JP2009224188A - Method of manufacturing lithium-ion secondary battery and its positive electrode plate - Google Patents
Method of manufacturing lithium-ion secondary battery and its positive electrode plate Download PDFInfo
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Abstract
Description
本発明は、リチウムイオン二次電池およびその正極板の製造方法に関し、特にその好適な正極用ペーストの製造方法に関する。 The present invention relates to a method of manufacturing a lithium ion secondary battery and a positive electrode plate thereof, and more particularly to a preferable method of manufacturing a positive electrode paste.
近年、携帯電話、ノートパソコン等の携帯用電子・通信機器等に用いられるリチウムイオン二次電池の代表として、リチウムイオンの吸蔵・放出が可能な炭素材料等を負極活物質とし、リチウム選移金属複合酸化物を正極活物質とするリチウムイオン二次電池が実用化されている。 In recent years, as a representative of lithium ion secondary batteries used in portable electronic and communication devices such as mobile phones and laptop computers, carbon materials that can occlude and release lithium ions are used as negative electrode active materials, and lithium selected metals. A lithium ion secondary battery using a composite oxide as a positive electrode active material has been put into practical use.
従来、リチウムイオン二次電池の製造方法に関して、リチウム系金属酸化物材料、導電剤、および結着剤を増粘剤水溶液に同時に配合・混練してペーストを製造する方法の他に、正極活物質と導電剤と界面活性剤を練合したスラリーを用いることにより、導電剤の分散性を向上させ、リチウムイオン二次電池の出力特性を良化させる方法が開示されている(特許文献1参照)。
しかしながら、従来の製造方法により作製した極板においては、ペースト製造直後の状態での正極活物質と結着剤および増粘剤との混合度は改善されたが、ペースト保管中において、過剰の界面活性剤の影響と推測される再凝集による分離や沈降などが生じる場合があった。 However, in the electrode plate produced by the conventional production method, the degree of mixing of the positive electrode active material, the binder and the thickener immediately after the paste production was improved, but the excess interface was reduced during paste storage. In some cases, separation or sedimentation due to reaggregation presumed to be due to the effect of the activator occurred.
このことにより、塗布、乾燥後の活物質同士の結着性および集電体の密着性が悪く、高温保存中や繰り返し充放電使用中に、集電体からの活物質の剥離、脱落が生じ、放電容量の低下や負荷特性の悪化を促すといった問題があった。 As a result, the adhesion between the active materials after coating and drying and the adhesion of the current collector are poor, and the active material peels off from the current collector during high-temperature storage or repeated charge / discharge use. There has been a problem that the discharge capacity is reduced and the load characteristics are deteriorated.
本発明は、このような技術的背景に鑑みてなされたものであって、簡単な工程で実施でき、ペーストを放置しておいても固液分離、凝集させることなく均一に分散を保ったまま塗料化する方法の提供を目的とする。 The present invention has been made in view of such a technical background, and can be carried out by a simple process. Even if the paste is left as it is, it remains uniformly dispersed without solid-liquid separation and aggregation. The object is to provide a method of coating.
前述の目的を達成するために、本発明のリチウムイオン二次電池用正極板の製造法は、界面活性剤であるポリオキシエチレンアルキルエーテルと増粘剤水溶液とを20℃以上50℃以下の温度に保った状態で加温処理した分散剤混合水溶液中に、導電剤とリチウム系金属酸化物材料を主体とした正極活物質を混合した後、さらに結着剤を投入して混合分散することによって得た正極用ペーストを、用いることを特徴としたものである。 In order to achieve the above-mentioned object, a method for producing a positive electrode plate for a lithium ion secondary battery according to the present invention comprises a surfactant having a polyoxyethylene alkyl ether and a thickener aqueous solution at a temperature of 20 ° C to 50 ° C. After mixing a positive electrode active material mainly composed of a conductive agent and a lithium-based metal oxide material in a dispersant mixed aqueous solution that is heated in a state of being kept at a high temperature, a binder is further added and mixed and dispersed. The obtained positive electrode paste is used.
