CN116477600A - High specific capacity silicon-carbon negative electrode material and preparation method and application thereof - Google Patents

High specific capacity silicon-carbon negative electrode material and preparation method and application thereof Download PDF

Info

Publication number
CN116477600A
CN116477600A CN202310257954.XA CN202310257954A CN116477600A CN 116477600 A CN116477600 A CN 116477600A CN 202310257954 A CN202310257954 A CN 202310257954A CN 116477600 A CN116477600 A CN 116477600A
Authority
CN
China
Prior art keywords
carbon
silicon
specific capacity
high specific
negative electrode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202310257954.XA
Other languages
Chinese (zh)
Inventor
张志杰
曾勤勤
钟明峰
罗子昊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
South China University of Technology SCUT
Original Assignee
South China University of Technology SCUT
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by South China University of Technology SCUT filed Critical South China University of Technology SCUT
Priority to CN202310257954.XA priority Critical patent/CN116477600A/en
Publication of CN116477600A publication Critical patent/CN116477600A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/05Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/02Silicon
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/134Electrodes based on metals, Si or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386Silicon or alloys based on silicon
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Nanotechnology (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Composite Materials (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention belongs to the field of high-performance lithium ion battery anode materials, and discloses a high-specific-capacity silicon-carbon anode material, and a preparation method and application thereof. The invention adopts the steps of coating an amorphous carbon layer on the surface of nano silicon particles in advance to obtain a core-shell structure silicon-carbon composite material which is coated in a sealing way, and then uniformly dispersing the core-shell structure silicon-carbon composite material in a carbon network matrix to obtain a final material. An electric conduction bridge is formed between the amorphous carbon layer on the surface of the nano silicon particles and the carbon network matrix material, so that the electric conductivity of the nano silicon particles can be effectively improved, the amorphous carbon layer can be used as a protective layer for buffering the volume expansion of the nano silicon particles to maintain the stability of the whole material structure, the electrochemical cycle performance is more excellent, and the amorphous carbon layer has a wide application prospect in a lithium ion battery system.

