WO2006025377A1 - 非水系二次電池用負極材料、非水系二次電池用負極、および非水系二次電池 - Google Patents
非水系二次電池用負極材料、非水系二次電池用負極、および非水系二次電池 Download PDFInfo
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- WO2006025377A1 WO2006025377A1 PCT/JP2005/015755 JP2005015755W WO2006025377A1 WO 2006025377 A1 WO2006025377 A1 WO 2006025377A1 JP 2005015755 W JP2005015755 W JP 2005015755W WO 2006025377 A1 WO2006025377 A1 WO 2006025377A1
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/043—Processes of manufacture in general involving compressing or compaction
- H01M4/0435—Rolling or calendering
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0404—Methods of deposition of the material by coating on electrode collectors
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0409—Methods of deposition of the material by a doctor blade method, slip-casting or roller coating
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
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- 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
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
- H01M4/1393—Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to a negative electrode material used for a non-aqueous secondary battery, a negative electrode using the negative electrode material, and a non-aqueous secondary battery including the negative electrode.
- the graphite granulated particles described in this patent document do not necessarily have sufficient performance as a negative electrode material for lithium ion secondary batteries, in particular, reduced irreversible capacity and improved cycle characteristics. There is no problem. The cause of this problem is not clear, but the graphite agglomerated particles described in the above patent document are too weak in the binding force between the graphite particles with few amorphous parts. This is thought to be because the electrode plate surface is in a state without gaps during pressing. If the graphite granulated particles are advanced too much, the characteristics at the time of producing a lithium ion secondary battery, in particular, the immersion property tends to be insufficient. [0006] In addition, when there are many amorphous parts, there is a problem that it is difficult to press, and when pressing and crushing forcibly, the mouth becomes large and it is difficult to obtain a high-capacity battery.
- An object of the present invention is to provide a negative electrode material made of graphite particles with improved performance, a negative electrode made of this material, and a non-aqueous secondary battery including the negative electrode.
- the negative electrode material for a non-aqueous secondary battery according to the present invention is mainly composed of graphite particles formed by combining a plurality of graphite particles.
- the median diameter of the particles in the volume-based particle size distribution measured by z-scattering particle size distribution measurement is 5 ⁇ m or more and 40 ⁇ m or less.
- the tap density of the material is 0.7 g / cm 3 or more, and the specific surface area force by the BET method is 0.2 m 2 Zg or more and 8 m 2 Zg or less.
- an electrode plate is manufactured by the following electrode plate manufacturing method, and the surface roughness curve when the surface of the manufactured electrode plate is measured with a laser type shape measuring microscope is defined by JIS B 060 1
- the skewness (Rsk) is -1.7 or more and 0 or less.
- predetermined electrode plate manufacturing method this method may be referred to as “predetermined electrode plate manufacturing method”.
- the electrode plate manufactured by this predetermined electrode plate manufacturing method may be referred to as “the predetermined electrode plate of the present invention”. .
- the negative electrode material for a non-aqueous secondary battery of the present invention (hereinafter sometimes referred to as "the negative electrode material of the present invention") is used, rapid charge / discharge characteristics with small charge / discharge irreversible capacity during the initial cycle are obtained. A non-aqueous secondary battery with excellent cycle characteristics is provided.
- FIG. 1 An illustration of skewness (Rsk), showing the relationship between the surface roughness curve and the probability density function, where A is the surface where the valley is wider than the peaks B represents a roughness curve, and B represents a surface roughness curve, with the peaks being wider than the valleys.
- the negative electrode material of the present invention contains graphite particles as the main component.
- the graphite particles are preferably carbonaceous particles bonded and / or covered by a heat-treated noinda capable of black lead! //!
- Examples of the carbonaceous particles constituting the graphite particles include carbonaceous particles that can be graphitized by firing, such as natural graphite, artificial graphite, coatas powder, two-dollar coatus powder, and carbide powder of rosin. . In the present invention, it is particularly preferable to use natural graphite or needle coat powder among these.
- noinder petroleum-based and coal-based condensed polycyclic aromatics having a soft pitch force up to a hard pitch, as long as they are carbonaceous capable of being graphitic, are preferably used.
- the carbonaceous particles as the primary particles are made of carbonaceous carbonaceous particles derived from the binder so that the crystallographic direction forms a randomly oriented microstructure.
- the alignment planes are non-parallel to each other.
- the median diameter of the graphite particles by volume reference particle size distribution by laser diffraction z-scattering particle size distribution measurement of the negative electrode material of the present invention is 5 ⁇ m or more, preferably 8 ⁇ m or more, more preferably 10 / zm. That's it. If the median diameter is too small, the specific surface area becomes large, and the strength when the electrode plate is formed tends to be weak. In addition, when pulverizing to such a diameter, the time required for the pulverization becomes longer, which is not economical.
- the median diameter of the graphite particles is 40 ⁇ m or less, preferably 35 ⁇ m or less, and more preferably 30 m or less. When the median diameter exceeds this upper limit, when used as a negative electrode material, irregularities occur on the surface of the electrode, and the separator used in the battery tends to be damaged.
- the volume reference particle size distribution by laser diffraction Z scattering type particle size distribution measurement is measured by the following method.
- the tap density of the negative electrode material of the present invention is 0.7 gZcm 3 or more.
- the tap density is 0.75 g / cm 3 or more, more preferably 0.8 g / cm 3 or more, particularly 0.9 g / cm 3 or more.
- the tap density is preferably 1.2 gZcm 3 or less.
