TW587350B - Composite graphite material and production method thereof, negative electrode material using the material, negative electrode and lithium ion rechargeable battery - Google Patents

Composite graphite material and production method thereof, negative electrode material using the material, negative electrode and lithium ion rechargeable battery Download PDF

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TW587350B
TW587350B TW092106053A TW92106053A TW587350B TW 587350 B TW587350 B TW 587350B TW 092106053 A TW092106053 A TW 092106053A TW 92106053 A TW92106053 A TW 92106053A TW 587350 B TW587350 B TW 587350B
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graphite
composite
negative electrode
carbon
graphite material
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TW200402162A (en
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Kunihiko Eguchi
Katsuhiro Nagayama
Hitomi Hatano
Norio Sato
Junichi Kitagawa
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Jfe Chemical Corp
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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
    • H01M4/58Selection 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
    • H01M4/583Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/20Graphite
    • C01B32/205Preparation
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/20Graphite
    • C01B32/21After-treatment
    • 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
    • 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
    • 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/80Particles consisting of a mixture of two or more inorganic phases
    • C01P2004/82Particles consisting of a mixture of two or more inorganic phases two phases having the same anion, e.g. both oxidic phases
    • C01P2004/84Particles consisting of a mixture of two or more inorganic phases two phases having the same anion, e.g. both oxidic phases one phase coated with the other
    • 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
    • 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 invention provides a composite graphite material, which provides structure that contains graphite B with lower crystallization outside graphite A than graphite A and part of the surface of graphite B contains graphite C with lower crystallization than the graphite B. Aside from this, the invention further provides the production method of the composite graphite material and innovation of its purpose. The composite graphite material is adapted to the negative electrode and negative electrode material for lithium ion rechargeable battery so that the performance disregarded when conventionally considering graphite for lithium ion rechargeable battery will be accommodated, i.e. both the high initial rechargeable and dissipation efficiency and large dissipation of lithium ion rechargeable battery are taken into account.

Description

(1)587350 玖、發明說明 【發明所 本發 次電池及 同之石墨 該複合石 【先前技 近年 於電池的 型的二次 高能量密 極、正極 解質所產 之間,形 料。而上 電位均等 2 3 4 3 3 號 < 石墨 面(本案 (本案中 (i n t e r ] a ; 出因石墨 屬之技術領域〕 明是關於放電| % — ♦大且初期放電效率高的鋰離子二 其構成材料。為n / -v體來說,(是至少由3種結晶性不 所形成的複合石 % 生 口墨材枓及其製沿方法、以及使用(1) 587350 玖, description of the invention [invented the secondary battery and the same graphite this composite stone [prior art in recent years in the battery-type secondary high-energy dense, positive electrode produced by decomposition, shape. The upper potential is equal to 2 3 4 3 3 < graphite surface (in this case (inter) a; the technical field due to graphite) is about the discharge |% — ♦ Large and high initial discharge efficiency lithium ion II Its constituent material. For n / -v body, (is composed of at least three kinds of crystalline composite stones that are not formed. Raw mouth ink material, its preparation method, and use.

墨材料的負極相.& _ V 1一 %枓、負極以及鎪離子二次電池)。 術】 來,隨著電子機器的小型化以及性能的提高,對 问倉b里也、度化的需求也日趨高漲。相較於其他類 电池’由於鋰離子二次電池可藉由高電壓化來提 度因而備受各界_目。鋰離子二次電池是以負 以及非水電解質作爲主要的構成要素。由非水電 生鍾離子,在充放電的過程中游移於負極與正極 成二次電池。 ’上述鋰離子二次電池的負極材料是使用碳材 A的碳材料,又以具有絕佳放電性、大放電量及 丨生的石璺最具發展潛力請參閱日本特公昭62 · 報等)。 ’由於其縮合多環(C ο n d e n s e d -i n g )六角網平 中稱爲碳網面)所衍生而成之立體結晶規則性 稱爲結晶性)的發達程度’可輕易於鋰的層間 /er )形成安定的化合物。(因此,有硏究報告指 的局結晶性,可在碳網面的層間內插入大量的 (2) 鋰,故能增進放電量)(如]993年日本電氣化學及工業化 學協會,6 ] ( 2 ) 5 ] 3 8 3等報告)。< 也有報告指出,藉由插 入該fe網面層間之鋰的數量所形成的各種層結構,可在其 共存的領域內產生平均且近乎鋰金屬的高電位^ 1993年 hEIectrochem-Soc*;Vol_M0,9,2490 等幸g 告)。因此,當 作爲組合電池使用時’可獲得極高的輸出電力。一般而 言,當使用石墨作爲負極材料時的理論容量,最終是以石 墨與鋰所形成之最佳石墨層間化合物Li C6的放電量作爲 基準,其最大放電量爲3 7 2 m A h / g。 〔但是,採用石墨作爲負極材料的鋰離子二次電池中, 倘若石墨結晶性過高,容易於首次進行充電時再石墨表面 產生電解液分解之類的副作用。該副作用將使分解的衍生 物持續堆積於石墨表面,直到形成石墨電子無法直接移動 至溶劑的厚度爲止)。ί、、由於首次充電時的副作用與電池反應 無關,因此在首次放電的過程中,將明顯增加無法釋出放 電量的所謂「不可逆容量」。換言之,也就是指首次充電 量與首次放電量之比率(本案中稱爲首次放電效率)不彰 的問題(如 1 970 年 J.E】ectrocheni.Soc.,Vol. 1 】7 22 2 等)。不可逆容量則如下列計算式所示: 不可逆容量=首次充電量-首次放電量 此外,也有報告指出共同插入溶劑分子與鋰離子將造 成時膜表面層剝落,剝落後外露的石墨表面與電解液產生 反應導致初期充放電效率不彰的情形(如]990年 J.E]ectrochem.Soc.,Vol.l3 7 2009 等)。 冬 (3) (3)587350 而用來解決上述初期充放電率不彰的手段,如業界所 為知追加二次電池之正極材料的方法。但是添加多餘的正 極材料’將導致降低能量密度的新問題產生。 如上所述地,在採用石墨作爲負極材料的鋰離子二次 電池中’對同樣依賴石墨結晶度的放電量與初期放電效率 而PZ? ’必須同時兼顧大放電量級高初期放電率的要求是背 道而馳的。 \\於是發展出一種:採用有利於增加放電量之高結晶性 的石墨作爲核心,並在其表面覆蓋有利於提高初期放電效 率之低結晶性石墨或碳的雙層結搆來解決上述的問題因 爲低結晶性的碳的放電量低,故與電解液產生分解反應性 也較低0 而這種採用不同結晶性之雙層結構碳材料與傳統技術 最大的不同在於: (1 )採用两烷、苯等有機化合物之熱分解所衍生的 低結晶性’覆盖作爲核心之高結晶性石墨的表面(譬如 曰本特開平4 - 3 6 8 7 7 8號公報、特開平5 - 2 7 5 0 7 6號公 報)。 (2 )採用液態的瀝青包覆或浸泡作爲核心的高結晶 性石墨後,以〗〇〇〇°c左右的溫度進行燒結,在其表層形 成低結晶性的石墨(譬如日本特開平5」21 〇66號公報、 特開平5-2 1 7604號公報、日本特開平6-84 5 1 6 8號公報、 特開平II-54112·3號公報及日本特開2000-229924號公 報)。 -9- (4) (4)587350 (3 )採用可藉由3 0 0 0 °C左右之燒結形成石墨的碳 (本案中稱爲易石墨化碳),譬如焦炭,於氣態或液態的 氧化性環境中,以3 00 °C左右的溫度進行氧化處理後形成 石墨(譬如日本特開平1 0- 3 2 66 1 1號公報、特開平10_ 2 ] 8 6 ] 5 6號公報)。 (4 )組合上述(])〜(3 )的方法者(譬如日本特開 平]0 - 2 ] 4 6 1 5號公報、特開平〗0 - 2 8 4 0 8 0號公報)。 但是,無論上述的哪一種方法,均無法充分滿足近年 來對增加放電量的需求標準。 而,就工業生產的觀點來看,由於上述(1 )與(4 ) 的製作過程繁瑣,以致生產本過高並具有生產上的困難。 更由於難以控制其表面之低結晶碳的厚度,因而產生比表 面積(specific surface area)與體密度(bu]k density) 之粉體特性、及放電量與初期放電效率之電池特性不穩定 的問題。 此外,上述(2 )的方法中,當利用1 0 0 0 °C進行燒結 之際,將使表層的低結晶性碳之間產生熔著,在其產生碎 解的狀態下,表層的低結晶性碳將由作爲核心的石墨處剝 落,進而導致比表面積與體密度之粉體特性、及放電量與 初期放電效率之電池特性不彰的問題。 在上述(1 )、( 2 )的方法中,由於核心的石墨與表 層的低結晶性碳在充放電的過程中所產生之膨脹與收縮的 反應不一致,隨著充覆充放電次數的增加,教導至表層的 低結晶性碳剝落,引發與上述相同的問題產生。 -10- (5) (5)587350 在上述(3 )的方法中,爲了獲得高初期充放電的效 率’必須降低高度氧化厚的表層結晶性,連帶地也降低表 層本身及其內部之易石墨化碳的結晶性,導致即使利用高 溫形成石墨化也無法獲得充分結晶性,進而產生放電量低 落的問題。 池的放電量,是取決於增加每個構成負極之石墨容 積的放電量j。QS此,爲了增加電池的放電量,最有效的方 法是將每個單位重量的放電量(m A h / g )大的石墨充塡成 高密度的方式)但是,利用將石墨充塡成高密度以形成負 極’將產生上述(1 ) 、 ( 2 )中所述,石墨與表層之低結 晶性碳間貼著力不足的傾向。一旦如此,低結晶性碳的披 膜將由石墨的表面剝離,使得與電解液產生高反應性的石 墨表面外露,導致初期放電效率下降的問題產生。 本發明的目的是獲得一種:可達到採用石墨作爲鋰離 j-一次電池之負極材料時無法兼顧之大放電量及高初期充 放電效率的鋰離子一次電池。具體來說,本發明的目的是 提供一種:可同時滿足兩種性能的石墨材料及其製造方 法、以及使用該復合石墨材料的負極材料、負極以及鋰離 子二次電池。除此之外,本發明更提供一種:可於製造復 合石墨材料的過程中’可抑制熔著、且生產性極佳的製造 方法。 【發明內容】 換S之,本發明的複合石墨材料,其具備的構造爲: -11 - (6)587350 在於石墨A的外側具有結晶性較該石墨A更低的石墨 B ’且該石墨B的外表面的至少其中一部份是存在著結晶 性較該石墨B更低的石墨C。 而’該複合石墨材料’以具有該石墨B來披覆該石墨 A ’並且以該石墨c來披覆該石墨B的構造者較佳。 而’無論上述的哪一種石墨材料,皆以球狀或者橢圓 體狀的造粒物最爲合適。 此外’無論上述的哪一種石墨材料,整體上以碳網面 層的面間隔(d㈣J是0.3 3 65謂以下,結晶子的c軸方 向的大小(Lc )是40nm以上,拉曼光譜的的峰The negative phase of the ink material. &Amp; _ V 1% yttrium, negative electrode and thallium ion secondary battery). In the future, with the miniaturization of electronic equipment and the improvement of performance, the demand for intermediary storage is also increasing. Compared with other types of batteries', lithium-ion secondary batteries can be promoted by increasing the voltage, and are therefore widely used. Lithium-ion secondary batteries have negative and non-aqueous electrolytes as the main constituent elements. Non-aqueous electricity generates clock ions and migrates between the negative and positive electrodes to form a secondary battery during charging and discharging. 'The negative electrode material of the above lithium-ion secondary battery is a carbon material using carbon material A, and it has excellent discharge properties, large discharge capacity, and the most potential for development. Please refer to Japanese Patent Publication No. 62. . 'The degree of development of the three-dimensional crystal regularity derived from its condensed polycyclic (C ndensed-ing) hexagonal mesh (called the carbon mesh surface) is known as the degree of development' can be easily interlayered / er of lithium) Forms stable compounds. (Therefore, there are local crystallinity indicated in research reports, and a large amount of (2) lithium can be inserted into the interlayer of the carbon mesh surface, so the discharge can be increased) (eg, Japan Electrical and Industrial Chemistry Association, 993, 6) (2) 5] 3 8 3 etc. reports). < It has also been reported that various layer structures formed by the amount of lithium interposed between the layers of the fe mesh surface can generate an average and nearly high lithium metal potential in the areas where they coexist ^ 1993 hEIectrochem-Soc *; Vol_M0 , 9,2490, etc.). Therefore, when used as an assembled battery ', extremely high output power can be obtained. In general, the theoretical capacity when graphite is used as the anode material is ultimately based on the discharge of the best graphite interlayer compound Li C6 formed by graphite and lithium, with a maximum discharge of 37 2 m A h / g . [However, in a lithium ion secondary battery using graphite as a negative electrode material, if the crystallinity of the graphite is too high, it is easy to cause side effects such as decomposition of the electrolyte when the graphite is charged for the first time. This side effect will cause the decomposed derivatives to continue to accumulate on the graphite surface until the formed graphite electrons cannot move directly to the thickness of the solvent). As the side effect during the first charging has nothing to do with the battery response, during the first discharging process, the so-called "irreversible capacity" that cannot release the discharged electricity will be significantly increased. In other words, it means that the ratio of the first charge amount to the first discharge amount (referred to as the first discharge efficiency in this case) is inconsistent (such as J.E in 1970] ectrocheni.Soc., Vol. 1] 7 22 2 and so on. The irreversible capacity is shown in the following calculation formula: Irreversible capacity = first charge capacity-first discharge capacity. In addition, there are reports that co-insertion of solvent molecules and lithium ions will cause the film surface layer to peel off, and the exposed graphite surface and electrolyte after peeling off. Reactions lead to poor initial charge and discharge efficiency (eg JE ectrochem. Soc. 990, Vol. 13 7 2009, etc.). Winter (3) (3) 587350 As a means known in the industry, a method for adding the positive electrode material of a secondary battery is used to solve the above-mentioned initial charge-discharge rate failure. However, the addition of excess positive electrode material 'will cause a new problem of lowering the energy density. As described above, in a lithium-ion secondary battery using graphite as a negative electrode material, 'for a discharge amount that also depends on the crystallinity of graphite and the initial discharge efficiency, PZ?', The requirement for both a large discharge level and a high initial discharge rate is The opposite. \\ Therefore, a kind of double-layer structure using low-crystalline graphite or carbon, which is helpful for increasing the initial discharge efficiency, is adopted as the core, and high-crystalline graphite which is good for increasing the discharge capacity is used to solve the above problems because Low-crystalline carbon has a low discharge capacity, so it has low decomposition reactivity with the electrolyte. The double-layer carbon material with different crystallinity is most different from the traditional technology in that: (1) the use of dioxane, Low crystallinity derived from the thermal decomposition of benzene and other organic compounds covers the surface of highly crystalline graphite as the core (for example, Japanese Patent Publication No. 4-3 6 8 7 7 8 and Japanese Patent Application Laid-Open No. 5-2 7 5 0 7 Bulletin 6). (2) High-crystalline graphite coated or soaked with liquid asphalt as the core is sintered at a temperature of about OO ° C to form low-crystalline graphite on its surface (for example, Japanese Patent Laid-Open No. 5 "21 〇66, Japanese Patent Application Laid-Open No. 5-2 1 7604, Japanese Patent Application Laid-Open No. 6-84 5 168, Japanese Patent Application Laid-Open No. II-54112 · 3, and Japanese Patent Application Laid-Open No. 2000-229924. -9- (4) (4) 587350 (3) Use carbon that can form graphite by sintering at about 300 ° C (referred to as easily graphitizable carbon in this case), such as coke, in the gaseous or liquid oxidation In a natural environment, graphite is formed after oxidation treatment at a temperature of about 300 ° C (for example, Japanese Unexamined Patent Publication No. 10- 3 2 66 1 1 and Japanese Unexamined Patent Publication No. 10_ 2] 8 6] 5 6). (4) Those who combine the methods ()) to (3) above (for example, Japanese Patent Application Laid-Open No. 0- 2] 4 6 1 5 and Japanese Patent Application Laid-Open No. 0-2 8 4 0 8 0). However, no matter which of the above-mentioned methods can not fully meet the demand standard for increasing the discharge capacity in recent years. However, from the viewpoint of industrial production, due to the cumbersome production process of the above (1) and (4), the production cost is too high and there are difficulties in production. In addition, it is difficult to control the thickness of the low crystalline carbon on the surface, which causes the problems of unstable powder characteristics such as specific surface area and bulk density, and unstable battery characteristics of discharge capacity and initial discharge efficiency. . In addition, in the method (2) above, when sintering is performed at 100 ° C, the low-crystalline carbons on the surface layer will be fused, and in a state where they are disintegrated, the low-crystallinity on the surface layer will be low. Sexual carbon will be exfoliated from the graphite as the core, leading to the problem of poor powder characteristics such as specific surface area and bulk density, and poor battery characteristics such as discharge capacity and initial discharge efficiency. In the above methods (1) and (2), since the expansion and contraction reactions of the core graphite and the surface of low-crystalline carbon during charging and discharging are not consistent, as the number of charging and discharging increases, The low-crystalline carbon exfoliation taught to the surface layer causes the same problems as described above. -10- (5) (5) 587350 In the method (3) above, in order to obtain high initial charge and discharge efficiency, the crystallinity of the highly oxidized and thick surface layer must be reduced, and the surface layer itself and the graphite inside it must also be reduced. The crystallinity of the carbonized carbon leads to a problem that sufficient crystallinity cannot be obtained even if graphitization is formed at a high temperature, and a problem arises in that the discharge amount is lowered. The discharge capacity of the cell is determined by increasing the discharge capacity j of each graphite volume constituting the negative electrode. QS, in order to increase the discharge capacity of the battery, the most effective method is to charge graphite with a high discharge capacity per unit weight (m A h / g) into a high density method). Density to form the negative electrode will cause a tendency that the adhesion force between graphite and the low-crystalline carbon of the surface layer is insufficient as described in (1) and (2) above. Once this is done, the coating of low crystalline carbon will be peeled off from the surface of graphite, so that the surface of graphite with high reactivity with the electrolyte will be exposed, leading to a problem of lowering the initial discharge efficiency. The object of the present invention is to obtain a lithium ion primary battery that can achieve a large discharge capacity and high initial charge-discharge efficiency that cannot be taken into account when using graphite as the anode material of a lithium ion j-primary battery. Specifically, an object of the present invention is to provide a graphite material and a manufacturing method thereof that can simultaneously satisfy two properties, and a negative electrode material, a negative electrode, and a lithium ion secondary battery using the composite graphite material. In addition, the present invention also provides a manufacturing method that can suppress fusion during production of a composite graphite material and has excellent productivity. [Summary of the invention] In other words, the composite graphite material of the present invention has a structure of: -11-(6) 587350 The outside of graphite A has graphite B ', which is lower in crystallinity than the graphite A, and the graphite B At least a part of the outer surface of graphite is graphite C, which is less crystalline than graphite B. The "composite graphite material" preferably has a structure in which the graphite B is coated with the graphite A and the graphite c is coated with the graphite B. Regardless of the above-mentioned graphite materials, spherical or ellipsoidal granules are most suitable. In addition, regardless of the above-mentioned graphite material, the interplanar spacing of the carbon mesh surface layer (d㈣J is 0.3 3 65 or less), the size (Lc) of the crystal in the c-axis direction is 40 nm or more, and the peak of the Raman spectrum

値強度U】36。)相對於158〇⑽·]的峰値強度(1]…)的 比値(I】36g/I〗58G)是0.05以上0.30以 (又,無論上述的哪一種石墨材料, 片狀石墨者最爲合適。;)値 intensity U】 36. ) The ratio 値 (I) to 36g / I to 58G with respect to the peak 値 intensity (1) of 158⑽⑽] is 0.05 or more and 0.30 or less (regardless of which of the above graphite materials, flake graphite is the most As appropriate.;)

下考最爲合適 前述石墨A 以鱗 再者,無論上述的哪一種 刖述石墨 A 碳網面層的面間隔(dG()2 )最好低於是〇 33 • ϋ J 3 b n m 以下。 i無論上述的哪一種石墨材料,前述石墨B之碳網面 的面間隔(dG()2 )最好低於0.3 3 7 0nm以下y 而’本案也提供一種含有上述任何〜項所述之複合The test is most suitable for the above-mentioned graphite A. In addition, no matter which type of graphite A, the surface interval (dG () 2) of the carbon mesh surface layer is preferably less than 0 33 • ϋ J 3 b n m or less. i Regardless of which of the above graphite materials, the interplanar spacing (dG () 2) of the carbon mesh surface of the aforementioned graphite B is preferably less than 0.3 37 nm, and ‘this case also provides a composite containing any of the above-mentioned items.