Description

High specific capacity silicon-carbon negative electrode material and preparation method and application thereof
Technical Field
The invention belongs to the field of high-performance lithium ion battery anode materials, and particularly relates to a high-specific-capacity silicon-carbon anode material, and a preparation method and application thereof.
Background
At present, in order to solve a series of environmental and health problems brought by the traditional fossil energy, energy transformation is urgent. The lithium ion battery is used as a novel power source under energy transformation, and is widely applied to various electronic products and new energy automobiles due to the characteristics of high energy density, safety, environmental protection and the like. The theoretical specific capacity of the graphite material used as the anode material for the earliest commercialized application is only 372mA/g, and the actual development requirement of the future new energy field can not be met. In the research of numerous negative electrode materials of lithium ion batteries, silicon-based negative electrode materials become a current research hot spot due to higher theoretical specific capacity and lower charge/discharge voltage platform. However, silicon-based anode materials still have many limitations in commercial applications, mainly because the intercalation and deintercalation of lithium ions in the battery during the charge and discharge process is accompanied by a large and irreversible volume expansion (about 300%) of the silicon material, and the huge volume expansion tends to cause the destruction of the material structure, so that the electrical contact between the silicon particles and the current collector is lost, thereby causing the rapid attenuation of the circulation capacity. In addition, silicon material, which is a typical semiconductor material, has poor conductivity, resulting in low first cycle efficiency of the material and severe cycle capacity fade.
In view of the above problems, a great deal of research is currently being conducted mainly on structural modification designs and composite materials of silicon-based anode materials. Silicon-carbon composite materials have proven to be an effective method for improving lithium storage performance of silicon-based anodes, where carbon materials play two main roles: firstly, as a buffer matrix for relieving the volume expansion of the silicon material, and secondly, as a conductive medium for improving the overall conductivity of the material, thereby obtaining more excellent electrochemical cycle performance. However, the specific capacity of the existing silicon-carbon composite material is not enough, and further modification is needed to be carried out on the silicon-based negative electrode material so as to obtain the silicon-carbon negative electrode material with high specific capacity.
Disclosure of Invention
In order to overcome the defects and shortcomings of the prior art, the primary purpose of the invention is to provide a preparation method of a high specific capacity silicon-carbon anode material. The invention adopts the steps of coating an amorphous carbon layer on the surface of nano silicon particles in advance to obtain a core-shell structure silicon-carbon composite material which is coated in a sealing way, and then uniformly dispersing the core-shell structure silicon-carbon composite material in a carbon network matrix to obtain a final material. An electric conduction bridge is formed between the amorphous carbon layer on the surface of the nano silicon particles and the carbon network matrix material, so that the electric conductivity of the nano silicon particles can be effectively improved, and the nano silicon particles can be used as a protective layer for buffering the volume expansion of the nano silicon particles to maintain the stability of the whole material structure, and have more excellent electrochemical cycle performance.
The invention also aims to provide the high specific capacity silicon-carbon anode material prepared by the method.
The invention also aims to provide the application of the high-specific-capacity silicon-carbon anode material in a lithium ion battery.
The aim of the invention is achieved by the following scheme:
the preparation method of the high specific capacity silicon-carbon negative electrode material comprises the following steps:
(1) Completely soaking purchased food-grade coconuts (BC, bacterial cellulose) in NaOH solution for heating treatment, filtering and washing to neutrality to obtain BC hydrogel, and drying the BC hydrogel by adopting a freeze-drying technology to obtain white BC aerogel;