- the tap density is too low, it is necessary to reduce the concentration of the slurry of the negative electrode material applied to the current collector during the production of the negative electrode, and the density of the coating film becomes small and the graphite particles break down when pressed. Battery performance is likely to deteriorate. On the contrary, a high tap density is preferable in terms of battery performance, but further steps are required to adjust the shape and particle size distribution of the graphite particles, resulting in a decrease in yield and an increase in cost.
- the tap density is measured by the following method.
- the negative electrode material was dropped through a 20 cm 3 cylindrical tap cell through a 300 m sieve. After filling the cell, tap 1000mm with a stroke length of 10mm and measure the tap density at that time.
- the specific surface area measured by the BET method of the negative electrode material of the present invention is 0.2 m 2 Zg or more, preferably 0.3 m 2 Zg or more, 8 m 2 Zg or less, preferably 6 m 2 Zg or less, particularly preferably 4 m. 2Zg or less.
- Value of specific surface area S Below this range, output characteristics when used as a negative electrode material tend to deteriorate. If the specific surface area exceeds this range, the initial irreversible capacity increases and the cycle characteristics tend to be poor.
- the specific surface area is measured, for example, by the following method.
- the BET 1-point method is measured by the nitrogen gas adsorption flow method. Specifically, about 0.4 g of sample (negative electrode material) was filled in a cell, heated to 350 ° C and pretreated, then cooled to liquid nitrogen temperature, and 30% nitrogen and 70% He gas were added. The amount of gas desorbed by saturation adsorption and then heated to room temperature is measured, and the resulting surface force is calculated using the usual BET method.
- the surface of the produced polar plate (hereinafter sometimes referred to as “predetermined polar plate of the present invention”).
- the skewness (Rsk) specified by JIS B 0601 is ⁇ 1.7 or higher, preferably —1.5 or higher, particularly preferably —1 .3 or more, 0 or less, preferably 0.3 or less.
- Skewness indicates the asymmetry of the surface roughness curve. An example is described below with reference to FIG.
- the probability density function is distributed toward the valley as shown in Fig. 1A.
- the probability density function shown in Fig. 1B has a distribution that is biased toward the peak, and the skewness has a large value toward the negative side.
- the skewness value in this case represents the difficulty of collapsing the negative electrode material in the electrode plate.
- a large skewness on the plus side indicates that the surface shape of the electrode plate after pressing is maintained, and that the negative electrode material is not easily crushed.
- a large skewness on the negative side means that the negative electrode material is easily crushed! / ⁇ ! /
- the negative electrode material on the electrode plate is appropriately crushed or immediately crushed so that the diffusion path of lithium ions and the like is not crushed, so that rate characteristics and the like are excellent.
- the graphite crystal orientation ratio on the electrode plate I 110 ZI 004 measured by the following method is preferable. ⁇ , 0.02 or more, especially 0.03 or more, and ⁇ or 0.04 or more, and preferably ⁇ , 0.20 or less, especially 0.18 or less, and further 0.16 or less.
- Orientation ratio I ⁇ ⁇ is above
- the on-plate graphite crystal orientation ratio I 110 ⁇ 004 is an index representing the degree of orientation of the graphite crystal hexagonal network surface with respect to the thickness direction of the electrode.
- a chart of the (110) plane and (004) plane of graphite on the electrode plate is measured by X-ray diffraction, and the asymmetric phase VII is used as a profile function for the measured chart.
- the peak separation is performed by fitting the peaks, and the integrated intensity of the peaks on the (110) plane and the (004) plane is calculated. From the obtained integrated intensity, a ratio represented by (110) area intensity ⁇ (004) area intensity is calculated and defined as the graphite crystal orientation ratio on the electrode plate.
- the X-ray diffraction measurement conditions here are as follows. “20” represents a diffraction angle.
- Sample preparation A predetermined electrode plate is fixed to a glass plate with double-sided tape 0.1 mm
- the press load when the predetermined electrode plate of the present invention is manufactured by the above-described predetermined electrode plate manufacturing method is preferably 350 kgf or more, particularly 4 OOkgf or more, in terms of length per 5 cm. In particular, it is 450 kgf or more, and preferably 1800 kgf or less, particularly 150 Okgf or less, especially 1200 kgf or less.
- the negative electrode material When the press load is below this range, the negative electrode material may be crushed or the immersion rate may be poor when the electrode is made difficult to control the electrode plate density. Furthermore, the negative electrode material may be crushed and block the lithium ion path, which may reduce the rate characteristics. If the pressing load exceeds this upper limit, the peeling of the electrode plate force tends to increase, and a pressing device with a higher capacity is required, which is not preferable in production.
- the immersion speed measured by the following method is preferably 10 seconds or more, preferably 400 Second Z ⁇ 1 or less, more preferably 200 seconds ⁇ ⁇ 1 or less.
- the electrolyte vanishing point is the point at which the boundary between the electrolyte contact surface and the non-contact surface cannot be visually determined.
- the negative electrode material of the present invention is obtained by using the predetermined electrode plate of the present invention manufactured by the aforementioned predetermined electrode plate manufacturing method.
- a non-aqueous secondary battery was produced by the following non-aqueous secondary battery production method, and the capacity retention rate after 200 cycles of charge and discharge was measured for the produced non-aqueous secondary battery by the following measurement method. It is preferably 70% or more, particularly 80% or more, more preferably 85% or more, and particularly preferably 90% or more.
- a negative electrode is arranged through a film separator to form a laminate.
- the laminate and electrolyte solution are enclosed in a laminate film to produce a laminate film-enclosed non-aqueous secondary battery.