本発明にかかるリチウムイオン二次電池正極用ペーストの製造方法によれば、界面活性剤であるポリオキシエチレンアルキルエーテルと増粘剤水溶液とを20℃以上50℃以下の温度に保った状態で加温処理した分散剤混合水溶液中に、導電剤とリチウム系金属酸化物材料を主体とした正極活物質を混合した後、さらに結着剤を投入して混合分散することによって均一に分散された正極用ペーストを用いることにより、集電体に塗布、乾燥して成る正極用極板を備えるリチウムイオン二次電池用正極板の製造が可能となる。 According to the method for producing a positive electrode paste for a lithium ion secondary battery according to the present invention, the surfactant polyoxyethylene alkyl ether and the aqueous thickener solution are added in a state maintained at a temperature of 20 ° C. or higher and 50 ° C. or lower. A positive electrode that is uniformly dispersed by mixing a positive electrode active material mainly composed of a conductive agent and a lithium-based metal oxide material in a temperature-treated dispersant mixed aqueous solution, and then adding a binder to mix and disperse. By using the paste for a lithium ion secondary battery, it is possible to manufacture a positive electrode plate for a lithium ion secondary battery including a positive electrode plate that is applied to a current collector and dried.
本発明の本旨は、分散剤混合水溶液の作成方法としてあらかじめ20℃以上50℃以下の温度と保った状態で増粘剤水溶液と混合したものを用いて練合することにあり、このことにより、効率的に均一に分散されたペーストを集電体表面に塗着することができる。 The gist of the present invention is to knead using a mixture with a thickener aqueous solution in a state where the temperature is kept at 20 ° C. or higher and 50 ° C. or lower in advance as a method for preparing the dispersant mixed aqueous solution. The paste that is efficiently and uniformly dispersed can be applied to the surface of the current collector.
以上述べた製造法によると、正極板の集電体露出がないため導電性が向上し、それらの正極板を用いることにより、電池特性も向上したリチウムイオン二次電池が実現できるものである。 According to the manufacturing method described above, the positive electrode plate is not exposed to the current collector, so that the conductivity is improved. By using these positive electrode plates, a lithium ion secondary battery with improved battery characteristics can be realized.
以下、本発明の実施例を図面を用いて詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
(実施例1)
本発明のリチウムイオン二次電池は図1に示すような円筒型リチウムイオン二次電池で、極板群と、電解液と、これらを収容する電池ケースからなる。極板群は、シート状の正極板5と、シート状の負極板6と、正極板5と負極板6間を絶縁するシート状のセパレータ7と、正極リード3と、負極リード9と、上部絶縁板4と、下部絶縁板10とからなる。正極板5はアルミニウム箔の両面に塗着形成したものである。セパレータ7は多孔質ポリプロピレンフィルムであり、これらが重ねられて渦巻き状に巻回されて、円筒型のケース本体8内にきっちりと収容されている。
Example 1
The lithium ion secondary battery of the present invention is a cylindrical lithium ion secondary battery as shown in FIG. 1 and comprises an electrode plate group, an electrolytic solution, and a battery case that houses them. The electrode plate group includes a sheet-like positive electrode plate 5, a sheet-like negative electrode plate 6, a sheet-like separator 7 that insulates between the positive electrode plate 5 and the negative electrode plate 6, a positive electrode lead 3, a negative electrode lead 9, and an upper portion. It consists of an insulating plate 4 and a lower insulating plate 10. The positive electrode plate 5 is formed by coating on both surfaces of an aluminum foil. The separator 7 is a porous polypropylene film, and these are overlapped and wound in a spiral shape, and are tightly accommodated in a cylindrical case body 8.
本実施例における円筒型電池のサイズとしては、直径17mm、高さ50mm、公称容量としては1440mAhの円筒型リチウムイオン二次電池を作製した。 As the size of the cylindrical battery in this example, a cylindrical lithium ion secondary battery having a diameter of 17 mm, a height of 50 mm, and a nominal capacity of 1440 mAh was manufactured.
先ず、図1の本発明に用いたリチウムイオン二次電池の断面図を用いて、正極板5の製造法を詳細に説明する。 First, the manufacturing method of the positive electrode plate 5 is demonstrated in detail using sectional drawing of the lithium ion secondary battery used for this invention of FIG.