(2) Placing the BC aerogel in a tube furnace, and carbonizing in a nitrogen atmosphere to obtain a CBC carbon material;
(3) Acidizing the prepared CBC carbon material;
(4) Coating the surfaces of the nano silicon particles with an organic carbon source, and carbonizing in an inert atmosphere or under nitrogen to obtain a Si/C composite material;
(5) Dispersing the CBC carbon material subjected to the acidification treatment in the step (3) in water, adding the Si/C composite material for liquid phase mixing, and then centrifugally filtering and vacuum drying to prepare the high specific capacity silicon-carbon anode material.
The heating treatment in the step (1) refers to water bath/oil bath treatment at 60-80 ℃ for 2-4 h.
Preferably, the heating treatment in the step (1) is preferably a water bath/oil bath treatment of completely immersing the coconut (15 mm cube) in 2-4 mol/L NaOH solution at 60-80 ℃ for 2-4 hours.
The step (1) of washing to neutrality is preferably washing with water firstly, then soaking with deionized water, and water is changed for a plurality of times until the soaking solution is neutral, wherein the soaking time is preferably 3-7d;
the freeze drying time in the step (1) is 72 hours, and the vacuum degree is 20-50 Pa.
The carbonization treatment in the step (2) is to heat to 300-500 ℃ at a heating rate of 1-3 ℃/min for 2-3 hours, and then heat to 600-800 ℃ at a heating rate of 4-5 ℃/min for 2-4 hours.
The carbonization treatment in the step (2) is preferably followed by grinding and pulverizing the obtained carbonized product and sieving with a 100-mesh sieve to obtain the CBC carbon material.
The acidification treatment in the step (3) refers to the use of HNO with the concentration of 2-4 mol/L 3 And (3) carrying out reflux treatment on the solution for 6-8 hours at 90 ℃, then centrifugally washing to obtain a supernatant which is neutral, collecting a sample, and drying to obtain the acidized CBC carbon material.
In the process of coating the organic carbon source in the step (4), resorcinol and formaldehyde are adopted as coating raw materials.
The step (4) of coating the surfaces of the nano silicon particles with organic carbon sources specifically comprises the following steps: fully dissolving nano silicon and CTAB in water, adding absolute ethyl alcohol, resorcinol, ammonia water and formaldehyde aqueous solution into the solution, uniformly stirring and dissolving, heating at 30-40 ℃ for 4-6 h, finally moving to room temperature and stirring overnight, centrifuging, filtering and washing, drying and collecting a sample, and obtaining the phenolic resin coated silicon composite material. Wherein the dosage ratio of each substance is as follows: resorcinol: formaldehyde=1: 2 (molar ratio), nano silicon: ctab=1: 2-1: 4 (mass ratio), nano silicon (Aladin, 60-100 nm): resorcinol=1: 0.5 to 1:4 (mass ratio).
The carbonization treatment in the step (4) means calcining for 2-4 hours at 600-800 ℃ at a heating rate of 2-4 ℃/min and cooling along with a furnace.
In the liquid phase mixing process in the step (5), the mass ratio of the Si/C composite material to the acidified CBC carbon material is 1:0.5 to 1:4, the liquid phase mixing time is 6-13 h, preferably, ultrasonic dispersion is carried out for 20-30 min, and then magnetic stirring is carried out for 6-12 h.
The vacuum drying in the step (5) refers to drying in a vacuum drying oven at 80-100 ℃ for 12-24 hours.
The high specific capacity silicon-carbon anode material prepared by the method can still effectively maintain the capacity at 1251.7mAh/g after being cycled for 100 circles under the current density of 500 mA/g.
The high specific capacity silicon-carbon anode material has excellent electrochemical performance and wide application prospect in a lithium ion battery system.
Compared with the prior art, the invention has the following advantages:
1) According to the high specific capacity silicon-carbon composite anode material, nano silicon particles are coated with an amorphous carbon layer in advance and then uniformly dispersed in a carbon network matrix, so that the silicon-carbon composite material with a relatively high specific surface area is obtained;
2) According to the invention, the proportion between the nano silicon and the resorcinol is regulated and controlled, the core-shell type silicon-carbon composite material is dispersed in the carbon fiber network matrix material, and a conductive bridge is formed between the amorphous carbon layer on the surface of the silicon particles and the carbon fiber, so that the conductivity of the material is effectively improved, and meanwhile, a strong buffer space is provided for the volume expansion of silicon.