- the laminated film-encapsulated non-aqueous secondary battery was allowed to stand for 24 hours, and then charged at a current density of 49 mAZcm 2 until the potential difference between the electrodes reached 4.2 V. After that, the potential difference reached 3.0 V.
- the operation of discharging at 70 mAZcm 2 was repeated as one cycle until the above, and the 100-minute ratio (capacity maintenance ratio%) of the value obtained by dividing the discharge capacity at 206th cycle by the discharge capacity at 6th cycle was determined.
- the capacity retention rate in the same way, and use the average value as the cycle capacity retention ratio after 200 cycles of charge and discharge.
- the negative electrode material of the present invention has a total number force of particles obtained when measuring the number-based circle equivalent diameter distribution by flow particle image analysis as described above, preferably 30 X 10 6 pieces or less, particularly 25 X 10 6 pieces. Zg or less is preferred.
- a large total number generally means a large amount of fine particles, and the initial charge / discharge irreversible capacity, battery cycle characteristics, etc. are likely to deteriorate. The smaller the total number, the better. However, from the viewpoint of cost and workability, it is preferably 1 ⁇ 10 6 pieces / g or more.
- the negative electrode material of the present invention is based on particle volume based on the particle size by laser diffraction / scattering particle size measurement.
- the cumulative volume fraction is 90 for the particle size (d) when the cumulative volume fraction is 10%.
- the ratio (d / ⁇ ) of the particle size (d) in% is preferably 5 or less.
- d / ⁇ represents the spread of the particle size distribution, and the smaller the ratio, the narrower the particle size distribution.
- d / ⁇ is preferably 4 or less.
- Fine particles adsorbed on the electrode plate forming binder added when manufacturing the negative electrode are filled in the voids between the particles, and the communication holes, which are the diffusion paths of lithium ions, are closed, and the rapid charge / discharge characteristics deteriorate.
- d / ⁇ is preferably from the viewpoint of the operation for adjusting the particle size distribution and the yield.
- the strength of the negative electrode can be improved.
- the number of coarse particles is small, it is possible to avoid the problem that unevenness occurs on the surface of the electrode plate and the separator used in the battery is easily damaged in the process of manufacturing the negative electrode by applying the slurry of the negative electrode material to the current collector. .
- the negative electrode material of the present invention has an average frequency ( ⁇ ) in the range of 20 + ⁇ —5% in terms of the cumulative frequency even though the equivalent circle diameter is small in the measurement of the equivalent circle diameter distribution by the flow particle image analysis described above. It is preferable that the ratio ( ⁇ ⁇ ) of the average frequency ( ⁇ ) in the range of 80 + ⁇ – 5% in terms of the cumulative frequency from those with a small equivalent circle diameter to be 1.2 to 8.0.
- the particles in the small particle size portion have an initial charge with little influence on the cumulative volume distribution based on the above particle size. It has been found that this affects the irreversible discharge capacity, rapid charge / discharge characteristics, and cycle characteristics.
- the ratio ( ⁇ ) in the above flow-type particle image analysis is an index representing the characteristics of the small particle size portion, and is an index based on the number of particles, so that the characteristics of the small particle size portion can be well expressed.
- ⁇ The force with a small equivalent circle diameter is the ratio of the frequency at the 20% and 80% cumulative frequency, and increases with the ratio of fine particles with a small particle size.
- the value of AZB is not particularly limited, but a smaller value is preferable from the viewpoint of battery performance. However, from the viewpoint of cost and yield of particle size preparation in producing graphite particles, it is preferably 1. 2 or more, more preferably 1.3 or more, more preferably 1.4 or more, still more preferably 1.5 or more, particularly preferably 1.6 or more, preferably 8.0 or less, more preferably 7 0 or less, more preferably 6.0 or less.
- the graphite particles present on the surface of the negative electrode plate are broken during the pressing process, which is one of the processes for processing the graphite particles into a non-aqueous secondary battery negative electrode. It is presumed that the communication hole, which is a diffusion path, is blocked, resulting in a decrease in rapid charge / discharge characteristics and a decrease in cycle characteristics.
- the number-based circle equivalent diameter distribution for obtaining AZB is measured by the flow-type particle image analysis described above.
- the surface roughness (Ra) of the predetermined electrode plate of the present invention produced by the above-mentioned predetermined electrode plate production method using the negative electrode material of the present invention is preferably 0.1 or more, more preferably 0.2 or more. Preferably, it is 1.2 or less, more preferably 1 or less.
- the electrode plate may be too flat and the immersion property may be reduced. If the surface roughness is above this range, the active material density in the battery cannot be increased. Is likely to drop.
- the surface roughness can be measured in the same manner as the skewness described above. [0053] d (002) and Lc (002)
- the negative electrode material of the present invention has a value of d (002) of 0.3359 nm or less, preferably 0.3356 nm or less by X-ray diffraction analysis, and is 0.3354 nm or more, which is the value of highly crystalline graphite. Is desirable.
- d (002) is too large, the crystallinity as graphite is insufficient, the charge / discharge capacity as the negative electrode material is reduced, and the strength of the graphite particles is too high.
- the formed active material layer is press-molded to a predetermined bulk density, a high pressure is required and it may be difficult to increase the density.
- the negative electrode material of the present invention desirably has a value of Lc (002), which is a crystal thickness by X-ray diffraction analysis, of 80 nm or more, and preferably 10 nm or more. Even when Lc (002) is less than 80 nm, the crystallinity as graphite is insufficient, the charge / discharge capacity as the negative electrode material is reduced, and the strength of the graphite particles is too high.