界面活性剤としてポリオキシエチレンアルキルエーテル(日油株式会社製)1重量部に対して増粘剤としてカルボキシメチルセルロース(第一工業製薬株式会社製セロゲンEP)を1重量部に対して水99重量部に溶解した水溶液30重量部を配合し、35℃に加温する。 99 parts by weight of water per 1 part by weight of carboxymethyl cellulose (Serogen EP by Daiichi Kogyo Seiyaku Co., Ltd.) as a thickener for 1 part by weight of polyoxyethylene alkyl ether (manufactured by NOF Corporation) as a surfactant 30 parts by weight of the aqueous solution dissolved in is mixed and heated to 35 ° C.
このようにして加温処理された増粘剤水溶液および分散剤混合水溶液中に、導電剤として工業のアセチレンブラック(電化株式会社製)1.5重量部、正極活物質としてLiCoO2粉末(日亜化学工業株式会社製)を50重量部を20分間混合する。混合後、結着剤としてPTFE(ダイキン工業株式会社製ポリフロンD−1)50重量部水溶液を5重量部混合分散して正極用ペーストを得た。 In the thus-heated thickener aqueous solution and dispersant mixed aqueous solution, 1.5 parts by weight of industrial acetylene black (manufactured by Denka Co., Ltd.) as the conductive agent and LiCoO 2 powder (Nichia Chemical) as the positive electrode active material 50 parts by weight of Kogyo Co., Ltd.) is mixed for 20 minutes. After mixing, 5 parts by weight of an aqueous solution of 50 parts by weight of PTFE (polyflon D-1 manufactured by Daikin Industries, Ltd.) as a binder was mixed and dispersed to obtain a positive electrode paste.
次に、この正極用ペーストを厚み20μmのアルミニウム箔(昭和電工株式会社製1085材)にダイコーターを用いて片側の厚さを180μmに塗布して乾燥後、PTFEの溶融温度である200〜300℃で正極板を加熱して、集電体と正極合剤層の密着層を改良させる。この後、厚み0.18mmに圧延し、所定の幅に切断して正極板を得た。 Next, this positive electrode paste is applied to an aluminum foil having a thickness of 20 μm (1085 material manufactured by Showa Denko KK) using a die coater to a thickness of 180 μm on one side and dried, and then a melting temperature of PTFE of 200 to 300 The positive electrode plate is heated at 0 ° C. to improve the adhesion layer between the current collector and the positive electrode mixture layer. After that, it was rolled to a thickness of 0.18 mm and cut to a predetermined width to obtain a positive electrode plate.
本発明のリチウム2次電池の一実施形態は図1に示すような円筒型リチウム2次電池で、前記本発明の正極用ペーストの製造法により得られた正極板5を用いた極板群と、電解液と、これらを収容する電池ケースからなる。極板群は、シート状の正極板5と、シート状の前記負極板6と、正極板5と負極板6間を絶縁するシート状のセパレータ7と、正極リード3と、負極リード9と、上部絶縁板4と、下部絶縁板10とからなる。 One embodiment of the lithium secondary battery of the present invention is a cylindrical lithium secondary battery as shown in FIG. 1, and an electrode plate group using the positive electrode plate 5 obtained by the method for producing a positive electrode paste of the present invention; And an electrolyte solution and a battery case containing them. The electrode plate group includes a sheet-like positive electrode plate 5, a sheet-like negative electrode plate 6, a sheet-like separator 7 that insulates between the positive electrode plate 5 and the negative electrode plate 6, a positive electrode lead 3, a negative electrode lead 9, It consists of an upper insulating plate 4 and a lower insulating plate 10.
正極板5はアルミニウム箔の両面に塗着形成したものである。セパレータ7は多孔質ポ
リプロピレンフィルムであり、これらが重ねられて渦巻き状に巻回されて、円筒型の電池ケース内にきっちりと収容されている。
The positive electrode plate 5 is formed by coating on both surfaces of an aluminum foil. The separator 7 is a porous polypropylene film, and these are overlapped and wound in a spiral shape, and are tightly accommodated in a cylindrical battery case.
次に負極板6の製造方法を説明する。 Next, a method for manufacturing the negative electrode plate 6 will be described.