Drawings
Fig. 1 is an XRD pattern of the silicon carbon composites prepared in examples 1 to 4 and the commercialized nano-silicon particles of comparative example 1.
Fig. 2 is a TEM image of the silicon carbon composite material prepared in examples 2 and 4.
FIG. 3 is a thermogravimetric analysis curve of the silicon carbon composites prepared in examples 1 to 4 and the commercial nano-silicon particles of comparative example 1.
Fig. 4 is a raman spectrum of the silicon-carbon composite materials prepared in examples 1 to 4 and the commercialized nano-silicon particles of comparative example 1.
Fig. 5 is an N2 adsorption/desorption isothermal curve and pore size distribution diagram of the silicon carbon composite material prepared in examples 2 and 4 and the commercialized nano-silicon particles of comparative example 1.
FIG. 6 is a graph comparing the cycle performance of the silicon carbon composites prepared in examples 1 to 4 and the commercial nano-silicon particles of comparative example 1 at a current density of 500 mA/g.
Detailed Description
The present invention will be described in further detail with reference to examples and drawings, but embodiments of the present invention are not limited thereto. The specific conditions are not noted in the examples and are carried out according to conventional conditions or conditions recommended by the manufacturer. The reagents or apparatus used were conventional products commercially available without the manufacturer's attention.
The reagents used in the examples are commercially available as usual unless otherwise specified.
Example 1
The preparation method of the high specific capacity silicon-carbon negative electrode material comprises the following steps:
1) Coating the nano silicon particles with phenolic resin according to resorcinol: formaldehyde=1: 2 (molar ratio), nano silicon: ctab=1: 2 (mass ratio), nano silicon (Aladin, 60-100 nm): resorcinol=1: 0.5 Firstly, weighing 0.5g SiNPs and 1g CTAB, adding into a beaker filled with 50mL deionized water, and performing ultrasonic dispersion for 20min; to the solution was then added 25mL of absolute ethanol, 0.25g of resorcinol, 0.2mL of aqueous ammonia solution, and 0.35mL of formaldehyde solution (37 wt% formaldehyde solution for Melin), and the solution was dissolved by magnetic stirring and then transferred to a 40℃water bath for 4h water bath. And finally, moving to room temperature and stirring overnight, and then centrifuging, filtering, washing, drying and collecting a sample to obtain the phenolic resin coated silicon composite material.
2) Drying the collected sample under N 2 Under the atmosphereAnd (3) performing high-temperature carbonization treatment, calcining for 3 hours at 700 ℃ at a heating rate of 2 ℃/min, cooling to room temperature, and taking out to obtain the silicon-carbon negative electrode material for the lithium ion battery.
Half cell assembly and performance characterization: the silicon-carbon composite material prepared in example 1 was mixed with a conductive agent acetylene black, a binder PVDF at 8:1:1, slowly adding NMP organic solvent in the grinding process to form uniform electrode slurry, coating the electrode slurry on the surface of a copper foil current collector, and carrying out vacuum drying, punching and tabletting to obtain the negative plate. The prepared negative electrode sheet was placed in a glove box, and a coin cell (CR 2016) was prepared from an active electrode, a separator (PE separator (polyethylene) having a thickness of 25 μm, available from Celgard Co., USA), and an electrolyte (LiPF having a concentration of 1 mol/L) 6 The solute is LiPF 6 The solvent is an EC+DMC+EMC (volume ratio is 1:1:1) system), the metal lithium sheet is used as a counter electrode, and the anode and cathode shells are assembled in a glove box. The assembled battery cycle performance test conditions: the current density is 500mA/g, and the voltage interval is 0.01-3V, and the cycle is 100 circles. The test results are shown in Table 1.
Example 2:
the preparation method of the high specific capacity silicon-carbon negative electrode material comprises the following steps:
1) Coating the nano silicon particles with phenolic resin according to resorcinol: formaldehyde=1: 2 (molar ratio), nano silicon: ctab=1: 2 (mass ratio), nano silicon (Aladin, 60-100 nm): resorcinol=1: 1 (mass ratio), firstly weighing 0.5g SiNPs and 1g CTAB, adding into a beaker filled with 50mL deionized water, and performing ultrasonic dispersion for 20min; then, 25mL of absolute ethyl alcohol, 0.5g of resorcinol, 0.2mL of ammonia water solution and 0.7mL of formaldehyde solution were added to the solution, and the solution was dissolved by magnetic stirring and then transferred to a water bath kettle at 40 ℃ for 4h of water bath. And finally, moving to room temperature and stirring overnight, and then centrifuging, filtering, washing, drying and collecting a sample to obtain the phenolic resin coated silicon composite material.
2) Drying the collected sample under N 2 And (3) carrying out high-temperature carbonization treatment in the atmosphere, calcining for 3 hours at 700 ℃ at a heating rate of 2 ℃/min, cooling to room temperature, and taking out to obtain the silicon-carbon anode material for the lithium ion battery.
The battery assembly and performance characterization conditions were the same as in example 1, except that the negative electrode materials were different, and the test results are shown in table 1.
Example 3:
the preparation method of the high specific capacity silicon-carbon negative electrode material comprises the following steps:
1) Coating the nano silicon particles with phenolic resin according to resorcinol: formaldehyde=1: 2 (molar ratio), nano silicon: ctab=1: 2 (mass ratio), nano silicon (Aladin, 60-100 nm): resorcinol=1: 2 (mass ratio), firstly weighing 0.5g SiNPs and 1g CTAB, adding into a beaker filled with 50mL deionized water, and performing ultrasonic dispersion for 20min; then, 25mL of absolute ethyl alcohol, 1g of resorcinol, 0.2mL of aqueous ammonia solution and 1.4mL of formaldehyde solution were added to the solution, and the solution was magnetically stirred and dissolved, and then transferred to a water bath kettle at 40℃for 4h of water bath. And finally, moving to room temperature and stirring overnight, and then centrifuging, filtering, washing, drying and collecting a sample to obtain the phenolic resin coated silicon composite material.
2) Drying the collected sample under N 2 And (3) carrying out high-temperature carbonization treatment in the atmosphere, calcining for 3 hours at 700 ℃ at a heating rate of 2 ℃/min, cooling to room temperature, and taking out to obtain the silicon-carbon anode material for the lithium ion battery.
The battery assembly and performance characterization conditions were the same as in example 1, except that the negative electrode materials were different, and the test results are shown in table 1.
Example 4:
the preparation method of the high specific capacity silicon-carbon negative electrode material comprises the following steps:
1) Completely soaking coconuts (15 mm cubes) in 4mol/L NaOH solution, treating the coconuts in water bath/oil bath at 80 ℃ for 4 hours, filtering the coconuts, washing the coconuts with deionized water for multiple times, soaking the coconuts in the deionized water for 3 days, and changing water for multiple times until the soaking solution is neutral, thereby obtaining the BC hydrogel. Freeze-drying the obtained BC hydrogel for 72 hours with the vacuum degree of 30Pa to obtain BC aerogel;
2) Carbonizing the BC aerogel, heating to 400 ℃ at a heating rate of 2 ℃/min, preserving heat for 2 hours, and heating to 700 ℃ at a heating rate of 4 ℃/min, preserving heat for 2 hours;
3) Acidizing the prepared CBC material in 3mol/L nitric acid solution, refluxing at 90 ℃ for 6 hours, centrifugally washing for many times until the supernatant is neutral, collecting a sample, and drying to obtain a pretreated CBC carbon material;
4) Coating the nano silicon particles with phenolic resin according to resorcinol: formaldehyde=1: 2 (molar ratio), nano silicon: ctab=1: 2 (mass ratio), nano silicon (Aladin, 60-100 nm): resorcinol=1: 1 (mass ratio), firstly weighing 0.5g SiNPs and 1g CTAB, adding into a beaker filled with 50mL deionized water, and performing ultrasonic dispersion for 20min (ultrasonic power is 360W, ultrasonic frequency is 40 KHz); then, 25mL of absolute ethyl alcohol, 0.5g of resorcinol, 0.2mL of ammonia water solution and 0.7mL of formaldehyde solution were added to the solution, and the solution was dissolved by magnetic stirring and then transferred to a water bath kettle at 40 ℃ for 4h of water bath. Finally, the mixture is moved to room temperature and stirred overnight, and then the mixture is subjected to centrifugation, suction filtration and washing, drying and sample collection, and the collected sample is carbonized in a tube furnace, calcined for 3 hours at 700 ℃ at a heating rate of 2 ℃/min and cooled with the furnace, so that a material coated by an organic carbon source is obtained;
