CN108110231A - A kind of carbon coating Fe4N nanocomposites, preparation method and applications - Google Patents

A kind of carbon coating Fe4N nanocomposites, preparation method and applications Download PDF

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CN108110231A
CN108110231A CN201711265934.8A CN201711265934A CN108110231A CN 108110231 A CN108110231 A CN 108110231A CN 201711265934 A CN201711265934 A CN 201711265934A CN 108110231 A CN108110231 A CN 108110231A
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carbon coating
nanocomposites
small
powder
fecl
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CN108110231B (en
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张博栋
詹世英
马美品
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Yinlong New Energy Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • 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
    • H01M4/133Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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

Abstract

The present invention provides a kind of carbon coating Fe for ion cathode material lithium4N nanocomposites, preparation method and applications.The carbon coating Fe4The size of N nanocomposites is 30 100nm, and the thickness of carbon coating layer is 5 10nm.Method includes:By dicyandiamide and FeCl3·6H2The solution that O dissolvings are uniformly mixed, heating evaporating water obtain dicyandiamide and FeCl3·6H2The mixture of O, the temperature reaction in tube furnace obtain Fe after cooling4N powder coats Fe using glucose4N powder obtains carbon coating Fe after carbonization4N nanometer combined electrode materials.This method manufacturing cost is low, simple for process, the carbon coating Fe being prepared4N nanocomposite patterns are homogeneous, for ion cathode material lithium, have good storage lithium performance, cycle life and high rate performance.

Description

A kind of carbon coating Fe4N nanocomposites, preparation method and applications
Technical field
The present invention relates to novel energy resource material technology fields, and in particular to a kind of carbon bag for lithium ion battery negative material Cover Fe4N nanocomposites, preparation method and its application in lithium ion battery negative material.
Background technology
Lithium ion battery due to its high-energy, high power density, high security and it is environmental-friendly the features such as it is extensive For fields such as mobile electronic device energy storage.At present, for lithium ion battery research just towards high-energy or power density, compared with Good cryogenic property and the direction of the power battery material of high rate capability are developed.Existing lithium ion battery negative material master If carbon negative pole material, but due to the theoretical capacity of commercial graphite cathode relatively low (372mAh/g), poor high rate performance, The S EI films (solid electrolyte film) that first charge-discharge is formed greatly cause the loss of capacity and easily safety problem etc. are triggered to lack Point strongly limits the application in high power density type power battery field.In order to develop a kind of high-energy density and high safety Property lithium ion battery negative material meet the needs of high power type power battery, realize higher economic benefits, social benefit And the development strategy deployment of country, so there is an urgent need to find the substitute of graphite cathode material.The spy of new electrode materials Rope is most important for developing the rechargeable lithium ion batteries with high power capacity and excellent stability.Graphite cathode material at present Substitute includes modified graphite, Si sills, Sn sills and MnXmType (M is transition metal, X be it is nonmetallic including O, S, N, P, B or polymer) material.For MnXmThe storage lithium mechanism of section bar material resolves into M for active material portion or completely reversibility0And phase The lithium salts answered, wherein can be expressed simply as
Transition metal nitride due to its with excellent chemical property, high chemical stability and be expected to be applied to power In cell negative electrode material.The specific electronic structure of transition elements (IIIB-VIII races) is characterized in that valence electron can take up portion Divide the d tracks of filling, because energy level of the electronics between 4s and 3d, 5s and 4d or 6s and 5d approaches.When nitride participates in During redox reaction, multivalent state is generated effectively to store energy.However up to the present, the nitride as active material Practical application is far from, this is because its larger volume expansion causes the capacity during electrochemical reaction is cycled quickly to decline Subtract.
The content of the invention
To solve the above-mentioned problems, the present invention provides a kind of carbon coating Fe4N nanocomposites, preparation method and its In the application of lithium ion battery negative material.By by Fe4N active materials are reduced in size to nanoscale, shorten lithium ion Diffusion path and storage time and the cycling for effectively reducing mechanical stress to adapt to the variation of different volumes and improve electrode material Ability, also, by by Fe4N active materials are compounded to form carbon coating structure with carbon, it is prevented to be reacted with electrolyte, and protection is lived Property substance Fe4N, improves the stability of material, while inhibits its Volumetric expansion and Fe4The shortcomings of N easily reunites, also, carbon There is the variation of buffers active substance excess volume during embedding lithium/de- lithium is cycled, carbon material is due to the lithium of its own Ion storage ability and have certain contribution to the promotion of battery capacity, the compound electric conductivity for improving electrode of carbon and contribute to By the electron transmission generated during the redox reaction of active material to collector, so as to improve as lithium ion battery Cycle performance and high rate performance during negative material.