先ず、鱗片状黒鉛粉末(関西熱化学株式会社製)50質量部、結着剤としてスチレンブタジエンゴム(JSR株式会社製)5質量部、そして増粘剤としてカルボキシルメチルセルロース(第一工業製薬株式会社製セロゲンEP)1質量部に対して水99質量部に溶解した水溶液23質量部とを混合分散して負極用ペーストを得た。得られた負極用ペーストをダイコーターを用いて厚さ10μmの銅箔(福田金属箔粉工業株式会社製)からなる負極集電体の両面に塗布乾燥し、厚み0.2mmに圧延し、切断してシート状の負極板6を作製した。 First, flaky graphite powder (manufactured by Kansai Thermochemical Co., Ltd.) 50 parts by mass, styrene butadiene rubber (manufactured by JSR Co., Ltd.) 5 parts by mass as a binder, and carboxylmethylcellulose (manufactured by Daiichi Kogyo Seiyaku Co., Ltd.) as a thickener. A paste for negative electrode was obtained by mixing and dispersing 23 parts by mass of an aqueous solution dissolved in 99 parts by mass of water with respect to 1 part by mass of (Serogen EP). The obtained negative electrode paste was applied to and dried on both sides of a negative electrode current collector made of a 10 μm thick copper foil (Fukuda Metal Foil Powder Co., Ltd.) using a die coater, rolled to a thickness of 0.2 mm, and cut. Thus, a sheet-like negative electrode plate 6 was produced.
電解液(三菱化学株式会社製)は、25℃において炭酸エチレン30vol%、炭酸ジエチル50vol%、プロピオン酸メチル20vol%となる混合液に、LiPF6を1mol/literの濃度に溶解したものを用いた。この電解液は、電池ケース内に収容され、正極活物質層および負極活物質層内に含浸されて、電池反応において、多孔質なセパレータ7の微少孔を通して正極板5と負極板6間のLiイオンの移動を担う。 As an electrolytic solution (manufactured by Mitsubishi Chemical Corporation), a solution obtained by dissolving LiPF 6 at a concentration of 1 mol / liter in a mixed solution of ethylene carbonate 30 vol%, diethyl carbonate 50 vol%, and methyl propionate 20 vol% at 25 ° C. was used. . This electrolytic solution is accommodated in the battery case, impregnated in the positive electrode active material layer and the negative electrode active material layer, and in the battery reaction, the Li between the positive electrode plate 5 and the negative electrode plate 6 passes through the minute holes of the porous separator 7. Responsible for the movement of ions.
電池ケースは、耐有機電解液性のステンレス鋼板を深絞り成形して得たケース本体8と、封口板1と、封口板1とケース本体8との間を絶縁する絶縁ガスケット2とからなる。 The battery case includes a case main body 8 obtained by deep drawing an organic electrolyte resistant stainless steel plate, a sealing plate 1, and an insulating gasket 2 that insulates the sealing plate 1 from the case main body 8.
このようにして円筒型リチウムイオン二次電池を作製し、その初期放電容量またサイクル特性を確認した。また、電池を作製する前に、電池に用いた正極極板の質量を測定し、初期放電容量と比較した。上記の電池を本実施例の電池1とした。 Thus, a cylindrical lithium ion secondary battery was produced, and its initial discharge capacity and cycle characteristics were confirmed. Moreover, before producing a battery, the mass of the positive electrode plate used for the battery was measured and compared with the initial discharge capacity. The above battery was designated as battery 1 of this example.
(実施例2)
界面活性剤としポリオキシエチレンアルキルエーテル1重量部に対して増粘剤としてカルボキシメチルセルロースを1重量部に対して水99重量部に溶解した水溶液30重量部を配合し、22℃に加温する以外は、実施例1と全く同様の条件で作製した正極用ペーストを本実施例2のペースト2、これを用いて作成された正極板を本実施例2の極板2とし、これを用いた電池を本実施例2の電池2とした。
(Example 2)
Other than blending 30 parts by weight of an aqueous solution in which 99 parts by weight of water is dissolved in 99 parts by weight of water with respect to 1 part by weight of carboxymethyl cellulose as a thickener with respect to 1 part by weight of polyoxyethylene alkyl ether as a surfactant, and heating to 22 ° C The positive electrode paste produced under exactly the same conditions as in Example 1 was used as paste 2 in this Example 2, and the positive electrode plate produced using this paste was used as the electrode plate 2 in this Example 2, and a battery using this. Was used as the battery 2 of Example 2.
