product into an aqueous solution, and removing a sodium chloride template through multiple times of water washing; dispersing the template-removed product into dilute H 2 SO 4 And (3) in the aqueous solution, continuously stirring at 80 ℃ for 5h, and performing water washing, suction filtration and vacuum drying to obtain the chromium-based inorganic matter coupling transition metal nitrogen doped carbon catalyst.
2. The method for preparing the chromium-based inorganic matter-coupled transition metal nitrogen-doped carbon catalyst according to claim 1, which is characterized in that: in the first step, the molar ratio of the metal M salt to the bipyridine is 1: 1-4.
3. The method for preparing the chromium-based inorganic matter-coupled transition metal nitrogen-doped carbon catalyst according to claim 1, which is characterized in that: in the first step, the bipyridine is 2,2 '-bipyridine or 4,4' -bipyridine.
4. The method for preparing the chromium-based inorganic matter-coupled transition metal nitrogen-doped carbon catalyst according to claim 1, which is characterized in that: in the second step, the molar ratio of the chromium salt to the metal M salt is 1-8: 1, the mass ratio of the organic ammonium salt to the chromium salt is 3:1.
5. the method for preparing the chromium-based inorganic matter-coupled transition metal nitrogen-doped carbon catalyst according to claim 1, which is characterized in that: in the second step, the chromium salt is one of chromium chloride, chromium sulfate and chromium nitrate.
6. The method for preparing the chromium-based inorganic matter-coupled transition metal nitrogen-doped carbon catalyst according to claim 3, wherein the method comprises the following steps: in the third step, the protective atmosphere is Ar or N 2 The calcining temperature is 650-800 ℃, the time is 1-3h, and the heating rate is 2-10 ℃/min.
7. A chromium-based inorganic coupled transition metal nitrogen-doped carbon catalyst prepared by the method of any one of claims 1-6.
8. Use of a chromium-based inorganic coupled transition metal nitrogen-doped carbon catalyst prepared by the method of any one of claims 1-6 in fuel cells, metal-air cell cathode oxygen reduction reactions, and electrolytic water oxygen evolution reactions.
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