The present invention adopts the following technical scheme that:
A kind of carbon coating Fe4N nanocomposites, the Fe4The surface of N particles has carbon coating layer, the carbon coating layer Thickness be 5-10nm, carbon coating Fe4The size of N nanocomposites is 30-100nm.
A kind of carbon coating Fe4The preparation method of N nanocomposites, this method comprises the following steps:
(1) by dicyandiamide and FeCl3·6H2O is dissolved in deionized water, with magnetic stirrer, is uniformly mixed Solution
(2) solution obtained to step (1) heats, until the moisture in solution is evaporated completely, obtain dicyandiamide with FeCl3·6H2The mixture of O;
(3) mixture obtained by step (2) is placed in porcelain boat, be positioned in tube furnace, is warming up under argon atmosphere 850-950℃;
(4) when the reaction tube internal temperature in tube furnace reaches 850-950 DEG C, argon gas is closed, is passed through into reaction tube Ammonia, the temperature in reaction tube continue to be increased to 950-1050 DEG C, when keeping 1-2 small, are continually fed into ammonia until tube furnace drops To room temperature, the powder for collecting brown on porcelain boat obtains Fe4N;Wherein, ammonia flow velocity is 80-120mL/min;
(5) Fe for obtaining step (4)4N powder is with glucose according to 1:The mass ratio of (1-8) is dissolved in deionized water, After when mechanical agitation 3-5 is small, final solution is transferred in polytetrafluoroethylliner liner reaction kettle, is positioned in drying box, in When 160-200 DEG C of heat preservation 8-12 is small, Fe is coated by centrifuging and being dried to obtain glucose4The powder of N;
(6) powder that step (5) obtains is placed in tube furnace, heat up carbonization under the atmosphere of argon gas, finally obtains carbon Coat Fe4N nanocomposites.
Preferably, in step (1), dicyandiamide, FeCl3·6H2O and the mass ratio of deionized water are (5-10):(3-5): (250-350).Preferably, in step (3), argon gas flow velocity is 60-100mL/min.
Preferably, in step (3), 900 DEG C are warming up under argon atmosphere.
Preferably, in step (4), the temperature in reaction tube continues to be increased to 1000 DEG C, when holding 1.5 is small.
Preferably, in step (5), when 180 DEG C of heat preservations 10 are small.
Preferably, in step (6), in tube furnace, be warming up under the atmosphere of argon gas 500-900 DEG C maintain 1-2 it is small when It is carbonized, it is furthermore preferred that when carbonization time is that 800 DEG C of maintenances 1 are small.
The carbon coating Fe that the present invention is prepared4N nanocomposites, Fe4The surface of N nano particles has carbon coating layer, The thickness of the carbon coating layer is 5-10nm, carbon coating Fe4The size of N nanocomposites is 30-100nm.
Carbon coating Fe of the present invention4N nanocomposites are used for lithium ion battery negative material, are cycled through electrical property Testing experiment shows there is good storage lithium performance, cycle life and high rate performance:After charging and discharging cycle 100 times, material The specific capacity of material remains at more than 730mAh/g;Also, high rate performance experiments have shown that, the material is in high current density After carrying out multiple charge and discharge under 100mA/g, the high reversible capacity of more than 740mAh/g is still kept, the material is in high magnification charge and discharge Invertibity is good after electricity.