(実施例3)
界面活性剤としポリオキシエチレンアルキルエーテル1重量部に対して増粘剤としてカルボキシメチルセルロースを1重量部に対して水99重量部に溶解した水溶液30重量部を配合し、48℃に加温する以外は、実施例1と全く同様の条件で作製した正極用ペーストを本実施例3のペースト3、これを用いて作成され正極板を本実施例3の極板3とし、これを用いた電池を本実施例3の電池3とした。
(Example 3)
Other than blending 30 parts by weight of an aqueous solution in which 99 parts by weight of water is dissolved in 99 parts by weight of water with respect to 1 part by weight of carboxymethyl cellulose as a thickener, 1 part by weight of polyoxyethylene alkyl ether as a surfactant, and heating to 48 ° C Is a paste for positive electrode produced under the same conditions as in Example 1 and paste 3 of Example 3, and a positive electrode plate prepared using this paste is used as electrode plate 3 of Example 3, and a battery using this is used. The battery 3 of Example 3 was obtained.
(比較例1)
界面活性剤であるポリオキシエチレンアルキルエーテルを投入しなかった以外は、実施例1と全く同様の条件で作製した正極用ペーストを本比較例1のペースト1、このペーストを用いて作成した正極板を比較例1の極板1とし、これを用いた電池を本比較例1の電池1とした。
(Comparative Example 1)
A positive electrode paste prepared by using the paste 1 of this comparative example 1, this positive electrode paste prepared under exactly the same conditions as in Example 1 except that the surfactant polyoxyethylene alkyl ether was not added. Was the electrode plate 1 of Comparative Example 1, and the battery using this was the battery 1 of Comparative Example 1.
(比較例2)
界面活性剤としポリオキシエチレンアルキルエーテル1重量部に対して増粘剤としてカルボキシメチルセルロースを1重量部に対して水99重量部に溶解した水溶液30重量部を配合し、10℃にする以外は、実施例1と全く同様の条件で作製した正極用ペーストを
本比較例2のペースト2、このペーストを用いて作成した正極板を本比較例2の極板2とし、これを用いた電池を本比較例2の電池2とした。
(Comparative Example 2)
Except for blending 30 parts by weight of an aqueous solution in which 99 parts by weight of water is dissolved in 99 parts by weight of water with respect to 1 part by weight of carboxymethylcellulose as a thickener with respect to 1 part by weight of polyoxyethylene alkyl ether as a surfactant, The positive electrode paste produced under exactly the same conditions as in Example 1 was used as Paste 2 in this Comparative Example 2, and the positive electrode plate produced using this paste was used as the Electrode 2 in this Comparative Example 2, and a battery using this was used. The battery 2 of Comparative Example 2 was obtained.
(比較例3)
界面活性剤としポリオキシエチレンアルキルエーテル1重量部に対して増粘剤としてカルボキシメチルセルロースを1重量部に対して水99重量部に溶解した水溶液30重量部を配合し、60℃に加温する以外は、実施例1と全く同様の条件で作製した正極用ペーストを本比較例3のペースト3、このペーストを用いて作製した正極板を本比較例3の極板3とし、これを用いた電池を本比較例2の電池2とした。
(Comparative Example 3)
Other than blending 30 parts by weight of an aqueous solution in which 99 parts by weight of water is dissolved in 99 parts by weight of water with respect to 1 part by weight of carboxymethylcellulose as a thickener with respect to 1 part by weight of polyoxyethylene alkyl ether as a surfactant, and heating to 60 ° C The positive electrode paste produced under exactly the same conditions as in Example 1 was used as paste 3 of this comparative example 3, and the positive electrode plate produced using this paste was used as the electrode plate 3 of this comparative example 3, and a battery using this. Was designated as Battery 2 of Comparative Example 2.