- Lc (002) is a crystal thickness by X-ray diffraction analysis
- the negative electrode material of the present invention comprising graphite particles as a main component is mixed with carbonaceous particles, solder, etc. as raw materials, and molded, devolatilized, fired, graphitized, pulverized, and classified as necessary. It is manufactured by this.
- the negative electrode material of the present invention satisfying the above-mentioned physical properties, it is preferable to use -dolcotus or natural graphite as the main component of the carbonaceous particles.
- a binder In the process of mixing carbonaceous particles and a binder to graphitize, optimize the type and amount of the catalyst during graphitization (for example, in the case of SiC, which is commonly used as a graphite catalyst) Further, it is preferable to maintain an appropriate amorphous amount by a method such that the addition amount is 30 parts or less with respect to 100 parts of the base material.
- the carbonaceous particles and the binder are mixed while heating.
- a graphitization catalyst may be added if desired.
- Suitable carbonaceous particles, noinders and graphite soot catalysts are as follows:
- a raw coatas containing a volatile component (Volatile Matter: hereinafter sometimes referred to as “VM”) is used.
- VM Volatile Matter
- carbonaceous particles containing 2 to 10 wt% of volatile components that volatilize during heat treatment it is preferable to use carbonaceous particles containing 2 to 10 wt% of volatile components that volatilize during heat treatment.
- natural graphite may be used in combination with natural graphite.
- the median diameter of the volume-based particle size distribution measured by the Z-scattering particle size distribution measurement is not particularly limited, but is 5 ⁇ m or more, especially 6 ⁇ m or more, especially 8 ⁇ m or more. Also, it is preferably 40 ⁇ m or less, particularly preferably 35 ⁇ m or less, particularly preferably 30 ⁇ m or less.
- the median diameter of the carbonaceous particles is below this lower limit, the cost required for pulverizing the carbonaceous particles increases, and if the upper limit is exceeded, the initial irreversible capacity of the graphite particles tends to increase.
- the median diameter of the carbonaceous particles can be measured in the same manner as the median diameter of the negative electrode material described above.
- the average particle diameter of the carbonaceous particles is preferably smaller than the average particle diameter of the target graphite particles.
- the average particle size of the carbonaceous particles is preferably not more than twice the average particle size of the intended graphite particles, more preferably not more than the same size, preferably 1 Z10 or more of the average particle size, more preferably Is more than 1Z5.
- the average circularity of the carbonaceous particles is preferably 0.82 or more, more preferably 0.90 or more, preferably 1.00 or less, more preferably 0.96 or less.
- the average circularity of the carbonaceous particles is below this range, the orientation tends to decrease or immediately above the cost, and the cost tends to increase.
- the average circularity of the carbonaceous particles can be measured in the same manner as the average circularity of the negative electrode material described above.
- Noinda include impregnated pitch, coal tar pitch, coal-based heavy oil such as coal liquefied oil, straight-run heavy oil such as Fasuarten, ethylene heavy end tar, etc. And heavy petroleum oils such as cracked heavy oils.
- the quinoline-insoluble component contained in the noinda is usually 0 to: LOwt%, but the smaller the amount, the better the hardness of the graphite particles and the capacity of the battery. If the content of the quinoline-insoluble component in the binder is too high, the resulting graphite particles are hardened even if the active material layer applied to the current collector is pressed. There is a tendency to become difficult, and the capacity also tends to decrease.
- the ratio of the binder derived from the binder to the graphite particles obtained through the carbonization treatment obtained by carbonization / graphite is preferably 5 wt% or more, more preferably 10 wt% or more. And preferably 60 wt% or less, more preferably 40 wt% or less, and even more preferably 3 Owt% or less.
- the amount of the binder is too large, the amorphous part derived from the binder is increased in the final product, so that the battery capacity when used as a battery may be reduced.
- the obtained graphite particles are hardened, when the active material layer applied to the current collector is pressed, the aggregate particles themselves are more likely to break at the node portion.
- the amount of the binder in the negative electrode material is controlled by the amount of the binder added in the stage before the combination. For example, when the residual carbon ratio of the binder obtained by the method described in JIS K2270 is X%, a desired amount of the binder is added 100ZX times.
- a device for adding a binder such as pitch and tar it is preferable to uniformly disperse as much as possible at a low temperature and in a short time in order to reduce the initial irreversible capacity and the press load.
- stirring In order to disperse at a low temperature for a short time, stirring should be strengthened to such an extent that the carbonaceous particles are not broken.
- Graphitization catalyst In order to increase the charge / discharge capacity and improve the pressability, it is preferable to add a graphite soot catalyst when mixing the carbonaceous particles and the binder.
- the graphite catalyst include metals such as iron, nickel, titanium, silicon and boron, and compounds such as carbides, oxides and nitrides thereof. Of these, silicon carbide is preferable among the key compounds, and silicon iron is particularly preferable among the iron compounds.
- the carbon carbide produced by heating is thermally decomposed at a temperature of 2800 ° C or higher to grow graphite with extremely good crystallinity.
- the charge transfer reaction and diffusion of lithium ions inside the particles can be promoted, and the battery performance can be improved.
- iron or a compound thereof is used as the graphite soot catalyst, graphite having good crystallinity can be grown by the mechanism of dissolution and precipitation of carbon in the catalyst, and the same effect as that of silicon can be exhibited.
- the amount of these graphite soot catalysts added is preferably 30 wt% or less, more preferably 20 wt% or less, still more preferably 10 wt% or less, particularly preferably 5 wt% with respect to the carbonaceous primary particles as a raw material. It is as follows. If there are too many graphitization catalysts, the graphite will progress too much, causing problems such as insufficient lithium immersion battery characteristics, particularly immersion. At the same time, the strength of the particles is reduced because of the generation of pores in the graphite particles. As a result, the surface is smoothened during the pressing process during electrode plate production, and the movement of ions is inhibited. There is also.
- the raw materials such as the carbonaceous particles, the noder, and the optionally added graphite catalyst are first combined under heating.
- the liquid binder is attached to the carbonaceous particles and the raw material that does not melt at the compounding temperature.
- all the raw materials may be charged into the compounding machine, and the compounding and temperature rising may be performed simultaneously, or components other than the binder may be charged into the compounding machine and heated in a stirring state, and the temperature rises to the compounding temperature.
- a binder at room temperature or in a vulcanized molten state may be charged later.
- the heating temperature is equal to or higher than the softening point of the binder. If the heating temperature is too low, the viscosity of the binder becomes high and uniform combination becomes difficult. It is carried out at a temperature, preferably 20 ° C higher than the soft saddle point. If the heating temperature is too high, the viscosity of the combined system becomes too high due to the volatilization and polycondensation of the binder, so it is usually 300 ° C or less, preferably 250 ° C or less.
- a general-purpose machine having a stirring blade is preferred as the compounding machine.
- a general type such as a Z type or a gussetar type can be used.
- the amount of the raw material charged into the compounding machine is usually 10 vol% or more, preferably 15 vol% or more, and 50 vol% or less, preferably 30 vol% or less of the compounding machine volume.
- the mixing time is 5 minutes or more, and it takes up to a maximum viscosity change due to volatilization of the volatile matter, usually 30 to 120 minutes. It is preferable to preheat the compounding machine to the compounding temperature prior to the compounding.
- the obtained compound may be used as it is in the de-VM firing process for the purpose of removing volatile components (VM) and carbonizing, but after being molded for easy handling, it is used in the de-VM firing process. It is preferable.
- the molding method is not particularly limited as long as the shape can be maintained, and extrusion molding, mold molding, isostatic pressing, and the like can be employed.
- the particles are easily oriented in the molded body, and the extrusion is easy, and the operation is relatively easy compared to the hydrostatic pressure molding in which the orientation of the particles is kept at random but the productivity is not easily increased. Mold molding that can obtain a molded body without destroying the oriented structure is preferred.
- the molding temperature may be room temperature (cold) or under heating (hot, temperature above the soft softening point of the binder).
- cold forming it is desirable to preliminarily crush the compound that has been cooled after compounding to a maximum dimension of 1 mm or less in order to improve moldability and obtain uniformity of the compact.
- the shape and size of the molded product are not particularly limited. However, in hot forming, if the molded product is too large, there is a problem that it takes time to perform uniform preheating prior to molding, so the maximum size is preferably 150 cm. The size is less than or equal to.
- the molding pressure is preferably 3tfZcm 2 (294MPa) or less, and more preferable properly 500kgfZcm 2 (49MPa) or less, further preferably 10kgfZcm 2 (0. 98MPa) hereinafter.
- the lower limit pressure is not particularly limited, but is preferably set to such a degree that the shape of the molded body can be maintained in the VM removal process.
- the resulting molded body is de-VM fired to remove carbonaceous particles and volatile components (VM) of the binder, and to prevent contamination of the filler during black lead conversion and adhesion of the filler to the molded body.
- the VM calcination is usually carried out at a temperature of 500 ° C or higher, preferably 600 ° C or higher, preferably 1700 ° C or lower, more preferably 1400 ° C or lower, preferably for 0.1 to 10 hours.
- the heating is usually performed in a non-acidic atmosphere in which an inert gas such as nitrogen or argon is circulated, or a granular carbon material such as a breath or packing coatus is filled in the gap.
- Equipment used for VM removal firing is not particularly limited as long as firing is possible in a non-oxidizing atmosphere, such as an electric furnace, a gas furnace, and a lead hammer furnace for electrode materials! It is desirable that the heating rate during heating is low in order to remove the volatile matter. Normally, around 200 ° C, where the low-boiling point begins to volatilize. Raise the temperature at ⁇ 100 ° CZhr.
- the carbide molded body obtained by removing the VM is heated at a high temperature to be graphitized.
- the lower the heating temperature during graphitization the lower the AZB of the obtained negative electrode material, and the smaller the AZB of the obtained negative electrode material, the harder the graphite particles become, and the active material layer applied to the current collector has a predetermined volume.
- Heating is preferably performed at 2900 ° C or higher, more preferably 3000 ° C or higher, because high pressure is required when press-molding to density and it tends to be difficult to increase the density. Further, if the heating temperature is too high, the sublimation of graphite becomes remarkable, so the heating temperature is preferably 3300 ° C or lower.
- the heating time may be performed until the binder and the carbonaceous particles become graphite, and is preferably 1 to 24 hours.
- the atmosphere during graphitization is a non-acidic atmosphere in which an inert gas such as nitrogen or argon flows or a granular carbon material such as please or knocking coat is filled in the gap to prevent oxidation. To do.
- an inert gas such as nitrogen or argon flows or a granular carbon material such as please or knocking coat is filled in the gap to prevent oxidation.
- the equipment used for graphitization is the above-mentioned purpose such as an electric furnace, a gas furnace, an electrode material Atchison furnace, etc.
- the temperature rise rate, cooling rate, heat treatment time, etc. can be arbitrarily set within the allowable range of the equipment used.
- the graphitized product thus obtained usually does not have the particle size distribution defined in the present invention as it is, and is adjusted to a desired particle size distribution by pulverization and sieving.