Compared with prior art, the present invention with advantageous effect following prominent:
(1) present invention prepares carbon coating Fe by hydro-thermal method and high temperature pyrolytic cracking (HTP)4It is prepared by N composite nano materials, production It is at low cost, it is simple for process, it is easy to control;
(2) the carbon coating Fe that the present invention is prepared4N nanocomposite patterns are homogeneous, Fe4The surface tool of N nano particles There is carbon coating layer, the thickness of the carbon coating layer is 5-10nm, carbon coating Fe4The size of N nanocomposites is 30-100nm , by the way that active material is reduced to nanoscale, the diffusion path and storage time of lithium ion are shortened, effectively reducing machinery should Power significantly improves the circulation ability of electrode material to adapt to the variation of different volumes;
(3) present invention is by by Fe4N active materials are compounded to form carbon coating structure with carbon, it is prevented to be reacted with electrolyte, Protection activity substance Fe4N, improves the stability of material, while inhibits its Volumetric expansion and Fe4The shortcomings of N easily reunites;
(4) the carbon coating Fe that the present invention is prepared4N nanocomposites have good for ion cathode material lithium Storage lithium performance, cycle life and high rate performance, electrical property loop test experiments have shown that:After charging and discharging cycle 100 times, Specific capacity remains at more than 730mAh/g;And high rate performance experiments have shown that, the material carries out more at higher current densities After secondary charge and discharge, the reversible capacity of more than 740mAh/g is still kept, i.e., the invertibity of material is good after high power charging-discharging.
Description of the drawings
Fig. 1 is Fe4The XRD diagram of N materials;
Fig. 2 is carbon coating Fe of the present invention4The TEM figures of N composite nano materials, (a) and (b) is respectively carbon coating Fe4N is compound Low power and high-resolution the projection figure of nano material;
Fig. 3 is carbon coating Fe of the present invention4Cycle performance when N composite nano materials are as lithium ion battery negative material Figure;
Fig. 4 is carbon coating Fe of the present invention4High rate performance when N composite nano materials are as lithium ion battery negative material Figure.
Specific embodiment
Embodiment 1:
(1) by dicyandiamide and FeCl3·6H2O is dissolved in deionized water, with magnetic stirrer 4h, is uniformly mixed Solution, wherein dicyandiamide, FeCl3·6H2O and the mass ratio of deionized water are 5:3:250;
(2) solution obtained to step (1) heats, until the moisture in solution is evaporated completely, obtain dicyandiamide with FeCl3·6H2The mixture of O;
(3) mixture obtained by step (2) is placed in porcelain boat, be positioned in tube furnace, be 60mL/min's in flow velocity 850 DEG C are warming up under argon atmosphere;
(4) when the reaction tube internal temperature in tube furnace reaches 850 DEG C, argon gas is closed, 80mL/ is passed through into reaction tube The ammonia of min, the temperature in reaction tube continue to be increased to 950 DEG C, and continue 2 it is small when, it is still 80mL/min to be continually fed into flow velocity Ammonia until tube furnace is down to room temperature, the powder for collecting brown on porcelain boat can obtain Fe4N;
(5) Fe for obtaining step (4)4N is with glucose according to 1:1 mass ratio is dissolved in deionized water, mechanical agitation 3 After hour, final solution is transferred in polytetrafluoroethylliner liner reaction kettle, is positioned in drying box, in 160 DEG C of heat preservations 12 it is small when, by centrifuge and be dried to obtain glucose coat Fe4The powder of N;
(6) powder that step (5) obtains is placed in tube furnace, be warming up under the atmosphere of argon gas 500 DEG C maintain 2 it is small when It is carbonized, finally obtains carbon coating Fe4N composite materials.
Embodiment 2:
(1) by dicyandiamide and FeCl3·6H2O is dissolved in deionized water, with magnetic stirrer 4h, is uniformly mixed Solution, wherein dicyandiamide, FeCl3·6H2O and the mass ratio of deionized water are 6:4:280;
(2) solution obtained to step (1) heats, until the moisture in solution is evaporated completely,
Obtain dicyandiamide and FeCl3·6H2The mixture of O;
(3) mixture obtained by step (2) is placed in porcelain boat, be positioned in tube furnace, be 80mL/min's in flow velocity 900 DEG C are warming up under argon atmosphere;
(4) when the reaction tube internal temperature in tube furnace reaches 900 DEG C, argon gas is closed, is passed through into reaction tube The ammonia of 100mL/min, the temperature in reaction tube continue to be increased to 1000 DEG C, and continue 1.5 it is small when, being continually fed into flow velocity is still For the ammonia of 100mL/min until tube furnace is down to room temperature, the powder for collecting brown on porcelain boat can obtain Fe4N;
(5) Fe for obtaining step (4)4N is with glucose according to 1:2 mass ratio is dissolved in deionized water, mechanical agitation 4 After hour, final solution is transferred in polytetrafluoroethylliner liner reaction kettle, is positioned in drying box, in 180 DEG C of heat preservations 10 it is small when, by centrifuge and be dried to obtain glucose coat Fe4The powder of N;
(6) powder that step (5) obtains is placed in tube furnace, be warming up under the atmosphere of argon gas 600 DEG C maintain 1 it is small when It is carbonized, finally obtains carbon coating Fe4N composite materials.