5) The material coated by the organic carbon source and the CBC carbon material obtained in the step (3) are mixed according to the mass ratio of 1:1, carrying out liquid phase mixing, dispersing the pretreated CBC carbon material in a beaker filled with deionized water, adding the Si/C composite material into the beaker, dispersing for 20min by ultrasonic waves (the ultrasonic power is 360W, and the ultrasonic frequency is 40 KHz), magnetically stirring for 8h, centrifuging, filtering, and drying in a vacuum drying oven at 100 ℃ for 24h to obtain a silicon-carbon anode material for the lithium ion battery;
the battery assembly and performance characterization conditions were the same as in example 1, except that the negative electrode materials were different, and the test results are shown in table 1.
Comparative example 1:
the commercial nano silicon particles (Aladin, 60-100 nm) are directly used as the cathode material for half-cell assembly and performance characterization, and the battery assembly mode and performance characterization conditions are the same as those of the embodiment 1, except that the cathode material is different, and the test results are shown in table 1.
Performance test:
fig. 1 is an XRD pattern of the silicon carbon composites prepared in examples 1 to 4 and the commercialized nano-silicon particles of comparative example 1. Wherein (a) is the XRD patterns of examples 1 to 3 and comparative example 1; (b) is the XRD patterns of example 2 and example 4. As is clear from XRD patterns of examples 1 to 4 and comparative example 1, the materials all show three strong peaks of silicon, and no diffraction peak of the carbon material appears, which means that the thin carbon layer formed after pyrolysis and carbonization of the organic matter and the CBC carbon material all belong to an amorphous carbon material, and the amorphous peak is masked by the diffraction peak of silicon with stronger crystallinity;
fig. 2 is a TEM image of the silicon carbon composite material prepared in examples 2 and 4, wherein (a) to (c) are TEM images of example 2; (d) - (f) are TEM images of example 4. From the TEMs of (a) to (c) of example 2, it is clear that: the TEM of examples 4 (d) to (f) showed that the surface carbon layer was coated with a layer having a thickness of about 7 nm: good conductive bridges are formed between the amorphous carbon layer on the surface of the silicon particles and the CBC carbon material, and the material is uniformly distributed on the CBC carbon network matrix;
FIG. 3 shows thermogravimetric analysis curves of examples 1 to 4 and comparative example 1. As can be seen from fig. 3, as the ratio of the amount of nano-silicon to resorcinol increases, the carbon content increases gradually;
fig. 4 is a raman spectrum of the silicon-carbon composite materials prepared in examples 1 to 4 and the commercialized nano-silicon particles of comparative example 1. As can be seen from the figure, as the carbon content increases, I in the composite material D /I G The ratio of (2) is gradually increased, which indicates that the defect degree of the material is large, and the electron conductivity and the rapid diffusion of lithium ions are more favorable to be improved.
FIG. 5 is N of commercial nano-silicon particles of the silicon-carbon composite materials prepared in examples 2 and 4 and comparative example 1 2 Adsorption/desorption isothermal curves and pore size distribution diagrams. As can be seen from the figure, the silicon-carbon negative electrode material prepared in example 4 has a large specific surface area.
The silicon-carbon composite materials prepared in examples 1 to 4 and the commercialized nano-silicon particles of comparative example 1 were subjected to battery assembly and performance tests, and the test results are shown in the following table:
results of cycle performance test of examples 1 to 4 and comparative example 1
FIG. 6 is a graph comparing the cycle performance of the silicon carbon composites prepared in examples 1 to 4 and the commercial nano-silicon particles of comparative example 1 at a current density of 500 mA/g. As can be seen from fig. 6 and table 1, the silicon carbon negative electrode material prepared in example 4 has a higher cycle capacity.
The above examples are preferred embodiments of the present invention, but the embodiments of the present invention are not limited to the above examples, and any other changes, modifications, substitutions, combinations, and simplifications that do not depart from the spirit and principle of the present invention should be made in the equivalent manner, and the embodiments are included in the protection scope of the present invention.