(評価)
上記本実施例1、2、3及び比較例1、2、3で得られた正極用ペーストを下記に示すように評価した。
(Evaluation)
The positive electrode pastes obtained in Examples 1, 2, and 3 and Comparative Examples 1, 2, and 3 were evaluated as shown below.
(正極用ペーストの粘度評価)
正極用ペーストを200ccの容器に100g入れペースト作製日から3日間放置し、作製当日及び1日おきに3日間B型粘度計(東機産業株式会社製)にてペースト粘度を測定した。測定条件は○号ロータを用いて○rpmで測定した。その結果を表1に示した。
(Viscosity evaluation of positive electrode paste)
100 g of the positive electrode paste was put in a 200 cc container and allowed to stand for 3 days from the date of paste preparation, and the paste viscosity was measured with a B-type viscometer (manufactured by Toki Sangyo Co., Ltd.) for 3 days from the date of preparation and every other day. The measurement conditions were measured at ○ rpm using a ○ rotor. The results are shown in Table 1.
界面活性剤の分散が不十分な場合、結着剤や導電材の偏析が生じることにより正極用ペースト内で沈降が発生するため、溶媒分だけが上澄みとなるため粘度が著しく低下する。 When the dispersion of the surfactant is insufficient, the binder and the conductive material are segregated, so that sedimentation occurs in the positive electrode paste, so that only the solvent component becomes a supernatant and the viscosity is remarkably lowered.
また正極用ペーストが高温になると高アルカリとなり増粘剤でカルボキシメチルセルロース分子鎖が切断されることによりペースト粘度が著しく低下する。 Moreover, when the paste for positive electrodes becomes high temperature, it becomes highly alkaline, and the viscosity of the paste is remarkably lowered by cutting the carboxymethyl cellulose molecular chain with a thickener.
表1に示した比較例1,2,3はその状態を顕著に示しており、作製当日から3日間放置の間にペースト粘度の低下が観察される。すなわち、完成ペーストの状態が不安定であり生産性、品質面において課題が大きいと言える。 Comparative Examples 1, 2, and 3 shown in Table 1 show the state remarkably, and a drop in paste viscosity is observed during the period of 3 days from the production date. That is, the state of the finished paste is unstable, and it can be said that there are significant problems in terms of productivity and quality.
一方、本実施例1、2、3はペースト作成当日から3日間放置してもペースト粘度の変化は観察されず、完成ペーストとしての状態は極めて安定しており、生産性、品質面において優れていることが明確である。 On the other hand, in Examples 1, 2, and 3, no change in paste viscosity was observed even when left for 3 days from the day of paste preparation, the state as a finished paste was extremely stable, and excellent in terms of productivity and quality. It is clear that
(正極板の面質評価)
作製した正極板1000cm2の表面に存在する凝集塊、ピンホールを目視により計数し、表2に示した。
(Evaluation of surface quality of positive electrode plate)
Agglomerates and pinholes present on the surface of the produced positive electrode plate 1000 cm 2 were visually counted and are shown in Table 2.
凝集塊は1mm以上の活物質塊様の固まりを不良1としてカウントした。ピンホールは
1mm以上で集電体まで貫通した穴または凹みを不良1としてカウントした。
The agglomerates were counted as defective 1 in the mass of an active material lump of 1 mm or more. The pinhole was 1 mm or more, and a hole or dent penetrating to the current collector was counted as a defect 1.
界面活性剤の分散が不十分な場合、結着剤や導電材の偏析が生じることにより集電体と合剤の密着性が低下し極板脱落が生じる。また正極用ペーストが高温になるとアルミニウム箔の腐食が促進され、箔と活物質との界面で水素ガスが発生しピンホールが発生することで、そこからの極板脱落が生じる。 When the dispersion of the surfactant is insufficient, segregation of the binder and the conductive material occurs, so that the adhesion between the current collector and the mixture is lowered and the electrode plate is dropped. Further, when the paste for the positive electrode becomes high temperature, corrosion of the aluminum foil is promoted, and hydrogen gas is generated at the interface between the foil and the active material to generate pinholes.
表2から明らかなように、本発明の実施例1、2、3では前述したような現象は確認されず、凝集塊やピンホールの発生が面質として優れている。 As is apparent from Table 2, in Examples 1, 2, and 3 of the present invention, the phenomenon as described above was not confirmed, and the generation of aggregates and pinholes was excellent as the surface quality.
一方、比較例1、2、3は凝集塊、ピンホールが多数発生しており極板の面質として著しく劣化している様子が伺え品質的にも課題が大きい。 On the other hand, in Comparative Examples 1, 2, and 3, many agglomerates and pinholes are generated, and it can be seen that the surface quality of the electrode plate is remarkably deteriorated.
もう少し詳細に説明すると、実施例1,2,3のように界面活性剤としポリオキシエチレンアルキルエーテル1重量部に対して増粘剤としてカルボキシメチルセルロースを1重量部に対して水99重量部に溶解した水溶液30重量部を配合する際に所定条件の温度下で混合を行うことによって、界面活性剤を投入しない比較例1や混合時の温度が低い比較例2と比較して十分に分散されているために、結着剤の偏析などが見られないため活物質が箔から脱落したり、あるいは浮き上がったりすることがなく塗着工程の歩留が向上する。 More specifically, as in Examples 1, 2 and 3, carboxymethyl cellulose as a surfactant and 1 part by weight of polyoxyethylene alkyl ether as a surfactant was dissolved in 99 parts by weight of water with respect to 1 part by weight. By mixing 30 parts by weight of the aqueous solution at a predetermined temperature, the mixture is sufficiently dispersed as compared with Comparative Example 1 where no surfactant is added and Comparative Example 2 where the temperature during mixing is low. For this reason, no segregation of the binder is observed, so that the active material does not fall off or rise from the foil, and the yield of the coating process is improved.
一方、比較例3に示すように混合時の温度が高すぎる場合は正極ペーストのアルカリ成分によるアルミニウム箔の腐食が促進され、箔と活物質との界面で水素ガスが発生しピンホールが増加するとともに、活物質が箔から脱落したり、あるいは浮き上がったりすることにより、そこからの亀裂が入り活物質の脱落が発生した。 On the other hand, when the temperature at the time of mixing is too high as shown in Comparative Example 3, corrosion of the aluminum foil by the alkali component of the positive electrode paste is promoted, and hydrogen gas is generated at the interface between the foil and the active material to increase pinholes. At the same time, the active material dropped from the foil or floated up, causing cracks from the active material to fall off.
(サイクル寿命特性評価)
これらの正極板を用いて作製した円筒型リチウムイオン二次電池のサイクル寿命特性の測定結果を図2に示す。
(Cycle life characteristics evaluation)
The measurement result of the cycle life characteristic of the cylindrical lithium ion secondary battery produced using these positive electrode plates is shown in FIG.
図2は本発明の実施例で作製した円筒型リチウムイオン二次電池の容量維持率とサイクル数の関係を示した図であり、サイクル寿命特性を比較したものである。 FIG. 2 is a diagram showing the relationship between the capacity retention rate and the cycle number of the cylindrical lithium ion secondary battery produced in the example of the present invention, and compares the cycle life characteristics.
充電は500mAの定電流で行い、4.1Vになった時点で4.1Vの定電圧充電にきりかえ、合計2時間充電を行った。放電は、20℃720mAで行い、放電電位が3.0Vになった時点で放電を終了し次の充電を開始して、300サイクルの確認を行った。 Charging was performed at a constant current of 500 mA. When the voltage reached 4.1 V, charging was replaced with constant voltage charging of 4.1 V, and charging was performed for a total of 2 hours. Discharge was performed at 20 ° C. and 720 mA. When the discharge potential reached 3.0 V, the discharge was terminated and the next charge was started, and 300 cycles were confirmed.
図2から明らかなように、本実施例1、2、3(図2中の101〜103)の電池は比較例1、2、3(図2中の104〜107)に比べて、充放電を繰り返しても容量の劣化が少なく、サイクル特性に優れていることがわかった。 As is clear from FIG. 2, the batteries of Examples 1, 2, and 3 (101 to 103 in FIG. 2) are charged and discharged compared to Comparative Examples 1, 2, and 3 (104 to 107 in FIG. 2). It was found that there was little deterioration of the capacity even when the process was repeated, and the cycle characteristics were excellent.
これは本実施例の電池は正極ペーストの分散性が改善されたことにより活物質が箔から脱落したり、あるいは浮き上がったりすることがなくなり、正極合剤の集電体との密着性が改良されたために、充放電での合剤の膨張収縮でも、集電体から合剤がはがれにくく、活物質の集電性が保持され電池特性が改善されたと考えられる。 In the battery of this example, the dispersibility of the positive electrode paste was improved, so that the active material was not dropped from the foil or lifted up, and the adhesion of the positive electrode mixture to the current collector was improved. For this reason, it is considered that even when the mixture expands and contracts during charge and discharge, the mixture is difficult to peel off from the current collector, and the current collecting property of the active material is maintained, and the battery characteristics are improved.
本発明によって集電体が露出することがなくなり、正極板の歩留まりが向上する。また、正極板の集電体露出がないため導電性,電池特性も向上するリチウムイオン二次電池が実現できるものである。そのため、ポータブル電気機器の電源等として有用である。 According to the present invention, the current collector is not exposed and the yield of the positive electrode plate is improved. Further, since there is no current collector exposure of the positive electrode plate, a lithium ion secondary battery with improved conductivity and battery characteristics can be realized. Therefore, it is useful as a power source for portable electric devices.
1 封口板
2 絶縁ガスケット
3 正極リード
4 上部絶縁板
5 正極用極板
6 負極用極板
7 セパレータ
8 ケース本体
9 負極リード
10 下部絶縁板
DESCRIPTION OF SYMBOLS 1 Sealing plate 2 Insulation gasket 3 Positive electrode lead 4 Upper insulating plate 5 Positive electrode plate 6 Negative electrode plate 7 Separator 8 Case body 9 Negative electrode lead 10 Lower insulating plate
Claims (2)
The lithium ion secondary battery which comprised the positive electrode plate obtained by the manufacturing method of the positive electrode plate for lithium ion secondary batteries of Claim 1.
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Cited By (3)
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JP2012199025A (en) * | 2011-03-18 | 2012-10-18 | San Nopco Ltd | Dispersion element for nonaqueous electrochemical element, member for nonaqueous electrochemical element fabricated using the dispersion element, and nonaqueous electrochemical element including the member |
JP2014143078A (en) * | 2013-01-24 | 2014-08-07 | Denki Kagaku Kogyo Kk | Electrode slurry |
US10439222B2 (en) | 2014-12-12 | 2019-10-08 | Samsung Sdi Co., Ltd. | Positive electrode composition for rechargeable lithium battery, and positive electrode for rechargeable lithium battery and rechargeable lithium battery including same |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2000260424A (en) * | 1999-03-12 | 2000-09-22 | Asahi Chem Ind Co Ltd | Preserving method of coating liquid |
JP2002151057A (en) * | 2000-11-13 | 2002-05-24 | Matsushita Electric Ind Co Ltd | Manufacturing method of paste for positive electrode of lithium secondary battery |
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2008
- 2008-03-17 JP JP2008067516A patent/JP2009224188A/en active Pending
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JP2000260424A (en) * | 1999-03-12 | 2000-09-22 | Asahi Chem Ind Co Ltd | Preserving method of coating liquid |
JP2002151057A (en) * | 2000-11-13 | 2002-05-24 | Matsushita Electric Ind Co Ltd | Manufacturing method of paste for positive electrode of lithium secondary battery |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012199025A (en) * | 2011-03-18 | 2012-10-18 | San Nopco Ltd | Dispersion element for nonaqueous electrochemical element, member for nonaqueous electrochemical element fabricated using the dispersion element, and nonaqueous electrochemical element including the member |
JP2014143078A (en) * | 2013-01-24 | 2014-08-07 | Denki Kagaku Kogyo Kk | Electrode slurry |
US10439222B2 (en) | 2014-12-12 | 2019-10-08 | Samsung Sdi Co., Ltd. | Positive electrode composition for rechargeable lithium battery, and positive electrode for rechargeable lithium battery and rechargeable lithium battery including same |
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