Embodiment 3:
(1) by dicyandiamide and FeCl3·6H2O is dissolved in deionized water, with magnetic stirrer 4h,
The solution being uniformly mixed, wherein dicyandiamide, FeCl3·6H2O and the mass ratio of deionized water are 8:5:300;
(2) solution obtained to step (1) heats, until the moisture in solution is evaporated completely,
Obtain dicyandiamide and FeCl3·6H2The mixture of O;
(3) mixture obtained by step (2) is placed in porcelain boat, be positioned in tube furnace, be 100mL/min's in flow velocity 950 DEG C are warming up under argon atmosphere;
(4) when the reaction tube internal temperature in tube furnace reaches 950 DEG C, argon gas is closed, is passed through into reaction tube The ammonia of 120mL/min, the temperature in reaction tube continue to be increased to 1050 DEG C, and continue 1 it is small when, being continually fed into flow velocity is still For the ammonia of 120mL/min until tube furnace is down to room temperature, the powder for collecting brown on porcelain boat can obtain Fe4N;
(5) Fe for obtaining step (4)4N is with glucose according to 1:4 mass ratio is dissolved in deionized water, mechanical agitation 5 After hour, final solution is transferred in polytetrafluoroethylliner liner reaction kettle, is positioned in drying box, 8 are kept the temperature in 200 DEG C Hour, coat Fe by centrifuging and being dried to obtain glucose4The powder of N;
(6) powder that step (5) obtains is placed in tube furnace, be warming up under the atmosphere of argon gas 800 DEG C maintain 1 it is small when It is carbonized, finally obtains carbon coating Fe4N composite materials.
Embodiment 4:
(1) by dicyandiamide and FeCl3·6H2O is dissolved in deionized water, with magnetic stirrer 4h, is uniformly mixed Solution, wherein dicyandiamide, FeCl3·6H2O and the mass ratio of deionized water are 10:5:350;
(2) solution obtained to step (1) heats, until the moisture in solution is evaporated completely, obtain dicyandiamide with FeCl3·6H2The mixture of O;
(3) mixture obtained by step (2) is placed in porcelain boat, be positioned in tube furnace, be 80mL/min's in flow velocity 900 DEG C are warming up under argon atmosphere;
(4) when the reaction tube internal temperature in tube furnace reaches 900 DEG C, argon gas is closed, is passed through into reaction tube The ammonia of 100mL/min, the temperature in reaction tube continue to be increased to 1000 DEG C, and continue 1.5 it is small when, being continually fed into flow velocity is still For the ammonia of 100mL/min until tube furnace is down to room temperature, the powder for collecting brown on porcelain boat can obtain Fe4N;
(5) Fe for obtaining step (4)4N is with glucose according to 1:8 mass ratio is dissolved in deionized water, mechanical agitation 4 After hour, final solution is transferred in polytetrafluoroethylliner liner reaction kettle, is positioned in drying box, in 180 DEG C of heat preservations 10 it is small when, by centrifuge and be dried to obtain glucose coat Fe4The powder of N;
(6) powder that step (5) obtains is placed in tube furnace, be warming up under the atmosphere of argon gas 900 DEG C maintain 1 it is small when It is carbonized, finally obtains carbon coating Fe4N composite materials.
Further, the carbon coating Fe embodiment of the present invention being prepared4N composite materials carry out tem observation analysis, Middle Fig. 2 (a) and Fig. 2 (b) are respectively carbon coating Fe4Low power and high-resolution the projection figure of N composite nano materials, it is seen that institute of the present invention The carbon coating Fe being prepared4N composite materials are nanostructured, and pattern is homogeneous, Fe4The surface of N nano particles has carbon coating Layer, the thickness of the carbon coating layer is 5-10nm, carbon coating Fe4The size of N nanocomposites is 30-100nm.