墨材料的鋰離子二次電池用的負極材料。 X ’本案也提供一種含有上述任何〜項所述之複合石 SS材料的鋰離子二次電池用的負極。 本案也提供一種含有上述任何一 子二次電池。 項所述之負極的鋰離 -12- (7) 最後,本發明提供一種複合石墨材料之製造方法,是 用以製造具有:在於石墨A的外側具有較之該石墨A更 低的結晶性的石墨B,且該石墨B的外表面的至少其中一 部份是存在著較之該石墨B更低的結晶性的部分的構造之 複合石墨材料,該製造方法是具有:在於石墨的外側附著 上具有易於石墨化特性的碳的過程;以使該具有易於石墨 化特性的碳實質上尙未石墨化的程度,對於該附著體進行 第一次燒結的過程;對於該第一次燒結體,以實質上不加 以粉碎的方式施予機械能量而予以改質的過程;對於該改 質體進行直到該具有易於石墨化特性的碳實質上已經石墨 化爲止的第二次燒結的過程。 在上述的製造方法中,前述石墨以鱗片狀石墨最爲合 適。 此外,無論上述的哪一種製造方法中,前述石墨之碳 網面層的面間隔(d〇 〇2 )最好低於0.3 35 8nm以下。 而無論上述的哪一種製造方法中,前述具有易於石墨 化特性的碳最好是由:焦油、瀝青以及中間相所組成的群 組中所選出的至少一種。 再者,無論上述的哪一種製造方法中,最好在進行前 述附著過程之前,具有將該石墨予以造粒的過程。 而,無論上述的哪一種製造方法中,前述附著過程最 好是利用:融熔、溶解或分散所選出的至少一種方法先將 該具有易於石墨化特性的碳變成液狀,再使其附著於該石 墨上。 -13- (8) (8)587350 又,無論上述的哪一種製造方法中,前述第一次燒結 過程最好是使得該具有易於石墨化特性的碳中所殘留的揮 發成分變成2.0質量%以上20質量%以下。 最後,無論上述的哪一種製造方法中,最好於前述第 一次燒結過程後,具有將二次凝集以上的凝集體加以碎解 (disagglomerate )白勺過程 ° 【實施方式〕 接下來,對本發明進行詳細的說明。 本發明的複合式石墨材料,其具備的構造爲:在於石 墨A的外側具有結晶性較該石墨A更低的石墨B,且該 石墨B的外表面的至少其中一部份是存在著結晶性較該石 墨B更低的石墨C。 據此,本發明的複合石墨材料,首先其所謂的一次結 構,是在石墨A的外側具有結晶性較該石墨A更低的石 墨B。這裡所指的「石墨A的外側」,可爲該石墨A的 外表面全體或者局部。因此,該一次結構亦可形成複數個 該石墨A由外部該石墨B包覆的樣態。舉例來說,可由2 個石墨A將石墨B包夾成啞鈴狀。在上述的任何一種狀 態下,即使該石墨B形成局部間斷,或者沒有間斷地使該 石墨A的局部外露都沒有關係。 上述一次結構的狀態整理如下所示: (1)石墨B附著於1個石墨A,或者石墨B包覆1 個石墨A的狀態。 -14- (9) (9)587350 (2 )聚集複數個上述(1 )的狀態。 (3 )複數個石墨A被石墨B所包覆。 (4 )聚集複數個上述(3 )的狀態。 ί亦可將上述的狀態中的任何1種或2種以上加以組 合。而其中以(3 )的狀態最佳/特別是由石墨Β包覆複 數個石墨A,且形成近似球形者最爲合適> (構成本發明中複合石墨材料的石墨c,只需存在上述 一次結構之石墨B外表面的局部即可> 其中又以存在石墨 B整個外表面上’並與石墨B形成一體者最佳。而,本發 明中所述的石墨’除了石墨本身之外’也食有部分用來使 石墨之間產生結合的碳質,業界將其稱爲「石黑質材 料」。 在本發明中,石墨A的結晶性高於石墨b。舉例來 說,石墨A可爲人造石墨、天然石墨、膨脹石墨、石墨 碳纖維、石墨化碳黑等)淇中更含有使中間相燒結碳(原 料爲焦油、瀝青)'中間相小球體、焦炭(生焦炭、濕焦 灰、瀝㈢焦炭、天然焦炭 '石油焦炭等)之類的易石墨化 碳經3 00 (TC左右處理後的石墨化物質。其中以有助於獲 得大放電量的高結晶性石墨最佳,特別是天然石墨最適 合。) L石墨的結晶性,可由X光廣角繞射法中之碳網面層 的面間隔(docn )來判斷 > 換言之,採用CuK 〇光作爲X 光源,並以局純度的矽作爲標準物質來測量石墨() 的繞射峰値,再藉由該峰値位置算出d㈣2。計算的方法是 (10) 根據學振法(日本學術振興會第I 1 7委員會所製定的測定 法),具體的方可適用如「碳纖維」第7 3 3〜7 4 2頁(近代 糠輯社,1 9 8 6年3月發行)所記載的方法。 〔在本發明中,雖然並未特別限定石墨A的結晶性必 須高於石墨B,但以d 〇 〇 2低於0 · 3 3 5 8 nm以下者最爲適 當。丨 石墨 A的形狀可爲球狀 '橢圓體狀、鱗片狀、塊 狀、板狀、纖維狀及粒狀等各種形狀。即使利用塊狀的石 墨加工而成者亦無妨。 而石墨A又以鱗片狀的石墨最爲合適。其中,又以 聚集或造粒出複數個鱗片狀石墨,並形成球狀或橢圓體狀 的外形者最佳。在這種情形下,雖然在最後所獲得的複合 石墨材料中,石墨 A以形成球狀或橢圓體狀者較佳,但 如果預先造粒出複數鱗片狀石墨,並使其形成緊密的球狀 或橢圓體狀的石墨 A則更爲合適。具體來說,造粒成緊 密的球狀或橢圓體狀的石墨A,其造粒體的空隙率以低於 50體積%以下者爲宜,其中又以低於30體積%以下者最 佳。倘若造粒體的空隙率低於5 0體積%以下,將使後續 加工過程中易石墨化性碳形成適當的附著量,可輕易獲得 充分的放電量。況且,一旦複合石墨材料中不易殘存空隙 的話,即使製作出高密度的負極,也恐有複合石墨材料破 裂導致初期衝放電效率下降之虞。 石墨A的粒于徑,根據體積換算以1〜1〇〇μΓΠ較爲合 適,其中又以2〜30μηι最爲適當> -16- (11) 石墨A與石墨B的比例,就石墨B的質量單位來 說’石墨A最好爲50〜1000質量單位,其中石墨a的比 例又以100〜2 0 0 0質量單位最佳)。 本發明的石墨B,只要是結晶性低於石墨a者,無論 哪種石墨皆適用。譬如’(石墨B可爲易石墨化性碳的石墨 化物。所謂的易石墨化性碳,是指藉由3 0 0 0 °C左右的鍛 燒而轉變成石墨的碳 > 易石墨化性碳中的成分,可藉由如 增加一次 QI ( Primary Quinoline Insoluble)的比例、或 降低若干石墨化時的溫度來獲得結晶性低於石墨A的石 墨B。其中又以採用焦油、瀝青作爲原料,並進行鍛燒形 成中間相後於3 0 0 0 °C左右形成石墨化者最爲合適。石墨b 的結晶性最好是d 〇 〇 2低於〇 · 3 3 7 0 n m以下。 本發明的複合石墨材料,至少在構成上述一次結構之 石墨B外表面的局部,存在結晶性低於石墨b的石墨c。 舉例來說,@石墨C可藉由對作爲石墨b原料的易石墨 化性碳施以壓縮、剪斷、衝擊及/或磨擦等機械性能量來 進行改質處理後,利用產生石墨化來製作或形成) ί辉由上述改質處理所獲得的易石墨化性碳),(由於其表 面至少有部分的結晶結構紊亂,因此改質處理後形成石墨 化的石墨C的結晶性較石墨β更低^)。構成本發明之複合 石墨材料的石墨C,可利用上述的方法形成於構成上述一 次結構之石墨Β的局部表面。當然也能採用其他方法所取 得的石墨C藉由貼著或插入之類的手段使其存在於石墨β 的表面。就生產效率的觀點來看,使石墨C 一體形成於石 -17- (12) 墨B表面的方法,較採用其他製程製造者更有效率。 只要是能製作出具有前述型態的複合石墨材料,任何 方法皆適用於本發明的複合石墨材料,並無特別的限制。 爲了有助於對本發明的理解,乃列舉一個製作上述複 合石墨材料的製造方法,以下便針對本發明所揭示的部分 製造方法進行說明。 本發明所揭示的製造方法,(是用來製造具有:在於石 墨A的外側具有結晶性低於該石墨A的石墨B,且該石 墨B的外表面的至少其中一部份是存在著結晶性低於該石 墨B的部分之構造的複合石墨材料,$亥製造方法是具有: 在於石墨的外側附著上具有易於石墨化特性的碳的過程; 以使該具有易於石墨化特性的碳實質上尙未石墨化的程 度,對於該附著體進行第一次燒結的過程;對於該第一次 燒結體,以實質上不加以粉碎的方式施予機械能量而予以 改質的過程;對於該改質體進行直到該具有易於石墨化特 性的碳實質上已經石墨化爲止的第二次燒結的過程。以 下,將其稱爲「本發明的方法」。 (依據本發明的方法,可輕易獲得石墨A >石墨B >石 墨 C之結晶性的本發明複合石墨材料‘)。ί特別是在石墨B 與石墨C之間不存在界面所一體成形的複合體j 相對於石墨B,石墨C的結晶性更低。特別是與石墨 B —體形成後,最好是以薄層的狀態存在。當利用上述的 方法形成石墨C時,雖然因石墨B與石墨C的分界不明 顯,無法淸楚地限定石墨C的厚度,但石墨C的厚度以 -18- (13) Ο · Ο 1〜5 μ m最爲合適y。 在本發明中,石墨A、石墨及石墨C的結晶性必須維 持石墨A >石墨B >石墨C的順序。(^藉此,可在使石墨A 維持原本的大放電量的同時,保有石墨C所具有之高初期 放電效率的特徵> 再者,藉由緊緻地包含於其中之石墨B 的作用,即使將複合石墨材料進行高密度充塡形成負極的 狀態下,也能維持上述優越的電池特性。 在本發明中,複合石墨材料的外表面結晶性,也就是 指石墨C的結晶性,可藉由採用氬雷射的拉曼光譜來進行 評估。換言之,在石墨結構的9種晶格振動中,對應相當 於碳網面內晶格振動的E2g型之1 58〇C1rT]附近的拉曼光 譜、及反應因主要存在於表層隻結晶缺陷與積層不平之類 的紊亂結晶結構之1 5 8 0 cm·1附近的拉曼光譜,可採用波 長爲5 1 4 · 5 nm之氬雷射的拉曼分光分析器(日本分光股份 有限公司生產,型號爲N R 1 1 0 0 )來進行量測。分別根據 拉曼光譜的峰値強度計算出其強度比 R ( R = I136Q / I] 5 8 〇 ) ’並判定出強度比越大者表面結晶性低的結論。由 增加初期充放電效率的觀點來看,強度比R最好是g 〇·〇5。這樣做是基於爲了降低表層結晶化在略呈紊亂之複 合石墨材料表面上的電解液分解反應。而,由將放電量之 下降抑制到最小的觀點來看,R最好小於〇. 3 〇。 另外,複合石墨材料全體的結晶性,可藉由與前述相 同的X光廣角繞射法來求取其平均値。也可由碳網面層 的面間隔(dou )及結晶子C軸方向的尺寸(Lc )來判 (14) 疋。也就是指採用CuK α光作爲χ光源,並以高純度的 矽作爲標準物質來測量石墨(002 )的繞射峰値’再藉由 該峰値位置及其半値寬度,分別算出d^2與Lc。 本發明之全體複合石墨材料,其de()2最好低於 〇.3365nni以下,而Lc則最好高於4〇nm以上。其中又以 d〇〇2低於o.3 3 62nm以下,Lc高於5〇nm以上者最爲合 適。倘若hG2低於〇.3 3 6 5謂以下,且Lc高於4〇謂以上 時,由於複合石墨材料的平 用複合石墨材料作爲鋰離子 鋰的摻雜量變大,故能獲得 本發明的複合石墨材料 粒子徑。當作爲電極材料使 電池特性的調整等來選擇平 合石墨材料作爲鋰離子二次 均粒子徑爲5〜]〇 〇 μ η],其中 ^發明的複合石墨材料 狀的形狀。)球狀或橢圓體狀 佳的電解液注入性及保持性 環性,所以非常適合用於鋰 若採用以鱗片狀石墨爲代表 Α ’可輕易形成形狀趨近於 的複合石墨材料的平均長寬 2以下最適合。 又’由於該複合石墨材 均石墨結構非常的發達,當使 二次電池的負極材料時,由於 極大的放電量。 ’可視用途選擇其是當的平均 用時,可視電極的設計厚度、 均粒子徑。當採用本發明的複 電池的負極材料時,其最佳平 又以5〜30μιτι最合適。 ’最好儘可能地形成趨近於球 的複合石墨材料,由於具有極 ’並能提高急速放電效率及循 離子二次電池的負極材料。倘 之天然石墨的造粒物作爲石墨 球狀的被合石墨材料。本發曰月 比最好低於3以下,其中又以 料形成趨近於球體的形狀,故 -20- (15)587350 可形成極高的體密度。在高體密度的狀態下製作 負極之際’無須施加額外的壓力,有助於降低石 破壞等問題。體密度最好高於0.5g/cm3 ]: 〇.7g/cm3以上較合適,其中又以i.〇g/cm3以上最 本發明之複合石墨材料的比表面積,可配合 次電池的特性、及負極黏合劑的糊狀特性可任意 而BET比表面積低於20m2/g以下者,其鋰離子 的安全性也較佳。一般BET比表面積爲0.3〜5m 於3m2/g者更合適,其中又以低於1 m2/g者最合 接下來,針對上述的本發明製造方法作更 明。 在本發明的方法中,是令易石墨化性碳附著 外側。換言之,只需使一個或複數個石墨包夾於 性碳中即可。 該石墨相當於本發明複合石墨材料中的石墨 用的石墨,以碳網面層之面間隔(dG()2 )低於 以下者最爲合適。而易石墨化性碳至少是由焦油 中間相所形成的物質中所選出的1種。其中又以 油、瀝青等石油系或石炭重油中選出一種作爲原 次燒結處理受所形成的中間相物質較佳。 在該附著處理中,該易石墨化性碳最好是利 溶解或分散的其中一種方法形成液體狀,使其附 墨。舉例來說,再加熱的狀態下對熔融狀態的易 碳與石墨加以捏揉,可獲得彼此緊密混合的石墨 高密度的 墨材料的 乂上’以 佳。 鋰離子二 的設計。 —次電池 2/§ ,以低 適。 詳細的霞兌 於石墨的 易石墨化 A。所便 0.3 3 5 8 η 、瀝青及 至少由焦 料,經〜 用熔融、 著於該石 石墨化性 與易石墨 -21 - (16) (16)587350 化性碳的混合物。在該方法中,最好是將加熱捏揉物冷卻 固化後加以碎解’再調整成所需的形狀。或者,亦可在石 墨內添加少量溶融狀的易石墨化性碳,再將其造粒形成所 需的粒子形狀。具體來說,可將焦油及瀝青等易石墨化 碳,溶解於苯、甲苯、喹、中焦油、重焦油等物之中形成 溶液’再將石墨浸入其中利用加熱、減壓處理,使易石墨 化性碳附者於石墨A後順便去除溶劑。而,所形成之附 者有易石墨化性碳的石墨’附著量不均勻亦無妨,中心部 與表面部的揮發量不同也無所謂。 而’在本發明的方法中’最好在進行附著處理之前, 先進行石墨的造粒處理。 由於本發明的複合石墨材料,以球狀或橢圓體狀最爲 合適,連帶地使石墨也形成該形狀。換言之,石墨A也 以球狀或橢圓體狀最合適。而利用複數鱗片狀石墨造粒而 成者最佳。而石墨的造粒方法,可採用傳統上對複數鱗片 狀石墨施以乾式、濕式的造粒方法。 在進行造粒的過程中’亦可使用黏結劑。而黏結劑的 成分可採用上述易石墨化性碳。黏著劑的成分亦可採用可 於稍後二次燒結中消失的成分。只要在不損及本發明效果 的範_內’即使未採用上述利用二次燒結來產生石墨構造 的方式易無妨。 此外’當採用焦油或瀝青作爲易石墨化性碳時,最好 含有更細的微粒子。藉由微粒子可降低一次燒結後的溶融 膠合性’將有助於碎解的執行。只要抑制一次燒結後的熔 -22- (17) (17)587350 融膠合性,便能以易石墨化性碳完全覆蓋於石墨的外側, 最終將可更進一步提高複合石墨材料的初期充放電效率。 對具有親油性之焦油、瀝青或前述兩者於一次燒結後 所形成的中間相而言,微粒子的附著性越低越好。一旦具 有附著性時,將降低碎解的改良效果。而該微粒子最好是 具有親水性的粒子。 雖然微粒子可採用在燒結的過程中與碳產生反應、或 者殘留於一次燒結後的複合石墨材料中的粒子,但該微粒 子或衍生物最好在二次燒結之前氣化、分解,避免殘留於 複合石墨材料中。 微粒子只需極小的尺寸及使用量,便能達到防止熔融 膠合及提高碎解性的效果。故微粒子的平均粒徑最好低於 1 μηι以下。只要低於]μηι以下,不必添加大量的微粒 子,也不會導致電容量等電池性能下降的問題產生。 微粒子的使用量,以複合石墨材料中之石墨 Β的 0·0】〜]0質量%最合適。其中又以 0.05〜3質量%最佳。當 大於0 · 0 1質量%以上時,將增加碎解性的改良效果,當低 於1 0質量%以下時,將使所製成之複合石墨材料形成適 當的比表面積,並形成適當的粒子徑,不易產生初期放充 放電效率下降的情形。 符合上述條件的微粒卞’譬如氧化较、氧化銘、氧化 鈦之類的無機微粉;和金屬氧化物、經氧化處理之碳黑之 類的碳質粒子;和鐵黑、鉻黃、鋅黃、黃色氧化鐵、黃鐵 華、鈦黃、氧化鐵紅、鉛丹、氧化鋅、鋅白、硫酸鉛、鋅 -23- (18) 鋇白、氧化鈦、氧化銻、矽鋁、釉白、硫酸鈣、石膏之類 的顏料;和高嶺土、滑石黏土、燒結黏土、含水矽酸鋁合 成物之類的矽酸鋁類;和白堊、粉筆之類的碳酸鈣類;和 白雲石粉末之類的鈣•鎂碳酸鹽類、菱鎂礦粉末 '鹼基硫 酸鎂等的硫酸鎂類;和砂灰石、含水砂酸錦合成品之類的 矽酸鈣類;和滑石、雲母等矽酸鎂類;和石英粉末、粉化 石夕酸、砂藻土等矽酸類;及樹脂球等物。 在本發明的方法中,可以單獨使用一種、或者混合使 用數種前述的物質。其中又以不會與易石墨化性碳產生反 應、利用氣相法製成的氧化矽、氧化鋁及氧化鈦之類的無 機微粉最合適。 雖然並沒有特別限制將微粒子加入易石墨化性碳的混 合方法,、本案中是採用預先將微粒子溶入溶劑中,再將該 含有微粒子的溶劑注入熔融狀態的焦油或瀝青中進行攪泮 的方法。而溶劑可採用前述的溶劑。 在本發明的方法中,係於易石墨化性碳附著於石墨 後,對該附著體進行一次燒結,該一次燒結並不會使附著 於表面的易石墨化性碳產生實質上石墨化的程度。 所謂「不會形成實質上的石墨化」的程度,是指在下 個流程的改質處理中,可使結晶結構產生不穩定的狀態, 也就是分子結構中具有流動性的狀態。在該處理過程中, 也進行若干易石墨化性碳的重縮合反應。這種狀態可藉由 殘存之易石墨化性碳的揮發量來顯示適合的範圍。一次燒 結後之易石墨化性碳,其含有的揮發量最好是2.0質量% -24- (19) 以上〜不滿20質量%以下。其中又以4質量%以上〜不滿 1 5質量%以下最佳。在本發明中’揮發量是根據JIS K242 5所規範的固定碳法,並藉由以下方法所測得。 易石墨化性碳揮發量的測量方法:量取1 g的測量對 象物(易石墨化性碳)置於坩堝,在不加蓋的狀態下放入 電爐內以4 3 0 °C加熱3 0分鐘。接下來,該採雙層坩堝以 8 00 C加熱3 0分鐘來除去揮發量,所減少的部分就等於 揮發量。 倘若以其他的方式來表示一次燒結後的易石墨化性碳 的話’是指軟化點(梅特勒法)約高於3 6 0 °C以上的固 體’喹的不溶量(QI)爲50質量%以上〜100質量%以 下,其中又以80質量%以上〜99.5質量%以下更爲合適。 在本發明中,Q I是根據·ΤΙ S K 2 4 2 5的規範,採用下列 的過濾法進行測量。 QI測量法:將粉末狀的碳材料(易石墨化性碳)溶 解於喹中,以7 5 °c加熱3 0分鐘後,在熱的狀態下進行吸 引過濾。按照喹、丙酮的順序來淸洗殘渣,直到每種濾液 形成無色狀態後(以目視判斷),將其乾燥後測量其質 量,便完成整個QI( Quinoline insoluble)。其中係採用 矽藻土作爲助濾劑。過濾器則採用jlS R3 5 3 0所規定的壺 型過濾器1G4。 揮發量大、或者QI低的易石墨化性碳,可顯示利用 二次燒結形成石墨化過程中的熔融性。這種易石墨化性 碳,在二次燒結時其形狀將產生變化,其因於材料間產生 -25- (20) 熔融之故。因此,一次燒結後揮發量低於20質量%以下 者,在利用機械性能量進行改質處理的過程中,容易使表 層的結晶解構紊亂’而容易在稍後的二次燒結中形成石黑 化。根據這個理由,本發明所使用的易石_化性碳,以可 藉由一次燒結將揮發量抑制在適當範圍內省較佳。 反觀掉發里少、或者Q】局的易石墨化性碳,則不旦 上述的熔融特性。只要揮發量大於2 · 0質籩%以上,在施 加機械性能量後容易在易石墨化性碳的外表面形成棄亂白勺 結晶結構,並於二次燒結後形成合適的低結晶性石墨c。 據此’在本發明中,一次燒結所產的易石龜化性碳的揮發 量,最好調整在2 · 0質量%以上〜未滿2 0質量%以下的範 圍內。 一次燒結,可在減壓、常壓或加壓的任何一種狀態下 進行。而一次燒結的溫度通常爲300〜]20〇艺,最好是在 3 5 0〜6 0 0 °C的溫度範圍內進行。雖然最好在非氧化性的 環境下進行,但也能在部分氧化性環境下執行熱處理。而 一次燒結亦可分多次來進行。燒結時間並無特殊限制,約 爲0 · 5〜1 0 0小時左右。 雖然經一次燒結之燒結物的形狀並無特別的限制,可 爲粒狀、鱗片狀、球狀、針狀及纖維狀等的任何一種,但 以球狀或橢圓體狀最爲合適。在一次燒結後僅形成熔融膠 合的狀態下,可使用習知的各種粉碎機來碎解熔融膠合 物。而碎解的方法,可採用滾子式、衝擊式、磨擦式、壓 縮式、石臼式、動力衝突式、渦流式、氣流式、剪斷式及 -26- (21) (21)587350 振動式等各種市面販賣的粉碎機。 在本發明的方法中,是對利用上述一次燒結所獲得的 一次燒結體,施以不會產生實質上粉碎的機械性能量來進 行改質處理。 藉由該改質處理,可於二次燒結後獲得複合石墨材 料,該複合石墨材料的結構爲:於高結晶性的石墨 A外 側形成結晶性低於石墨A的石墨B ’並至少在該石墨b 的局部外表面上存在結晶性低於石墨B的石墨C。 在該製造方法中,最好是在碎解該一次燒結體並將其 形狀調整至近似完成品後,再施以機械性能量。話雖如 此,也可以在碎解由複數石墨與易石墨化性碳所形成之熔 融膠合物時,施以連續的機械性能量。 本發明中所稱的機械性能量,是指各種壓縮、剪斷、 衝突、摩擦之類的應力。該機械性能量,最好是作用於一 次燒結後之易石墨化性碳的外表面。倘若採用一般的機械 化學處理來進行這類操作,所獲得的機械性能量,將大於 一般攪拌所賦予的力量。但是,至少不要對構成一次燒結 體之石墨(石墨A )的粒子及凝集體產生實質上的破壞。 一但形成過度的破壞,反而產生初期充放電率下降的傾 向。具體來說,因施加機械性能量所導致一次燒結體之平 均粒徑的下降率,最好抑制在2 0 %以下。 改質處理,可對一次燒結體的外表面施以機械性能 量。任何裝置皆適用,並無構造及種類的限制。舉例來 說,用來施加機械性能量的裝置,可爲加壓揉合機、2根 -27- (22) (22)587350 轉子之類的捏揉機、旋轉球磨機、HYBRIDIZATION SYSTEM (商品名’奈良機械製作所出品)、me CHAN 0 MICROS (商品名,奈良機械製作所出品)及A negative electrode material for a lithium ion secondary battery using an ink material. X 'The present invention also provides a negative electrode for a lithium ion secondary battery containing the composite stone SS material described in any one of the above items. The present invention also provides a secondary battery including any one of the above. (7) Finally, the present invention provides a method for manufacturing a composite graphite material, which is used to produce a graphite material having a lower crystallinity on the outside of the graphite A than the graphite A. Graphite B, and at least a part of the outer surface of the graphite B is a composite graphite material having a structure having a lower crystalline portion than the graphite B. The manufacturing method includes: A process of carbon with easy graphitization characteristics; a process of performing the first sintering on the adherend to such an extent that the carbon with easy graphitization characteristics is substantially ungraphitized; for the first sintered body, A process of reforming by applying mechanical energy substantially without pulverizing; performing a second sintering process on the reformed body until the carbon having easy graphitization characteristics has been substantially graphitized. In the above manufacturing method, the graphite is most preferably flaky graphite. Moreover, in any of the above-mentioned manufacturing methods, the interplanar spacing (d002) of the carbon network surface layer of the graphite is preferably less than 0.3 35 8 nm. Regardless of which of the above-mentioned manufacturing methods, the aforementioned carbon having easy graphitization characteristics is preferably at least one selected from the group consisting of tar, pitch, and mesophase. Furthermore, in any of the above-mentioned manufacturing methods, it is preferable to have a process of granulating the graphite before performing the aforementioned adhesion process. Regardless of which of the above-mentioned manufacturing methods, the aforementioned attachment process is preferably made by melting, dissolving, or dispersing at least one of the selected methods to first convert the carbon having an easily graphitizable property into a liquid state, and then attach it to The graphite. -13- (8) (8) 587350 In any of the above-mentioned manufacturing methods, it is preferable that the first sintering process is such that the volatile components remaining in the carbon having easy graphitization characteristics become 2.0% by mass or more 20% by mass or less. Finally, no matter which of the above-mentioned manufacturing methods, it is preferable to have a process of disagglomerating the aggregates above the secondary aggregation after the first sintering process described above. [Embodiment] Next, the present invention Explain in detail. The composite graphite material of the present invention has a structure in which a graphite B having a lower crystallinity than the graphite A is outside the graphite A, and at least a part of an outer surface of the graphite B has crystallinity. Graphite C is lower than this graphite B. According to this, the composite graphite material of the present invention firstly has a so-called primary structure, which has graphite B on the outside of graphite A having lower crystallinity than graphite A. The "outer side of graphite A" referred to herein may be the whole or a part of the outer surface of the graphite A. Therefore, the primary structure can also form a plurality of forms in which the graphite A is covered by the outer graphite B. For example, two graphites A and graphite B can be sandwiched into a dumbbell shape. In any of the above states, it does not matter whether the graphite B is locally discontinuous or the graphite A is partially exposed without interruption. The state arrangement of the above primary structure is as follows: (1) The state where graphite B is attached to one graphite A, or graphite B is coated with one graphite A. -14- (9) (9) 587350 (2) A plurality of states (1) above are gathered. (3) A plurality of graphites A are covered with graphite B. (4) A plurality of states (3) above are gathered. You can combine any one or more of these states. Among them, the state of (3) is the best / especially the one in which a plurality of graphites are coated with graphite B and form an approximately spherical shape is most suitable. (The graphite c constituting the composite graphite material in the present invention need only exist once. A part of the outer surface of the graphite B of the structure may suffice. Among them, it is best that the graphite B is present on the entire outer surface of the graphite B and is integrated with the graphite B. Moreover, the graphite described in the present invention is not only the graphite itself, There are some carbonaceous materials used to make the graphite bond with each other, and the industry calls them "lithocene materials." In the present invention, the crystallinity of graphite A is higher than that of graphite b. For example, graphite A may be Artificial graphite, natural graphite, expanded graphite, graphite carbon fiber, graphitized carbon black, etc.) Qi also contains mesophase sintered carbon (raw materials are tar and pitch) 'mesophase spheroids, coke (green coke, wet coke ash, bitumen Graphite that is easily graphitizable carbon such as coke, natural coke, petroleum coke, etc. after being treated at about 3 00 (TC. Among them, the most crystalline graphite that helps to obtain a large discharge capacity is the best, especially natural stone Ink is best ) The crystallinity of L graphite can be judged by the interplanar spacing (docn) of the carbon mesh surface layer in the X-ray wide-angle diffraction method. In other words, CuK light is used as the X light source, and local purity silicon is used as the standard material. Measure the diffraction peak 値 of graphite (), and calculate d㈣2 from the position of the peak 値. The calculation method is (10) The specific method can be applied according to the "Study method" (measurement method developed by the Japan Society for the Promotion of Science, Committee I 17), such as "Carbon Fiber", pages 7 3 3 ~ 7 4 2 Company, March 1986). [In the present invention, although it is not particularly limited that the crystallinity of graphite A must be higher than that of graphite B, it is most appropriate that d 002 is less than 0. 3 3 5 8 nm.丨 The shape of graphite A can be spherical, ellipsoid, scale, block, plate, fibrous, and granular. Even those made from blocky graphite are fine. The most suitable graphite A is flaky graphite. Among them, those in which a plurality of flaky graphites are aggregated or granulated and formed into a spherical or ellipsoidal shape are the best. In this case, although in the composite graphite material finally obtained, graphite A is preferably formed into a spherical or ellipsoidal shape, if a plurality of flaky graphites are granulated in advance and formed into a compact spherical shape Or ellipsoidal graphite A is more suitable. Specifically, graphite A granulated into a dense spherical or ellipsoidal shape preferably has a porosity of less than 50% by volume, and more preferably less than 30% by volume. If the porosity of the granules is less than 50% by volume, an appropriate amount of easily graphitizable carbon will be formed during subsequent processing, and a sufficient discharge amount can be easily obtained. Moreover, once voids are difficult to remain in the composite graphite material, even if a high-density negative electrode is produced, there is a possibility that the composite graphite material is cracked and the initial discharge efficiency may decrease. The particle diameter of graphite A is more suitable from 1 to 100 μΓΠ based on volume conversion, and 2 to 30 μηι is the most appropriate. -16- (11) The ratio of graphite A to graphite B is In terms of mass units, 'graphite A is preferably 50 to 1,000 mass units, and the proportion of graphite a is again 100 to 2000 mass units.) The graphite B of the present invention is applicable to any graphite as long as it is less crystalline than graphite a. For example, "(graphite B may be a graphitizable compound of graphitizable carbon. The so-called graphitizable carbon refers to carbon that is converted to graphite by calcination at about 300 ° C. ≫ Graphitizable The components in carbon can be obtained by increasing the proportion of QI (Primary Quinoline Insoluble) or reducing the temperature during graphitization to obtain graphite B, which is less crystalline than graphite A. Among them, tar and pitch are used as raw materials. After calcining to form a mesophase, it is most suitable to form graphitization at about 3 0 0 ° C. The crystallinity of graphite b is preferably d 〇2 is less than 0.33 370 nm. The present invention For composite graphite materials, at least in part of the outer surface of graphite B constituting the above-mentioned primary structure, there is graphite c that is less crystalline than graphite b. For example, @GraphicC can be used for the graphitizable carbon as the raw material of graphite b After applying the mechanical properties such as compression, shearing, impact, and / or friction to the modification treatment, it is produced or formed by generating graphitization. 辉 Hui The graphitizable carbon obtained by the above modification treatment), ( As its surface is at least partially Disordered crystal structure, the crystallinity than the graphite after the formation of the modified process of graphitization of the graphite C lower ^ β). The graphite C constituting the composite graphite material of the present invention can be formed on a partial surface of the graphite B constituting the primary structure by the method described above. Of course, graphite C obtained by other methods can also be made to exist on the surface of graphite β by means such as adhesion or insertion. From the viewpoint of production efficiency, the method of integrally forming graphite C on the surface of stone -17- (12) ink B is more efficient than the manufacturer using other processes. As long as a composite graphite material having the aforementioned shape can be produced, any method is applicable to the composite graphite material of the present invention, and there is no particular limitation. In order to facilitate the understanding of the present invention, a manufacturing method for manufacturing the above-mentioned composite graphite material is enumerated, and a part of the manufacturing method disclosed in the present invention will be described below. The manufacturing method disclosed in the present invention (is used to produce graphite B which has crystallinity lower than that of graphite A on the outside of graphite A, and at least a part of the outer surface of graphite B has crystallinity The composite graphite material having a structure lower than that of the graphite B has a manufacturing method of: a process of attaching carbon having easy graphitization characteristics on the outside of the graphite; so that the carbon having easy graphitization characteristics substantially 尙The degree of non-graphitization, the first sintering process is performed on the adherend; the first sintered body is modified by applying mechanical energy in a manner that does not substantially pulverize; and the modified body The second sintering process is performed until the carbon having easy graphitization characteristics has been substantially graphitized. Hereinafter, this is referred to as "the method of the present invention." (According to the method of the present invention, graphite A can be easily obtained > Graphite B > The crystalline composite graphite material of the present invention '). In particular, the composite body integrally formed without the interface between graphite B and graphite C is opposite. The crystallinity of graphite B and graphite C is lower. Especially after the formation of graphite B, it is best to exist in a thin layer. When graphite C is formed by the above method, although the boundary between graphite B and graphite C is formed, It is not obvious that the thickness of graphite C cannot be constrained, but the thickness of graphite C is -18- (13) 〇 · Ο 1 ~ 5 μm is most suitable. In the present invention, graphite A, graphite, and graphite C The crystallinity must be maintained in the order of Graphite A > Graphite B > Graphite C. (^ In this way, while maintaining the original high discharge capacity of Graphite A, the characteristics of high initial discharge efficiency possessed by Graphite C are maintained> In addition, by the action of graphite B contained tightly, the above excellent battery characteristics can be maintained even in a state where the composite graphite material is charged at a high density to form a negative electrode. In the present invention, the composite graphite The crystallinity of the outer surface of the material, that is, the crystallinity of graphite C, can be evaluated by using Raman spectroscopy with argon laser. In other words, the nine lattice vibrations of the graphite structure correspond to the carbon mesh surface. 