Claims (10)

1. The preparation method of the high specific capacity silicon-carbon anode material is characterized by comprising the following steps of:
(1) Completely soaking coconuts in NaOH solution for heating treatment, filtering and washing to neutrality to obtain BC hydrogel, and drying the BC hydrogel by adopting a freeze drying technology to obtain white BC aerogel;
(2) Placing the BC aerogel in a tube furnace, and carbonizing in a nitrogen atmosphere to obtain a CBC carbon material;
(3) Acidizing the prepared CBC carbon material;
(4) Coating the surfaces of the nano silicon particles with an organic carbon source, and carbonizing in an inert atmosphere or under nitrogen to obtain a Si/C composite material;
(5) Dispersing the CBC carbon material subjected to the acidification treatment in the step (3) in water, adding the Si/C composite material for liquid phase mixing, and then centrifugally filtering and vacuum drying to prepare the high specific capacity silicon-carbon anode material.
2. The method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
the heating treatment in the step (1) refers to water bath/oil bath treatment at 60-80 ℃ for 2-4 hours;
the concentration of the NaOH solution in the step (1) is 2-4 mol/L.
3. The method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
the carbonization treatment in the step (2) is to heat to 300-500 ℃ at a heating rate of 1-3 ℃/min for 2-3 hours, and then heat to 600-800 ℃ at a heating rate of 4-5 ℃/min for 2-4 hours.
4. The method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
the acidification treatment in the step (3) refers to the use of HNO with the concentration of 2-4 mol/L 3 And (3) carrying out reflux treatment on the solution for 6-8 hours at 90 ℃, then centrifugally washing to obtain a supernatant which is neutral, collecting a sample, and drying to obtain the acidized CBC carbon material.
5. The method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
in the process of coating the organic carbon source in the step (4), resorcinol and formaldehyde are adopted as coating raw materials.
6. The method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
the step (4) of coating the surfaces of the nano silicon particles with organic carbon sources specifically comprises the following steps: fully dissolving nano silicon and CTAB in water, adding absolute ethyl alcohol, resorcinol, ammonia water and formaldehyde aqueous solution into the solution, uniformly stirring and dissolving, heating at 30-40 ℃ for 4-6 h, finally moving to room temperature and stirring overnight, centrifuging, filtering and washing, drying and collecting a sample to obtain the phenolic resin coated silicon composite material; wherein the dosage ratio of each substance is as follows: the molar ratio of resorcinol to formaldehyde is 1: 2. the mass ratio of the nano silicon to CTAB is 1: 2-1: 4. the mass ratio of the nano silicon to the resorcinol is 1:0.5 to 1:4.
7. the method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
the carbonization treatment in the step (4) means calcining for 2-4 hours at 600-800 ℃ at a heating rate of 2-4 ℃/min and cooling along with a furnace.
8. The method for preparing the high specific capacity silicon-carbon negative electrode material according to claim 1, wherein the method comprises the following steps:
in the liquid phase mixing process in the step (5), the mass ratio of the Si/C composite material to the acidified CBC carbon material is 1:0.5 to 1:4, the liquid phase mixing time is 6-13 h.
9. A high specific capacity silicon carbon negative electrode material prepared by the method of any one of claims 1-8.
10. The use of the high specific capacity silicon-carbon negative electrode material according to claim 9 in lithium ion batteries.
CN202310257954.XA 2023-03-16 2023-03-16 High specific capacity silicon-carbon negative electrode material and preparation method and application thereof Pending CN116477600A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202310257954.XA CN116477600A (en) 2023-03-16 2023-03-16 High specific capacity silicon-carbon negative electrode material and preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202310257954.XA CN116477600A (en) 2023-03-16 2023-03-16 High specific capacity silicon-carbon negative electrode material and preparation method and application thereof