Further, the carbon coating Fe embodiment of the present invention being prepared4N nanocomposites are used for lithium-ion electric Pond negative material, carries out electrical property loop test experiment, result of the test cycle performance figure as shown in Figure 3 and shown in Fig. 4 times Rate performance map, with good storage lithium performance, cycle life and high rate performance:After being charged and discharged 100 times, specific capacity is still Be maintained at more than 730mAh/g, material of the present invention shown in Fig. 4 different current densities for 100mA/g, 200mA/g, 500mA/g, Corresponding reversible capacity is respectively 766mAh/g, 665mAh/g, 475mAh/ under 1000mA/g and 100mA/g, after multiple charge and discharge G, 250mAh/g and 746mAh/g, it is seen that after the material carries out multiple charge and discharge at higher current densities, still keep higher Reversible capacity, i.e., described material still keeps higher reversible capacity in high power charging-discharging, and the invertibity of material is good.
Invention described above specific embodiment, is not intended to limit the scope of the present invention..It is any this Modifications, equivalent substitutions and improvements made within the spirit and principle of invention etc., should be included in the claim of the present invention Within protection domain.

Claims (9)

1. a kind of carbon coating Fe for lithium ion battery negative material4N nanocomposites, it is characterised in that:Fe4N particles Surface has carbon coating layer, and the thickness of the carbon coating layer is 5-10nm, carbon coating Fe4The size of N nanocomposites is 30- 100nm。
2. a kind of prepare carbon coating Fe described in claim 14The method of N nanocomposites, it is characterised in that:Including walking as follows Suddenly:
(1) by dicyandiamide and FeCl3·6H2O is dissolved in deionized water, and with magnetic stirrer, what is be uniformly mixed is molten Liquid;
(2) solution obtained to step (1) heats, until the moisture in solution is evaporated completely, obtain dicyandiamide with FeCl3·6H2The mixture of O;
(3) mixture obtained by step (2) is placed in porcelain boat, be positioned in tube furnace, 850- is warming up under argon atmosphere 950℃;
(4) when the reaction tube internal temperature in tube furnace reaches 850-950 DEG C, argon gas is closed, ammonia is passed through into reaction tube, Temperature in reaction tube continues to be increased to 950-1050 DEG C, when keeping 1-2 small, is continually fed into ammonia until tube furnace is down to room Temperature, the powder for collecting brown on porcelain boat obtain Fe4N;Wherein, ammonia flow velocity is 80-120mL/min;
(5) Fe for obtaining step (4)4N powder is with glucose according to 1:The mass ratio of (1-8) is dissolved in deionized water, and machinery stirs Mix 3-5 it is small when after, final solution is transferred in polytetrafluoroethylliner liner reaction kettle, is placed in drying box, in 160-200 DEG C heat preservation 8-12 it is small when, by centrifuge and be dried to obtain glucose coat Fe4The powder of N;
(6) powder that step (5) obtains is placed in tube furnace, heat up carbonization under the atmosphere of argon gas, finally obtains carbon coating Fe4N nanocomposites.
3. according to the method described in claim 2, it is characterized in that:In step (1), dicyandiamide, FeCl3·6H2O and deionization The mass ratio of water is (5-10):(3-5):(250-350).
4. according to the method in claim 2 or 3, it is characterised in that:In step (3), argon gas flow velocity is 60-100mL/min, 900 DEG C are warming up under argon atmosphere.
5. according to the method in claim 2 or 3, it is characterised in that:In step (4), the temperature in reaction tube continues to raise To 1000 DEG C, when holding 1.5 is small.
6. according to the method in claim 2 or 3, it is characterised in that:It in step (5), is placed in drying box, in 180 DEG C Keep the temperature 10 it is small when.
7. according to the method in claim 2 or 3, it is characterised in that:In step (6), 500-900 DEG C of maintenance 1-2 is warming up to Hour is carbonized, it is furthermore preferred that when carbonization time is that 800 DEG C of maintenances 1 are small.
8. according to the method in claim 2 or 3, it is characterised in that:The carbon coating Fe being prepared4N nanocomposites, Fe4The surface of N nano particles has carbon coating layer, and the thickness of the carbon coating layer is 5-10nm, carbon coating Fe4The nano combined materials of N The size of material is 30-100nm.
9. a kind of carbon coating Fe described in claim 14The application of N nanocomposites, it is characterised in that:For lithium ion battery Negative material, after charge and discharge cycles 100 times, the specific capacity of material remains at more than 730mAh/g, also, the material exists After carrying out multiple charge and discharge under high current density 100mA/g, the reversible capacity of more than 740mAh/g is still maintained.
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