1 58 of E2g type with internal lattice vibration C1rT] near the Raman spectrum, and the reaction mainly exists in disordered crystal structures such as crystalline defects and uneven layers in the surface layer. The Raman spectrum near 1 5 8 0 cm · 1 can be used with a wavelength of 5 1 4 · 5 A Raman spectrometer (manufactured by JASCO Corporation, model: NR 1 1 0 0) is used for measurement. The intensity ratio R (R = I136Q / I] 5 8 〇) 'and determined that the larger the intensity ratio is, the lower the surface crystallinity is. From the viewpoint of increasing the initial charge-discharge efficiency, the intensity ratio R is preferably g 0. 05. Based on the electrolyte decomposition reaction to reduce the surface layer crystallization on the surface of the slightly disordered composite graphite material. On the other hand, from the viewpoint of suppressing the decrease in the discharge amount to a minimum, R is preferably less than 0.30. In addition, the crystallinity of the entire composite graphite material can be determined by the same X-ray wide-angle diffraction method as the average 値. It can also be judged by the interplanar spacing (dou) of the carbon mesh surface layer and the dimension (Lc) in the C-axis direction of the crystal (14) 疋. That is, CuK α light is used as the χ light source, and high-purity silicon is used as a standard substance to measure the diffraction peak 値 ′ of graphite (002). Then, by using the position of the peak 値 and its half-width, d ^ 2 and Lc. In the overall composite graphite material of the present invention, the de () 2 is preferably lower than 0.365 nni, and the Lc is preferably higher than 40 nm. Among them, it is most suitable that dOO2 is lower than 0.32 62nm, and Lc is higher than 50nm. If hG2 is lower than 0.3 3 65 5 and Lc is higher than 40 40, the amount of doped lithium graphite as the composite graphite material of flat graphite composite graphite material becomes larger, so the composite of the present invention can be obtained. Particle diameter of graphite material. When the electrode material is used to adjust the battery characteristics, etc., a flat graphite material is selected as the lithium ion secondary average particle diameter of 5 to [00 μη], where the composite graphite material of the invention has a shape. ) Spherical or ellipsoidal electrolyte with excellent electrolyte injectability and retentivity, so it is very suitable for lithium. If flaky graphite is used as a representative, the average length and width of composite graphite materials with similar shapes can be easily formed. 2 or less is most suitable. Also, since the composite graphite material has a highly developed graphite structure, when the negative electrode material of a secondary battery is used, it has a large discharge capacity. For the visible use, select the design thickness and average particle diameter of the visible electrode when averaging is used. When the negative electrode material of the secondary battery of the present invention is used, its optimum level is most preferably 5 to 30 µm. It is best to form a composite graphite material that approaches the sphere as much as possible. Since it has a pole, it can improve the rapid discharge efficiency and the negative electrode material of the ion secondary battery. Provided that the granules of natural graphite are graphite spherical bonded graphite materials. The monthly ratio of this hair is preferably below 3, and it is expected to form a shape close to a sphere, so -20- (15) 587350 can form a very high bulk density. When the negative electrode is produced under a high bulk density state, it is not necessary to apply additional pressure, and it helps reduce problems such as stone damage. The bulk density is preferably higher than 0.5 g / cm3]: 0.7 g / cm3 or more is suitable, and the specific surface area of the composite graphite material of the present invention above i. G / cm3 is more suitable to match the characteristics of the secondary battery, and The paste-like characteristics of the negative electrode binder can be arbitrarily selected, and those having a BET specific surface area of less than 20 m2 / g or less have better lithium ion safety. Generally, a BET specific surface area of 0.3 to 5 m is more suitable for 3 m 2 / g, and the one with a BET specific surface area of less than 1 m 2 / g is most suitable. Next, the manufacturing method of the present invention described above will be described more clearly. In the method of the present invention, the graphitizable carbon adheres to the outside. In other words, it is only necessary to sandwich one or more graphites in sex carbon. This graphite corresponds to the graphite for graphite in the composite graphite material of the present invention, and it is most suitable that the interplanar spacing (dG () 2) of the carbon mesh surface layer is lower than the following. The easily graphitizable carbon is at least one selected from the group consisting of tar mesophases. Among them, it is preferable to select one of petroleum-based or petroleum-based heavy oil such as oil and asphalt as the mesophase substance formed by the primary sintering treatment. In this adhesion treatment, the easily graphitizable carbon is preferably formed into a liquid state by one of methods of dissolving or dispersing the carbon, and the ink is attached. For example, it is preferable that kneaded carbon and graphite in a molten state be kneaded under a reheated state to obtain a graphite high-density ink material which is intimately mixed with each other. Design of Lithium Ion II. — Secondary battery 2 / §, low. The detail of Xia Xia is compared with graphite's easy graphitization A. Therefore, 0.3 3 5 8 η, bitumen, and at least the coke are melted, and the stone is graphitized with a mixture of graphitizable and easily graphite -21-(16) (16) 587350 carbon. In this method, it is preferable that the heated kneaded material is cooled and solidified and then disintegrated 'and adjusted to a desired shape. Alternatively, a small amount of molten easily graphitizable carbon may be added to the graphite, and then granulated into a desired particle shape. Specifically, easily graphitizable carbon such as tar and pitch can be dissolved in benzene, toluene, quinine, medium tar, heavy tar, etc. to form a solution, and then the graphite can be immersed in it for heating and decompression to make it easy to graphitize. After the chemical carbon is attached to the graphite A, the solvent is removed by the way. In addition, it is not a problem that the adhered amount of the graphite to be formed of the graphitizable carbon is uneven, and the difference in the volatilization amount between the central portion and the surface portion does not matter. On the other hand, in the "method of the present invention", it is preferable to perform a graphite granulation treatment before the adhesion treatment. Since the composite graphite material of the present invention is most preferably spherical or ellipsoidal, graphite is also formed into this shape in conjunction. In other words, graphite A is most preferably spherical or ellipsoidal. It is best to use granules with a plurality of flaky graphite. As the graphite granulation method, a dry and wet granulation method is conventionally applied to a plurality of flaky graphites. It is also possible to use a binder during the granulation process. As the component of the binder, the above-mentioned easily graphitizable carbon can be used. The component of the adhesive may also be a component which can disappear in the subsequent secondary sintering. As long as it is within the range that does not impair the effect of the present invention ', it is easy to use the method of generating a graphite structure by using the secondary sintering. In addition, when tar or pitch is used as the easily graphitizable carbon, it is preferable to contain finer particles. The use of fine particles can reduce the melting and adhesiveness after one sintering ', which will facilitate the disintegration. As long as the melting -22- (17) (17) 587350 fusion bond is suppressed after one sintering, the outer side of graphite can be completely covered with easily graphitizable carbon, and the initial charge and discharge efficiency of the composite graphite material can be further improved in the end . For the tar, bitumen, or mesophase formed by one-time sintering of oleophilic tar, the adhesion of fine particles is lower as possible. Once it has adhesion, it will reduce the improvement effect of disintegration. The fine particles are preferably hydrophilic particles. Although the fine particles can be particles that react with carbon during the sintering process or remain in the composite graphite material after primary sintering, the fine particles or derivatives are preferably vaporized and decomposed before secondary sintering to avoid remaining in the composite Graphite material. Microparticles need only a small size and amount to achieve the effects of preventing melt-gluing and improving disintegrability. Therefore, the average particle diameter of the fine particles is preferably less than 1 μm. As long as it is less than [μm], it is not necessary to add a large amount of fine particles, and it does not cause problems such as degradation of battery performance such as electric capacity. The amount of fine particles used is most preferably 0% to 0% by mass of graphite B in the composite graphite material. Among them, 0.05 to 3% by mass is the best. When it is greater than 0.01% by mass, the improvement effect of disintegrability will be increased. When it is less than 10% by mass, the prepared composite graphite material will have an appropriate specific surface area and appropriate particles. Diameter, it is difficult to cause a decrease in the initial discharge / discharge efficiency. Particles that meet the above conditions, such as inorganic fine powders such as oxides, oxides, and titanium oxide; and carbon particles such as metal oxides and oxidized carbon black; and iron black, chrome yellow, zinc yellow, Yellow iron oxide, yellow iron, yellow titanium, iron oxide red, lead, zinc oxide, zinc white, lead sulfate, zinc-23- (18) barium white, titanium oxide, antimony oxide, silicon aluminum, glaze white, calcium sulfate, Pigments such as gypsum; and aluminum silicates such as kaolin, talc clay, sintered clay, hydrous aluminum silicate composites; and calcium carbonates such as chalk and chalk; and calcium and magnesium such as dolomite powder Carbonate, magnesite powder, base magnesium sulfate, and other magnesium sulfates; and calcium silicates such as limestone, water-containing sand acid brocade synthetic products; and magnesium silicates, such as talc and mica; and quartz Silicates such as powder, pulverized fossil acid, and diatomaceous earth; and resin pellets. In the method of the present invention, one of the foregoing substances may be used singly or in combination. Among them, inorganic fine powders such as silicon oxide, alumina, and titanium oxide, which are not reacted with easily graphitizable carbon, are produced by a gas phase method. Although there is no particular limitation on the mixing method of adding fine particles to easily graphitizable carbon, in this case, a method of dissolving fine particles in a solvent in advance, and then injecting the fine particle-containing solvent into molten tar or pitch to stir is used. . As the solvent, the aforementioned solvents can be used. In the method of the present invention, after the easily graphitizable carbon is attached to graphite, the adherend is sintered once, and the primary sintering does not cause the graphitizable carbon attached to the surface to be substantially graphitized . The degree that "substantial graphitization does not occur" refers to the state where the crystal structure can be unstable during the modification process in the next process, that is, the state where the molecular structure has fluidity. During this treatment, a number of graphitizable carbons undergo heavy condensation reactions. In this state, a suitable range can be shown by the amount of volatilization of the remaining easily graphitizable carbon. It is preferable that the volatile content of the easily graphitizable carbon after primary sintering is 2.0 mass% to -24- (19) or more and less than 20 mass%. Among them, it is more preferably 4 mass% to less than 15 mass%. In the present invention, the 'volatility' is measured in accordance with the fixed carbon method regulated by JIS K242 5 by the following method. Method for measuring the volatile amount of easily graphitizable carbon: Measure 1 g of the measurement object (easy graphitizable carbon) and place it in a crucible without a lid and heat it at 4 3 0 ° C for 3 0 minute. Next, the double-layered crucible was heated at 800 C for 30 minutes to remove the volatile amount, and the reduced portion was equal to the volatile amount. If the graphitizable carbon after primary sintering is expressed in other ways, 'the softening point (Mettler method) is higher than 3 60 ° C and the solid' quinone has an insoluble amount (QI) of 50 mass. % To 100% by mass, and more preferably 80% to 99.5% by mass. In the present invention, Q I is measured according to the specification of TI S K 2 4 2 5 using the following filtering method. QI measurement method: Dissolve powdery carbon material (easy-graphitizable carbon) in quinine, heat it at 7 5 ° C for 30 minutes, and then perform suction filtration under hot state. Rinse the residues in the order of quine and acetone. After each filtrate has formed a colorless state (by visual judgment), dry it and measure its quality to complete the entire QI (Quinoline insoluble). Among them, diatomite is used as a filter aid. The filter is a pot filter 1G4 specified by jlS R3 5 3 0. Graphitizable carbon with a large volatility or low QI can show the meltability during the graphitization by secondary sintering. The shape of this easily graphitizable carbon will change during secondary sintering due to the -25- (20) melting between the materials. Therefore, if the volatile content after primary sintering is less than 20% by mass, during the modification process using mechanical properties, it is easy to disturb the crystal destructuring of the surface layer, and it is easy to form stone blackening in the subsequent secondary sintering. . For this reason, it is preferable to reduce the amount of volatilizable carbon used in the present invention in a suitable range by one-time sintering. On the other hand, if the hair loss is small or the graphitizable carbon is weak, the above-mentioned melting characteristics are lost. As long as the volatile content is greater than 2.0% by mass, it is easy to form a crystalline structure on the outer surface of easily graphitizable carbon after applying mechanical properties, and form a suitable low-crystalline graphite after secondary sintering. . Accordingly, in the present invention, it is preferable that the volatile amount of the easily-to-tolerate carbon produced by one-time sintering is adjusted within a range from 2.0% by mass to less than 20% by mass. The primary sintering can be performed under any of reduced pressure, normal pressure, or increased pressure. The temperature of primary sintering is usually 300 to 200 ° C, and it is preferably carried out in a temperature range of 350 to 600 ° C. Although it is best to perform in a non-oxidizing environment, heat treatment can also be performed in a partially oxidizing environment. And one sintering can be performed in multiples. The sintering time is not particularly limited, and is about 0.5 to 100 hours. Although the shape of the sintered body subjected to primary sintering is not particularly limited, and may be any of granular, scaly, spherical, needle, and fibrous shapes, it is most suitable to be spherical or ellipsoidal. In a state where only the melted glue is formed after one sintering, various kinds of pulverizers can be used to disintegrate the melted glue. The disintegration method can adopt roller type, impact type, friction type, compression type, stone mortar type, dynamic conflict type, eddy current type, air flow type, shear type and -26- (21) (21) 587350 vibration type Crushers sold in various markets. In the method of the present invention, the primary sintered body obtained by the above-mentioned primary sintering is subjected to a modification treatment by applying a mechanical property amount that does not cause substantial pulverization. Through the modification treatment, a composite graphite material can be obtained after secondary sintering. The structure of the composite graphite material is: forming a graphite B ′ having lower crystallinity than the graphite A outside the highly crystalline graphite A and at least the graphite Graphite C, which is less crystalline than graphite B, is present on the local outer surface of b. In this manufacturing method, it is preferred that the primary sintered body is disintegrated and its shape is adjusted to an approximate finished product, and then mechanical properties are applied. That being said, it is also possible to apply a continuous mechanical energy amount when dissolving a fused colloid formed of a plurality of graphite and easily graphitizable carbon. The mechanical properties referred to in the present invention refer to various stresses such as compression, shearing, collision, and friction. This mechanical property is preferably applied to the outer surface of the easily graphitizable carbon after one sintering. If a general mechanochemical treatment is used to perform this kind of operation, the mechanical properties obtained will be greater than the power given by general stirring. However, at least the particles and aggregates of graphite (graphite A) constituting the primary sintered body should not be substantially damaged. Once excessive damage occurs, the initial charge-discharge rate tends to decrease. Specifically, it is preferable that the decrease rate of the average particle diameter of the primary sintered body due to the application of the mechanical properties is suppressed to 20% or less. The modification treatment can apply mechanical properties to the outer surface of the primary sintered body. Any device is applicable, and there are no restrictions on the structure and type. For example, the device for applying mechanical energy may be a pressure kneader, two kneaders such as -27- (22) (22) 587350 rotors, a rotary ball mill, a HYBRIDIZATION SYSTEM (trade name 'Nara (Produced by Nippon Kogaku Seisakusho), me CHAN 0 MICROS (trade name)

MECHANOFUSION SYSTEM (商品名,H0S0KaWA MICRON GROUP 出品)等。 在上述的裝置中,以利用旋轉速度差並同時賦予剪斷 力與壓縮力者最佳。譬如,於第2圖(a) 、 (b)中顯示 局邰結構之 Η 0 S Ο K A W A MICRON GROUP 出品的 MECHA NOFUSION S Y S TEM便符合上述條件。也就是 說’可採用如第2圖(b )所示之具有轉動滾筒]i、和與 轉動滾筒1】之轉動速度不同的內部構件(內部螺絲) 1 2、及用於一次燒結體]3之循環機構]4與排出機構j 5 的裝置。在該裝置中,如第2圖(a )所示地,改質處理 可藉由對被供應至轉動滾筒】]與內部構件1 2之間的一次 燒結體】3賦予離心力的同時,反覆同步施加導致內部構 件]2與轉動滾筒η產生速度差之壓縮力與剪斷力的方式 進行。 此外、亦可使用如第3圖所示,奈良機械製作所出品 的 HYBRIDIZATION SYSTEM。換言之,改質處理可採用 具有固定滾筒2 1、可高速轉動的轉子22、用於一次燒結 體2 3的循環機構2 4與排出機構2 5、葉片2 6、定子2 7及 夾套2 8的裝置,並利用將一次燒結體2 3供應至固定滾筒 2 ]與轉子22之間,對一次燒結體23施加造成固定滾筒 2 1與轉子2 2產生速度差之壓縮力與剪斷力的方式進行。 -28- (23) 雖然改質處理的條件視採用的裝置而有所不同’無法 一慨而論’但最好將因處理所導致複合石墨材料之平均粒 徑的下降率’設定成抑制在2 0 %以下。舉例來說,當使 用具備轉動滾筒與內部構件的裝置(第2圖)時,最好在 採下述條件來進行,轉動滾筒與內部構件的周邊速度差: 5〜5 0 m / s,兩者間的距離:1〜1 〇 〇 ni m,處理時間:5〜6 0分 鐘。 當使用具備固定滾筒與高轉速轉子的裝置(第3圖) 時’最好在採下述條件來進行,固定滾筒與轉子周邊速度 差:1 0〜1 0 0 m / s,處理時間:3 0秒〜5分鐘。 此外,只要在不損及本發明效果的範圍內,無論在改 質處理前、處理過程中 '或者處理過程後的哪個階段,皆 能摻加各種習知的導電性材料、離子傳導性材料、界面活 性劑、金屬化合物及結合劑等物。 在本發明的方法中,將對經改質處理之一次燒結體 (本案中稱爲改質體)進行二次燒結,直到其中所包含的 易石墨化性碳形成實質的石墨化爲止。 譬如,將改質體放入坩堝中,在非氧化性的環境下執 行二次燒結。利用二次燒結可使易石墨化性碳素形成石墨 化,並產生石墨B及石墨C。雖然二次燒結的溫度並無特 別的限制,但由提高石墨化程度的觀點來看越高越好。最 好是高於〗 5 00°C ’高於2 5 00 °C以上更合適。若由裝置耐 熱性及防止石墨昇華的觀點來看,大約爲3 3 0 0 °C左右, 其中以2 8 00〜3 2 0 0 t最佳。在上述的高溫環境下需加熱 -29- (24) 0.5〜50小時,其中又以加熱2〜2〇小時較佳。經由上述的 處理,可獲得本發明的石墨材料,採用該石墨材料作爲負 極材料,便能製作出放電量大的鋰離子二次電池。 在本發明的方法中,在好在一次燒結處理後,進行可 將二次凝集以上之凝集體加以碎解的碎解處理。在本發明 的二次燒結時,固體之間不會產生熔融膠合及熔融變形。 因此,倘若提供符合最終成品形狀的前述複合體,可簡化 二次燒結後爲了形成所需形狀而進行的粉碎及成形處理。 再者’由於可使利用該處理所形成的表面保持低結晶化, 故能充分達成本發明效果以上的功效。因此,一次燒結後 的碎解,只要在一次燒結後進行的話,任何處理方式皆適 用。舉例來說,亦可於二次燒結後進行。不要使構成石墨 A的石墨產生碎解,只需使大於所需複合石墨材料粒子徑 的二次凝結體產生碎解即可。 1\摩據本發明的方法,可在不變更X光廣角繞射法中 d 0 0 2與Lc的狀態下,增加拉曼光譜中的R値。所獲得的 複合石墨材料,具有核心(由高結晶性之石墨 A所形 成)、及披覆層(由結晶性低於石墨A的石墨B所形 成),並於石墨B的位表面形成結晶性最低的石墨C。由 於石墨A與石墨B皆爲石墨材質,故兩者可於連接界面 形成牢固的緊密結合。特別在複數個石墨A造粒體被石 墨B所披覆的狀態下,因固定效果使得石墨A與石墨B 產生極高的緊密結合性。(再者石墨C是由部分石墨B所 改質形成的,故三者可形成一體化+因此’由於石墨A、 -30- (25) (25)587350 石墨B及石墨C不易產生剝離,並能兼顧石墨A所原本 具有的大放電量、及石墨B所原本具有的高初期充放電效 率,故非常適合作爲鋰離子二次電池的負極材料使用。 雖然本發明之複合石墨材料的R値小於傳統技術的R 値,但具有極佳的初期充放電效率。雖然其結構不容易分 辨’但可藉由僅對易石墨化性碳的外表面施加機械性能量 後形成石墨化的新技術所達成。 在本發明中,提供含有上述任何一種複合石墨材料的 負極材料。 (、本發明的複合石墨材料,可活用其特徵而具有負極以 外的用途,譬如,可當作燃料電池隔板所採用的導電材料 或耐火性石墨等,但最適合作爲上述鋰離子二次電池的負 極材料使用^)。 換言之,本發明之負極材料的基本條件,是至少含有 上述的複合石墨材料。因此,本發明的複合石墨材料,本 身也是本發明的負極材料。此外,本發明的複合石墨材料 與結合劑混合而成的負極合劑、及更進一步添加溶劑而成 的負極合劑膏、及將負極合劑膏塗布於聚電材而成的構 件,都屬於本發明之負極材料的範圍。 接下來’針對採用本發明複合石墨材料作爲負極材料 的鍵離子二次電池的負極、以及該鋰離子二次電池進行說 明。 <鋰離子二次電池用之負極> -31 - (26) 本案中提供一種:採用含有本發明中任何一種複合石 墨材料作爲鋰離子二次電池之負極材料的發明。 本發明的負極,是將上述本發明之負極材料加以固化 及/或塑形而成。雖然該負極的形狀通常是以成形的方式 來製造,但只要能充分發揮石墨的性能,並對粉末賦予極 高的塑形性,進而獲得化學性及電氣性安定的負極時,任 何方法均適用並無特別的限制。 在負極的製造過程中,[可採用在複合石墨材料內添加 結合劑而成的負極合劑/ i而負極合劑,最好採用對電解質 及電解液溶劑具有化學安定性、電氣化學安定性者j。譬 如,可採用聚偏二氯乙烯、四氯乙烯聚合物之類的氟系樹 脂;和聚乙烯、聚氯乙烯醇、苯乙烯-丁二烯橡膠;以及 羧甲基纖維素等。當然同時採用上述各物。 結合劑的使用量,通常以占負極合劑整體之1〜2 0質 量°/。左右的量較爲合適。 負極合劑,具體來說是利用分級將複合石墨材料調整 成適當的粒徑後,藉由與結合劑混合調製成負極合劑,通 常,該負極合劑可塗布於聚電體的其中一面或兩面。塗布 時可使用一般的溶劑,當負極合劑溶解於溶劑內形成膏狀 後,只需將其塗布於聚電體並加以乾燥,便可使負極合劑 平均且堅固地貼著於聚電體並獲得負極。前述的膏狀物, 可利用各種攪拌機進行攪拌調製。 舉例來說,可將本發明的複合石墨材料、及四氯乙烯 聚合物等氟系樹脂粉末,放入異丙醇等溶劑類中加以混 -32- (27) (27)587350 合、揉捏,接著在塗布之後便形成負極合劑層。或者可將 本發明的複合石墨材料、及聚偏二氯乙烯等氟系樹脂粉末 或者羧甲基纖維素等水溶性黏結劑,利用n -甲基吡咯〇定 酮、二甲基甲醯胺或水、酒精之類的溶劑混合成懸浮液 後,進行塗部並形成負極合劑層。 當於聚電體塗布由本發明之複合石墨材料與結合劑混 合而成的負極合劑時,其塗布的厚度以I 〇〜3 00 μηι較爲合 適。 倘右在形成負極合劑後進行衝壓加壓之類的壓著時, 可更進一步提高負極合劑層與聚電體的貼著強度。 在本發明的鋰離子二次電池中,並無特別限制負極所 採用的聚電體形狀,可採用箔狀或者網目、膨脹金屬等網 狀的形狀。而聚電材可採用銅、不鏽鋼、鎳等金屬。當形 成箔狀時,聚電體的厚度以5〜20 μη較爲合適。 在本發明中,更進一步提供採用上述任何一種負極的 鋰離子二次電池。 <鋰離子二次電池> 通常,鋰離子二次電池的主要電池結構爲:負極、正 極及非水系電解質。並分別由正極與負極擔任鋰離子的載 體。該電池結構在充電時,鋰離子將滲入負極內,而放電 時則由負極內脫出。 本發明的鋰離子二次電池,除了採用由含有本發明複 合石墨材料之負極材料所構成的負極之外,並無其他的限 -33- (28) (28)587350 制。其他的構成要件,採用一般鋰離子二次電池的構件即 可。 正極的材料(正極活性物質) ,最好選擇可滲入/脫 出相當份量之鋰離子的材料。舉例來說,上述的正極活性 物質可爲鋰與過渡金屬之複合硫厲化物、或者鋰與過渡金 屬之複合氧化物。 鋰與過渡金屬的複合氧化物(或稱爲含有鋰的過渡金 屬氧化物),以鋰與2種以上的過渡金屬固熔而成者較 佳。具體來說,如L i Μ ( 1 )】.x Μ ( 2 ) X Ο 2 (化學式中:0 S X S 1,Μ ( 1 ) 、Μ ( 2 )至少是由一種過渡金屬所形 成)或者 LiM(l) 2·υΜ(2) γ〇4(化學式中:0SYS1, Μ ( ] ) 、Μ ( 2 )至少是由一種過渡金屬所形成)。 上述的說明中,Μ所表示的過渡金屬可爲 C 〇、N i、 Μη、Cr、Ti、V、Fe、Zn、A卜 In 及 Sn 等金屬。 上述含有鋰的過渡金屬氧化物,譬如可採用 L i、過 渡金屬的氧化物或者鹽類作爲起始原料,並根據起始原料 的組合進彳了混合’在存·有氧氣的環境下以 6 0 0 °C〜]〇 0 0 °C 的溫度範圍進行燒結來獲得。而起始原料並沒有限定氧化 物或鹽類,只要可由氫氧化合物合成即可。 在本發明中,正極活性物質可以單獨使用1種、或混 合上述2種以上使用。舉例來說,可在正極中添加碳酸鋰 之類的碳酸鹽。 藉由上述的正極材料形成正極時,譬如,可將由正極 材料與結合劑、及賦予電極導電性的導電劑所形成的正極 -34- (29) 合劑塗布於聚電體的兩面後形成正極合劑層。而結合劑可 採用製作負極時所列舉的任何一種。導電劑則可採用碳材 料、石墨或碳黑。 聚電體的形狀並無特殊的限制,可採用箔狀或者網 目、膨脹金屬之類的網狀形狀。舉例來說,聚電體可爲鋁 箔、不鏽鋼箔或鎳箔等。其厚度以i 〇〜4〇 μη1較佳。 正極的製造方法與負極相同,先使正極合劑溶解於溶 劑中形成膏狀,再將膏狀的正極合劑塗布於聚電體後,可 藉由乾燥形成正極合劑層,同樣地於形成正極合劑層後, 可藉由衝壓加壓之類的壓著,使正極合劑層平均且堅固地 貼著於聚電體。 在本發明中,在形成上述負極與正極的過程中,可適 當添加傳統上慣用的導電劑或結合劑之類的各種添加劑。 本發明所使用的電解質,可採用由溶劑與電解質鹽所 形成的有機電解質、或由高分子與電解質鹽所形成的聚合 物電解質等。而電解質鹽,可採用如LiPF6、LiBF4、MECHANOFUSION SYSTEM (trade name, produced by H0S0KaWA MICRON GROUP), etc. In the above-mentioned device, it is best to use a difference in rotational speed and simultaneously provide a shearing force and a compressive force. For example, as shown in Figure 2 (a) and (b), Η 0 S 〇 K A W A MICRON GROUP MECHA NOFUSION S Y S TEM meets the above conditions. That is, 'the rotating drum as shown in FIG. 2 (b)] i, and internal components (internal screws) different from the rotating speed of the rotating drum 1] 1 can be used, and 2 can be used for a primary sintered body] 3 Cycle mechanism] 4 and the discharge mechanism j 5 device. In this device, as shown in FIG. 2 (a), the modification process can be performed by applying a centrifugal force to the primary sintered body [3] supplied to the rotating drum]] and the internal member 12] while repeating synchronization. The application of the compression force and the shearing force that causes a speed difference between the internal member 2 and the rotating drum η is performed. Alternatively, as shown in Figure 3, the HYBRIDIZATION SYSTEM manufactured by Nara Machinery Works can also be used. In other words, the modification process can be adopted with a fixed roller 21, a rotor 22 capable of rotating at a high speed, a circulation mechanism 2 4 and a discharge mechanism 2 5 for a primary sintered body 2 3, a blade 2 6, a stator 2 7, and a jacket 2 8 And using a method of supplying the primary sintered body 23 to the fixed drum 2] and the rotor 22, and applying a compressive force and a shearing force to the primary sintered body 23 to cause the speed difference between the fixed drum 21 and the rotor 2 2 get on. -28- (23) Although the conditions for the modification process vary depending on the equipment used, 'It cannot be said', but it is best to set the rate of decrease in the average particle size of the composite graphite material due to the treatment to be suppressed to Less than 20%. For example, when using a device with a rotating drum and internal components (Figure 2), it is best to use the following conditions, the peripheral speed difference between the rotating roller and the internal components: 5 ~ 50 m / s, two Distance between participants: 1 ~ 100m, processing time: 5 ~ 60 minutes. When using a device with a fixed drum and a high-speed rotor (Figure 3), it is best to use the following conditions, the speed difference between the fixed drum and the rotor: 10 ~ 100 m / s, processing time: 3 0 seconds to 5 minutes. In addition, as long as the effect of the present invention is not impaired, various conventional conductive materials, ion conductive materials, or Surfactants, metal compounds and binders. In the method of the present invention, the modified primary sintered body (referred to as a modified body in this case) is subjected to secondary sintering until the easily graphitizable carbon contained therein forms substantially graphitization. For example, the modified body is placed in a crucible, and secondary sintering is performed in a non-oxidizing environment. Using secondary sintering, graphitizable carbon can be graphitized, and graphite B and graphite C are produced. Although the temperature for the secondary sintering is not particularly limited, from the viewpoint of increasing the degree of graphitization, the higher the better. Preferably it is higher than 5 00 ° C, and higher than 2 500 ° C is more suitable. From the viewpoint of device heat resistance and prevention of sublimation of graphite, it is about 3300 ° C, and among them, 2800 to 3200t is the best. In the above-mentioned high-temperature environment, it is necessary to heat -29- (24) for 0.5 to 50 hours, and it is preferable to heat for 2 to 20 hours. Through the above processing, the graphite material of the present invention can be obtained, and by using the graphite material as a negative electrode material, a lithium ion secondary battery with a large discharge capacity can be produced. In the method of the present invention, after the primary sintering treatment, a disintegration treatment capable of disintegrating aggregates having a secondary aggregation or more is performed. During the secondary sintering of the present invention, no melt-glue or melt deformation occurs between the solids. Therefore, if the aforementioned composite body is provided that conforms to the shape of the final product, it is possible to simplify the pulverization and forming process for forming the desired shape after the secondary sintering. In addition, since the surface formed by this treatment can be kept low in crystallization, it is possible to sufficiently achieve the effects of the present invention. Therefore, as long as the disintegration after the primary sintering is performed after the primary sintering, any processing method is applicable. For example, it may be performed after secondary sintering. Instead of disintegrating the graphite constituting graphite A, it is only necessary to disintegrate the secondary agglomerate larger than the particle diameter of the required composite graphite material. According to the method of the present invention, R 値 in the Raman spectrum can be increased without changing the states of d 0 02 and Lc in the X-ray wide-angle diffraction method. The obtained composite graphite material has a core (formed from highly crystalline graphite A) and a coating layer (formed from graphite B having lower crystallinity than graphite A), and forms crystallinity on the surface of the graphite B site Lowest graphite C. Since graphite A and graphite B are both graphite materials, they can form a strong and tight bond at the connection interface. Particularly in a state where a plurality of graphite A granules are covered with graphite B, graphite A and graphite B have extremely high tight bonding due to the fixing effect. (Furthermore, graphite C is formed by the modification of part of graphite B, so the three can be integrated. Therefore, because graphite A, -30- (25) (25) 587350, graphite B and graphite C are not easy to peel off, and It can take into account the large discharge capacity originally possessed by graphite A and the high initial charge and discharge efficiency originally possessed by graphite B, so it is very suitable as a negative electrode material for lithium ion secondary batteries. Although the R 値 of the composite graphite material of the present invention is less than R 値 of traditional technology, but it has excellent initial charge and discharge efficiency. Although its structure is not easy to distinguish ', it can be achieved by new technology of forming graphitization by applying mechanical properties only to the outer surface of easily graphitizable carbon In the present invention, a negative electrode material containing any of the above-mentioned composite graphite materials is provided. (The composite graphite material of the present invention can utilize its characteristics to have uses other than the negative electrode. For example, it can be used as a fuel cell separator A conductive material or refractory graphite, etc., but it is most suitable for use as the negative electrode material of the above lithium ion secondary battery ^). In other words, the basic conditions of the negative electrode material of the present invention are Contains the above-mentioned composite graphite material. Therefore, the composite graphite material of the present invention itself is also the negative electrode material of the present invention. In addition, the negative electrode mixture obtained by mixing the composite graphite material of the present invention with a binder, and further comprising a solvent The negative electrode mixture paste and the member obtained by applying the negative electrode mixture paste to a polymer material belong to the scope of the negative electrode material of the present invention. Next, for the negative electrode of a bond ion secondary battery using the composite graphite material of the present invention as the negative electrode material, And the lithium ion secondary battery will be described. ≪ Negative electrode for lithium ion secondary battery > -31-(26) This case provides a method of using a composite graphite material containing any of the present invention as a lithium ion secondary battery. Invention of the negative electrode material. The negative electrode of the present invention is obtained by curing and / or shaping the above-mentioned negative electrode material of the present invention. Although the shape of the negative electrode is generally manufactured by molding, as long as the performance of graphite is fully utilized, , And give the powder extremely high plasticity, and then obtain a chemically and electrically stable negative electrode, any There are no particular restrictions on the methods used. In the manufacturing process of the negative electrode, [the negative electrode mixture / i can be used by adding a binder in the composite graphite material, and the negative electrode mixture is preferably a chemical stabilizer for the electrolyte and the electrolyte solvent. Those with good electrical and chemical stability j. For example, fluorine-based resins such as polyvinylidene chloride and tetrachloroethylene polymers; polyethylene, polyvinyl chloride, styrene-butadiene rubber; and carboxyl Methylcellulose, etc. Of course, the above are used together. The amount of binder used is usually about 1 to 20% of the mass of the negative electrode mixture. The negative electrode mixture is specifically classified. After the composite graphite material is adjusted to an appropriate particle size, it is mixed with a binder to prepare a negative electrode mixture. Generally, the negative electrode mixture can be applied to one or both sides of a polymer. A common solvent can be used for coating. After the negative electrode mixture is dissolved in the solvent to form a paste, the negative electrode mixture can be evenly and firmly adhered to the polymer body by simply coating it on the polymer and drying it. negative electrode. The aforementioned paste can be prepared by stirring with various mixers. For example, the composite graphite material of the present invention and fluorine-based resin powder such as tetrachloroethylene polymer can be mixed in a solvent such as isopropyl alcohol. -32- (27) (27) 587350 Then, a negative electrode mixture layer is formed after coating. Alternatively, the composite graphite material of the present invention, a fluorine-based resin powder such as polyvinylidene chloride, or a water-soluble binder such as carboxymethyl cellulose may be used with n-methylpyrrolidone, dimethylformamide, or After a solvent such as water and alcohol is mixed to form a suspension, a coating portion is applied to form a negative electrode mixture layer. When the negative electrode mixture obtained by mixing the composite graphite material of the present invention with a binder is applied to a polymer, the thickness of the negative electrode mixture is preferably 100-300 μm. If pressing and the like such as pressing and pressing are performed after the negative electrode mixture is formed, the adhesion strength between the negative electrode mixture layer and the polymer can be further increased. In the lithium ion secondary battery of the present invention, the shape of the polymer used for the negative electrode is not particularly limited, and a foil shape or a mesh shape such as a mesh or an expanded metal may be used. The polyelectric material can use copper, stainless steel, nickel and other metals. When forming a foil, the thickness of the polymer is preferably 5 to 20 μηι. In the present invention, there is further provided a lithium ion secondary battery using any of the foregoing negative electrodes. < Lithium-ion secondary battery > Generally, the main battery structure of a lithium-ion secondary battery is a negative electrode, a positive electrode, and a nonaqueous electrolyte. The positive and negative electrodes serve as lithium ion carriers, respectively. In the battery structure, lithium ions will penetrate into the negative electrode during charging, and will be released from the negative electrode during discharging. The lithium ion secondary battery of the present invention is not limited to a negative electrode made of -33- (28) (28) 587350, except that the negative electrode is composed of a negative electrode material containing the composite graphite material of the present invention. As the other constituent elements, a general lithium-ion secondary battery may be used. As the material of the positive electrode (positive electrode active material), it is preferable to select a material that can infiltrate / extract a considerable amount of lithium ions. For example, the above-mentioned positive electrode active material may be a complex thionide of lithium and a transition metal, or a complex oxide of lithium and a transition metal. A composite oxide of lithium and a transition metal (or a lithium metal-containing transition metal oxide) is preferably formed by solid-melting lithium with two or more transition metals. Specifically, for example, L i Μ (1)]. X Μ (2) X Ο 2 (in the chemical formula: 0 SXS 1, M (1), M (2) is formed of at least one transition metal) or LiM ( l) 2 · υM (2) γ〇4 (in the chemical formula: 0SYS1, M (]), M (2) is formed of at least one transition metal). In the above description, the transition metal represented by M may be metals such as C0, Ni, Mn, Cr, Ti, V, Fe, Zn, Al, In, and Sn. The lithium-containing transition metal oxides, for example, may use Li, transition metal oxides, or salts as starting materials, and may be mixed according to the combination of starting materials. 0 0 ° C ~] 〇0 0 ° C is obtained by sintering. The starting materials are not limited to oxides or salts, as long as they can be synthesized from hydroxides. In the present invention, the positive electrode active material may be used singly or in combination of two or more kinds. For example, a carbonate such as lithium carbonate may be added to the positive electrode. When a positive electrode is formed from the above-mentioned positive electrode material, for example, a positive electrode -34- (29) mixture formed of a positive electrode material and a binding agent and a conductive agent that imparts conductivity to the electrode can be applied to both surfaces of a polymer to form a positive electrode mixture. Floor. The binding agent may be any of those listed in the production of the negative electrode. The conductive agent can be carbon material, graphite or carbon black. The shape of the polymer is not particularly limited, and a foil shape or a mesh shape such as a mesh or an expanded metal may be used. For example, the polymer may be an aluminum foil, a stainless steel foil, a nickel foil, or the like. Its thickness is preferably i 0 to 40 μη1. The manufacturing method of the positive electrode is the same as that of the negative electrode. First, the positive electrode mixture is dissolved in a solvent to form a paste, and then the paste-like positive electrode mixture is applied to a polymer, and then the positive electrode mixture layer can be formed by drying. Similarly, the positive electrode mixture layer is formed. Thereafter, the positive electrode mixture layer can be evenly and firmly adhered to the polymer by pressing such as pressing. In the present invention, in the process of forming the above-mentioned negative electrode and positive electrode, various additives such as a conventionally used conductive agent or a binding agent may be appropriately added. The electrolyte used in the present invention may be an organic electrolyte formed of a solvent and an electrolyte salt, or a polymer electrolyte formed of a polymer and an electrolyte salt. For electrolyte salts, such as LiPF6, LiBF4,

LiAsF6 、LiC104 、LiB ( C6H5 ) 、LiC】、LiBr、LiAsF6, LiC104, LiB (C6H5), LiC], LiBr,

LiCF3S03、LiCH3、S〇3、LiN ( CF3S〇2 ) 2、LiCF3S03, LiCH3, S〇3, LiN (CF3S〇2) 2.

LiN ( CF3SO2 ) 3、LiN ( CF3CH2〇S〇2 ) 2、LiN (CF3SO2) 3, LiN (CF3CH2〇S〇2) 2,

LiN ( CF3CF2OSO2) 2 > LiN ( HCF2CF2CH2OSO2 ) 2 'LiN (CF3CF2OSO2) 2 > LiN (HCF2CF2CH2OSO2) 2 '

LiN ( ( CF3 ) 2CHOSO2 ) 、LiB[C6H3 ( CF3) 2]4、LiN ((CF3) 2CHOSO2), LiB [C6H3 (CF3) 2] 4,

LiA]Cl4、LiSiF6等。其中,由於LiPF6、LiBF4的氧化安 疋性佳5故最爲合適。 有機系電解質中的電解質鹽濃度,以〇.]〜5 mol/L較 -35· (30) (30)587350 佳,其中又以0.5〜3.0 mol/L更合適。 有機系電解質的溶劑,可採用碳酸乙烯酯;碳酸丙烯 酯;二甲基碳酸酯;二乙基碳酸酯;乙基甲基碳酸酯; 1、1-或2、二甲氧基乙烷;1、2 -乙二醇乙醚、四氫夫 喃;C 6 Η ] 2 〇 ( 2 - M e t h y ] t e t r a h y d r 〇 p y r a η ) ; C 4 H 6 〇 2 ( 7 -LiA] Cl4, LiSiF6, etc. Among them, LiPF6 and LiBF4 are most suitable because of their good oxidation stability5. The concentration of the electrolyte salt in the organic electrolyte is preferably from 0.5 to 5 mol / L rather than -35 · (30) (30) 587350, among which 0.5 to 3.0 mol / L is more suitable. Solvents for organic electrolytes include ethylene carbonate; propylene carbonate; dimethyl carbonate; diethyl carbonate; ethyl methyl carbonate; 1, 1 or 2; dimethoxyethane; 1 , 2-ethylene glycol ether, tetrahydrofuran; C 6 Η] 2 〇 (2-Methy] tetrahydr 〇pyra η); C 4 H 6 〇2 (7-

Butyrola clone ) ; C3H6O2 ( 1,3-Dioxolane ) ; C 4 H 6 〇 3 (Propylene Carbonate );苯甲醚;二乙醚;環丁; C8H】8〇4S2 ( Methylsulfona]);乙騰;氯睛;丙酸膳,二 甲基硼酸;Si (OCH3) 4 (Tetramethyl Orthosilicate); 硝基甲烷;二甲基甲醯胺;N -甲基吡咯啶酮;乙酸乙酯; 三甲基正甲酸酯;硝基苯;過氧苯醯;溴化甲苯基;四氫 吩;二甲亞砸;乙二醇;3-Methy卜2-OxazoIidone ;甲硫 醚等非質子性有機溶劑。 當使用非水電解質作爲聚合物電解質時,含有利用可 塑劑(非水電解液)形成膠化的基體高分子,該基體高分 子可以單獨或混合使用聚氧化乙烯及其架橋體之類的醚系 高分子;聚酯系;聚丙烯酸酯系;聚偏二氟乙烯及聚偏二 藏乙細Hi丙傭共重合體之類的氯系局分子。 根據氧化還原安定性的觀點,上述列舉的高分子中以 聚偏二氟乙烯及聚偏二氟乙烯-六氟丙烯共重合體之類的 氟系高分子最佳。Butyrola clone); C3H6O2 (1,3-Dioxolane); C 4 H 6 〇3 (Propylene Carbonate); anisole; diethyl ether; cyclobutane; C8H] 8〇4S2 (Methylsulfona)); ethidium; Propionic acid diet, dimethyl boric acid; Si (OCH3) 4 (Tetramethyl Orthosilicate); nitromethane; dimethylformamide; N-methylpyrrolidone; ethyl acetate; trimethyl n-formate; Nitrobenzene; peroxyphenylhydrazone; tolyl bromide; tetrahydrophene; dimethylene; ethylene glycol; 3-Methy bu 2-OxazoIidone; aprotic organic solvents such as methyl sulfide. When a non-aqueous electrolyte is used as the polymer electrolyte, it contains a matrix polymer that is gelled by using a plasticizer (non-aqueous electrolyte). The matrix polymer can be used alone or in combination with ethers such as polyethylene oxide and its bridging body. Macromolecules; polyesters; polyacrylates; chlorine-based local molecules such as polyvinylidene fluoride and polyvinylidene-zirconium hi-propene co-coincidences. From the viewpoint of redox stability, the above-listed polymers are preferably fluorine-based polymers such as polyvinylidene fluoride and polyvinylidene fluoride-hexafluoropropylene copolymers.

而構成含於聚合物電解質內之可塑劑的電解質鹽及溶 劑,可採用前述的任何一種。電解液中的電解質(可塑 劑)濃度,以0 . 1〜5 m ο 1 / L較佳,其中又以〇 . 5〜2.0 m 0 1 / L -36- (31) 最佳。 -t述聚合物電解質的製作方法並無特別的限制,舉例 來p兌’可將形成基體的高分子化合物、鋰鹽與溶劑混和後 加熱裕解之類的方法。此外,亦可採用使高分子化合物、 錐鹽及溶劑溶解於適量的混合用有機溶劑後,再使混合用 有機裕劑蒸發的方法。或者將單分子、鋰鹽及溶劑混合, 利用紫外線、電子射線或者分子射線對其照射後形成聚合 物的方法。 而’聚合物電解質中之溶劑的添加比例,以]〇〜9〇質 量%較佳,其中又以3〇〜8〇質量%最合適。當上述的添加 比例爲10〜90質量%時,導電率高、且機械強度高並容易 形成薄膜化。 仕本發明的鋰離子二次電池中,也能採用隔板。 而該隔板也無特別的限制。可採用如織布、不織布及 合成樹脂製成的微細多孔膜。其中又以合成樹脂製成的微 細多孔膜最合適。而合成樹脂製微細多孔膜中,以聚烯烴 系微細多孔膜的厚度、膜強度及膜磨擦面最佳。具體來 說’可採用聚乙烯及聚丙烯製成的微細多孔膜,或前述二 者的複合微細多孔膜。 在本發明的鋰離子二次電池中,由於初期放電率高的 緣故’可採用聚合物電解質。 使用聚合物電解質的鋰離子二次電池,通常稱爲聚合 物I電 '池。其結構可由含有本發明複合石墨材料的負極、正 極及聚合物電解質所構成。舉例來說,可按照負極、聚合 -37- (32) (32)587350 物電解質、正極的順序堆疊,並收容於電池外包材內的方 式製成。除此之外,也能在負極與正極的外側配設聚合物 電解質。在使用本發明複合石墨材料作爲負極的聚合物電 池中,可於聚合物電解質中含有碳酸丙烯酯。一般來說, 雖然碳酸丙烯酯對石墨具有激烈的電氣分解反應,但對本 發明之複合石墨材料的分解反應性極低。 此外,本發明之鋰離子二次電池的結構可爲任意的結 橇,其形狀及形態也無特別的限制。可選用圓筒型、方 型、錢幣型、鈕扣型中的任何一種。爲了能製作出安全性 更高的密閉型非水電解液電池,可配置能於發生過量充電 等異常時偵測出電池內壓力上升,並切斷電流的手段。在 採用聚合物電解質製作聚合物電池時,可採用封入堆疊薄 膜的結構。 實施例 接下來’具體地說明本發明的實施例,但本發明並不 侷限於下述的實施例。此外,在後述的實施例及比較例 中’是採用複合石墨材料製作成第]圖中所示之評估用鈕 扣型一次電池來進行評估。而該電池是根據本案的技術思 想’並依一般的製作方法所製得。在該評估用電池中,作 用極係指負極’而對極則相當於正極。 <負極合劑膏的調製> 對應於複合石墨材料9〇質量%,採用]〇質量%的聚 -38- (33) (33)587350 偏二氟乙烯作爲結合劑,並使用N -甲基吡咯啶酮作爲溶 劑進行混和,接著採用乳化混合裝置以2000 RPM攪拌3 0 分鐘後,調製成有機溶劑系負極合劑膏。 <負極的製作> 先將上述負極合劑膏在銅箔(聚電材)上塗布一致的 厚度’再於真空環境下加熱至90 °C使溶劑揮發後乾燥。 接著利用滾子衝壓機對塗布於銅箔上的負極合劑加壓,藉 由與銅箔一起衝製作成直徑1 5 . 5 m m的圓筒形,可製作出 緊密附著於銅箔(聚電體7b )的負極合劑層(負極2 )。 <正極的製作> 將鋰金屬箔按壓於鎳的網狀箔後,衝製成直徑 1 5 · 5 mm的圓柱狀,可獲得由鎳的網狀箔所形成的聚電體 7 a、與緊密附著於該劇電體之鋰金屬箔所形成的正極4。 <電解質> 使L i P F 6溶解於由3 3 v 〇】%的碳酸乙烯指與6 7 v 〇 ] % 的乙基甲基碳酸酯所構成的混合溶劑中形成1 mol/dm3的 濃度後,調製成非水電解液。使所製得的非水電解液浸染 入聚丙烯多孔體內,形成浸染有電解液的隔板5。 <評估用電池的製作> 評估用電池,是製作成具有第1圖所示之結構的鈕扣 -39- (34)587350 型二次電池。 首先,將浸染有電解液的隔板5放入緊密附著於聚電 體7 b的負極2、與緊密附著於聚電體7 a的正極4之間形 成包夾並進行層合。接著,將負極聚電體7b側放入外杯 1內,並將正極聚電體7 a側放入外罐3內後,將外杯] 及外罐3裝配組合。此時,使絕緣襯墊6夾介於外杯1與 外罐3的周緣部,進而封閉兩個外緣部形成密閉。 而根據上述方式所製得的評估用電池,是在2 5 t的 環境下完成下述的充放電實驗。 <充放電實驗> 以 0.9mA的電流進行定量電流充電,直到迴路電壓 達到OmV爲止。接著,當迴路電壓達到OmV時切換成定 量電壓充電,直到電流値達到2 Ομ A爲止。完成上述充電 後,暫停]2 0分鐘。 接下來,以 〇 . 9mA的電流進行定量電流放電,直到 迴路電壓達到2.5 V爲止。爲了由第]循環中的通電量求 出充電量與放電量,乃根據以下的計算式來計算出初期充 放電效率。 初期充放電效率(% (第1循環的放電量) (第]循環的充電量) 在上述的實驗中,充電是指鋰離子滲入複合石墨材料 內的過程,而放電則是鋰離子由複合石墨材料脫出的過 -40- (35)587350 程。 相當於 ]g 測定用複合石墨材料的放電量 (mAh/g )、與初期充放電效率(% )等電池的特性係如 表2所示。 如表2所示地,使用本發明複合石墨材料作爲負極的 鋰離子二次電池,具有大放電量,且初期充放電效率高。 接下來,第2循環則是在進行與第1循環相同的充電 後,利用]8mA的電流進行定量電流放電,直到迴路電壓 達到2.5 V爲止。此時,根據第1循環中的放電量與第2 循環中的放電量,按照下列計算式來評估急速放電效率。 急速放電效率(% ) (第2循環的放電量) (第1循環的放電量) 此外,採用與第1循環相同的條件重複充放電 20 次,來進行與前述實驗不同的實驗,並按照下列的計算是 來評估循環特性。 · 循環特性(% ) (第20循環的放電量) (第20循環的充電量) 上述的實驗是在負極之電極密度爲].6 g/cm2與】.8 g/cm2的條件下,分別採用評估電池所進行。 (實施例1 ) <複合石墨材料的調製> -41 - (36) 溶解80質量單位、且內含約40質量%揮發量的煤焦 油(川崎製鐵(股)生產,品名爲PK-QL ),並於其中添 加 5 0質量單位的天然石墨(中越石墨工業所(股)生 產,品名爲B F 5 A,平均粒徑爲5 μ】η ),以加熱揉合機進 行揉合。 ¥寸所得的附著體施以粗粉碎加工形成碎解後,於非氧 化性的環境中進行一次燒結,可獲得具有下列特性的一次 燒結體。原料與一次燒結體的特性,以及是否經改質處理 等’全數彙整如表I所示。 此外,對煤焦油施以一次燒結形成之易石墨化性碳的 部分,其軟化點(梅特勒法)爲4 4 5 t。 在所獲得的一次燒結體中,含有5 0質量單位之經一 次燒結的煤焦油、與5 0質量單位的天然石墨。 利用渦流式粉碎機來碎解上述的一次燒結體,將其製 成調製成平均粒徑爲20 的塊狀粒子。將該塊狀粒子投 入第 2 圖(a) 、 (b)所示的改質處理裝置 ( HOSOKA WA MICRON GROUP 出 品 的 MECHANOFUSION SYSTEM ),施以機械性能量。此時, 在轉動滾筒的周速度爲2 0 m / s、處理時間爲]〇分鐘、及 轉動滾筒與內部構件之間的距離爲5mm的條件下,重覆 施以壓縮力及剪斷力。而改質處理後之一次燒結物的平均 1 9 μ m。 接下來,將該値處理後的一次燒結體放入石墨坩堝 中,並於坩堝周圍充塡焦碳粉後以3 000 t加熱5個小 -42 - (37) (37)587350 時,可獲得二次燒結後的複合石墨材料。所獲得的複合石 墨材料內不會產生融著及變形,可保持其粒子的形狀。接 著’使用前述複合石墨材料製作評估用電池,並對電池特 丨生進仃δΐ估。所測得的結晶性與相當於1 g複合石墨材料 的放電量(mAh/g )、初期充放電效率(% )及急速放電 效率(% )等値如表2所示。 如表2所示地,實施例]的複合石墨材料(本發明的 範例),其放電量大於比較例1之不含天然石墨且未經改 質處理的材料,且初期充放電效率更高。再者,相較於含 有天然石墨卻未經改質處理的比較例2,具有更好的初期 充放電效率、急速放電效率及循環特性。此外,經該改質 處理之實施例1的複合石墨材料表面,可形成低結晶化。 (實施例2 ) <石墨造粒物的調製> 使用天然石墨(中越石墨工業所(股)生產的 HG3 0A,平均例徑爲30 μηι )進行造粒,可獲得緊緻的球 狀或橢圓體狀的石墨造粒物。該石墨造粒物’其平均粒徑 爲2 0 μ m,長寬比爲].8,根據X廣角銳射法所測得的 d 〇 〇 2 = 0.3355 nm、L c = 86nm 〇 對所製成的石墨造粒體表面進行硏磨’當使用掃描型 電子顯微鏡測量粒子內的空隙率(面積率)時’約爲15 體積% 。 -43- (38) <石墨與易石墨化性碳之複合體的調製> 將42質量單位、且內含約40質量%揮發量的煤焦油 (川崎製鐵(股)生產,品名爲PK-QL )溶解於58質量 單位的中焦油內形成溶液,並預先準備1 〇 〇質量單位的該 溶液。 將1 0 0質量單位之先前製得的石墨造粒體、與上述 ]〇〇質量單位的溶液一起複入攪拌機內,以150°C攪拌30 分鐘後將該石墨造粒體浸染於該煤焦油溶液內,接著在 ]0 m m H g的壓力下,以相同的溫度過濾掉作爲溶劑的中焦 油。 將製成的石墨造粒體的瀝青附著體充塡入鋼鐵製容器 內。在具備可燃燒處理揮發氣體之裝置的燒結爐內,在流 通著鈍氣的狀態下,以4 5 0 °C對該附著體進行20分鐘的 一次燒結。該燒結體僅在石墨造粒體表面的易石墨化性碳 之間形成熔融附著的狀態。 採用衝擊式粉碎機碎解一次燒結體。碎解所得的一次 燒結體,其平均粒徑爲22 μηι,長寬比爲1 .7。 <改質處理> 接下來,將一次燒結體投入第2圖(a ) 、 ( b )所示 的改質處理裝置(HOSOKAWA MICRON GROUP出品的 MECHANOFUSION SYSTEM)內,賦予機械性能量。也就 是在:轉動滾筒周速度2 0 m / s、處理時間3 0分鐘、轉動 滾筒與內部構件保持5mm距離的條件下,重複施加壓縮 -44 - (39) (39)587350 力與剪斷力。改質處理後之一次燒結體的平均例子徑爲 2 2 μηα、長寬比爲1 · 7,相較於改質處理前的平均例子徑 與長寬比,並未產生變化。 <複合石墨材料的製造> 接下來’將所製成的改質處理體充塡入石墨坩鍋內, 並在石墨堪·堝的周圍充塡焦油粉後以3 000。(:加熱5個小 時形成石墨化’最後製成複合石墨材料。經確認後,複合 石墨材料內並未產生熔融附著及變形,可保持原有的粒子 形狀。複合石墨材料的平均粒徑爲2 2 μ m、長寬比爲1 · 7、 比表面積爲〇·5 m**/g、體密度爲1.02 g/cm。。根據X廣角 瞒射法所測得的fe晶性d 〇 〇 2 = 〇 · 3 3 5 7 n m、L c = 8 8 n m,根 據拉曼分光法所測得的R値爲〇. 〇 8。第4圖中,便是顯 示所製成之複合石墨材料的掃描型電子顯微鏡相片。 採用該複合石墨材料來製作評估用電池的負極,並將 其電池特性的評估結果彙整於表2。 (實施例3〜5 ) 預先在實施例2所採用之]00質量單位的煤焦油中, 添加〇 . 5質量單位之利用氣相法製成的無水氧化矽粉末 (日本AEROSIL (股)生產之「AEROSIL300」,平均粒 徑爲0 · )後進行一次燒結,並採用變更揮發量後的易 石墨化性碳。其他的條件,則採用與實施例2相同的條件 來製造複合石墨化材料。可於一次燒結後的碎解過程中, -45- (40) (40)587350 減輕粉碎機的負荷輕易形成碎解。對所製成的複合石墨材 料進行各種評估,其結晶性及電池特性彙整於表2。 如表2所示地,使用實施例2〜5之複合石墨材料的評 估用電池,具有趨近於石墨理論容量(3 72 mAh/g )的 大放電量,更具有極高的初期充放電效率。其中,在易石 墨化性碳中添加利用氣相法製成之無水氧化矽粉末的實施 例 3〜5,更具有極佳的初期充放電效率。具有可抑制「導 致熔融附著後易石墨化性碳容易產生碎解之易石墨化性碳 披膜剝離」的效果。此外,也具有極佳的急速放電效率與 循環特性。即使在設成高電極密度的狀態下,同樣具有極 佳的急速放電效率與循環特性。 (比較例1 ) 除了不在與實施例1相同的易石墨化性碳中添加天然 石墨’且不執行改質處理之外,採用與實施例]相同的條 件來製作石墨材料。 所製成的石墨材料,其石墨材料間將於二次燒結後形 成熔融附著,且無法保持一次燒結後所碎解而成的形狀。 因此,必須再次對熔融附著後的石墨材料進行碎解,將其 平均粒徑調整爲1 9 μη]後製作成評估用電池。其結晶性與 電 '池特性的評估結果如表2所示。 如表2所示地,採用不含天然石墨且未經改質處理之 石墨材料的比較例1,其放電量及初期充放電效率顯著地 下降。 -46 - (41) (41)587350 (比較例2 ) 除了省略實施例1中的改質處理之外,採用與實施例 ]相同的方式來製作石墨材料。所製得的石墨材料,經二 次燒結後石墨材料之間產生些微的熔融附著,且無法保持 一次燒結後碎解而成的形狀。因此,必須再次對熔融附著 後的石墨材料進行碎解,將其平均粒徑調整爲1 9 μηι後製 作成評估用電池。其結晶性與電池特性的評估結果如表2 所示。 如表2所示地,未經本發明特徵之改質處理的比較例 2 ’其石墨表面不會形成低結晶化,且初期充放電效率也 顯著地下降。 (比較例3 ) 除了將實施例1中的二次燒結溫度改爲! 3 〇 〇它之 外’採用與實施例1相同的方法製作石墨材料。所製成的 石墨材料’相當於傳統的製品,在非石墨質材料中含有天 然石墨。此外,所製成的材料中並未發現熔融附著現象, 其粉碎後的形狀可獲得保持。以該石墨材料採用與實施例 1相同的方式來製作評估用電池。其結晶性與電池特性的 S平估結果如表2所示。 如表2所示地,在降低二次燒結溫度,導致易石墨化 性碳無法充分石墨化的比較例3中,材料的結晶性低,且 放電量也顯著地下降。 -47- (42) (42)587350 (比較例4 ) 適用實施例1之改質處理的條件’直接對天然石墨 (中越石墨工業所(股)生產’品名爲BF] 0A ’平均粒徑 爲1 0 μηι )進行改質處理。改質處理後的石墨內並未發現 熔融附著及變形’其粉碎後的形狀可獲得保持。其平均粒 子徑爲9μη:ι。接著,採用該天然石墨製作與實施例1相同 的評估用電池,並評估其電池特性。其結晶性與電池特性 如表2所示。 如表2所示地,嘗試直接對天然石墨進行改質處理’ 以降低表面結晶性的必較例4 ’其初期充放電效率低。而 其急速放電效率與循環特性不彰。一旦提高電極密度將使 石墨粒子產生定向,導致上述特性再度下降。 (比較例5 ) 直接採用天然石墨(中越石墨工業所(股)生產,品 名爲B F ] 0 A,平均粒徑爲I 〇 μηι )來製作評估用電池。評 估電池的製作方法與評估方法採用與實施例1相同的方 式。其結晶性與電池特性的評估結果如表2所示。 如表2所示地,單獨使用天然石墨的比較例5,雖然 其放電Μ大,但初期充放電效率、急速放電效率及循環特 性不彰。倘若提高其電極密度,將導致上述特性明顯下 降。 -48- (43) (43)587350 (比較例6) 除了省略實施例2中的改質處理之外,採用與實施例 2相同的方式來製作石墨材料。其結晶性與電池特性的評 估結果如表2所示。 如表2所示地,未經改質處理來製成石墨材料的比較 例6,其初期充放電效率低。此外,相較於比較例6,可 得知實施例2的R値較大,並可選擇性地在石墨材料的表 面形成低結晶化。As the electrolyte salt and the solvent constituting the plasticizer contained in the polymer electrolyte, any of the foregoing may be used. The concentration of the electrolyte (plasticizer) in the electrolytic solution is preferably from 0.1 to 5 m ο 1 / L, and the most preferably 0.5 to 2.0 m 0 1 / L -36- (31). The method for preparing the polymer electrolyte is not particularly limited. For example, in the p-d 'method, a matrix-forming polymer compound, a lithium salt, and a solvent may be mixed and then heated to decompose. Alternatively, a method in which a polymer compound, a cone salt and a solvent are dissolved in an appropriate amount of an organic solvent for mixing, and then the organic solvent for mixing is evaporated. Alternatively, a method in which a single molecule, a lithium salt, and a solvent are mixed and irradiated with ultraviolet rays, electron rays, or molecular rays to form a polymer. The addition ratio of the solvent in the 'polymer electrolyte is preferably from 0 to 90% by mass, and the most suitable is 30 to 80% by mass. When the above-mentioned addition ratio is 10 to 90% by mass, the electrical conductivity is high, the mechanical strength is high, and it is easy to form a thin film. In the lithium ion secondary battery of the present invention, a separator can also be used. The separator is not particularly limited. Fine porous membranes such as woven, non-woven, and synthetic resins can be used. Among them, a microporous membrane made of synthetic resin is most suitable. Among the microporous membranes made of synthetic resin, the thickness, membrane strength, and film friction surface of polyolefin-based microporous membranes are the best. Specifically, 'a fine porous film made of polyethylene and polypropylene, or a composite fine porous film of the two may be used. In the lithium ion secondary battery of the present invention, a polymer electrolyte can be used because of its high initial discharge rate. A lithium ion secondary battery using a polymer electrolyte is commonly referred to as a polymer I battery. Its structure can be composed of a negative electrode, a positive electrode, and a polymer electrolyte containing the composite graphite material of the present invention. For example, it can be made by stacking the negative electrode, polymer electrolyte -37- (32) (32) 587350, and the positive electrode in the order of being stored in the battery outer cover. In addition, a polymer electrolyte can also be provided outside the negative electrode and the positive electrode. In a polymer battery using the composite graphite material of the present invention as a negative electrode, propylene carbonate may be contained in the polymer electrolyte. In general, although propylene carbonate has an intense electrical decomposition reaction to graphite, it has extremely low decomposition reactivity to the composite graphite material of the present invention. In addition, the structure of the lithium ion secondary battery of the present invention may be any structure, and its shape and form are not particularly limited. Any of cylindrical, square, coin, and button types can be selected. In order to make a sealed non-aqueous electrolyte battery with higher safety, a means can be provided to detect an increase in the internal pressure of the battery and cut off the current when an abnormality such as overcharging occurs. When a polymer battery is manufactured using a polymer electrolyte, a structure in which a stacked film is enclosed may be adopted. Examples Next, examples of the present invention will be specifically described, but the present invention is not limited to the following examples. In the examples and comparative examples described later, the evaluation was performed by using a composite graphite material to produce a button-type primary battery for evaluation as shown in FIG. The battery is manufactured according to the technical idea of the present case and according to a general manufacturing method. In this evaluation battery, the working electrode refers to the negative electrode 'and the counter electrode corresponds to the positive electrode. < Preparation of negative electrode mixture paste > Corresponding to 90% by mass of the composite graphite material, poly-38- (33) (33) 587350 vinylidene fluoride was used as a binding agent, and N-methyl was used as a binder. The pyrrolidone was mixed as a solvent, followed by stirring at 2000 RPM for 30 minutes using an emulsifying mixing device, and then preparing an organic solvent-based negative electrode mixture paste. < Production of negative electrode > The above negative electrode mixture paste was first coated on a copper foil (polyelectric material) to a uniform thickness', and then heated to 90 ° C in a vacuum environment to evaporate the solvent and dry. Next, the negative electrode mixture coated on the copper foil is pressed by a roller press, and punched together with the copper foil to form a cylindrical shape having a diameter of 15.5 mm, and a copper foil (polyelectric body) that is closely adhered to the copper foil can be produced. 7b) of the negative electrode mixture layer (negative electrode 2). < Production of positive electrode > After pressing a lithium metal foil onto a nickel mesh foil, punching it into a cylindrical shape having a diameter of 15 mm, a polymer body formed of the nickel mesh foil 7 a, And a positive electrode 4 formed of a lithium metal foil tightly adhered to the electric body. < Electrolyte > Li PF 6 was dissolved in a mixed solvent composed of 3 3 v 〇]% of ethylene carbonate fingers and 67 v 〇]% of ethyl methyl carbonate to a concentration of 1 mol / dm3 Then, a non-aqueous electrolyte was prepared. The prepared non-aqueous electrolytic solution was impregnated into a polypropylene porous body to form a separator 5 impregnated with the electrolytic solution. < Production of evaluation battery > The evaluation battery was fabricated as a button-39- (34) 587350 secondary battery having a structure shown in FIG. 1. First, a separator 5 impregnated with an electrolytic solution is placed between the negative electrode 2 closely adhered to the polymer 7 b and the positive electrode 4 tightly adhered to the polymer 7 a to form a sandwich and laminate. Next, the side of the negative electrode collector 7b is placed in the outer cup 1, and the side of the positive electrode collector 7a is placed in the outer tank 3. Then, the outer cup] and the outer tank 3 are assembled. At this time, the insulating gasket 6 is sandwiched between the peripheral portions of the outer cup 1 and the outer tank 3, and the two outer edge portions are closed to form a hermetic seal. On the other hand, the evaluation battery prepared according to the above-mentioned method was subjected to the following charge-discharge experiment under an environment of 2 5 t. < Charge-discharge experiment > A quantitative current was charged at a current of 0.9 mA until the loop voltage reached 0 mV. Then, when the loop voltage reaches OmV, it switches to a fixed voltage and charges until the current 値 reaches 2 0 μA. After completing the above charging, pause] for 20 minutes. Next, perform a quantitative current discharge with a current of 0.9 mA until the loop voltage reaches 2.5 V. In order to obtain the charge and discharge amounts from the energized amount in the 1st cycle, the initial charge and discharge efficiency was calculated according to the following calculation formula. Initial charge and discharge efficiency (% (discharge amount in the first cycle) (charge amount in the first cycle) In the above experiment, charging refers to the process of lithium ions infiltrating into the composite graphite material, while discharging is the lithium ion from the composite graphite The material release process is -40- (35) 587350. It is equivalent to the characteristics of the battery, such as the discharge capacity (mAh / g) and initial charge and discharge efficiency (%) of the composite graphite material for measurement, as shown in Table 2. As shown in Table 2, the lithium ion secondary battery using the composite graphite material of the present invention as a negative electrode has a large discharge capacity and high initial charge and discharge efficiency. Next, the second cycle is the same as the first cycle After charging, use a current of 8 mA to perform a quantitative current discharge until the loop voltage reaches 2.5 V. At this time, based on the amount of discharge in the first cycle and the amount of discharge in the second cycle, use the following calculation formula to evaluate the rapid discharge Efficiency: Rapid discharge efficiency (%) (discharge amount in the second cycle) (discharge amount in the first cycle) In addition, the same conditions as in the first cycle were used to repeat the charge and discharge 20 times to perform experiments different from the previous experiments, and according to The following calculations are used to evaluate the cycle characteristics: · Cycle characteristics (%) (discharge amount at the 20th cycle) (charge amount at the 20th cycle) The above experiment was performed at the negative electrode electrode density]. 6 g / cm2 and []. (Embodiment 1) < Preparation of composite graphite material > -41-(36) Dissolving 80 mass units and containing about 40 mass% volatile content Coal tar (produced by Kawasaki Iron & Steel Co., Ltd. under the trade name PK-QL), and added with 50 mass units of natural graphite (produced by China-Vietnam Graphite Institute (Shares) under the trade name of BF 5 A, with an average particle size of 5 μ] η), and kneaded with a heating kneader. After the coarsely crushed attachments are obtained to form a disintegrated body, the primary adhered body is sintered in a non-oxidizing environment to obtain a primary sintered body having the following characteristics. The characteristics of the raw material and the primary sintered body, and whether or not they have been modified, are shown in Table I. In addition, the softening point (met Lefa) is 4 4 5 t. Once obtained The sintered body contains 50 mass units of primary sintered coal tar and 50 mass units of natural graphite. The above-mentioned primary sintered body was disintegrated by a vortex mill, and the average particle size was adjusted to be 20 pieces of particles. Put the pieces of particles into the modification processing device (MECHANOFUSION SYSTEM by HOSOKA WA MICRON GROUP) shown in Figure 2 (a) and (b), and apply mechanical energy. At this time, at Under the conditions that the peripheral speed of the rotating drum is 20 m / s, the processing time is 0 minutes, and the distance between the rotating drum and the internal components is 5 mm, compressive force and shearing force are repeatedly applied. The average of the primary sintered product after the modification treatment was 19 μm. Next, the primary sintered body treated with this plutonium was placed in a graphite crucible, and then filled with coke powder around the crucible, and heated for 5 small -42-(37) (37) 587350 at 3 000 t. Composite graphite material after secondary sintering. The obtained composite graphite material does not cause fusion and deformation, and can maintain the shape of its particles. Next, a battery for evaluation was produced using the aforementioned composite graphite material, and the battery characteristics were evaluated. The measured crystallinity and discharge capacity (mAh / g) equivalent to 1 g of the composite graphite material, initial charge and discharge efficiency (%), and rapid discharge efficiency (%) are shown in Table 2. As shown in Table 2, the composite graphite material according to the embodiment (an example of the present invention) has a higher discharge capacity than the material without the natural graphite and no modification treatment of Comparative Example 1, and has a higher initial charge and discharge efficiency. Furthermore, it has better initial charge and discharge efficiency, rapid discharge efficiency, and cycle characteristics than Comparative Example 2 containing natural graphite without modification. In addition, the surface of the composite graphite material of Example 1 subjected to the modification treatment can be formed with low crystallinity. (Example 2) < Preparation of graphite granules > Granulation was performed using natural graphite (HG3 0A produced by Sino-Vietnam Graphite Industry Co., Ltd., with an average diameter of 30 μm) to obtain a compact spherical shape or Spheroidal graphite granules. The graphite granules' had an average particle diameter of 20 μm and an aspect ratio of [.8]. D 〇〇2 = 0.3355 nm, L c = 86nm measured according to the X wide-angle acute method. The surface of the graphite granules formed was honed 'when the porosity (area ratio) in the particles was measured using a scanning electron microscope' was about 15% by volume. -43- (38) < Preparation of a complex of graphite and easily graphitizable carbon > Coal tar (manufactured by Kawasaki Iron & Steel Co., Ltd.) with a mass of 42 mass units and a content of about 40 mass% of volatile matter is produced. PK-QL) was dissolved in 58 mass units of medium tar to form a solution, and 1,000 mass units of this solution were prepared in advance. 100 mass units of the previously prepared graphite granules were put into the blender together with the above-mentioned solution of 1000 mass units, and the graphite granules were impregnated with the coal tar after stirring at 150 ° C for 30 minutes. In the solution, the medium tar as a solvent was then filtered off at the same temperature under a pressure of 0 mm H g. The prepared graphite granules were filled with an asphalt adherend in a steel container. In a sintering furnace equipped with a device capable of burning volatile gases, the adherend was subjected to primary sintering at 450 ° C for 20 minutes while flowing inert gas. This sintered body is in a state of being melt-adhered only between the graphitizable carbons on the surface of the graphite granules. An impact pulverizer was used to disintegrate the primary sintered body. The obtained primary sintered body had an average particle diameter of 22 μηι and an aspect ratio of 1.7. < Modification treatment > Next, the primary sintered body is put into a modification treatment device (a MECHANOFUSION SYSTEM by HOSOKAWA MICRON GROUP) shown in Figs. 2 (a) and (b), and mechanical properties are imparted. That is, under the conditions of a rotating drum peripheral speed of 20 m / s, a processing time of 30 minutes, and a distance of 5 mm between the rotating drum and the internal components, the compression-44-(39) (39) 587350 force and shear force are repeatedly applied. . The average example diameter of the primary sintered body after the modification treatment was 2 2 μηα, and the aspect ratio was 1 · 7. Compared with the average example diameter and aspect ratio before the modification treatment, there was no change. < Manufacturing of composite graphite material > Next, a graphite crucible was filled with the prepared modified body, and tar powder was filled around the graphite can. (: Heated for 5 hours to form graphitization 'and finally made a composite graphite material. After confirmation, the composite graphite material did not cause fusion adhesion and deformation, and could maintain the original particle shape. The average particle size of the composite graphite material was 2 2 μm, aspect ratio is 1.7, specific surface area is 0.5 m ** / g, bulk density is 1.02 g / cm .. Fe crystallinity d 〇〇2 measured by X wide-angle concealment method = 〇 · 3 3 5 7 nm, L c = 8 8 nm, R 値 measured by Raman spectroscopy is 0.08. Figure 4 shows a scan of the composite graphite material produced. Photograph of a type electron microscope. This composite graphite material was used to make the negative electrode of an evaluation battery, and the evaluation results of the battery characteristics are summarized in Table 2. (Examples 3 to 5) 00 mass units used in advance in Example 2 After adding 0.5 mass unit of anhydrous silicon oxide powder ("AEROSIL300" manufactured by Japan Aerosil Corporation, average particle size is 0 ·) to coal tar, it was sintered once, and changed. Easily graphitizable carbon after volatilization. For other conditions, use and The same conditions were used in Example 2 to produce a composite graphitized material. During the disintegration process after one sintering, -45- (40) (40) 587350 reduced the load of the pulverizer and easily formed disintegration. Various evaluations are performed on the graphite material, and the crystallinity and battery characteristics are summarized in Table 2. As shown in Table 2, the evaluation battery using the composite graphite material of Examples 2 to 5 has a theoretical capacity approaching that of graphite (3 72 mAh / g) has a large discharge capacity, and has a very high initial charge and discharge efficiency. Among them, Examples 3 to 5 in which anhydrous silicon oxide powder made by a gas phase method is added to easily graphitizable carbon are more excellent. The initial charge and discharge efficiency of the product has the effect of suppressing "lead-graphitizable carbon that is liable to be disintegrated after melt adhesion and easy peeling of the graphitizable carbon film". In addition, it also has excellent rapid discharge efficiency and cycle characteristics. Even in the state of high electrode density, it also has excellent rapid discharge efficiency and cycle characteristics. (Comparative Example 1) Except that natural graphite is not added to the easily graphitizable carbon as in Example 1, it is not insistent. Except for the modification treatment, the graphite material was produced under the same conditions as in the example. The graphite material produced will have a molten adhesion between the graphite materials after the second sintering, and it cannot maintain the disintegration after the first sintering. Therefore, it is necessary to disintegrate the graphite material after fusion and adjust its average particle size to 19 μη] to produce an evaluation battery. The evaluation results of the crystallinity and battery characteristics are shown in the table. As shown in Table 2. As shown in Table 2, Comparative Example 1 using a graphite material that does not contain natural graphite and has not been modified has a significantly reduced discharge capacity and initial charge-discharge efficiency. -46-(41) (41 587350 (Comparative Example 2) A graphite material was produced in the same manner as in Example 1 except that the modification treatment in Example 1 was omitted. The obtained graphite material has a slight melting adhesion between the graphite materials after the second sintering, and cannot maintain the shape obtained after the first sintering. Therefore, it is necessary to disintegrate the graphite material after melting and adjust the average particle diameter to 19 μm to prepare an evaluation battery. The results of evaluation of the crystallinity and battery characteristics are shown in Table 2. As shown in Table 2, Comparative Example 2 'without the modification treatment characteristic of the present invention did not form low crystallization on the graphite surface, and the initial charge and discharge efficiency was significantly reduced. (Comparative Example 3) Except that the secondary sintering temperature in Example 1 was changed to! Other than 300 ′, graphite material was produced in the same manner as in Example 1. The produced graphite material is equivalent to a conventional product, and natural graphite is contained in a non-graphite material. In addition, no fusion adhesion was observed in the produced material, and the shape after pulverization was maintained. An evaluation battery was produced in the same manner as in Example 1 with this graphite material. Table 2 shows the results of S-evaluation of crystallinity and battery characteristics. As shown in Table 2, in Comparative Example 3 where the secondary sintering temperature was lowered and the graphitizable carbon was not sufficiently graphitized, the crystallinity of the material was low, and the discharge amount was also significantly reduced. -47- (42) (42) 587350 (Comparative Example 4) The conditions for applying the modification treatment of Example 1 'Directly to natural graphite (produced by China-Vietnam Graphite Industry Institute (stock)', product name is BF] 0A, the average particle size is 10 μηι) for modification. No melt adhesion and deformation were found in the graphite after the modification treatment, and the shape after pulverization was maintained. Its average particle diameter is 9 μη: ι. Next, the same graphite as in Example 1 was produced using this natural graphite, and its battery characteristics were evaluated. The crystallinity and battery characteristics are shown in Table 2. As shown in Table 2, inevitable Comparative Example 4 ', which attempts to directly modify the natural graphite to reduce the surface crystallinity, has a low initial charge and discharge efficiency. However, its rapid discharge efficiency and cycle characteristics are not good. Increasing the electrode density will orient the graphite particles, causing the above characteristics to deteriorate again. (Comparative Example 5) A battery for evaluation was produced by using natural graphite (produced by China Vietnam Graphite Industry Co., Ltd. under the trade name of B F] 0 A and average particle size of 100 μm). The manufacturing method and evaluation method of the evaluation battery were the same as those in the first embodiment. The evaluation results of the crystallinity and battery characteristics are shown in Table 2. As shown in Table 2, Comparative Example 5 in which natural graphite was used alone had a large discharge M, but had poor initial charge and discharge efficiency, rapid discharge efficiency, and cycle characteristics. If the electrode density is increased, the above characteristics will be significantly reduced. -48- (43) (43) 587350 (Comparative Example 6) A graphite material was produced in the same manner as in Example 2 except that the modification treatment in Example 2 was omitted. The evaluation results of the crystallinity and battery characteristics are shown in Table 2. As shown in Table 2, Comparative Example 6, which was made of a graphite material without modification treatment, had low initial charge and discharge efficiency. In addition, compared with Comparative Example 6, it can be seen that R 値 in Example 2 is larger, and low crystallinity can be selectively formed on the surface of the graphite material.

-49- 587350 1谳 備註 /-~s ψ ^ /-Ν /^N ψ ( 改質處理 1 1_ & 句; UJ, 揉 一次燒結後之易石墨化性碳的物性 1 \〇 C\ 〇\ 〇〇 ο <η 〇\ (Ν ON Ό C\ Ό CN 〇 〇 κη 〇\ 揮發量(%) (N 寸· (N Ο 〇〇 rn ΓΝ1 寸 00 〇 ν〇 (Ν 寸· (N 'sT 〇 〇 (N vd 微粒子 含有量(%) 〇 〇 ^Γί Ο 〇 Ο 〇 〇 ο 種類 氣相氧化矽 氣相氧化矽 氣相氧化矽 层 石墨B的原料 (易石墨化性碳) 煤焦油 煤焦油 煤焦油 煤焦油 煤焦油 煤焦油 煤焦油 煤焦油 煤焦油 石墨A 含有量(%) § § § 〇 〇 〇 形狀 鱗片狀 造物粒 造物粒 造物粒 造物粒 鱗片狀 鱗片狀 鱗片狀 鱗片狀 造物粒 實施例1 實施例2 實施例3 實施例4 實施例5 比較例1 比較例2 比較例3 比較例4 比較例5 比較例6 。鋈运^写杉晾騍匀刍111鞠銮111绞刼鲳屮^鹚堤_^:::衾3(1 -50- 587350 s .1 1 1 ili3 /s /^N 電池特性 ΓΛ r-1 I oo w 循環特性 (% ) (N C\ m G\ G\ ^T) oc VO OO ν〇 VO C\ \〇 OO 急速放電 率(% ) Ό 〇〇 5; rsi m Os (N Cs r- g § oo 初期充放 電率(% ) (N 〇 m oo oc m oc 放電量 (mAh/g) 360 m ^sO m v〇 m Ό 354 360 292 Ό VO m VO m m 電極密度:1.6 g/c.m3 循環特性 (% ) m CN v〇 ON On oo oo oo σ> 00 rn OO On (N 急速放電 率(% ) g ^T) c\ 客 ON m oc oc oc oo rn OC VO g 初期充放 電率(% ) m 〇\ tn Ch to o oc oo 〇\ oc \〇 oo ON 00 放電量 (mAh/g) 360 to 366 <n m m m 355 CN (N 368 369 to VO < &PI 拉曼分 光R値 0.12 0.08 0.06 0.09 0.13 0.03 0.04 0.32 0.02 0.02 0.04 X光廣角 繞射(_) oo oo ON OO to 00 JO vo oo m to On OO rsi 〇 0.3358 0.3357 0.3357 0.3357 0.3358 0.3360 0.3358 0.3367 0.3356 0.3356 0.3357 實施例1 實施例2 實施例3 實施例4 實施例5 比較例1 比較例2 比較例3 比較例4 比較例5 比較例6 OOP- ^sin壊 csii 隹 黯。雲震^iis#_^si-s讓sn_ (e-49- 587350 1 谳 Note /-~ s ψ ^ / -N / ^ N ψ (Modification treatment 1 1_ &sentence; UJ, physical properties of easily graphitizable carbon after kneading once sintering 1 \ 〇C \ 〇 \ 〇〇ο < η 〇 \ (N ON Ό C \ Ό CN 〇〇κη 〇 \ Volatility (%) (N inch · (N 〇 〇〇〇rn ΓΝ1 inch 00 〇νν (N ' sT 〇〇 (N vd microparticle content (%) 〇〇 ^ Γί 〇 〇 〇 〇〇ο ο kind of fumed silica fumed silica fumed silica fumed silica graphite raw material of graphite B (easy graphitizable carbon) coal tar coal Tar coal tar coal tar coal tar coal tar coal tar coal tar coal tar graphite A content (%) § § § 00 shape shape flaky granules granules granules granules granules scales scales scales scales scales scales Example 1 Example 2 Example 3 Example 4 Example 5 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Comparative Example 5 Comparative Example 6 ^ 鹚 堤 _ ^ ::: 衾 3 (1 -50- 587350 s .1 1 1 ili3 / s / ^ N Battery characteristics Γ r-1 I oo w cycle characteristics (%) (NC \ m G \ G \ ^ T) oc VO OO ν〇VO C \ \ 〇OO rapid discharge rate (%) Ό 〇〇5; rsi m Os (N Cs r- g § oo Initial charge and discharge rate (%) (N 〇m oo oc m oc Discharge (mAh / g) 360 m ^ sO mv〇m Ό 354 360 292 Ό VO m VO mm Electrode density: 1.6 g / c .m3 cycle characteristics (%) m CN v〇ON On oo oo oo σ > 00 rn OO On (N rapid discharge rate (%) g ^ T) c \ customer ON m oc oc oc oo rn OC VO g initial charge and discharge Rate (%) m 〇 \ tn Ch to o oc oo 〇 \ oc \ 〇oo ON 00 Discharge volume (mAh / g) 360 to 366 < nmmm 355 CN (N 368 369 to VO < & PI Raman spectrometry R 値 0.12 0.08 0.06 0.09 0.13 0.03 0.04 0.32 0.02 0.02 0.04 X-ray wide-angle diffraction (_) oo oo ON OO to 00 JO vo oo m to On OO rsi 〇0.3358 0.3357 0.3357 0.3357 0.3358 0.3360 0.3358 0.3367 0.3356 0.3356 0.3357 Example 1 Example 2 Example 3 Example 4 Example 5 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Comparative Example 5 Comparative Example 6 OOP- ^ sin 壊 csii Yunzhen ^ iis # _ ^ si-s let sn_ (e

-51 · (46) (46)587350 【產業上的利用性】 本發明的複合石墨材料,可適用於負極及負極材料。 使用該負極材料的鋰離子二次電池,可充分地同時達到高 初期充放電效率與大放電量之兩種背道而馳的特性。此 外,根據本發明的方法,可抑制石墨化過程中的熔融附著 等現象,並製作出生產性佳的前述複合石墨材料。因此, 藉由本發明的複合石墨材料,可滿足近年來對電池能源高 密度化的要求。再者,搭載有本發明之負極材料、負極以 及鋰離子二次電池的機器,可有效地小型化並達到高效能 化,對社會有廣大的貢獻。 【圖式簡單說明】 第1圖:用來說明本案實施例與比較例所採用之評估 周電池結構的示意剖面圖。 第2圖:(a )是說明對本案所採用之機械性能量進 行改質處理裝置的作用機構圖,(b )是該裝置的結構示 意圖。 第3圖:是對本条所採用之機械性能量進行改臂處理 裝置的示意圖。 第4圖:是根據實施例2所製成之複合石墨材 Ή枓的掃 描型電子顯微鏡圖像 【符號說明】 •52- (47)587350 1 外杯 2 負極 3 外罐 4 正極 5 隔板 6 絕緣襯墊-51 · (46) (46) 587350 [Industrial applicability] The composite graphite material of the present invention can be applied to a negative electrode and a negative electrode material. A lithium ion secondary battery using this negative electrode material can sufficiently achieve both of the characteristics that run counter to high initial charge and discharge efficiency and large discharge capacity. In addition, according to the method of the present invention, it is possible to suppress the phenomenon of fusion adhesion and the like in the graphitization process, and to produce the aforementioned composite graphite material with high productivity. Therefore, with the composite graphite material of the present invention, it is possible to satisfy the demand for higher density of battery energy in recent years. Furthermore, a device equipped with the negative electrode material, the negative electrode, and the lithium ion secondary battery of the present invention can effectively be miniaturized and achieve high performance, and can contribute to society. [Brief Description of the Drawings] Figure 1: A schematic cross-sectional view for explaining the structure of the evaluation battery used in the examples and comparative examples of this case. Figure 2: (a) is an action mechanism diagram illustrating a modification of a mechanical property used in the present case, and (b) is a schematic view of the structure of the device. Figure 3: Schematic diagram of a modified arm handling device for the mechanical properties used in this section. Figure 4: Scanning electron microscope image of a composite graphite material made according to Example 2 [Symbols] • 52- (47) 587350 1 Outer cup 2 Negative electrode 3 Outer can 4 Positive electrode 5 Separator 6 Insulation pad

7 a 聚電體 7b 聚電體 1 1 轉動滾筒 1 2 內部構件(內部螺 絲) 1 3 一次燒結體 14 循環機構 15 排出機構7 a Polyelectric body 7b Polyelectric body 1 1 Rotate the drum 1 2 Internal components (internal screw) 1 3 Primary sintered body 14 Circulation mechanism 15 Discharge mechanism

2 1 固定滾筒 22 轉子 23 一次燒結體 24 循環機構 25 排出機構 2 6 葉片 2 7 定子 2 8 夾套 •53-2 1 Fixed roller 22 Rotor 23 Primary sintered body 24 Circulation mechanism 25 Discharge mechanism 2 6 Blade 2 7 Stator 2 8 Jacket • 53-

Claims (1)

(1) (1)587350 拾、申清專利範圍 1. 一種複合石墨材料,其具有的構造是: 在於石墨A的外側具有較之該石墨A更低的結晶性 的石& B,且該石墨β的外表面的至少其中一部份是存在 著較之該石墨B更低的結晶性的石墨c。 -·如申阳專利範圍第1項之複合石墨材料,其具有 以該石墨B來披覆該石墨a,並且以該石墨C來披覆該 石墨B的橇造。 3 ·如申請專利範圍第丨項之複合石墨材料,其中前 述複合石璺材料是球狀或者橢圓體狀的造粒物。 4 .如申請專利範圍第1項之複合石墨材料,其中前 述複合石_材料整體上,碳網面層的面間隔(d㈣2 )是 〇·3 3 6 5 ηΠ1以下,結晶子的C軸方向的大小(L〇是4〇nm 以上 拉愛光譜的]3 6 0 c m ·】的峰値強度(113 6 〇 )相對方々 1 5 8 0 cm。的峰値強度(1]$8。)的比値(1136g/ I15S。)是 0.0 5以上〇 · 3 〇以下。 5 ·如申請專利範圍第1項之複合石墨材料,其中前 述石墨A韙鱗片狀石墨。 6 ·如申請專利範圍第1項之複合石墨材料,其中前 述石墨A裹碳網面層的面間隔(dGQ2)是〇.3 3 5 Snm以卞 者。 7 ·如申請專利範圍第1項之複合石墨材料,其ψ前 述石墨B楚碳網面層的面間隔(do。2)是〇.337〇nm以卞 者0 -54- (2) (2)587350 8 . —種鋰離子二次電池用的負極材料,係含有如申 請專利範圍第1項至第7項的任何一項所述的複合石墨材 料。 · 9. 一種鋰離子二次電池用的負極,係含有如申請專 利範圍第1項至第7項的任何一項所述的複合石墨材料。 10. —種鋰離子二次電池,係含有如申請專利範圍第 9項所述的負極。 Π . —種複合石墨材料之製造方法,是用以製造具 有:在於石墨A的外側具有較之該石墨A更低的結晶性 的石墨B,且該石墨B的外表面的至少其中一部份是存在 著較之該石墨B更低的結晶性的部分的構造之複合石墨材 料,該製造方法是具有: 在於石墨的外側附著上具有易於石墨化特性的碳的過 程; 以使該具有易於石墨化特性的碳實質上尙未石墨化的 程度,對於該附著體進行第一次燒結的過程; 對於該第一次燒結體,以實質上不加以粉碎的方式施 予機械能量而予以改質的過程; 對於該改質體進行直到該具有易於石墨化特性的碳實 質上已經石墨化爲止的第二次燒結的過程。 ]2 .如申請專利範圍第1 1項之複合石墨材料之製造 方法,其中前述石墨是鱗片狀石墨。 13.如申請專利範圍第1 1項之複合石墨材料之製造 方法,其中前述石墨是碳網面層的面間隔(dG()2 )是 -55- (3) (3)587350 0..3 3 5 8nm 以下者。 ]4 ·如申請專利範圍第1 1項之複合石墨材料之製造 方法’其中前述具有易於石墨化特性的碳是由:焦油、瀝 青以及中間相所組成的群組中所選出的至少一種。 ]5·如申請專利範圍第1 1項之複合石墨材料之製造 方法’其中在進行前述附著過程之前,具有將該石墨予以 造粒的過程。 16.如申請專利範圍第1 1項之複合石墨材料之製造 方法,(其中前述附著過程是利用:融熔、溶解或分散所選 出的至少一種方法先將該具有易於石墨化特性的碳變成液 狀’再使其附著於該石墨上> I 7 .如申請專利範圍第1 1項之複合石墨材料之製造 方法,其中前述第一次燒結過程是使得該具有易於石墨化 特性的碳中所殘留的揮發成分變成2.0質量%以上2 0質 量%以下。 1 8 ·如申請專利範圍第1 1項之複合石墨材料之製造 方法,其中前述第一次燒結過程之後,又具有將二次凝集 以上的凝集體加以碎解(d i s a g g I 〇 m e r a t e )的過程。 -56-(1) (1) 587350 Scope of claiming and claiming patents 1. A composite graphite material having a structure in which a stone & B on the outside of graphite A has lower crystallinity than the graphite A, and the At least a part of the outer surface of the graphite β is a graphite c having lower crystallinity than the graphite B. -The composite graphite material according to item 1 of the Shenyang patent scope, which has a skid made of the graphite B covering the graphite a and the graphite C covering the graphite B. 3. The composite graphite material according to the scope of the patent application, wherein the composite ballast material is a spherical or ellipsoidal granule. 4. The composite graphite material according to item 1 of the scope of the patent application, in which the above-mentioned composite stone material as a whole, the interplanar spacing (d㈣2) of the carbon mesh surface layer is below 0.33 6 5 ηΠ1, and the crystal axis The size (L0 is the ratio of the spectroscopy of 40nm or more) of 3 6 0 cm ·] peak 値 intensity (113 6 〇) relative square 々 15 8 0 cm. Peak 値 intensity (1) $ 8.。 (1136g / I15S.) Is 0.0 5 or more and 0.30 or less. 5 • The composite graphite material as described in the first item of the patent application, wherein the aforementioned graphite A is flaky graphite. 6 • The compound as the first item of the patent application Graphite materials, in which the above-mentioned graphite A-wrapped carbon mesh surface layer has a surface interval (dGQ2) of 0.3 35 Snm. 7 · As in the case of the composite graphite material in the first scope of the patent application, the above-mentioned graphite B Chu carbon The interplanar spacing (do. 2) of the mesh surface layer is 0.333 nm, which is 0 -54- (2) (2) 587350 8. A negative electrode material for lithium ion secondary batteries, which contains, for example, a patent application The composite graphite material according to any one of the items 1 to 7. 9. A negative electrode for a lithium ion secondary battery, Contains the composite graphite material as described in any one of the scope of claims 1 to 7. 10. A lithium ion secondary battery that contains the negative electrode as described in the scope of claims 9. Π. — A method for manufacturing a composite graphite material is used to produce graphite B which has a lower crystallinity than graphite A on the outside of graphite A, and at least a part of the outer surface of the graphite B is present. Compared with the graphite B, a composite graphite material having a structure with a lower crystalline part, the manufacturing method has: a process of attaching carbon having an easy graphitization property on the outside of the graphite; Carbon is substantially ungraphitized, and the first sintering process is performed on the adherend; the first sintered body is modified by applying mechanical energy in a manner that does not substantially crush; The modified body undergoes the second sintering process until the carbon with easy graphitization characteristics has been substantially graphitized.] 2. Compounding as in item 11 of the scope of patent application The manufacturing method of the ink material, wherein the foregoing graphite is flaky graphite. 13. The manufacturing method of the composite graphite material according to item 11 of the patent application scope, wherein the foregoing graphite is a carbon mesh surface layer with an inter-space (dG () 2) of -55- (3) (3) 587350 0..3 3 5 8nm or less.] 4 · As in the method of manufacturing a composite graphite material in the scope of patent application No. 11 'wherein the aforementioned carbon having easy graphitization characteristics is : At least one selected from the group consisting of tar, pitch, and mesophase. [5] The method for manufacturing a composite graphite material according to item 11 of the scope of patent application ', wherein the graphite is granulated before the aforementioned attachment process. 16. The method for manufacturing a composite graphite material according to item 11 of the scope of patent application (wherein the aforementioned attachment process is to use at least one method selected by melting, dissolving or dispersing the carbon which has easy graphitization characteristics into a liquid And then make it adhere to the graphite > I 7. As in the method of manufacturing a composite graphite material according to item 11 of the patent application, wherein the first sintering process described above makes the carbon having easy graphitization characteristics The remaining volatile component becomes 2.0% by mass or more and 20% by mass or less. 1 8 · The manufacturing method of the composite graphite material according to item 11 of the patent application scope, wherein after the aforementioned first sintering process, the secondary agglomeration is further increased. The process of disaggregating the disaggregated aggregates (disagg I omerate). -56-
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