- the pulverizing means is mechanically pulverizing means such as ball mill, hammer mill, CF mill, atomizer mill, pulverizer.
- a pulverizing means using wind power such as a jet mill, is exemplified.
- a pulverization method using impact force such as a jaw crusher, a hammer mill, or a roller mill may be used.
- the timing of pulverization may be before or after graphitization.
- the latter is preferred because it does not require crucible filling and can be manufactured at low cost.
- the volume-based particle size distribution by laser diffraction / scattering particle size measurement is 3% or less of the total particle size of 100 m or more and 1 ⁇ m or less of the particle size. It is desirable to adjust the size so that the product is 1% or less of the total.
- a screen fixing type There are a screen fixing type, an in-plane motion type, a rotary sieving type, etc. for sieving for removing large-diameter granular materials.
- a screen-fixing blow-through type sieve is used. Is particularly preferred.
- the size of the sieve mesh to be used is 80 m or less and 30 m or more, and it can be used. It is appropriately selected and used according to the distribution and average particle size adjustment requirements. When the size exceeds 80 m, the removal of the particulate matter becomes insufficient. When the size is less than 30 m, it leads to excessive removal of the granulated product, resulting in a lot of product loss and difficulty in adjusting the particle size distribution. This is not preferable.
- sieves with a mesh size of 45 m and 38 m which are sold as general-purpose sizes, can be preferably used.
- Classification can be carried out by methods such as wind classification, wet classification, and specific gravity classification, and is not particularly limited for removing particulates of 100 ⁇ m or more.
- an air classifier such as a swirl classifier.
- the air volume and the wind speed it is possible to adjust the removal of the granular material and the particle size distribution and average particle size of the granulated material in the same way as adjusting the size of the mesh opening. it can.
- the negative electrode material of the present invention can be suitably used as a negative electrode active material for non-aqueous secondary batteries, particularly lithium secondary batteries.
- the negative electrode constituting the non-aqueous secondary battery is formed by forming, on a current collector, an active material layer containing a negative electrode active material, an electrode plate-forming binder, a thickener, and, if necessary, a conductive material.
- an active material layer a slurry containing a negative electrode active material, a binder for forming an electrode plate, a thickener, and a conductive material and a solvent as necessary is generally prepared, and this is applied, dried, and pressed onto an electric body. Can be obtained.
- the negative electrode active material in addition to the negative electrode material of the present invention, a material usually used as a negative electrode active material may be used in combination.
- any material can be used as long as it is a material that is stable with respect to a solvent and an electrolytic solution used during electrode production.
- examples thereof include polyvinylidene fluoride, polytetrafluoroethylene, polyethylene, polypropylene, styrene / butadiene rubber, isoprene rubber, butadiene rubber, ethylene acrylic acid copolymer, and ethylene-methacrylic acid copolymer.
- the weight ratio of the active material Z electrode plate forming binder in the electrode plate forming binder is preferably 90Z10 or more, more preferably 95Z5 or more, and preferably 99.9 / 0.1 or less, preferably 99.
- the range is 5 / 0.5 or less.
- the thickener examples include carboxymethyl cellulose, methyl cellulose, hydroxymethyl cellulose, ethyl cellulose, polybutyl alcohol, oxidized starch, phosphate starch, and casein.
- Examples of the conductive material include carbon materials such as graphite and carbon black; metal materials such as copper and nickel.
- Examples of the material of the current collector include copper, nickel, and stainless steel. Of these, copper foil is preferred because it is easy to process into a thin film, and has the advantage of cost and cost.
- the density of the active material layer is preferably 1.
- the density is too low, the battery capacity per unit volume is not always sufficient. In addition, if the density is too high, the rate characteristics deteriorate, so 1.9 gZcm 3 or less is preferable.
- the active material layer is a mixture layer composed of an active material on a current collector, an electrode plate forming binder, a thickener, a conductive material, and the like.
- the bulk density is a mixture layer composed of an active material on a current collector, an electrode plate forming binder, a thickener, a conductive material, and the like.
- the negative electrode for a nonaqueous secondary battery of the present invention produced using the negative electrode material of the present invention is extremely useful as a negative electrode for a nonaqueous secondary battery such as a lithium secondary battery.
- the non-aqueous secondary battery of the present invention usually comprises the above-described negative electrode, positive electrode and electrolyte of the present invention.
- the positive electrode is formed by forming an active material layer containing a positive electrode active material, a conductive agent and an electrode plate forming binder on a positive electrode current collector.
- the active material layer is usually obtained by preparing a slurry containing a positive electrode active material, a conductive agent, and an electrode plate forming binder, and applying and drying the slurry on a current collector.
- Examples of the positive electrode active material include lithium cobalt oxide, lithium nickel oxide, lithium Lithium transition metal composite oxide materials such as thidium manganate; transition metal oxide materials such as manganese dioxide; and materials that can occlude and release lithium such as carbonaceous materials such as fluorinated graphite can do.
- lithium cobalt oxide lithium nickel oxide
- lithium Lithium transition metal composite oxide materials such as thidium manganate
- transition metal oxide materials such as manganese dioxide
- materials that can occlude and release lithium such as carbonaceous materials such as fluorinated graphite can do.
- the positive electrode current collector it is preferable to use a metal or an alloy thereof that forms a passive film on the surface by anodic oxidation in an electrolytic solution.
- a metal or an alloy thereof that forms a passive film on the surface by anodic oxidation in an electrolytic solution.
- Ilia, IVa, Va group (3B, 4B, 5B Examples thereof include metals belonging to (Group) and alloys thereof.
- Al, Ti, Zr, Hf, Nb, Ta and alloys containing these metals can be exemplified, and Al, Ti, Ta and alloys containing these metals can be preferably used.
- A1 and its alloys are desirable because of their light weight and high energy density.
- Examples of the electrolyte include an electrolytic solution, a solid electrolyte, a gel electrolyte, and the like. Among these, an electrolytic solution, particularly a non-aqueous electrolytic solution is preferable.
- a non-aqueous electrolytic solution a solution in which a solute is dissolved in a non-aqueous solvent can be used.
- an alkali metal salt, a quaternary ammonium salt, or the like can be used as the solute.
- LiN (CF SO) (C F SO), LiC (CF SO)
- C F SO LiN (CF SO)
- non-aqueous solvent examples include cyclic carbonates such as ethylene carbonate, butylene carbonate, and bilen carbonate, cyclic ester compounds such as ⁇ petit ratatone; chain ethers such as 1,2 dimethoxyethane; crown ethers Cyclic etherol such as 2-methyltetrahydrofuran, 1,2 dimethyltetrahydrofuran, 1,3 dioxolane, tetrahydrofuran, etc .; chain carbonates such as jetinole carbonate, ethylmethyl carbonate, dimethylenocarbonate, etc.
- One kind of solute and one solvent may be selected and used, or two or more kinds may be mixed and used. Among these, those containing non-aqueous solvent power cyclic carbonate and chain carbonate are preferable.
- the content of these solutes in the electrolyte solution is 0.2 mol / l or more, particularly 0.5 mol / l or more.
- the non-aqueous secondary battery prepared by combining the negative electrode according to the present invention, a metal chalcogenide positive electrode for a commonly used lithium ion battery, and an organic electrolyte mainly composed of a carbonate solvent is provided. , Irreversible capacity is observed in the initial cycle with large capacity, rapid charge / discharge capacity is small (rate characteristics are good), cycle characteristics are excellent, and battery storage and reliability in high temperature storage It has excellent high discharge efficiency and low temperature discharge characteristics.
- the nonaqueous electrolytic solution may contain a film-forming agent.
- film forming agents include carbonate compounds such as vinylene carbonate, vinylenoretinocarbonate and methylphenolate carbonate, alkensulfides such as ethylene sulfide and propylene sulfide, 1,3 propane sultone, and 1,4 butane sultone. Examples thereof include acid anhydrides such as sultone compounds, maleic anhydride, and succinic anhydride.
- the content of the film forming agent is usually 10% by weight or less, preferably 8% by weight or less, more preferably 5% by weight or less, and most preferably 2% by weight or less. If the content of the film forming agent is too large, other battery characteristics such as an increase in initial irreversible capacity, low temperature characteristics, and deterioration in rate characteristics may be adversely affected.
- a separator is usually provided between the positive electrode and the negative electrode so that the positive electrode and the negative electrode are not in physical contact.
- the separator preferably has a high ion permeability and a low electric resistance.
- the material and shape of the separator are not particularly limited, but those that are stable with respect to the electrolyte and excellent in liquid retention are preferable.
- a porous sheet or a nonwoven fabric made of polyolefin such as polyethylene and polypropylene can be used.
- the shape of the non-aqueous secondary battery of the present invention is not particularly limited, and a cylinder type in which a sheet electrode and a separator are spiral, a cylinder type having an inside-out structure in which a pellet electrode and a separator are combined, a pellet electrode and a separator are provided. Examples include stacked coin types.
- Example 1 Amorphous carbon material (needle coatus) is coarsely pulverized and further pulverized by a fine pulverizer (“Sample Mill” manufactured by Hosokawa Micron Co., Ltd.). Carbonaceous particles having 2 / ⁇ ⁇ , maximum / J ⁇ particle size of 1.5 / ⁇ ⁇ , maximum particle size of 68 m, and average circularity of 0.80 were obtained.
- the obtained molded body was stored in a metal sagar as a heat-resistant container, and the gap was filled with graphite please.
- the temperature was raised from room temperature to 1000 ° C in an electric furnace over 48 hours, held at 1000 ° C for 3 hours, and de-VM firing was performed.
- the compact was stored in a graphite crucible, and the gap was filled with a graphite please.
- Graphite was fired by heating to 3000 ° C for 4 hours in an Atchison furnace.
- the obtained graphite compact was roughly crushed with a jaw crusher, then finely pulverized with a sample mill, coarse particles were removed with a sieve having a mesh opening of 45 / zm, and air classification (Japan-Eumatic Industrial Co., Ltd.).
- the particles were sized to obtain graphite particles having a median diameter of 21.1 ⁇ m.
- the predetermined electrode plate of the present invention is manufactured by the above-described predetermined electrode plate manufacturing method, and the skewness (Rsk), surface roughness Ra, graphite crystal orientation ratio (I ZI) on the electrode plate, press
- a separator made of porous polyethylene film impregnated with an electrolytic solution dissolved so as to be 1 was placed, and a 2016 coin-type battery was produced.
- the manufactured 2016 coin-type battery has a current density of 0.16 mAZcm 2 and a potential difference between both electrodes. Until OV and charges, then 1. The discharge capacity when discharged at 7. OmAZcm 2 until 5V, 100 percentage of the value obtained by dividing the discharge capacity when discharged at 0. 7mAZcm 2 (rate Characteristic). For each of the three coin-type batteries, the rate characteristics were determined and the average value was determined.
- the obtained graphite particles have a tap density of 0.79 gZcm 3 , a BET specific surface area of 2.9 m 2 Zg, a total number of 21.
- a coin-type battery was produced in the same manner as in Example 1, and the initial charge / discharge capacity, initial charge reversible capacity, and rate characteristics were determined.
- a predetermined electrode plate of the present invention was prepared, and after skewness (Rsk), surface roughness Ra, graphite crystal orientation ratio on electrode plate (I / 1), press load, immersion speed, 200 cycles of charge / discharge Capacity maintenance rate measurement
- the fully mixed compound is filled in a mold of a mold press machine preheated to 108 ° C in advance, and left for 5 minutes.
- the plunger is pushed, and 5kgf / c Molding was performed by applying a pressure of m 2 (0.20 MPa). After maintaining this pressure for 1 minute, the driving was stopped, and after the pressure drop had subsided, the molded body was taken out.
- the obtained molded body was stored in a metal sagar as a heat-resistant container, and the gap was filled with graphite.
- the temperature was raised from room temperature to 1300 ° C in an electric furnace over 48 hours, held at 1300 ° C for 3 hours, and de-VM firing was performed.
- the compact was stored in a graphite crucible, and the gap was filled with a graphite please.
- Graphite was fired by heating to 3000 ° C for 4 hours in an Atchison furnace.
- the obtained graphite compact was coarsely crushed with a jaw crusher, then finely pulverized with a high-speed rotary mill, and the coarse particles were removed with a 45-m sieve and the median diameter was 15.8 m. Got.
- Natural graphite with a median diameter of 21.7 / ⁇ ⁇ , maximum / J, particle size of 7.7 / ⁇ ⁇ , maximum particle size of 77. is used as the starting material, and the weight with a softer point of 88 ° C noder pitch
- Graphite particles having a median diameter of 22. O / zm were obtained by mixing, forming, removing VM, graphitizing, crushing, and sizing with a binder in the same manner as in Example 3 except that the ratio was set to 100: 40. Got.
- Graphite particles having a median diameter of 16.7 m were obtained in the same manner as in Example 2 except that the added graphite catalyst was carbon carbide and the addition amount was 50 parts with respect to 100 parts by weight of the carbonaceous particles.
- a coin-type battery was produced in the same manner as in Example 1, and the initial charge / discharge capacity, initial charge reversible capacity, and rate characteristics were determined.
- a predetermined electrode plate of the present invention was prepared, and after skewness (Rsk), surface roughness Ra, graphite crystal orientation ratio on electrode plate (I / 1), press load, immersion speed, 200 cycles of charge / discharge Capacity maintenance rate measurement
- Example 1 0 21.1 0.79 2.3 23.3 3.8 1.6
- Example 2 30 20.5 0.79 2.9 21.0 4.0 0.8
- Example 3 0 15.8 1.16 1.9 3.6 2.5 0.7
- Example 4 0 22.0 1.05 3.7 26.7 3.0 1.1
- Comparative Example 1 50 16.7 0.77 4.7 18.5 3.0 1.2
- Ra Capacity maintenance rate Rsk (kgf / 5cm) (sec / ju l) (mAh / g) (mAh / g) (%)
- the negative electrode material of the present invention By using the negative electrode material of the present invention, the charge / discharge irreversible capacity observed in the initial cycle when making a non-aqueous secondary battery is small. Since the negative electrode and the non-aqueous secondary battery can be stably and efficiently manufactured, the present invention is very useful industrially in the field of various non-aqueous secondary batteries.
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Abstract
Description
Claims
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EP05776633A EP1798790A4 (en) | 2004-08-30 | 2005-08-30 | NEGATIVE ELECTRODE MATERIAL FOR NONAQUEOUS SECONDARY CELLS, NEGATIVE ELECTRODE FOR NONAQUEOUS SECONDARY CELLS, AND NONAQUEOUS SECONDARY CELL |
US11/574,423 US20090214954A1 (en) | 2004-08-30 | 2005-08-30 | Negative electrode material for nonaqueous secondary cells, negative electrode for nonaqueous secondary cells, and nonaqueous secondary cell |
JP2006532715A JP4992426B2 (ja) | 2004-08-30 | 2005-08-30 | 非水系二次電池用負極材料、非水系二次電池用負極、および非水系二次電池 |
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PCT/JP2005/015754 WO2006025376A1 (ja) | 2004-08-30 | 2005-08-30 | 非水系二次電池用負極材料、非水系二次電池用負極、および非水系二次電池 |
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EP (2) | EP1801903B1 (ja) |
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US20090214954A1 (en) | 2009-08-27 |
CN100524911C (zh) | 2009-08-05 |
EP1798790A1 (en) | 2007-06-20 |
JP5556755B2 (ja) | 2014-07-23 |
JP4992425B2 (ja) | 2012-08-08 |
JPWO2006025377A1 (ja) | 2008-05-08 |
WO2006025376A1 (ja) | 2006-03-09 |
KR20070072512A (ko) | 2007-07-04 |
JPWO2006025376A1 (ja) | 2008-05-08 |
JP2011238622A (ja) | 2011-11-24 |
US8404383B2 (en) | 2013-03-26 |
JP4992426B2 (ja) | 2012-08-08 |
KR20070065875A (ko) | 2007-06-25 |
CN101053098A (zh) | 2007-10-10 |
CN101053099A (zh) | 2007-10-10 |
EP1798790A4 (en) | 2009-07-15 |
KR101106966B1 (ko) | 2012-01-20 |
EP1801903A1 (en) | 2007-06-27 |
EP1801903B1 (en) | 2012-09-26 |
CN100527488C (zh) | 2009-08-12 |
US20080199777A1 (en) | 2008-08-21 |
EP1801903A4 (en) | 2009-07-15 |
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