Publications (1)

Publication Number Publication Date
CN116477600A true CN116477600A (en) 2023-07-25

Family

ID=87225838

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202310257954.XA Pending CN116477600A (en) 2023-03-16 2023-03-16 High specific capacity silicon-carbon negative electrode material and preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN116477600A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102709536A (en) * 2012-06-28 2012-10-03 东华大学 Silicon-carbon composite material and preparation method thereof
CN103474667A (en) * 2013-08-16 2013-12-25 深圳市贝特瑞新能源材料股份有限公司 Silicon-carbon composite negative electrode material for lithium ion battery and preparation method thereof
CN105609711A (en) * 2014-11-21 2016-05-25 国家纳米科学中心 Micro-nano structured silicon-carbon composite microsphere, preparation method and application thereof
CN111470486A (en) * 2020-04-14 2020-07-31 陕西煤业化工技术研究院有限责任公司 Three-dimensional silicon-carbon composite negative electrode material, preparation method thereof and application thereof in lithium ion battery
CN112510185A (en) * 2020-11-30 2021-03-16 南通路远科技信息有限公司 Silicon-carbon composite negative electrode material and manufacturing method thereof
RU2767168C1 (en) * 2020-12-29 2022-03-16 Федеральное государственное бюджетное учреждение науки Институт проблем химической физики РАН (ИПХФ РАН) Silicon-carbon material of negative electrode of lithium-ion battery and method of preparation thereof (embodiments)
CN114709386A (en) * 2022-03-24 2022-07-05 华南理工大学 Porous silicon-carbon composite material and preparation method and application thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102709536A (en) * 2012-06-28 2012-10-03 东华大学 Silicon-carbon composite material and preparation method thereof
CN103474667A (en) * 2013-08-16 2013-12-25 深圳市贝特瑞新能源材料股份有限公司 Silicon-carbon composite negative electrode material for lithium ion battery and preparation method thereof
CN105609711A (en) * 2014-11-21 2016-05-25 国家纳米科学中心 Micro-nano structured silicon-carbon composite microsphere, preparation method and application thereof
CN111470486A (en) * 2020-04-14 2020-07-31 陕西煤业化工技术研究院有限责任公司 Three-dimensional silicon-carbon composite negative electrode material, preparation method thereof and application thereof in lithium ion battery
CN112510185A (en) * 2020-11-30 2021-03-16 南通路远科技信息有限公司 Silicon-carbon composite negative electrode material and manufacturing method thereof
RU2767168C1 (en) * 2020-12-29 2022-03-16 Федеральное государственное бюджетное учреждение науки Институт проблем химической физики РАН (ИПХФ РАН) Silicon-carbon material of negative electrode of lithium-ion battery and method of preparation thereof (embodiments)
CN114709386A (en) * 2022-03-24 2022-07-05 华南理工大学 Porous silicon-carbon composite material and preparation method and application thereof

Similar Documents

Publication Publication Date Title
WO2022121136A1 (en) Artificial graphite negative electrode material for high-rate lithium ion battery and preparation method therefor
CN107170965B (en) Silicon-carbon composite material and preparation method and application thereof
WO2017121069A1 (en) Preparation of hard carbon negative electrode material for lithium ion power battery and modification method therefor
CN109626352B (en) Hard carbon-like graphite negative electrode material for high-rate lithium ion battery and preparation method thereof
CN108269982B (en) Composite material, preparation method thereof and application thereof in lithium ion battery
CN115259132B (en) Preparation method and application of ultra-high first-effect hard carbon anode material
CN107337205B (en) Method for converting waste corn straw into sodium-ion battery electrode material
CN106159198A (en) A kind of asphaltic base amorphous carbon negative material, its preparation method and application
CN108123110A (en) A kind of preparation method and application of nitrogenous big pore volume porous carbon materials
CN114335522A (en) Coal-based carbon negative electrode material, preparation method and application thereof, and battery containing coal-based carbon negative electrode material
CN113415799A (en) PTCDA modified resin-based carbon material and preparation method and application thereof
CN114702022B (en) Preparation method and application of hard carbon anode material
CN113078320B (en) Melamine modified graphite negative electrode material and preparation method and application thereof
CN116741992B (en) Porous hard carbon material and preparation method thereof, negative electrode plate and sodium ion battery
CN108565431B (en) Method for preparing silicon-carbon composite negative electrode material of lithium ion battery by taking konjac flour as carbon source
CN114873591B (en) Low-temperature long-life natural graphite anode material and preparation method and application thereof
CN114314556B (en) Resin-based carbon negative electrode material, preparation method and application thereof, and battery containing resin-based carbon negative electrode material
CN116014146A (en) Self-supporting biomass carbon current collector, composite current collector and application
CN109256547A (en) A kind of preparation method of porous graphene-lithium iron phosphate positive material
CN116477600A (en) High specific capacity silicon-carbon negative electrode material and preparation method and application thereof
CN111086981B (en) Biomass carbon nanosheet lithium ion battery cathode material and preparation method thereof
CN111276683A (en) Silicon dioxide sulfur positive electrode rich in aluminum hydroxyl and preparation method thereof
CN111129440A (en) Silicon dioxide-carbon composite material, preparation method thereof and application thereof in lithium ion battery cathode material
CN114400307B (en) Tin-carbon composite material and preparation method and application thereof
CN108899534B (en) Preparation method of vanadium oxide as positive electrode material of lithium ion battery capacitor

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination