CN114477124A - Carbon material, platinum-carbon catalyst, and preparation method and application thereof - Google Patents

Carbon material, platinum-carbon catalyst, and preparation method and application thereof Download PDF

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CN114477124A
CN114477124A CN202011152369.6A CN202011152369A CN114477124A CN 114477124 A CN114477124 A CN 114477124A CN 202011152369 A CN202011152369 A CN 202011152369A CN 114477124 A CN114477124 A CN 114477124A
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carbon
platinum
carbon material
sulfur
source
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荣峻峰
赵红
谢南宏
顾贤睿
张家康
王厚朋
彭茜
张云阁
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Sinopec Research Institute of Petroleum Processing
China Petroleum and Chemical Corp
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China Petroleum and Chemical Corp
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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
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    • B82Y40/00—Manufacture or treatment of nanostructures
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90—Selection of catalytic material
    • H01M4/92—Metals of platinum group
    • H01M4/925—Metals of platinum group supported on carriers, e.g. powder carriers
    • H01M4/926—Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite

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Abstract

The invention relates to a carbon material, a platinum-carbon catalyst, and a preparation method and application thereof. The carbon material is sulfur nitrogen phosphorus boron doped conductive carbon black, and the fuel cell platinum carbon catalyst using the carbon material as a carrier, particularly the platinum carbon catalyst with high platinum loading amount, has excellent catalytic performance and good carbon corrosion resistance.

Description

Carbon material, platinum-carbon catalyst, and preparation method and application thereof
Technical Field
The invention relates to a carbon material, a platinum-carbon catalyst, and a preparation method and application thereof. In particular to a carbon material doped with sulfur, nitrogen, phosphorus and boron, a platinum-carbon catalyst using the carbon material as a carrier, and preparation methods and applications of the carbon material and the platinum-carbon catalyst.
Background
In the field of chemistry, carbon materials are both important supports and commonly used catalysts. The carbon element has rich bonding modes, and the carbon material can be modified in various modes so as to obtain more suitable performance.
The Oxygen Reduction Reaction (ORR) is a key reaction in the electrochemical field, for example in fuel cells and metal air cells, and is a major factor affecting cell performance. The carbon material doped with atoms can be directly used as a catalyst for oxygen reduction reaction. When used as an oxygen reduction catalyst, it has been reported in the literature that a carbon material is doped with elements such as nitrogen, phosphorus, boron, sulfur, fluorine, chlorine, bromine, iodine, etc., wherein nitrogen has a radius close to that of carbon atoms and easily enters into a carbon lattice, and thus is the most commonly used doping element. Although there are many reports of the direct use of doped carbon materials as fuel cell catalysts and some research results show better activity, there is a wide gap and distance from commercial use compared to platinum carbon catalysts. On the one hand, the knowledge of the bonding mode of the heteroatom and the carbon material, the interaction between the heteroatoms and the catalytic mechanism is not sufficient in the field; on the other hand, each heteroatom has multiple bonding modes with the carbon material, and multiple functions exist among the heteroatoms, so that the situation is very complicated when multiple heteroatoms are doped, and therefore, how to control the bonding modes and the interactions among the heteroatoms and the carbon material is difficult for doping atoms. In addition, such catalysts are generally not suitable for acidic environments, especially for important Proton Exchange Membrane Fuel Cells (PEMFCs).
To date, the most effective oxygen reduction catalyst is the platinum carbon catalyst, but the platinum carbon catalyst still has deficiencies for large scale commercial applications. On the one hand, platinum is scarce and expensive, and the cost thereof accounts for about 40% of the total cost of the fuel cell. On the other hand, the currently used commercial platinum-carbon catalyst has undesirable platinum metal dispersion and is easy to agglomerate and deactivate, and the platinum surface area of the hydrogen fuel cell cathode is obviously reduced along with the time due to platinum dissolution and agglomeration, so that the service life of the fuel cell is influenced. It is highly desirable in the art to greatly increase the utilization of platinum metal and to increase its catalytic activity and stability in order to facilitate its large-scale commercial use. Factors influencing the activity and stability of the platinum-carbon catalyst are many and complex, and some literatures believe that the activity and stability of the platinum-carbon catalyst are related to the particle size, morphology and structure of platinum, and the type, property and platinum loading of a carrier. In the prior art, the performance of the platinum-carbon catalyst is improved mainly by controlling the particle size, morphology and structure of platinum, the specific surface area and pore structure of a carrier; there is also a literature report of improving the performance of platinum carbon catalysts by modifying the carbon support.
The carbon carrier can improve the specific surface area of the catalyst, reduce the agglomeration of metal particles and improve the metal utilization rate. The platinum-carrying amount of the carbon carrier is increased, so that the membrane electrode with thinner thickness and better performance can be manufactured, but the platinum-carrying amount is greatly increased, so that the accumulation among platinum metal particles is easily caused, and the utilization rate of an active site is sharply reduced. How to more effectively utilize the catalytic active sites of the platinum metal particles and increase the contactable three-phase catalytic reaction interface, thereby improving the platinum utilization rate and the comprehensive performance of the fuel cell and the metal-air battery, is a key problem to be solved in the field. In addition, the platinum loading of the platinum-carbon catalyst for the hydrogen fuel cell in practical application is at least more than 20 wt%, which is much more difficult than the manufacturing difficulty of the chemical platinum-carbon catalyst (the platinum loading is less than 5 wt%).
The problem of deactivation of platinum carbon catalysts due to carbon corrosion in proton exchange membrane fuel cells has attracted a great deal of attention in the art. It is reported in the literature that, theoretically, when the potential is more than 0.2V, corrosion of the carbon support occurs. In practice, the problem of carbon corrosion is only obvious when the potential is greater than 1.2V. When the battery is in open-circuit operation, the cathode potential can be higher than 0.9V, and in the starting/stopping process of the battery, the cathode local interface potential can even reach 1.6V, so that the carbon corrosion reaction is greatly accelerated, and the performance of the platinum-carbon catalyst is sharply reduced. In addition, platinum also accelerates the carbon corrosion rate, with greater amounts of platinum loading causing faster carbon corrosion. The conductive carbon black is low in price and is a platinum carbon catalyst carrier used in industry, but the corrosion resistance of the conductive carbon black is poor. On the one hand, the carbon carrier has a large number of defect sites, which is beneficial to increasing the platinum carrying amount, but at the same time, the carbon corrosion is intensified. On the other hand, increasing the degree of graphitization alleviates carbon corrosion, but also renders the surface of the carbon support chemically inert, making it difficult to uniformly disperse platinum on the carbon support.
The chemical reduction method is a commonly used method for preparing the platinum-carbon catalyst, and has the advantages of simple process and low utilization rate and catalytic activity of platinum. The reason for this may be that the platinum nanoparticles are not uniformly dispersed due to irregularities in the pore structure of the carbon support.
The information disclosed in the foregoing background section is only for enhancement of background understanding of the invention and may include information that is not already known to those of ordinary skill in the art.
Disclosure of Invention
It is a first object of the present invention to provide a carbon material of unique properties and a simple process for its preparation. The second purpose of the invention is to improve the carbon corrosion resistance of the platinum-carbon catalyst on the basis of the carbon material. The third object of the present invention is to provide a platinum-carbon catalyst having more excellent overall performance and a simple process for producing the same, based on the aforementioned objects. It is a fourth object of the present invention to provide a platinum-carbon catalyst with a higher platinum loading in addition to the aforementioned objects.
In order to achieve the above object, the present invention provides the following technical solutions.
1. A carbon material which is sulfur nitrogen phosphorus boron doped conductive carbon black.
2. A carbon material according to any one of the preceding claims, characterized in that S is analyzed by XPS2PIn the spectrum peaks, the peak area of the thiophene-type sulfur is 70% or more, preferably 80% or more, and more preferably 90% or more of the total area of the characteristic peaks between 160ev and 170 ev.
3. A carbon material according to any one of the preceding claims, characterized in that N is analyzed by XPS1sIn the spectrum peaks, one characteristic peak exists between 399ev and 400.5ev, one characteristic peak exists between 397.5ev and 398.5ev, and no other characteristic peak exists between 390ev and 410evCharacteristic peak of (2).
4. A carbon material according to any one of the preceding claims, characterized in that it is B as analyzed by XPS1sAmong the peaks, there was a characteristic peak at 190.3. + -. 0.5 eV.
5. A carbon material according to any one of the preceding claims, characterized in that it is B as analyzed by XPS1sAmong the spectrum peaks, four characteristic peaks are arranged between 189ev and 195 ev.
6. A carbon material according to any one of the preceding claims, characterized in that P is analyzed by XPS2PAmong the spectral peaks, there are two characteristic peaks between 133ev and 135 ev.
7. The carbon material according to any one of the preceding claims, characterized in that, in XPS analysis, the mass fraction of sulfur is 0.01% to 6%, the mass fraction of nitrogen is 0.01% to 6%, the mass fraction of phosphorus is 0.01% to 6%, and the mass fraction of boron is 0.01% to 6%; preferably, the mass fraction of sulfur is 0.1-2%, preferably the mass fraction of nitrogen is 0.1-4%, preferably the mass fraction of phosphorus is 0.1-2.5%, preferably the mass fraction of boron is 0.1-3%.
8. A carbon material according to any one of the above, characterized in that it has a resistivity of <10. omega. m, preferably < 5. omega. m, more preferably < 3. omega. m.
9. A carbon material according to any one of the preceding claims, characterized in that it has a specific surface area of 10m2/g～2000m2A/g, preferably of 200m2/g～2000m2(ii)/g; the pore volume is 0.02mL/g to 6.0mL/g, preferably 0.2mL/g to 3.0 mL/g.
10. A carbon material according to any one of the preceding claims, characterized in that the conductive carbon Black is EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXAXK 40B 2.
11. A method of producing a carbon material, comprising: and (2) contacting the conductive carbon black with a sulfur source, a nitrogen source, a phosphorus source and a boron source, and treating for 0.5-10 h at 400-900 ℃ in an inert gas to obtain the carbon material.
12. The method for producing a carbon material according to any one of the preceding claims, characterized in that the mass ratio of the conductive carbon black to the sulfur source is 20: 1-2: 1; preferably 10: 1-4: 1; more preferably 8: 1-4: 1.
13. the method for producing a carbon material according to any one of the preceding claims, characterized in that the mass ratio of the conductive carbon black to the nitrogen source is 500: 1-5: 1; preferably 200: 1-10: 1.
14. the method for producing a carbon material according to any one of the preceding claims, characterized in that the mass ratio of the conductive carbon black to the phosphorus source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
15. the method for producing a carbon material according to any one of the preceding claims, characterized in that the mass ratio of the conductive carbon black to the boron source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
16. a method for producing a carbon material according to any one of the preceding claims, characterized in that the sulfur source is elemental sulfur.
17. The method for producing a carbon material according to any one of the above methods, wherein the nitrogen source is ammonia water or urea.
18. A method for producing a carbon material according to any one of the preceding claims, characterized in that the phosphorus source is one or more of phosphoric acid, phosphate, pyrophosphate, polyphosphate, hydrogenphosphate, dihydrogenphosphate, phosphite and hypophosphite.
19. A method of producing a carbon material according to any one of the preceding claims, characterized in that the boron source is one or more of boric acid and a borate.
20. The method for producing a carbon material according to any one of the preceding claims, wherein the treatment time is 1 to 5 hours, preferably 2 to 4 hours.
21. A method for producing a carbon material according to any one of the preceding claims, characterized in that the temperature is 500 ℃ to 900 ℃.
22. A process for the preparation of a carbon material according to any one of the preceding claims, characterized in that the conductive carbon Black is EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXAXK 40B 2.
23. The method for producing a carbon material according to any one of the preceding claims, wherein the conductive carbon black has an oxygen mass fraction of more than 4%, preferably 4% to 15%, in XPS analysis.
24. A method for producing a carbon material according to any one of the preceding claims, characterized in that the conductive carbon black has a resistivity of <10 Ω -m, preferably <5 Ω -m, more preferably <2 Ω -m.
25. A method for producing a carbon material according to any one of the preceding claims, characterized in that the conductive carbon black has a specific surface area of 10m2/g～2000m2A/g, preferably of 200m2/g～2000m2(ii)/g; the pore volume is 0.02mL/g to 6mL/g, preferably 0.2mL/g to 3 mL/g.
26. A carbon material produced by any one of the above production methods.
27. Use of a carbon material according to any of the preceding claims as an electrode material in electrochemistry.
28. A platinum-carbon catalyst comprises a carbon carrier and platinum metal loaded on the carbon carrier, and is characterized in that the carbon carrier is sulfur nitrogen phosphorus boron doped conductive carbon black.
29. A platinum-carbon catalyst according to any one of the preceding claims, characterized in that S is analyzed in its XPS2PIn the spectrum peaks, the peak area of the thiophene-type sulfur is 70% or more, preferably 80% or more, and more preferably 90% or more of the total area of the characteristic peaks between 160ev and 170 ev.
30. A platinum-carbon catalyst according to any one of the preceding claims, N as analyzed by XPS thereof1sIn the spectrum peaks, except that the peak area is between 398.7ev and 399.7ev, no other characteristic peak exists between 390ev and 410 ev.
31. A platinum-carbon catalyst according to any one of the preceding claims, characterised in that N is analysed in its XPS1sIn the spectrum peaks, except for the characteristic peak area between 396.7ev and 399.7ev, no other characteristic peak exists between 390ev and 410 ev.
32. The platinum-carbon catalyst according to any one of the preceding claims, characterized in that it has no B between 185eV and 200eV in XPS analysis1sAnd no P between 125ev and 145ev2pCharacteristic peak of (2).
33. The platinum-carbon catalyst according to any one of the above, wherein the carbon support is a carbon material of any one of the above.
34. A platinum-carbon catalyst according to any one of the preceding claims, characterised in that the conductive carbon Black is EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXAXK 40B 2.
35. The platinum-carbon catalyst according to any of the preceding claims, characterized in that the platinum-carbon catalyst has a resistivity of <10 Ω · m, preferably <2 Ω · m.
36. A method of preparing a platinum carbon catalyst comprising:
(1) a step of manufacturing a carbon support: contacting conductive carbon black with a sulfur source, a nitrogen source, a phosphorus source and a boron source, and treating for 0.5-10 h at 400-900 ℃ in inert gas to obtain a carbon carrier;
(2) a step of supporting platinum with the carbon carrier obtained in (1).
37. The method for preparing a platinum-carbon catalyst according to any one of the preceding claims, characterized in that in (1), the sulfur source is elemental sulfur.
38. The method for preparing a platinum-carbon catalyst according to any one of the preceding claims, wherein in (1), the mass ratio of the conductive carbon black to the sulfur source is 20: 1-2: 1; preferably 10: 1-4: 1; preferably 8: 1-4: 1.
39. the process for producing a platinum-carbon catalyst according to any one of the preceding claims, wherein in (1), the nitrogen source is ammonia water or urea.
40. The preparation method of any one of the platinum-carbon catalysts described above, wherein in (1), the mass ratio of the conductive carbon black to the nitrogen source is 500: 1-5: 1.
41. the preparation method of any one of the platinum-carbon catalysts is characterized in that in the step (1), the phosphorus source is one or more of phosphoric acid, phosphate, pyrophosphate, polyphosphate, hydrogen phosphate, dihydrogen phosphate, phosphite and hypophosphite.
42. The preparation method of any one of the platinum-carbon catalysts is characterized in that in the step (1), the mass ratio of the conductive carbon black to the phosphorus source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
43. the preparation method of any one of the platinum-carbon catalysts is characterized in that in the step (1), the boron source is one or more of boric acid and borate.
44. The method for preparing a platinum-carbon catalyst according to any one of the preceding claims, wherein in (1), the mass ratio of the conductive carbon black to the boron source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
45. the method for producing a platinum-carbon catalyst according to any of the above processes, wherein the temperature in the step (1) is 500 to 900 ℃.
46. The process for producing a platinum-carbon catalyst according to any one of the preceding claims, wherein the treatment time in (1) is 1 to 5 hours, preferably 2 to 4 hours.
47. A process for preparing a platinum-carbon catalyst according to any one of the preceding claims, wherein in (1), the conductive carbon Black is EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXK 40B 2.
48. The method for producing a platinum-carbon catalyst according to any one of the preceding claims, wherein in (1), the conductive carbon black has an oxygen mass fraction of more than 4%, preferably 4% to 15%, in XPS analysis.
49. The method for preparing a platinum-carbon catalyst according to any one of the above processes, wherein the conductive carbon black in (1) has a resistivity of <10 Ω · m, preferably <5 Ω · m, more preferably <2 Ω · m.
50. The process for producing a platinum-carbon catalyst according to any of the above processes, wherein in the step (1), the conductive carbon black has a specific surface area of 10m2/g～2000m2A/g, preferably of 200m2/g～2000m2(ii)/g; the pore volume is 0.02mL/g to 6mL/g, preferably 0.2mL/g to 3 mL/g.
51. The method for preparing a platinum-carbon catalyst according to any one of the preceding claims, wherein the step (2) of supporting platinum comprises:
(a) dispersing the carbon carrier and the platinum precursor obtained in the step (1) in a water phase, and adjusting the pH value to 8-12 (preferably, adjusting the pH value to 10 +/-0.5);
(b) adding a reducing agent for reduction;
(c) separating out solid, and post-treating to obtain the platinum-carbon catalyst.
52. The preparation method of any one of the platinum-carbon catalysts is characterized in that in (a), the platinum precursor is chloroplatinic acid, potassium chloroplatinate or sodium chloroplatinate; the concentration of the platinum precursor is 0.5-5 mol/L.
53. The preparation method of any one of the platinum-carbon catalysts is characterized in that in the step (b), the reducing agent is one or more of citric acid, ascorbic acid, formaldehyde, formic acid, ethylene glycol, sodium citrate, hydrazine hydrate, sodium borohydride or glycerol; the molar ratio of the reducing agent to the platinum is 2-100; the reduction temperature is 60-90 ℃; the reduction time is 4-15 h.
54. A platinum-carbon catalyst is characterized by being prepared by any one of the preparation methods of the platinum-carbon catalyst.
55. A hydrogen fuel cell, characterized in that any one of the foregoing platinum-carbon catalysts is used in an anode and/or a cathode of the hydrogen fuel cell.
The heteroatoms and the carbon material have various combination modes and various interactions, and the combination modes of the heteroatoms and the carbon material and the interactions among the heteroatoms can be influenced by different preparation methods and raw materials and different operation steps and conditions in the doping process, so that the properties of the heteroatoms and the carbon material are different, and the functions of the heteroatoms and the carbon material are changed. In the art, how to control the bonding mode of the heteroatom and the carbon material and the interaction between the heteroatoms is a difficulty in doping atoms. Controlling the manner in which the heteroatoms are bound to the carbon material and the interactions between the heteroatoms makes it possible to produce carbon materials with unique properties that make them suitable for particular applications. The research of the invention finds that the carbon corrosion resistance of the platinum-carbon catalyst can be improved more favorably when the carbon carrier is subjected to multi-element co-doping. The carbon material with unique properties can be obtained by carrying out sulfur nitrogen phosphorus boron four-doping on the carbon material by a simple method, and XPS analysis spectrum of the carbon material shows that sulfur doped on the surface of the carbon material mainly exists in the form of thiophene sulfur, nitrogen doped on the surface mainly exists in the form of pyrrole nitrogen, and the boron doped on the surface has a characteristic peak at 190.3 +/-0.5 ev. The inventor researches and discovers that the characteristics are beneficial to improving the performance of the platinum-carbon catalyst of the hydrogen fuel cell.
Compared with the prior art, the invention can realize the following beneficial technical effects.
Compared with the existing doped carbon material, the carbon material with unique properties is prepared by a low-temperature co-doping method, the sulfur doped on the surface of the carbon material mainly exists in the form of thiophene sulfur, the nitrogen doped on the surface mainly exists in the form of pyrrole nitrogen, and the boron doped on the surface has a characteristic peak at 190.3 +/-0.5 ev. The present inventors have found that these features are advantageous in improving the catalytic performance of the platinum-carbon catalyst.
Secondly, the carbon material of the invention is suitable for being used as a carrier of a platinum-carbon catalyst, and the platinum-carbon catalyst manufactured by using the carbon material still has excellent comprehensive catalytic performance and carbon corrosion resistance when the platinum loading reaches 70 wt%.
And thirdly, the platinum carrying amount of the platinum-carbon catalyst of the hydrogen fuel cell in practical application is generally more than 20 wt%, and the difficulty in manufacturing the high platinum carrying amount catalyst with excellent performance is great. The chemical reduction method has simple process, but the utilization rate of platinum is low and the catalytic activity is lower. However, a high-platinum-loading catalyst having excellent specific activity and stability can be easily produced by an aqueous chemical reduction method using the carbon material produced by the present invention as a carrier.
Additional features and advantages of the invention will be set forth in the detailed description which follows.
Drawings
FIG. 1 is an XPS spectrum of sulfur for a S-N-P-B doped carbon material of example 1.
FIG. 2 is an XPS spectrum of nitrogen for a S-N-P-B doped carbon material of example 1.
FIG. 3 is an XPS spectrum of the phosphorus of the S-N-P-B doped carbon material of example 1.
FIG. 4 is an XPS spectrum of boron from a S-N-P-B doped carbon material of example 1.
FIG. 5 is an XPS spectrum of sulfur for S-N-P-B doped carbon material of example 2.
FIG. 6 is an XPS spectrum of nitrogen for a S-N-P-B doped carbon material of example 2.
FIG. 7 is an XPS spectrum of phosphorus for a S-N-P-B doped carbon material of example 2.
FIG. 8 is an XPS spectrum of boron from a S-N-P-B doped carbon material of example 2.
Fig. 9 is an XPS spectrum of sulfur for the platinum carbon catalyst of example 3.
Figure 10 is an XPS spectrum of nitrogen for the platinum carbon catalyst of example 3.
Fig. 11 is an XPS spectrum of sulfur for the platinum carbon catalyst of example 5.
Figure 12 is an XPS spectrum of nitrogen for the platinum carbon catalyst of example 5.
Fig. 13 is a TEM image of the platinum-carbon catalyst of example 5.
FIG. 14 is an XPS spectrum of phosphorus for the phosphorus-doped carbon material of comparative example 4.
Fig. 15 is an XPS spectrum of boron of the boron-doped carbon material of comparative example 5.
Fig. 16 is an XPS spectrum of sulfur of the sulfur-doped carbon material of comparative example 6.
Fig. 17 is an XPS spectrum of nitrogen for the nitrogen-doped carbon material of comparative example 7.
Detailed Description
The present invention will be described in detail with reference to the following embodiments, but it should be understood that the scope of the present invention is not limited by these embodiments and the principle of the present invention, but is defined by the claims.
In the present invention, anything or matters not mentioned is directly applicable to those known in the art without any change except those explicitly described. Moreover, any embodiment described herein may be freely combined with one or more other embodiments described herein, and the technical solutions or ideas formed thereby are considered part of the original disclosure or description of the present invention and should not be considered as new matters not disclosed or contemplated herein, unless a person skilled in the art would consider such combination to be clearly unreasonable.
All of the features disclosed in this application can be combined in any combination which is understood to be disclosed or described in this application and which, unless clearly considered to be too irrational by a person skilled in the art, is to be considered as being specifically disclosed and described in this application. The numerical points disclosed in the present specification include not only the numerical points specifically disclosed in the examples but also the endpoints of each numerical range in the specification, and ranges in which any combination of the numerical points is disclosed or recited should be considered as ranges of the present invention.
Technical and scientific terms used herein are to be defined only in accordance with their definitions, and are to be understood as having ordinary meanings in the art without any definitions.
The "doping element" in the present invention means nitrogen, phosphorus, boron, sulfur, fluorine, chlorine, bromine and iodine.
The numerical ranges defined in this disclosure include the endpoints of the numerical ranges.
In the present invention, unless the term "carbon material containing a doping element" is uniquely defined depending on the context or the self-definition, the term "carbon material" refers to a carbon material containing no doping element. So does the underlying concept of carbon material.
In the present invention, "carbon black" and "carbon black" are terms of art that can be substituted for each other.
The "inert gas" in the present invention means a gas that does not have any appreciable influence on the properties of the sulfur, nitrogen, phosphorus and boron doped carbon material in the preparation method of the present invention. So does the underlying concept of carbon material.
In the present invention, all references to "pore volume" are to P/P, except where the context or self-definition may be clear0The maximum single point adsorption total pore volume.
The invention provides a carbon material which is sulfur nitrogen phosphorus boron doped conductive carbon black.
According to the carbon material of the present invention, sulfur, nitrogen, phosphorus and boron are chemically bonded to the conductive carbon black.
The carbon material according to the invention is free of doping elements other than sulphur, nitrogen, phosphorus and boron.
The carbon material according to the present invention contains no metal element.
Carbon material according to the invention, S analyzed in its XPS2PIn the spectrum peaks, the peak area of the thiophene-type sulfur is 70% or more, preferably 80% or more, and more preferably 90% or more of the total area of the characteristic peaks between 160ev and 170 ev.
According to the carbon material of the present invention, the characteristic peak of the thiophenic sulfur is between 162ev and 166 ev.
According to the carbon material of the present invention, the characteristic peaks of the thiophenic sulfur are two peaks, which are 163.5. + -. 0.5eV and 164.8. + -. 0.5eV, respectively.
Carbon material according to the invention, in some embodiments, S in its XPS analysis2PIn the spectrum peaks, the ratio of the characteristic peak area of the thiophene-type sulfur to the characteristic peak area at 168 +/-1 ev is 10-15.
Carbon material according to the invention, N analyzed in its XPS1sIn the spectrum peaks, one characteristic peak exists between 399eV and 400.5eV, one characteristic peak exists between 397.5eV and 398.5eV, and other characteristic peaks do not exist between 390eV and 410 eV.
Carbon material according to the invention, B in XPS analysis thereof1sAmong the peaks, there was a characteristic peak at 190.3. + -. 0.5 eV.
Carbon material according to the invention, B in XPS analysis thereof1sAmong the spectrum peaks, four characteristic peaks are arranged between 189ev and 195 ev.
Carbon material according to the invention, P analyzed in its XPS2PAmong the spectral peaks, there are two characteristic peaks between 133ev and 135 ev.
According to the carbon material, in XPS analysis, the mass fraction of sulfur is 0.01-6%, the mass fraction of nitrogen is 0.01-6%, the mass fraction of phosphorus is 0.01-6%, and the mass fraction of boron is 0.01-6%; preferably, the mass fraction of sulfur is 0.1-2%, preferably the mass fraction of nitrogen is 0.1-4%, preferably the mass fraction of phosphorus is 0.1-2.5%, preferably the mass fraction of boron is 0.1-3%.
The carbon material according to the present invention may, in some embodiments, have a sulfur mass fraction of 0.1% to 1.5%, a nitrogen mass fraction of 0.1% to 3.5%, a phosphorus mass fraction of 0.1% to 2%, and a boron mass fraction of 0.1% to 2.5% in XPS analysis.
The carbon material according to the invention has a resistivity of <10 Ω · m, preferably <5 Ω · m, more preferably <3 Ω · m.
The carbon material according to the present invention is not particularly limited in its oxygen content. Generally, the XPS analysis of the oxygen content of the compound is 2 to 15 percent.
The specific surface area and pore volume of the carbon material according to the invention may vary within a relatively large range, for example the specific surface area may be 10m2/g～2000m2The pore volume may be from 0.02mL/g to 6.0 mL/g. In one embodiment, the specific surface area is 200m2/g～2000m2The pore volume is 0.2mL/g to 3.0 mL/g.
According to the carbon material of the present invention, the Conductive carbon black may be common Conductive carbon black (Conductive Blacks), Super Conductive carbon black (Super Conductive Blacks) or Extra Conductive carbon black (Extra Conductive Blacks), for example, the Conductive carbon black may be one or more of Ketjen black series superconducting carbon black, Cabot series Conductive carbon black and series Conductive carbon black produced by winning and developing solid race company; preferably Ketjen Black EC-300J, Ketjen Black EC-600JD, Ketjen Black ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXK 40B 2.
The carbon material according to the present invention is not limited in the production method and source of the conductive carbon black. The conductive carbon black may be acetylene black, furnace black, or the like.
The invention also provides a preparation method of the carbon material, which comprises the following steps: and (2) contacting the conductive carbon black with a sulfur source, a nitrogen source, a phosphorus source and a boron source, and treating (preferably treating at constant temperature) for 0.5-10 h at 400-900 ℃ in inert gas to obtain the carbon material.
According to the method for preparing the carbon material of the present invention, the conductive carbon black may be one or more of Ketjen black series superconducting carbon black, Cabot series conductive carbon black and series conductive carbon black produced by winning-developing-solid-match company; preferably EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXK 40B 2.
According to the method for preparing the carbon material of the present invention, there is no limitation on the preparation method and source of the conductive carbon black. The conductive carbon black may be acetylene black, furnace black, or the like.
According to the preparation method of the carbon material, I of the carbon materialD/IGThe value is generally 0.8 to 5, preferably 1 to 4. In the Raman spectrum, it is located at 1320cm-1The nearby peak is the D peak and is located at 1580cm-1The nearby peak is the G peak, IDRepresents the intensity of the D peak, IGRepresenting the intensity of the G peak.
According to the method for producing a carbon material of the present invention, conductive carbon black is contacted with a sulfur source, a nitrogen source, a phosphorus source, and a boron source in a mixed manner. The present invention is not limited to the order and manner of mixing the conductive carbon black with the sulfur, nitrogen, phosphorus, and boron sources, and one skilled in the art can select an appropriate order and manner based on the teachings and/or prior knowledge of the present invention. The present invention provides a preferred mixing method: the conductive carbon black is first mixed with a nitrogen source, a phosphorus source, and a boron source solution (preferably an aqueous solution), impregnated, dried, and then mixed with a sulfur source (such as elemental sulfur).
According to the method for preparing the carbon material, the temperature is raised if necessary, and the temperature raising rate can be 1-20 ℃/min, preferably 3-15 ℃/min, and more preferably 3-7 ℃/min.
According to the method for producing a carbon material of the present invention, the temperature is preferably 500 to 900 ℃.
According to the method for producing a carbon material of the present invention, the treatment time is preferably 1 to 5 hours, and more preferably 2 to 4 hours.
According to the method for preparing the carbon material, the sulfur source is elemental sulfur.
According to the method for producing a carbon material of the present invention, the mass ratio of the conductive carbon black to the sulfur source is 20: 1-2: 1; preferably 10: 1-4: 1; more preferably 8: 1-4: 1.
according to the method for producing a carbon material of the present invention, the nitrogen source is ammonia water or urea.
According to the method for producing a carbon material of the present invention, the mass ratio of the conductive carbon black to the nitrogen source is 500: 1-5: 1, preferably 200: 1-10: 1.
according to the preparation method of the carbon material, the phosphorus source is one or more of phosphoric acid, phosphate, pyrophosphate, polyphosphate, hydrogen phosphate, dihydrogen phosphate, phosphite and hypophosphite.
According to the preparation method of the carbon material, the mass of the phosphorus source is calculated according to the mass of phosphorus contained in the carbon material, and the mass ratio of the conductive carbon black to the phosphorus source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
according to the method for producing a carbon material of the present invention, the boron source is one or more of boric acid and borate.
According to the method for producing a carbon material of the present invention, the mass ratio of the conductive carbon black to the boron source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
according to the method for producing a carbon material of the present invention, the inert gas is nitrogen or argon.
According to the method for producing a carbon material of the present invention, the conductive carbon black has a resistivity of <10 Ω · m, preferably <5 Ω · m, more preferably <2 Ω · m.
According to the preparation method of the carbon material, the conductive carbon black has an oxygen mass fraction of generally more than 4%, preferably 4% to 15% in XPS analysis.
According to the method for producing a carbon material of the present invention, the specific surface area of the conductive carbon black can be varied over a wide range. Generally, the specific surface area is 10m2/g～2000m2(ii)/g; the pore volume is 0.02 mL/g-6 mL/g.
According to one embodiment of the method for preparing the carbon material of the present invention, the conductive carbon black impregnated with the nitrogen source, the phosphorus source, and the boron source in the aqueous solution is dried, then uniformly mixed with the sulfur powder, and then placed in the tube furnace, the tube furnace is heated to 400 to 900 ℃ (preferably 500 to 900 ℃) at a rate of 3 to 7 ℃/min in the inert gas, and then the carbon material of the present invention is obtained after the constant temperature treatment for 0.5 to 10 hours.
The inert gas is nitrogen or argon.
According to the method for producing a carbon material of the present invention, a metal-containing catalyst is not used in the process of doping the conductive carbon black.
The invention also provides a carbon material prepared by any one of the methods.
Use of any of the foregoing carbon materials of the present invention as an electrode material in electrochemistry.
The invention provides a platinum-carbon catalyst, which comprises a carbon carrier and platinum metal loaded on the carbon carrier, wherein the carbon carrier is sulfur, nitrogen, phosphorus and boron doped conductive carbon black.
Platinum-carbon catalyst according to the invention, S analyzed in its XPS2PIn the spectrum peaks, the peak area of the thiophene-type sulfur is 70% or more, preferably 80% or more, and more preferably 90% or more of the total area of the characteristic peaks between 160ev and 170 ev.
According to the platinum-carbon catalyst of the present invention, in some examples, S of XPS analysis thereof2PIn the spectrum peak, the characteristic peak area of the thiophene sulfur accounts for 90-95% of the total area of the characteristic peak between 160ev and 170 ev.
According to the platinum-carbon catalyst, the characteristic peak of the thiophene sulfur is between 162ev and 166 ev.
According to the platinum-carbon catalyst, the characteristic peaks of the thiophene sulfur are double peaks and are respectively located at 163.3 +/-0.5 ev and 164.5 +/-0.5 ev.
Platinum-carbon catalyst according to the invention, N in its XPS analysis1sIn the spectrum peaks, except that the peak area is between 398.7ev and 399.7ev, no other characteristic peak exists between 390ev and 410 ev.
The platinum-carbon catalyst according to the present invention, N analyzed in XPS thereof1sAmong the spectral peaks, N in its XPS analysis1sIn the spectrum peak, except the characteristic peak area between 396.7eV and 399.7eV, no other characteristic peak exists between 390eV and 410 eV.
The platinum-carbon catalyst according to the present invention has no B between 185ev and 200ev in its XPS analysis1sIs characterized in thatA characteristic peak and no P between 125ev and 145ev2pCharacteristic peak of (2).
P, P was detected in the TG-MS test according to the platinum-carbon catalyst of the present invention2O3And P2O5Of the signal of (1).
According to the platinum-carbon catalyst of the present invention, boron signals (B and B) were detected in TG-MS (thermogravimetric-mass spectrometry) test2O3)。
The platinum-carbon catalyst according to the present invention does not contain doping elements other than sulfur, nitrogen, phosphorus and boron.
The platinum-carbon catalyst according to the present invention does not contain other metal elements than platinum.
According to the platinum-carbon catalyst of the present invention, sulfur, nitrogen, phosphorus and boron are chemically bonded to conductive carbon black.
According to the platinum-carbon catalyst of the present invention, the carbon support is any one of the carbon materials of the present invention described above.
According to the platinum carbon catalyst of the invention, the conductive carbon black can be one or more of Ketjen black series superconducting carbon black, Cabot series conductive carbon black and series conductive carbon black produced by Wingda Gusai company; preferably Ketjen Black EC-300J, Ketjen Black EC-600JD, Ketjen Black ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXK 40B 2.
According to the platinum-carbon catalyst of the present invention, the mass fraction of platinum is 0.1% to 80%, preferably 20% to 70%, and more preferably 40% to 70% based on the mass of the catalyst.
The platinum-carbon catalyst according to the invention has a resistivity of <10.0 Ω · m, preferably <2.0 Ω · m.
According to the platinum-carbon catalyst of the present invention, the specific surface area of the platinum-carbon catalyst is 80m2/g～1500m2A/g, preferably of 100m2/g～200m2/g。
The invention provides a preparation method of a platinum-carbon catalyst, which comprises the following steps:
(1) a step of manufacturing a carbon support: contacting conductive carbon black with a sulfur source, a nitrogen source, a phosphorus source and a boron source, and treating for 0.5-10 h at 400-900 ℃ in inert gas to obtain a carbon carrier;
(2) a step of supporting platinum with the carbon carrier obtained in (1).
According to the preparation method of the platinum-carbon catalyst of the present invention, (1), "the contact manner of the conductive carbon black with the sulfur source, the nitrogen source, the phosphorus source and the boron source" is the same as the corresponding parts in the foregoing, and the details are not repeated herein.
According to the preparation method of the platinum-carbon catalyst, the sulfur source is elemental sulfur.
According to the preparation method of the platinum-carbon catalyst, in the step (1), the mass of the sulfur source is calculated by the mass of sulfur contained in the sulfur source, and the mass ratio of the conductive carbon black to the sulfur source is 20: 1-2: 1; preferably 10: 1-4: 1; preferably 8: 1-4: 1.
according to the preparation method of the platinum-carbon catalyst, the nitrogen source is ammonia water or urea.
According to the preparation method of the platinum-carbon catalyst, in the step (1), the mass of the nitrogen source is calculated by the mass of the nitrogen contained in the nitrogen source, and the mass ratio of the conductive carbon black to the nitrogen source is 500: 1-5: 1.
according to the preparation method of the platinum-carbon catalyst, the phosphorus source is one or more of phosphoric acid, phosphate, pyrophosphate, polyphosphate, hydrogen phosphate, dihydrogen phosphate, phosphite and hypophosphite.
According to the preparation method of the platinum-carbon catalyst, in the step (1), the mass of the phosphorus source is calculated according to the mass of phosphorus contained in the phosphorus source, and the mass ratio of the conductive carbon black to the phosphorus source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
according to the preparation method of the platinum-carbon catalyst, the boron source is one or more of boric acid and borate.
According to the preparation method of the platinum-carbon catalyst, in the step (1), the mass of the boron source is calculated by the mass of boron contained in the boron source, and the mass ratio of the conductive carbon black to the boron source is 10000: 1-10: 1; preferably 2000: 1-20: 1.
according to the preparation method of the platinum-carbon catalyst, the temperature is increased as required in the step (1), and the temperature increase rate can be 1-20 ℃/min, preferably 3-15 ℃/min, and more preferably 3-7 ℃/min.
According to the preparation method of the platinum-carbon catalyst of the present invention, in (1), the temperature is preferably 500 to 900 ℃.
According to the preparation method of the platinum-carbon catalyst of the invention, (1), the treatment time is 1 h-5 h, preferably 2 h-4 h.
According to the preparation method of the platinum-carbon catalyst, in the step (1), the conductive carbon Black is EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXAXK 40B 2.
According to the preparation method of the platinum-carbon catalyst, the sulfur-nitrogen-phosphorus-boron doped conductive carbon black prepared in the step (1) can be easily dispersed in a water phase. However, it is difficult to disperse some conductive carbon blacks, such as ketjen black, directly in the aqueous phase.
According to the preparation method of the platinum-carbon catalyst of the invention, (1), in the XPS analysis of the conductive carbon black, the oxygen mass fraction is more than 4%, and preferably 4-15%.
According to the method for preparing a platinum-carbon catalyst of the present invention, (1), the conductive carbon black has a resistivity of <10 Ω · m, preferably <5 Ω · m, more preferably <2 Ω · m.
According to the preparation method of the platinum-carbon catalyst of the present invention, in (1), the specific surface area of the conductive carbon black is 10m2/g～2000m2A/g, preferably of 200m2/g～2000m2(ii)/g; the pore volume is 0.02mL/g to 6mL/g, preferably 0.2mL/g to 3 mL/g.
A platinum-carbon catalyst is prepared by any one of the preparation methods of the platinum-carbon catalyst.
A hydrogen fuel cell comprising an anode and/or a cathode, wherein any one of the platinum-carbon catalysts described above is used.
The present invention will be described in detail with reference to specific examples. The following examples will aid those skilled in the art in further understanding the present invention, but are not intended to limit the invention in any manner.
Reagents, instruments and tests
Unless otherwise specified, all reagents used in the invention are analytically pure, and all reagents are commercially available.
The invention detects elements on the surface of the material by an X-ray photoelectron spectrum analyzer (XPS). The adopted X-ray photoelectron spectrum analyzer is an ESCALB 220i-XL type ray photoelectron spectrum analyzer which is manufactured by VG scientific company and is provided with Avantage V5.926 software, and the X-ray photoelectron spectrum analysis test conditions are as follows: the excitation source is monochromatized A1K alpha X-ray, the power is 330W, and the basic vacuum is 3X 10 during analysis and test-9mbar. In addition, the electron binding energy was corrected with the C1s peak (284.3eV) of elemental carbon, and the late peak processing software was XPSPEAK. The characteristic peaks of thiophene-type sulfur, nitrogen, phosphorus and boron in the spectrogram are the characteristic peaks after peak separation.
Apparatus and method of elemental analysis, conditions: an element analyzer (Vario EL Cube), the reaction temperature is 1150 ℃, the sample is weighed by 5mg, the reduction temperature is 850 ℃, the flow rate of carrier gas helium is 200mL/min, the flow rate of oxygen is 30mL/min, and the oxygen introducing time is 70 s.
The instrument, the method and the conditions for testing the mass fraction of platinum in the platinum-carbon catalyst are as follows: and (3) taking 30mg of the prepared Pt/C catalyst, adding 30mL of aqua regia, condensing and refluxing at 120 ℃ for 12h, cooling to room temperature, taking supernatant liquid for dilution, and testing the Pt content in the supernatant liquid by ICP-AES.
The high-resolution transmission electron microscope (HRTEM) adopted by the invention is JEM-2100(HRTEM) (Nippon electronics Co., Ltd.), and the test conditions of the high-resolution transmission electron microscope are as follows: the acceleration voltage was 200 kV. The particle size of the nanoparticles in the sample is measured by an electron microscope picture.
BET test method: in the invention, the pore structure property of a sample is measured by a Quantachrome AS-6B type analyzer, the specific surface area and the pore volume of the catalyst are obtained by a Brunauer-Emmett-Taller (BET) method, and the pore distribution curve is obtained by calculating a desorption curve according to a Barrett-Joyner-Halenda (BJH) method.
The Raman detection adopts a LabRAM HR UV-NIR laser confocal Raman spectrometer produced by HORIBA company of Japan, and the laser wavelength is 532 nm.
Electrochemical performance test, instrument Model Solartron analytical energy Lab and Princeton Applied Research (Model 636A),the method and the test conditions are as follows: polarization curve LSV of catalyst at 1600rpm2Saturated 0.1M HClO4Test in (1), CV Curve under Ar atmosphere 0.1M HClO4To calculate the electrochemically active area ECSA. At O in the stability test2Saturated 0.1M HClO4After 5000 cycles of scanning in the range of 1.0V to 1.5V, LSV and ECSA were tested as described above. During the test, the catalyst is prepared into evenly dispersed slurry and coated on a glassy carbon electrode with the diameter of 5mm, and the platinum content of the catalyst on the electrode is 3-4 mu g.
Resistivity test four-probe resistivity tester, instrument model KDY-1, method and test conditions: the applied pressure is 3.9 plus or minus 0.03MPa, and the current is 500 plus or minus 0.1 mA.
TG-MS test method: the test is carried out by adopting a German Chiz-resistant STA449F5-QMS403D type thermogravimetric-mass spectrometer, an ion source is an EI source, a quadrupole mass spectrometer adopts an MID mode, a transmission pipeline is a capillary tube with the length of 3 meters, and the temperature is 260 ℃; the temperature range is 55-1000 ℃, and the heating rate is 10 ℃/min.
VXC72(Vulcan XC72, produced by Kabot, USA) was purchased from Suzhou wingong sandisk energy science and technology, Inc. The results of the tests by the instrument method show that: specific surface area 258m2(g), pore volume 0.388mL/g, oxygen mass fraction 8.72% by XPS analysis, ID/IG1.02, and a resistivity of 1.22. omega. m.
Ketjenblack ECP600JD (manufactured by Lion corporation, japan) was purchased from tsuzhou wingong sandisk energy science and technology limited. The results of the tests by the instrument method show that: specific surface area 1362m2Volume of pores/g, 2.29mL/g, XPS analysis oxygen mass fraction of 6.9%, ID/IG1.25, and resistivity of 1.31. omega. m.
Black Pearls 2000 (produced by Kabott, USA) is purchased from Suzhou wingong sandisk energy science and technology, Inc. The results of the tests by the instrument method show that: specific surface area 1479m2(g), XPS analysis oxygen mass fraction 9.13%; ID/IG1.14, and resistivity of 1.19. omega. m.
Commercial platinum carbon catalyst (trade name HISPEC4000, manufactured by Johnson Matthey corporation) was purchased from Alfa Aesar. The test result shows that: the mass fraction of platinum was 40.2%.
Example 1
This example illustrates the preparation of a carbon material doped with sulfur, nitrogen, phosphorus and boron in accordance with the present invention.
1g of Vulcan XC72 was immersed for 20h in 20mL of an aqueous solution having an ammonia concentration of 1.5 wt%, a sodium borate concentration of 0.4 wt% and a phosphoric acid concentration of 1.2 wt%; drying in an oven at 100 ℃; then evenly mixing the sulfur with 0.167g of elemental sulfur, putting the mixture into a tubular furnace, heating the tubular furnace to 900 ℃ at the speed of 8 ℃/min, and carrying out constant temperature treatment for 3 hours; and naturally cooling to obtain the sulfur nitrogen phosphorus boron doped carbon material which is numbered as a carbon carrier A.
Sample characterization and testing
Sulfur mass fraction by XPS analysis was 0.5%; the nitrogen mass fraction by XPS analysis was 3.1%; the mass fraction of phosphorus analyzed by XPS was 1.4%; the boron mass fraction of XPS analysis is 0.6%; the specific surface area is 230m2(ii)/g; resistivity 1.29. omega. m.
FIG. 1 is an XPS spectrum of sulfur for a S-N-P-B doped carbon material of example 1.
In FIG. 1, the ratio of the characteristic peak area of thiophenic sulfur to the characteristic peak area at 168. + -.1 eV is 12.1.
FIG. 2 is an XPS spectrum of nitrogen for a S-N-P-B doped carbon material of example 1.
FIG. 3 is an XPS spectrum of the phosphorus of the S-N-P-B doped carbon material of example 1.
FIG. 4 is an XPS spectrum of boron from a S-N-P-B doped carbon material of example 1.
Example 2
This example illustrates the preparation of a carbon material doped with sulfur, nitrogen, phosphorus and boron in accordance with the present invention.
Adding 10mL of absolute ethanol into 1g of Ketjenblack ECP600JD, and then adding 25mL of aqueous solution with the urea concentration of 0.5 wt%, the boric acid concentration of 1.0 wt% and the sodium dihydrogen phosphate concentration of 0.4 wt% for impregnation for 24 h; drying in an oven at 100 ℃; then evenly mixing the mixture with 0.25g of elemental sulfur and nitrogen, putting the mixture into a tubular furnace, heating the tubular furnace to 500 ℃ at the speed of 5 ℃/min, and carrying out constant temperature treatment for 3 h; and naturally cooling to obtain the sulfur nitrogen phosphorus boron doped carbon material which is numbered as a carbon carrier B.
Sample characterization and testing
The sulfur mass fraction by XPS analysis was 0.9%; the nitrogen mass fraction by XPS analysis was 1.7%; the mass fraction of phosphorus analyzed by XPS is 0.4%; the boron mass fraction of XPS analysis is 2.1%; specific surface area of 1341m2(ii)/g; resistivity was 1.39. omega. m.
FIG. 5 is an XPS spectrum of sulfur for S-N-P-B doped carbon material of example 2.
In FIG. 5, the ratio of the characteristic peak area of thiophenic sulfur to the characteristic peak area at 168. + -.1 eV was 11.7.
FIG. 6 is an XPS spectrum of nitrogen for a S-N-P-B doped carbon material of example 2.
FIG. 7 is an XPS spectrum of phosphorus for a S-N-P-B doped carbon material of example 2.
FIG. 8 is an XPS spectrum of boron from a S-N-P-B doped carbon material of example 2.
Example 3
This example illustrates the preparation of a platinum carbon catalyst according to the invention.
Dispersing a carbon carrier A into deionized water according to the proportion that 250mL of water is used for each gram of carbon carrier, adding 3.4mmol of chloroplatinic acid into each gram of carbon carrier, performing ultrasonic dispersion to form a suspension, and adding 1mol/L of sodium carbonate aqueous solution to enable the pH value of the system to be 10; heating the suspension to 80 ℃, adding formic acid to carry out reduction reaction while stirring, wherein the molar ratio of the formic acid to the chloroplatinic acid is 50:1, and continuously maintaining the reaction for 10 hours; and filtering the reacted mixture, washing the mixture by deionized water until the pH value of the filtrate is neutral, filtering the mixture, and drying the filtrate at 100 ℃ to obtain the platinum-carbon catalyst.
Sample characterization and testing
The platinum mass fraction of the platinum-carbon catalyst was 39.9%.
Fig. 9 is an XPS spectrum of sulfur for the platinum carbon catalyst of example 3.
In FIG. 9, the ratio of the characteristic peak area of thiophenic sulfur to the characteristic peak area at 168. + -.1 eV was 10.4.
Figure 10 is an XPS spectrum of nitrogen for the platinum carbon catalyst of example 3.
Platinum carbon catalystXPS analysis of the agents showed no P between 125eV and 145eV2pCharacteristic peak of (2).
P, P detected in TG-MS test of platinum-carbon catalyst2O3And P2O5Of the signal of (1).
No B was found in XPS analysis of the platinum-carbon catalyst at 185 to 200eV1sCharacteristic peak of (2).
Detection of B and B in TG-MS test of platinum-carbon catalyst2O3Of the signal of (1).
The results of the performance tests of the platinum carbon catalyst are shown in table 1.
Example 4
This example illustrates the preparation of a platinum carbon catalyst.
A platinum carbon catalyst was prepared according to the method of example 3, except that: per gram of carbon support 1.3mmol of chloroplatinic acid was added.
Sample characterization and testing
The platinum mass fraction of the platinum-carbon catalyst was 20.4%.
P, P detected in TG-MS test of platinum-carbon catalyst2O3And P2O5Of the signal of (1).
Detection of B and B in TG-MS test of platinum-carbon catalyst2O3Of the signal of (1).
The results of the performance tests of the platinum carbon catalyst are shown in table 1.
Example 5
This example illustrates the preparation of a platinum carbon catalyst according to the invention.
Dispersing a carbon carrier B into a solution according to the proportion of using 600mL of water and 600mL of glycol per gram of carbon carrier, adding 12mmol of chloroplatinic acid per gram of carbon carrier, adding sodium acetate according to the molar ratio of the sodium acetate to the chloroplatinic acid of 2:1, performing ultrasonic dispersion to form a suspension, and adding 1mol/L of sodium carbonate aqueous solution to enable the pH value of the system to be 10; heating the suspension to 80 ℃, adding sodium borohydride into the suspension under stirring to perform reduction reaction, wherein the molar ratio of the sodium borohydride to the chloroplatinic acid is 5:1, and continuously maintaining the reaction for 10 hours; and filtering the reacted mixture, washing the mixture by deionized water until the pH value of the filtrate is neutral, filtering the mixture, and drying the filtrate at 100 ℃ to obtain the platinum-carbon catalyst.
Sample characterization and testing
The platinum mass fraction of the platinum-carbon catalyst was 69.9%.
Fig. 11 is an XPS spectrum of sulfur for the platinum carbon catalyst of example 5.
In FIG. 11, the ratio of the characteristic peak area of thiophenic sulfur to the characteristic peak area at 168. + -.1 eV is 10.2.
Figure 12 is an XPS spectrum of nitrogen for the platinum carbon catalyst of example 5.
Fig. 13 is a TEM image of the platinum-carbon catalyst of example 5.
No P was found in XPS analysis of the platinum-carbon catalyst between 125eV and 145eV2pCharacteristic peak of (2).
P, P detected in TG-MS test of platinum-carbon catalyst2O3And P2O5Of the signal of (1).
No B was found in XPS analysis of the platinum-carbon catalyst at 185 to 200eV1sCharacteristic peak of (2).
Detection of B and B in TG-MS test of platinum-carbon catalyst2O3Of the signal of (1).
The results of the performance tests of the platinum carbon catalyst are shown in table 1.
Comparative example 1
Dispersing Vulcan XC72 in deionized water according to the proportion that each gram of carbon carrier uses 250mL of water, adding 3.4mmol of chloroplatinic acid into each gram of carbon carrier, performing ultrasonic dispersion to form suspension, and adding 1mol/L of sodium carbonate aqueous solution to ensure that the pH value of the system is 10; heating the suspension to 80 ℃, adding formic acid to carry out reduction reaction while stirring, wherein the molar ratio of the formic acid to the chloroplatinic acid is 50:1, and continuously maintaining the reaction for 10 hours; and filtering the reacted mixture, washing the mixture by deionized water until the pH value of the filtrate is neutral, filtering the mixture, and drying the filtrate at 100 ℃ to obtain the platinum-carbon catalyst.
Sample characterization and testing
The platinum mass fraction of the platinum-carbon catalyst was 40.1%.
The results of the platinum carbon catalyst performance tests are shown in table 1.
Comparative example 2
According to the proportion of using 600mL of water and 600mL of ethylene glycol per gram of carbon carrier, dispersing Ketjenblack ECP600JD in a solution, adding 12mmol of chloroplatinic acid per gram of carbon carrier, adding sodium acetate according to the molar ratio of the sodium acetate to the chloroplatinic acid of 2:1, performing ultrasonic dispersion to form a suspension, and adding 1mol/L of sodium carbonate aqueous solution to ensure that the pH value of the system is 10; heating the suspension to 80 ℃, adding sodium borohydride into the suspension under stirring to perform reduction reaction, wherein the molar ratio of the sodium borohydride to the chloroplatinic acid is 5:1, and continuously maintaining the reaction for 10 hours; and filtering the reacted mixture, washing the mixture by deionized water until the pH value of the filtrate is neutral, filtering the mixture, and drying the filtrate at 100 ℃ to obtain the platinum-carbon catalyst.
Sample characterization and testing
The platinum mass fraction of the platinum-carbon catalyst was 69.9%.
The results of the platinum carbon catalyst performance tests are shown in table 1.
Comparative example 3
The platinum carbon catalyst was a commercial catalyst purchased under the designation HISPEC 4000.
Sample characterization and testing
The platinum mass fraction of the platinum-carbon catalyst was 40.2%.
The results of the platinum carbon catalyst performance tests are shown in table 1.
Comparative example 4
This comparative example serves to illustrate the preparation of a phosphorus doped carbon material.
1g of Vulcan XC72 was immersed in 15mL of a 0.8 wt% aqueous phosphoric acid solution for 16 h; drying in an oven at 100 ℃; then placing the tube furnace into a tube furnace, heating the tube furnace to 400 ℃ at the speed of 8 ℃/min, and carrying out constant temperature treatment for 2 h; and naturally cooling to obtain the phosphorus-doped carbon material.
Sample characterization and testing
FIG. 14 is an XPS spectrum of phosphorus for the phosphorus-doped carbon material of comparative example 4.
Comparative example 5
This comparative example serves to illustrate the preparation of a boron doped carbon material.
1g of Vulcan XC72 was immersed for 16h in 15mL of 4.5 wt% aqueous sodium borate solution; drying in an oven at 100 ℃; then placing the tube furnace into a tube furnace, heating the tube furnace to 400 ℃ at the speed of 10 ℃/min, and carrying out constant temperature treatment for 3 h; and naturally cooling to obtain the boron-doped carbon material.
Sample characterization and testing
Fig. 15 is an XPS spectrum of boron of the boron-doped carbon material of comparative example 5.
Comparative example 6
This comparative example serves to illustrate the preparation of a sulfur-doped carbon material.
Uniformly mixing 1g of Ketjenblack ECP600JD with 0.25g of elemental sulfur, putting the mixture into a tube furnace, heating the tube furnace to 500 ℃ at the speed of 5 ℃/min, and carrying out constant-temperature treatment for 3 h; and naturally cooling to obtain the sulfur-doped carbon material.
Sample characterization and testing
Fig. 16 is an XPS spectrum of sulfur of the sulfur-doped carbon material of comparative example 6.
Comparative example 7
This comparative example serves to illustrate the preparation of a nitrogen-doped carbon material.
1g of Vulcan XC72 was immersed in 20mL of 2.5 wt% aqueous ammonia solution for 24 h; drying in an oven at 100 ℃; then placing the tube furnace into a tube furnace, heating the tube furnace to 1100 ℃ at the speed of 8 ℃/min, and carrying out constant temperature treatment for 3 h; and naturally cooling to obtain the nitrogen-doped carbon material.
Sample characterization and testing
Fig. 17 is an XPS spectrum of nitrogen for the nitrogen-doped carbon material of comparative example 7.
TABLE 1
Figure BDA0002741550330000271

Claims (29)

1. A carbon material is characterized in that the carbon material is sulfur nitrogen phosphorus boron doped conductive carbon black.
2. The carbon material according to claim 1, wherein S is analyzed by XPS2PIn the spectrum peak, the characteristic peak area of the thiophene type sulfur accounts for more than 70 percent of the total area of the characteristic peaks between 160ev and 170 ev.
3. The carbon material according to claim 1, wherein N is analyzed by XPS1sIn the spectrum peaks, one characteristic peak exists between 399eV and 400.5eV, one characteristic peak exists between 397.5eV and 398.5eV, and other characteristic peaks do not exist between 390eV and 410 eV.
4. The carbon material according to claim 1, wherein B is analyzed by XPS1sAmong the peaks, there was a characteristic peak at 190.3. + -. 0.5 eV.
5. A carbon material according to claim 4 wherein the conductive carbon Black is EC-300J, EC-600JD, ECP-600JD, VXC72, Black pearls 2000, PRINTEX XE2-B, PRINTEX L6 or HIBLAXAXK 40B 2.
6. The carbon material as claimed in claim 1, wherein the XPS analysis shows that the sulfur content is 0.01 to 6% by mass, the nitrogen content is 0.01 to 6% by mass, the phosphorus content is 0.01 to 6% by mass, and the boron content is 0.01 to 6% by mass.
7. A method of producing a carbon material, comprising: and (2) contacting the conductive carbon black with a sulfur source, a nitrogen source, a phosphorus source and a boron source, and treating for 0.5-10 h at 400-900 ℃ in an inert gas to obtain the carbon material.
8. The method for producing a carbon material as claimed in claim 7, wherein the mass ratio of the conductive carbon black to the sulfur source is 20: 1-2: 1.
9. the method for producing a carbon material as claimed in claim 7, wherein the mass ratio of the conductive carbon black to the nitrogen source is 500: 1-5: 1.
10. the method for producing a carbon material as claimed in claim 7, wherein the mass ratio of the conductive carbon black to the phosphorus source is 10000: 1-10: 1.
11. the method for producing a carbon material as claimed in claim 7, wherein the mass ratio of the conductive carbon black to the boron source is 10000: 1-10: 1.
12. the method for producing a carbon material as claimed in claim 7, wherein the sulfur source is elemental sulfur.
13. The method for producing a carbon material as claimed in claim 7, wherein the nitrogen source is ammonia and/or urea.
14. The method for producing a carbon material as claimed in claim 7, wherein the phosphorus source is one or more selected from phosphoric acid, phosphate, pyrophosphate, polyphosphate, hydrogenphosphate, dihydrogenphosphate, phosphite and hypophosphite.
15. The method for producing a carbon material as claimed in claim 7, wherein the boron source is one or more of boric acid and a borate.
16. A carbon material produced by the method according to any one of claims 7 to 15.
17. Use of the carbon material as claimed in any one of claims 1 to 6 and 16 as an electrode material in electrochemistry.
18. A platinum-carbon catalyst comprises a carbon carrier and platinum metal loaded on the carbon carrier, and is characterized in that the carbon carrier is sulfur nitrogen phosphorus boron doped conductive carbon black.
19. The platinum carbon catalyst according to claim 18, whereinThen, S in its XPS analysis2PIn the spectrum peak, the characteristic peak area of the thiophene sulfur accounts for more than 70 percent of the total area of the characteristic peaks between 160ev and 170 ev.
20. Platinum-carbon catalyst according to claim 18, characterised in that the N analyzed in its XPS1sIn the spectrum peaks, except that the peak area is between 398.7ev and 399.7ev, no other characteristic peak exists between 390ev and 410 ev.
21. Platinum-carbon catalyst according to claim 18, characterised in that the N analyzed in its XPS1sIn the spectrum peaks, except for the characteristic peak area between 396.7ev and 399.7ev, no other characteristic peak exists between 390ev and 410 ev.
22. Platinum-carbon catalyst according to claim 18, characterized in that in its XPS analysis there is no B between 185 and 200eV1sAnd no P between 125ev and 145ev2pCharacteristic peak of (2).
23. A platinum-carbon catalyst according to claim 18, wherein the carbon support is the carbon material according to any one of claims 2 to 6 and 16.
24. A method of preparing a platinum carbon catalyst comprising:
(1) a step of manufacturing a carbon support: contacting conductive carbon black with a sulfur source, a nitrogen source, a phosphorus source and a boron source, and treating for 0.5-10 h at 400-900 ℃ in inert gas to obtain a carbon carrier;
(2) a step of supporting platinum with the carbon carrier obtained in (1).
25. The method for preparing a platinum-carbon catalyst according to claim 23, wherein the step (2) of supporting platinum comprises:
(a) dispersing the carbon carrier and the platinum precursor obtained in the step (1) in a water phase, and adjusting the pH to 8-12;
(b) adding a reducing agent for reduction;
(c) separating out solid, and post-treating to obtain the platinum-carbon catalyst.
26. The method for preparing a platinum-carbon catalyst according to claim 23, wherein in (a), the platinum precursor is chloroplatinic acid, potassium chloroplatinate, or sodium chloroplatinate; the concentration of the platinum precursor is 0.5-5 mol/L.
27. The method for preparing a platinum-carbon catalyst according to claim 23, wherein in (b), the reducing agent is one or more of citric acid, ascorbic acid, formaldehyde, formic acid, ethylene glycol, sodium citrate, hydrazine hydrate, sodium borohydride or glycerol; the molar ratio of the reducing agent to the platinum is 2-100; the reduction temperature is 60-90 ℃; the reduction time is 4-15 h.
28. A platinum carbon catalyst, characterised in that it is obtainable by a process according to any one of claims 24 to 27.
29. A hydrogen fuel cell, characterized in that a platinum-carbon catalyst according to any one of claims 18 to 23 and 28 is used in an anode and/or a cathode of the hydrogen fuel cell.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439115A (en) * 2014-08-08 2016-03-30 中国石油化工股份有限公司 Heteroatom doping carbon nanoparticle and production method thereof
CN106219530A (en) * 2016-07-28 2016-12-14 中南大学 A kind of polyatom doped graphene material and preparation method thereof
US20180272320A1 (en) * 2017-03-22 2018-09-27 Tda Research, Inc Nitrogen and phosphorous doped carbon supported nanoparticle platinum electrocatalyst and method of making
CN110302769A (en) * 2018-03-20 2019-10-08 中国科学院大连化学物理研究所 A kind of catalyst carrier, loaded catalyst and its preparation method and application

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439115A (en) * 2014-08-08 2016-03-30 中国石油化工股份有限公司 Heteroatom doping carbon nanoparticle and production method thereof
CN106219530A (en) * 2016-07-28 2016-12-14 中南大学 A kind of polyatom doped graphene material and preparation method thereof
US20180272320A1 (en) * 2017-03-22 2018-09-27 Tda Research, Inc Nitrogen and phosphorous doped carbon supported nanoparticle platinum electrocatalyst and method of making
CN110302769A (en) * 2018-03-20 2019-10-08 中国科学院大连化学物理研究所 A kind of catalyst carrier, loaded catalyst and its preparation method and application

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
VIVIANE SANTOS PEREIRA ET AL.: "PtRu Nanoparticles Supported on Phosphorous-Doped Carbon as Electrocatalysts for Methanol Electro-Oxidation", ELECTROCATALYSIS, vol. 8, pages 245 - 19 *
XIAOMEI NING ET AL.: "Glycerol and formic acid electro-oxidation over Pt on S-doped carbon nanotubes: Effect of carbon support and synthesis method on the metal-support interaction", ELECTROCHIMICA ACTA, vol. 319, pages 129 *

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