JP6448352B2 - Positive electrode for alkaline metal-sulfur battery and method for producing secondary battery provided with the same - Google Patents
Positive electrode for alkaline metal-sulfur battery and method for producing secondary battery provided with the same Download PDFInfo
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Description
本明細書に開示された技術は、アルカリ金属−硫黄電池用正極及びこれを備えた二次電池に関する。 The technology disclosed in this specification relates to a positive electrode for an alkali metal-sulfur battery and a secondary battery including the same.
次世代の高容量二次電池の1つとしてアルカリ金属−硫黄二次電池が提案されている。アルカリ金属としてリチウムが用いられる一般的なリチウムイオン二次電池の正極活物質、例えばコバルト酸リチウムの理論容量は274mAh/gである。しかしながら、実際には層状構造の崩壊により可逆性を失うため、可逆容量は160mAh/g程度となっている。これに対し、硫黄活物質の理論容量は1675mAh/gと極めて大きいため、アルカリ金属−硫黄二次電池は次世代を担う高容量、高エネルギー密度二次電池として有望視されている。 Alkali metal-sulfur secondary batteries have been proposed as one of the next generation high capacity secondary batteries. A theoretical capacity of a positive electrode active material of a general lithium ion secondary battery in which lithium is used as an alkali metal, for example, lithium cobaltate is 274 mAh / g. However, since the reversibility is actually lost due to the collapse of the layered structure, the reversible capacity is about 160 mAh / g. On the other hand, since the theoretical capacity of the sulfur active material is as extremely large as 1675 mAh / g, the alkali metal-sulfur secondary battery is regarded as promising as a high capacity, high energy density secondary battery for the next generation.
しかしながら、アルカリ金属−硫黄二次電池では、絶縁物である硫黄を正極に用いるため、正極での電気抵抗が高くなり、正極層に多量の導電性物質の添加が必要となる。そのため、正極層内の硫黄量を高くすることが難しいとされている(非特許文献1参照)。 However, in an alkali metal-sulfur secondary battery, since sulfur, which is an insulator, is used for the positive electrode, the electrical resistance at the positive electrode is increased, and a large amount of a conductive material needs to be added to the positive electrode layer. Therefore, it is difficult to increase the amount of sulfur in the positive electrode layer (see Non-Patent Document 1).
また、硫黄の導入量や分布の違い等により電池特性が大きく変わるため、正極に効果的且つ容易に硫黄を導入するための方法が種々検討されている。例えば、特許文献1には、硫黄を二硫化炭素等の溶媒に溶解し、前処理した正極材料に含浸させることで正極層に硫黄を導入する方法が記載されている。また、昇華させた硫黄を高圧力下で正極の材料である多孔質の炭素に導入する方法(特許文献2参照)や、炭素材料上に硫黄顆粒や硫黄微粒子を撒布して加熱することで炭素材料に硫黄を導入する方法(特許文献3、4参照)などが検討されている。この他に、特許文献5には、表面が硫黄膜で被覆された導電性炭素材料が記載され、非特許文献2にも、炭素材料に硫黄を導入する方法が記載されている。 In addition, since battery characteristics vary greatly due to differences in the amount and distribution of sulfur, various methods for effectively and easily introducing sulfur into the positive electrode have been studied. For example, Patent Document 1 describes a method of introducing sulfur into a positive electrode layer by dissolving sulfur in a solvent such as carbon disulfide and impregnating a pretreated positive electrode material. In addition, a method of introducing sublimated sulfur into porous carbon, which is a positive electrode material, under high pressure (see Patent Document 2), or by dispersing and heating sulfur granules and sulfur fine particles on a carbon material. A method of introducing sulfur into the material (see Patent Documents 3 and 4) and the like has been studied. In addition, Patent Document 5 describes a conductive carbon material whose surface is coated with a sulfur film, and Non-Patent Document 2 also describes a method of introducing sulfur into the carbon material.
しかしながら、いずれの文献に記載された方法も、硫黄の導入量の制御や方法自体の実施に手間が掛かるという問題がある。 However, the methods described in any of the documents have a problem that it takes time and effort to control the amount of sulfur introduced and to carry out the method itself.
一方で、硫黄の導入量を高めても導電性を保つことができる多孔質カーボンや、カーボンナノチューブ(CNT)電極のような空隙率の高い材料が正極層内に利用されてきており(特許文献3〜5参照)、正極への硫黄の導入量が増えても導電性を保つことが可能になってきている。しかし、特許文献1〜5に記載された方法を用いてCNT電極への硫黄の導入量を増やす場合、導入処理の回数が増え、処理に長時間を要したり、硫黄がCNT表面に偏在して良好な電池特性を得ることができないといった不具合が生じた。 On the other hand, porous carbon that can maintain conductivity even when the amount of sulfur introduced is increased, and a material having a high porosity such as a carbon nanotube (CNT) electrode has been used in the positive electrode layer (Patent Literature). 3-5), it has become possible to maintain conductivity even if the amount of sulfur introduced into the positive electrode increases. However, when the amount of sulfur introduced into the CNT electrode is increased using the methods described in Patent Documents 1 to 5, the number of introduction treatments increases, and it takes a long time for the treatment, or sulfur is unevenly distributed on the CNT surface. Thus, there is a problem that good battery characteristics cannot be obtained.
本発明は、上記課題に鑑みて、制御性良く、短時間に多くの硫黄を正極層内に導入できる方法と、硫黄活物質本来の高い容量を発揮させることができるアルカリ金属−硫黄電池用正極とを提供することを目的とする。 In view of the above problems, the present invention provides a method capable of introducing a large amount of sulfur into the positive electrode layer in a short time with good controllability, and a positive electrode for an alkali metal-sulfur battery capable of exhibiting the inherent high capacity of the sulfur active material. The purpose is to provide.
本明細書に開示されたアルカリ金属−硫黄電池用正極は、複数の導電材で構成され、前記複数の導電材間に形成された空隙を有する多孔性導電材層と、前記多孔性導電材層の前記空隙内に保持された硫黄と、前記多孔性導電材層の少なくとも一部に直接載置された樹脂フィルムとを備えている。 A positive electrode for an alkali metal-sulfur battery disclosed in the present specification is composed of a plurality of conductive materials, a porous conductive material layer having voids formed between the plurality of conductive materials, and the porous conductive material layer And sulfur held in the gap, and a resin film placed directly on at least a part of the porous conductive material layer.
また、本明細書に開示されたリチウム−硫黄二次電池は、上述のアルカリ金属−硫黄電池用正極と、リチウムイオンを吸蔵及び放出する材料を含む負極と、前記アルカリ金属−硫黄電池用正極と前記負極との間に満たされた、リチウムイオン伝導性を持つ電解液と、前記電解液中で前記金属硫黄電池用正極と前記負極との間を絶縁するセパレータとを備えている。 Moreover, the lithium-sulfur secondary battery disclosed in the present specification includes the above-described alkali metal-sulfur battery positive electrode, a negative electrode including a material that absorbs and releases lithium ions, and the alkali metal-sulfur battery positive electrode. An electrolytic solution filled with the negative electrode and having lithium ion conductivity, and a separator for insulating between the positive electrode for metal sulfur battery and the negative electrode in the electrolytic solution are provided.
また、本明細書に開示されたアルカリ金属−硫黄電池用正極の製造方法は、複数の導電材で構成され、前記複数の導電材間に空隙を有する多孔性導電材層が上面に形成された集電体を準備する工程と、前記多孔性導電材層の少なくとも一部上に硫黄を含む樹脂フィルムを直接載置する工程と、前記樹脂フィルムに含まれる硫黄を前記多孔性導電材層中に挿入させる工程とを備えている。 In addition, the method for producing a positive electrode for an alkali metal-sulfur battery disclosed in the present specification is composed of a plurality of conductive materials, and a porous conductive material layer having voids between the plurality of conductive materials is formed on the upper surface. A step of preparing a current collector, a step of directly placing a resin film containing sulfur on at least a part of the porous conductive material layer, and sulfur contained in the resin film in the porous conductive material layer And a step of inserting.
本明細書に開示された方法によれば、制御性良く、短時間に多くの硫黄を均一に正極層内に導入し得るので、硫黄本来の高い容量を発揮できるアルカリ金属−硫黄電池用正極を提供することができる。 According to the method disclosed in the present specification, since a large amount of sulfur can be uniformly introduced into the positive electrode layer in a short time with good controllability, an alkaline metal-sulfur battery positive electrode capable of exhibiting a high capacity inherent in sulfur is obtained. Can be provided.
−アルカリ金属−硫黄二次電池及び正極層の構成−
図1は、本明細書に開示された実施形態に係る正極を備えたアルカリ金属−硫黄二次電池の概略構成を示す断面図である。同図は、アルカリ金属−硫黄二次電池の一例としてリチウム−硫黄二次電池1を示している。なお、本明細書では、便宜上後述する樹脂フィルム5も正極層3の一部であるとして説明する。
-Configuration of alkali metal-sulfur secondary battery and positive electrode layer-
FIG. 1 is a cross-sectional view illustrating a schematic configuration of an alkali metal-sulfur secondary battery including a positive electrode according to an embodiment disclosed in the present specification. FIG. 1 shows a lithium-sulfur secondary battery 1 as an example of an alkali metal-sulfur secondary battery. In the present specification, the resin film 5 described later is also described as a part of the positive electrode layer 3 for convenience.
本実施形態に係るリチウム−硫黄二次電池1は、正極(正極層)3と、リチウムイオンを吸蔵放出する材料を含む負極(負極層)15と、正極層3と負極層15との間に満たされた、リチウムイオン伝導性を持つ電解液17と、電解液17中で正極層3と負極層15との間を絶縁させるセパレータ13とを備えている。 A lithium-sulfur secondary battery 1 according to this embodiment includes a positive electrode (positive electrode layer) 3, a negative electrode (negative electrode layer) 15 containing a material that absorbs and releases lithium ions, and a positive electrode layer 3 and a negative electrode layer 15. A filled electrolytic solution 17 having lithium ion conductivity and a separator 13 that insulates between the positive electrode layer 3 and the negative electrode layer 15 in the electrolytic solution 17 are provided.
また、本実施形態の正極層3は、上面(平面)を有する集電体11と、複数の導電材10で構成され、集電体11の上面(平面)上に形成された多孔性導電材層7と、多孔性導電材層7内に保持された硫黄9と、多孔性導電材層7の少なくとも一部上に直接載置された樹脂フィルム5とを有している。多孔性導電材層7では、複数の導電材10間に多数の空隙が形成されるように当該複数の導電材10が配置されている。なお、本明細書では、集電体11の面のうち、負極層15に対向する面を便宜上「上面」というものとする。 In addition, the positive electrode layer 3 of the present embodiment includes a current collector 11 having an upper surface (planar) and a plurality of conductive materials 10, and a porous conductive material formed on the upper surface (planar) of the current collector 11. It has a layer 7, sulfur 9 held in the porous conductive material layer 7, and a resin film 5 placed directly on at least a part of the porous conductive material layer 7. In the porous conductive material layer 7, the plurality of conductive materials 10 are arranged so that a large number of voids are formed between the plurality of conductive materials 10. In the present specification, the surface of the current collector 11 that faces the negative electrode layer 15 is referred to as an “upper surface” for convenience.
集電体11は、金属等で構成された一般的なものであってよいが、例えばニッケル(Ni)からなる金属箔上に下地膜としてのアルミニウム(Al)膜と、導電材10を成長させる際の触媒層としての鉄(Fe)膜、Ni膜、コバルト(Co)膜のいずれかとを順次形成させたものであってもよい。集電体11の形状は特に限定されないが、図1に示す例では平坦な上面及び下面を有し、所定の平面形状を有する箔状となっている。 The current collector 11 may be a general one made of metal or the like. For example, an aluminum (Al) film as a base film and a conductive material 10 are grown on a metal foil made of nickel (Ni), for example. Any one of an iron (Fe) film, a Ni film, and a cobalt (Co) film may be sequentially formed as the catalyst layer. The shape of the current collector 11 is not particularly limited, but in the example illustrated in FIG. 1, the current collector 11 has a flat upper surface and a lower surface, and has a foil shape having a predetermined planar shape.
導電材10は、硫黄9を保持できる材料、例えば多孔性カーボンであればよいが、カーボンナノチューブ(CNT)であれば導電材10間の空隙に多くの硫黄9を保持しても導電性を確保し得るので好ましく、導電材10がCNTである場合、複数のCNTが集電体11の上面(平面)に対して垂直に配向することで、CNTと集電体11とが直接導通して高い導電性を保持できる。これまで一般的には、導電性カーボンと硫黄にバインダを加えて正極層を作製していたが、バインダにより電気抵抗が上がり、また界面のイオンパスも妨げられる。これに対し、垂直配向のCNTと硫黄とを含む正極層では、バインダを加えなくてもCNT間の空隙に硫黄を導入することが可能となるので、イオン伝導性と導電性の両方を高くすることが可能となる。 The conductive material 10 may be a material that can hold sulfur 9, for example, porous carbon, but if it is a carbon nanotube (CNT), conductivity is ensured even if a large amount of sulfur 9 is held in the gap between the conductive materials 10. Therefore, when the conductive material 10 is CNT, the plurality of CNTs are oriented perpendicularly to the upper surface (plane) of the current collector 11, so that the CNT and the current collector 11 are directly conducted and are high. Conductivity can be maintained. Conventionally, a positive electrode layer has been generally produced by adding a binder to conductive carbon and sulfur. However, the binder increases the electrical resistance and prevents the ion path at the interface. On the other hand, in the positive electrode layer containing vertically aligned CNT and sulfur, it is possible to introduce sulfur into the gap between CNTs without adding a binder, so that both ion conductivity and conductivity are increased. It becomes possible.
この構成により、後述する正極層3の作製時に、樹脂フィルム5から多孔性導電材層7へと挿入する硫黄9をCNT内の空隙に保持しやすくできる。 With this configuration, the sulfur 9 inserted from the resin film 5 into the porous conductive material layer 7 can be easily held in the voids in the CNT when the positive electrode layer 3 described later is manufactured.
多孔性導電材層7において、導電材(CNT)10の密度は、例えば1×108/cm2以上1×1012/cm2以下であってもよい。CNTの長さは、例えば100μm以上1000μm以下であってもよい。この構成によれば、CNT同士を適度な間隔及び長さで配置させることができるので、多孔性導電材層7内にリチウムイオンを含む電解液17を浸透させやすくなっているとともに、樹脂フィルム5から多孔性導電材層7へと挿入する硫黄9をCNT内に速やかに導入できることで、イオンパスと導電パスとを併存させ、硫黄活物質量を増やしても十分な電気化学的酸化還元反応が進行する。 In the porous conductive material layer 7, the density of the conductive material (CNT) 10 may be, for example, 1 × 10 8 / cm 2 or more and 1 × 10 12 / cm 2 or less. The length of the CNT may be, for example, 100 μm or more and 1000 μm or less. According to this configuration, since the CNTs can be arranged at an appropriate interval and length, the electrolytic solution 17 containing lithium ions can be easily infiltrated into the porous conductive material layer 7, and the resin film 5 Sulfur 9 to be inserted into the porous conductive material layer 7 can be quickly introduced into the CNT, so that sufficient electrochemical oxidation-reduction reaction proceeds even if the ion path and the conductive path coexist and the amount of the sulfur active material is increased. To do.
なお、多孔性導電材層7は、ポリエチレンオキシド(PEO)、ポリビニルピロリドン(PVP)、ポリビニルアセテート(PVAc)又はポリテトラフルオロエチレン(PTFE)等の樹脂成分や、分散剤及びレベリング剤等の添加剤を含んでいてもよい。後述する多孔性導電材層7への硫黄導入工程において、樹脂フィルム5が分散剤や添加剤を含んでいる場合、分散剤や添加剤も多孔性導電材層7へと導入され得る。 The porous conductive material layer 7 is made of resin components such as polyethylene oxide (PEO), polyvinyl pyrrolidone (PVP), polyvinyl acetate (PVAc) or polytetrafluoroethylene (PTFE), and additives such as dispersants and leveling agents. May be included. In the step of introducing sulfur into the porous conductive material layer 7 to be described later, when the resin film 5 contains a dispersant or additive, the dispersant or additive can also be introduced into the porous conductive material layer 7.
樹脂フィルム5は電解液17に不溶またはわずかに可溶で、硫黄9を含む電池内材料や、充放電時に新たに生成するポリスルフィド等の化合物と化学反応しない樹脂で構成されていればよく、例えばポリエチレンオキシド(PEO)、ポリビニルピロリドン(PVP)、ポリビニルアセテート(PVAc)又はポリテトラフルオロエチレン(PTFE)等で構成されていてもよい。この中で、PEOを樹脂フィルム5の構成材料として用いれば、正極層3の作製時に、樹脂フィルム5に含まれた硫黄9を容易且つ作業性良く多孔性導電材層7に挿入させることができ、硫黄が抜けた後に樹脂フィルム5のイオン伝導性を損ねることがないため、好ましい。 The resin film 5 may be made of a resin that is insoluble or slightly soluble in the electrolytic solution 17 and that does not chemically react with the in-battery material containing sulfur 9 or a compound such as polysulfide newly generated during charge and discharge. It may be composed of polyethylene oxide (PEO), polyvinyl pyrrolidone (PVP), polyvinyl acetate (PVAc), polytetrafluoroethylene (PTFE), or the like. Among these, if PEO is used as a constituent material of the resin film 5, the sulfur 9 contained in the resin film 5 can be easily and easily inserted into the porous conductive material layer 7 when the positive electrode layer 3 is produced. It is preferable because the ion conductivity of the resin film 5 is not impaired after sulfur is released.
なお、樹脂フィルム5の膜厚は特に限定されないが、例えば正極層3の作製時において50μm以上500μm以下程度であってもよい。樹脂フィルム5の膜厚を厚くし過ぎると樹脂フィルム5から多孔性導電材層7への硫黄9の移動がしにくくなる。 The film thickness of the resin film 5 is not particularly limited, but may be, for example, about 50 μm or more and 500 μm or less when the positive electrode layer 3 is manufactured. If the film thickness of the resin film 5 is excessively increased, it is difficult for the sulfur 9 to move from the resin film 5 to the porous conductive material layer 7.
導電材10としてCNTを用いる場合、充放電前の多孔性導電材層7中の単位面積当たりの硫黄原子としての密度が5mg/cm2以上であれば、硫黄9が持つ容量の大きさを十分に生かすことができるのでより好ましい。また、充電前のリチウム−硫黄二次電池1において硫黄が正極層3にしか含まれていない場合、多孔性導電材層7の単位面積当たりの「リチウム−硫黄二次電池1全体に含まれる硫黄及び硫黄化合物中の硫黄原子の総量」が、5mg/cm2以上であれば好ましい。 When CNT is used as the conductive material 10, the capacity of the sulfur 9 is sufficient if the density as sulfur atoms per unit area in the porous conductive material layer 7 before charging and discharging is 5 mg / cm 2 or more. It is more preferable because it can be utilized in the future. Further, in the case where sulfur is contained only in the positive electrode layer 3 in the lithium-sulfur secondary battery 1 before charging, “sulfur contained in the entire lithium-sulfur secondary battery 1 per unit area of the porous conductive material layer 7. And “the total amount of sulfur atoms in the sulfur compound” is preferably 5 mg / cm 2 or more.
なお、CNT層(多孔性導電材層7)には十分な空隙が存在するので、硫黄9の導入量が高くなっても正極層3の導電性を保持することが可能になっている。多孔性導電材層7全体の占有体積を100vol%とする場合、多孔性導電材層7の空隙率(空間が占める割合)が60vol%以上であれば硫黄9の保持量が多い場合でも正極層3の電気抵抗値が上昇しにくいので、好ましい。 Since the CNT layer (porous conductive material layer 7) has sufficient voids, the conductivity of the positive electrode layer 3 can be maintained even when the amount of sulfur 9 introduced is high. When the occupied volume of the entire porous conductive material layer 7 is set to 100 vol%, the positive electrode layer can be used even if the retained amount of sulfur 9 is large as long as the porosity (ratio occupied by the space) of the porous conductive material layer 7 is 60 vol% or more. 3 is preferable because the electrical resistance value of 3 is difficult to increase.
リチウム−硫黄二次電池1において、多孔性導電材層7内の硫黄9の多くは単体の硫黄であるが、樹脂フィルム5から導入された硫黄の一部は多硫アニオン(Sx2−)等の形で電解液17中に溶け出している。また、多孔性導電材層7中で導電材10内に保持された硫黄9の少なくとも一部は、界面活性剤、高分子系顔料、シリコーン系樹脂等の表面処理剤を含む有機成分で修飾されていてもよい。この場合、硫黄9中の有機成分の濃度は0.1重量%以上10重量%以下であってもよい。 In the lithium-sulfur secondary battery 1, most of the sulfur 9 in the porous conductive material layer 7 is simple sulfur, but part of the sulfur introduced from the resin film 5 is polysulfur anion (Sx 2− ) or the like. It is dissolved in the electrolytic solution 17 in the form of In addition, at least a part of the sulfur 9 retained in the conductive material 10 in the porous conductive material layer 7 is modified with an organic component containing a surface treatment agent such as a surfactant, a polymer pigment, or a silicone resin. It may be. In this case, the concentration of the organic component in the sulfur 9 may be 0.1 wt% or more and 10 wt% or less.
このように、適切な量の有機成分で硫黄9が修飾されていることにより、正極層3の作製時に樹脂フィルム5中の硫黄9の分散性が向上し、硫黄9を効果的に多孔性導電材層7へと挿入させることができる。 As described above, the sulfur 9 is modified with an appropriate amount of organic components, so that the dispersibility of the sulfur 9 in the resin film 5 is improved during the production of the positive electrode layer 3, and the sulfur 9 is effectively made porous conductive. It can be inserted into the material layer 7.
樹脂フィルム5の質量は、多孔性導電材層7に導入された硫黄9の質量(=充放電前の多孔性導電材層7に含まれる硫黄9の質量)に対して15%未満であれば、より好ましい。樹脂フィルム5の質量をこの範囲にすることにより、樹脂フィルム5から多孔性導電材層7へと硫黄9を挿入させる際に、樹脂フィルム5に捕捉され、樹脂フィルム5内に残留する硫黄9の量を低減することができる。 If the mass of the resin film 5 is less than 15% with respect to the mass of sulfur 9 introduced into the porous conductive material layer 7 (= the mass of sulfur 9 contained in the porous conductive material layer 7 before charging and discharging). More preferable. By making the mass of the resin film 5 within this range, when the sulfur 9 is inserted from the resin film 5 into the porous conductive material layer 7, the sulfur 9 that is captured by the resin film 5 and remains in the resin film 5. The amount can be reduced.
なお、充放電後には硫黄9の一部は正極層3から電解液17中に溶け出すので、樹脂フィルム5の質量は「充放電後のリチウム−硫黄二次電池1全体に含まれる、硫黄及び硫黄化合物の硫黄原子の総量」の15%未満であれば好ましいといえる。 In addition, since a part of sulfur 9 melts into the electrolyte solution 17 from the positive electrode layer 3 after charging / discharging, the mass of the resin film 5 is “sulfur and lithium contained in the entire lithium-sulfur secondary battery 1 after charging / discharging”. If it is less than 15% of the “total amount of sulfur atoms of the sulfur compound”, it can be said to be preferable.
本実施形態のリチウム硫黄二次電池1において、負極層15としては、リチウムイオン二次電池やリチウム硫黄二次電池の負極として一般的なものを用いることができる。具体的には、負極層15の材料として、例えば、Li、LiとAlもしくはIn等との合金、又は、リチウムイオンをドープしたSi、SiO、Sn、SnO2もしくはハードカーボン等を用いることができる。 In the lithium-sulfur secondary battery 1 of the present embodiment, as the negative electrode layer 15, a general one can be used as the negative electrode of a lithium ion secondary battery or a lithium sulfur secondary battery. Specifically, as the material of the negative electrode layer 15, for example, an alloy of Li, Li and Al or In, or Si, SiO, Sn, SnO 2 or hard carbon doped with lithium ions can be used. .
電解液17としては、例えば、テトラヒドロフラン、グライム、ジグライム、トリグライム、テトラグライムなどのエーテル系電解液、ジエチルカーボネート、プロピレンカーボネートなどのエステル系電解液のうちから選択された少なくとも1種、又は、これらのうちから選択された少なくとも1種(例えばグライム、ジグライムもしくはテトラグライム)に粘度調整のためのジオキソランを混合したものを用いることができる。 As the electrolytic solution 17, for example, at least one selected from ether-based electrolytic solutions such as tetrahydrofuran, glyme, diglyme, triglyme and tetraglyme, and ester-based electrolytic solutions such as diethyl carbonate and propylene carbonate, or these A mixture of at least one selected from among them (for example, glyme, diglyme or tetraglyme) with dioxolane for viscosity adjustment can be used.
セパレータ13としては、リチウムイオン二次電池やリチウム−硫黄二次電池のセパレータとして公知のものを用いることができる。例えば、セパレータ13は、ポリテトラフルオロエチレン、ポリプロピレン、ポリエチレンなどの合成樹脂製の多孔質膜、あるいは、セラミック製の多孔質膜により構成され、これらの2種以上の多孔質膜を積層した構造を有するものであってもよい。これらの中で、ポリオレフィン製の多孔質膜は短絡防止効果に優れているだけでなく、シャットダウン効果(過大電流が流れた時に空孔が閉鎖し、電流を閉鎖する効果)による電池の安全性向上を図ることができるので好ましい。 As the separator 13, a well-known thing can be used as a separator of a lithium ion secondary battery or a lithium-sulfur secondary battery. For example, the separator 13 is composed of a porous film made of synthetic resin such as polytetrafluoroethylene, polypropylene, or polyethylene, or a porous film made of ceramic, and has a structure in which two or more kinds of these porous films are laminated. You may have. Among these, the porous film made of polyolefin not only has an excellent short-circuit prevention effect, but also improves the safety of the battery by the shutdown effect (the effect of closing the vacancies and closing the current when an excessive current flows). This is preferable.
以上の構成を有するリチウム−硫黄二次電池1では、負極層15を金属リチウムで構成した場合、充電時にはLi2S等の硫黄活物質からの放電生成物が、正極で下記式(1)の通り
8Li2S → 16Li+ + S8 + 16e− ・・・(1)
の酸化反応が起こり、電解液17中にLi+が放出される。Li+はセパレータ13を介して負極に移動し、負極界面でLi+が下記式(2)の反応により酸化されることで充電される。
In the lithium-sulfur secondary battery 1 having the above configuration, when the negative electrode layer 15 is made of metallic lithium, a discharge product from a sulfur active material such as Li 2 S is charged at the positive electrode according to the following formula (1). Street 8Li 2 S → 16Li + + S 8 + 16e − (1)
Oxidation reaction occurs, and Li + is released into the electrolytic solution 17. Li + via separator 13 to move to the negative electrode, the negative electrode interface Li + is charged by being oxidized by the following reaction formula (2).
Li+ + e− → Li ・・・(2)
また、放電時には、充電時と逆の反応によりリチウム硫黄二次電池1の外部へと電流を取り出すことができる。
Li + + e − → Li (2)
Moreover, at the time of discharge, an electric current can be taken out of the lithium sulfur secondary battery 1 by a reaction reverse to that at the time of charging.
−正極層3の製造方法−
図2は、図1に示す本実施形態に係る正極層3の製造工程を示すフローチャート図である。
-Manufacturing method of positive electrode layer 3-
FIG. 2 is a flowchart showing manufacturing steps of the positive electrode layer 3 according to this embodiment shown in FIG.
同図に示すように、本実施形態に係る正極層3を作製する際には、まず単体の硫黄(例えば斜方硫黄S8)を含む樹脂フィルム5を作製する(ステップS1)。具体的には、単体の硫黄と所定の分子量を有する樹脂と有機溶媒とを容器中で攪拌した後、ボールミリング等により淡黄色のスラリーを作製する。次いで、このスラリーを樹脂シート等に塗布した後、乾燥して溶媒を除去し、樹脂シートからの剥離を行って、硫黄を含む所定の形状の樹脂フィルム5を形成する。なお、本工程で形成される樹脂フィルムは、樹脂と化学反応しない状態で硫黄を包含する硫黄と樹脂の混合フィルム(硫黄/樹脂シート)であり、所定の膜厚を有する。 As shown in the figure, when producing the positive electrode layer 3 according to the present embodiment, first, a resin film 5 containing simple sulfur (for example, orthorhombic sulfur S 8 ) is produced (step S1). Specifically, simple sulfur, a resin having a predetermined molecular weight, and an organic solvent are stirred in a container, and then a light yellow slurry is prepared by ball milling or the like. Next, after applying this slurry to a resin sheet or the like, drying is performed to remove the solvent, and peeling from the resin sheet is performed to form a resin film 5 having a predetermined shape containing sulfur. In addition, the resin film formed at this process is a mixed film (sulfur / resin sheet) of sulfur and resin including sulfur in a state that does not chemically react with the resin, and has a predetermined film thickness.
本工程では、スラリーを作製する際に加える樹脂の質量は特に限定されないが、スラリーに加える樹脂の質量を硫黄の質量の15%未満とすると、後の工程で樹脂フィルム5から多孔性導電材層7へと効率良く硫黄を移動させることができるので、好ましい。 In this step, the mass of the resin added when preparing the slurry is not particularly limited, but if the mass of the resin added to the slurry is less than 15% of the mass of sulfur, the porous conductive material layer is formed from the resin film 5 in a later step. This is preferable because sulfur can be efficiently transferred to 7.
本工程で用いる硫黄は、無修飾の単体硫黄であってもよいし、例えば硫黄全体に対して0.1重量%以上10重量%以下程度の量の有機成分で一部又は全体が修飾された硫黄であってもよい。有機成分で修飾されている硫黄を用いることで、スラリー中の硫黄の分散性を向上させ、均一に硫黄を含む樹脂フィルム5を作製しやすくできる。 The sulfur used in this step may be unmodified simple sulfur, for example, partially or entirely modified with an organic component in an amount of about 0.1 wt% to 10 wt% with respect to the total sulfur. Sulfur may be used. By using sulfur modified with an organic component, the dispersibility of sulfur in the slurry can be improved, and the resin film 5 containing sulfur uniformly can be easily produced.
また、樹脂フィルム5の作製とは別に、集電体11の上面に多孔性導電材層7を形成しておく(ステップS2)。具体的には、例えば金属箔等からなる集電体11の上面に厚さが5〜500nmの下地膜と、厚さが0.5〜20nmの触媒層とを順次形成する。下地膜は導電材10(例えばCNT)と集電体11との密着性を向上させるために設けられ、Al、Ti、V、Ta、Mo及びWから選択される少なくとも1種の金属、その金属を含む合金またはその金属の窒化物から構成される。触媒層は、例えば、Ni、FeまたはCoから選択される少なくとも1種の金属、またはそれらの金属を1種類以上含む合金から構成される。 Separately from the production of the resin film 5, the porous conductive material layer 7 is formed on the upper surface of the current collector 11 (step S2). Specifically, a base film having a thickness of 5 to 500 nm and a catalyst layer having a thickness of 0.5 to 20 nm are sequentially formed on the upper surface of the current collector 11 made of, for example, a metal foil. The base film is provided in order to improve the adhesion between the conductive material 10 (for example, CNT) and the current collector 11, and at least one metal selected from Al, Ti, V, Ta, Mo, and W, and the metal It is comprised from the alloy containing this, or the nitride of the metal. The catalyst layer is made of, for example, at least one metal selected from Ni, Fe, or Co, or an alloy containing one or more of these metals.
次いで、集電体11上に触媒層を介して公知の化学気相成長(CVD)法等によりCNT等の導電材10を所定の密度で成長させ、多孔性導電材層7を形成する。本工程でCNTを成長させる場合、集電体11の上面(平面)に対して垂直に配向するようにこのCNTを成長させることができる。この際に、CNTの配向方向には多少のばらつきがあっても許容される。 Next, a conductive material 10 such as CNT is grown at a predetermined density on the current collector 11 through a catalyst layer by a known chemical vapor deposition (CVD) method or the like to form the porous conductive material layer 7. When growing CNTs in this step, the CNTs can be grown so as to be oriented perpendicular to the upper surface (plane) of the current collector 11. At this time, even if there is some variation in the orientation direction of the CNT, it is allowed.
次に、樹脂フィルム5中に含まれる硫黄を多孔性導電材層7に導入する(図2のステップS3)。本工程では、樹脂フィルム5を多孔性導電材層7上に載置及び圧着させてから硫黄が液状になる温度、例えば115℃以上250℃以下程度で加熱する。この加熱温度は、硫黄の粘性が最低となる155℃近傍であれば、硫黄の挿入を速やかに行うことができるので、より好ましい。 Next, sulfur contained in the resin film 5 is introduced into the porous conductive material layer 7 (step S3 in FIG. 2). In this step, the resin film 5 is placed on the porous conductive material layer 7 and pressed and then heated at a temperature at which sulfur becomes liquid, for example, about 115 ° C. or more and 250 ° C. or less. If this heating temperature is around 155 ° C. at which the viscosity of sulfur is the lowest, sulfur can be inserted quickly, which is more preferable.
これにより、樹脂フィルム5中の硫黄が溶融し、毛細管現象によって多孔性導電材層7内の空隙へと挿入される(図1の硫黄9)。本行程は、大気下で行ってもよいし、窒素やアルゴンといった不活性ガスの雰囲気下で行ってもよく、減圧または真空下で行ってもよい。さらには、挿入時に減圧下から大気下に戻すなどの圧力操作を行ってもよい。本工程により、樹脂フィルム5から硫黄分が抜けるので、樹脂フィルム5の内部に多数の孔が形成される。 Thereby, the sulfur in the resin film 5 is melted and inserted into the voids in the porous conductive material layer 7 by capillary action (sulfur 9 in FIG. 1). This process may be performed in air | atmosphere, may be performed in the atmosphere of inert gas, such as nitrogen and argon, and may be performed under reduced pressure or a vacuum. Furthermore, a pressure operation such as returning from the reduced pressure to the atmosphere during insertion may be performed. By this step, sulfur content is removed from the resin film 5, so that a large number of holes are formed inside the resin film 5.
本工程の後、樹脂フィルム5を除去してもよいが、樹脂フィルム5を残すことにより簡単に、図1に示す本実施形態の正極層3を作製することができる。樹脂フィルム5が正極層3に残っていても正極層3リチウム硫黄二次電池1を作製した場合の性能に影響することはほとんどない。また、樹脂フィルム5中の樹脂量が少ないと硫黄9の多孔性導電材層7への導入後に樹脂フィルム5が剥離しにくくなるが、樹脂フィルム5を残すことにより、剥離の手間を省けるとともに樹脂フィルム5中の樹脂の含有率の範囲を広くとることが可能となる。 After this step, the resin film 5 may be removed, but the positive electrode layer 3 of the present embodiment shown in FIG. 1 can be easily produced by leaving the resin film 5. Even if the resin film 5 remains in the positive electrode layer 3, the performance when the positive electrode layer 3 lithium-sulfur secondary battery 1 is produced is hardly affected. In addition, if the amount of resin in the resin film 5 is small, the resin film 5 is difficult to peel off after the sulfur 9 is introduced into the porous conductive material layer 7. The range of the resin content in the film 5 can be widened.
その後、公知の方法により本実施形態の正極層3を用いたリチウム硫黄二次電池1を作製することができる(図2のステップS4)。 Thereafter, the lithium-sulfur secondary battery 1 using the positive electrode layer 3 of the present embodiment can be manufactured by a known method (step S4 in FIG. 2).
本実施形態の方法によれば、樹脂フィルム5中の硫黄の含有量、及び硫黄と樹脂との含有比率を適宜調節することにより、制御性良く短時間に硫黄を多孔性導電材層7に均一に挿入することが可能となる。また、本実施形態の方法を用いれば、硫黄の微粒子を多孔性導電材層7上に直接振りかける方法や、硫黄を昇華させて多孔性導電材層7に導入する方法に比べてより制御性良く、均一に硫黄9を多孔性導電材層7へと導入することができる。 According to the method of the present embodiment, the sulfur content in the resin film 5 and the content ratio of sulfur and resin are adjusted as appropriate, so that sulfur is uniformly distributed in the porous conductive material layer 7 in a short time with good controllability. Can be inserted. Moreover, if the method of this embodiment is used, controllability is better than the method of sprinkling sulfur fine particles directly on the porous conductive material layer 7 or the method of sublimating sulfur and introducing it into the porous conductive material layer 7. The sulfur 9 can be uniformly introduced into the porous conductive material layer 7.
また、一回の硫黄導入工程により多量の硫黄を多孔性導電材層7へと導入することができるため、導入作業を繰り返さなくても、リチウム−硫黄二次電池1が十分に高い容量を発揮できる量の硫黄9を多孔性導電材層7に導入することが可能となる。さらに、硫黄導入前において、樹脂フィルム5中の樹脂含有率を例えば7wt%以上にすることで、硫黄導入後に樹脂フィルム5を剥離しやすくすることができる。 Further, since a large amount of sulfur can be introduced into the porous conductive material layer 7 by a single sulfur introduction step, the lithium-sulfur secondary battery 1 exhibits a sufficiently high capacity without repeating the introduction operation. A possible amount of sulfur 9 can be introduced into the porous conductive material layer 7. Further, by setting the resin content in the resin film 5 to, for example, 7 wt% or more before introducing sulfur, the resin film 5 can be easily peeled after introducing sulfur.
なお、以上で説明した正極層3及びその製造方法、及びリチウム硫黄二次電池1は実施形態の一例であって、各構成要素の材料、形状、スラリーの調製手順等は本発明の趣旨を逸脱しない範囲において適宜変更可能である。 The positive electrode layer 3 and the manufacturing method thereof, and the lithium-sulfur secondary battery 1 described above are examples of the embodiment, and the material, shape, slurry preparation procedure, etc. of each component depart from the spirit of the present invention. It can be changed appropriately within the range not to be.
以下のようにして実施例1〜5及び比較例1〜4に係るアルカリ金属−硫黄電池用正極層と、実施例6に係るリチウム−硫黄二次電池とを作製した。
−実施例1−
厚さ20μmのNiからなる金属箔(集電体)上にCVD法によって平均長さ約350μmのCNTを成長させることで、CNTで構成された多孔性導電材層を形成した。CNTは金属箔の上面に垂直な方向に配向させた。多孔性導電材層中のCNTの密度は1〜5×1010本/cm2であった。以下、金属箔と多孔性導電材層とを合わせたものを「CNT電極」と呼ぶ。
The positive electrode layer for alkali metal-sulfur batteries according to Examples 1 to 5 and Comparative Examples 1 to 4 and the lithium-sulfur secondary battery according to Example 6 were produced as follows.
Example 1
A porous conductive material layer composed of CNTs was formed by growing CNTs having an average length of about 350 μm on a metal foil (current collector) made of Ni having a thickness of 20 μm by a CVD method. The CNTs were oriented in a direction perpendicular to the top surface of the metal foil. The density of CNT in the porous conductive material layer was 1 to 5 × 10 10 pieces / cm 2 . Hereinafter, a combination of a metal foil and a porous conductive material layer is referred to as a “CNT electrode”.
次に、1%の有機成分を修飾した硫黄(商品名:Sulfax PS、鶴見化学工業製)を5.0g、分子量300万のPEOを0.56g、直径2mmのジルコニアビーズ30gをそれぞれ秤量し、これらをポリエチレン容器に入れて撹拌した。このポリエチレン容器にアセトニトリル20gを加えてさらに撹拌した後、90rpmで12時間ボールミリングし、淡黄色の粘調なスラリーを作製した。スラリー中の硫黄の分散性は良好であった。 Next, 5.0 g of sulfur (trade name: Sulfax PS, manufactured by Tsurumi Chemical Co., Ltd.) modified with 1% organic component, 0.56 g of PEO having a molecular weight of 3 million, and 30 g of zirconia beads having a diameter of 2 mm were weighed. These were put in a polyethylene container and stirred. After adding 20 g of acetonitrile to this polyethylene container and further stirring, ball milling was performed at 90 rpm for 12 hours to prepare a pale yellow viscous slurry. The dispersibility of sulfur in the slurry was good.
次いで、ジルコニアビーズをメッシュを用いて除去し、スラリーを離型剤の塗布されたポリエチレンテレフタラート(PET)フィルム上に塗布し、乾燥した。これにより、硫黄を含む樹脂フィルム(硫黄/樹脂シート)を作製した。作製した樹脂フィルムは約100μmの厚みを有し、5mg/cm2の硫黄を含んでいた。作製したCNT電極と平面形状が同じになるよう成形し、樹脂フィルムの塗布面を多孔性導電材層の上面に圧着した。この状態で、約180℃に加熱することで硫黄を溶融させ、毛細管現象によって硫黄をCNT内の空隙へ導入した。硫黄導入後、硫黄の抜けた樹脂フィルムは多孔性導電材層上に残した。 Next, the zirconia beads were removed using a mesh, and the slurry was applied onto a polyethylene terephthalate (PET) film coated with a release agent and dried. Thereby, a resin film containing sulfur (sulfur / resin sheet) was produced. The produced resin film had a thickness of about 100 μm and contained 5 mg / cm 2 of sulfur. It shape | molded so that the produced CNT electrode might become the same planar shape, and the application | coating surface of the resin film was crimped | bonded to the upper surface of the porous conductive material layer. In this state, sulfur was melted by heating to about 180 ° C., and sulfur was introduced into the voids in the CNTs by capillary action. After the introduction of sulfur, the resin film from which sulfur was lost was left on the porous conductive material layer.
実施例1の方法によれば、1回の硫黄導入作業でほぼ全量の硫黄を樹脂フィルムから多孔性導電材層中へと導入させることができた。その結果、作業時間を短くすることができた。 According to the method of Example 1, almost the entire amount of sulfur could be introduced from the resin film into the porous conductive material layer by one sulfur introduction operation. As a result, the working time could be shortened.
また、目視により、実施例1に係る正極の外観は良好であることが確認できた。 Moreover, it has confirmed visually that the external appearance of the positive electrode which concerns on Example 1 is favorable.
−実施例2−
スラリーを作製する際に、有機成分で修飾されていない硫黄(商品名:和光純薬製)を使用した以外は実施例1と同様の方法によってアルカリ金属−硫黄電池用正極を作製した。実施例1に比べてスラリー中の硫黄の分散性は劣るものの、概ね良好な外観の正極を形成することができた。
-Example 2-
A positive electrode for an alkali metal-sulfur battery was prepared in the same manner as in Example 1 except that sulfur not modified with an organic component (trade name: manufactured by Wako Pure Chemical Industries) was used when the slurry was prepared. Although the dispersibility of sulfur in the slurry was inferior to that of Example 1, a positive electrode having a generally good appearance could be formed.
また、実施例2の方法によれば、1回の硫黄導入作業でほぼ全量の硫黄を樹脂フィルムから多孔性導電材層中へと導入させることができた。その結果、作業時間を実施例1と同程度に短時間で済ますことができた。正極の外観は良好であることが確認できた。 Moreover, according to the method of Example 2, it was possible to introduce almost the entire amount of sulfur from the resin film into the porous conductive material layer in one sulfur introduction operation. As a result, the working time could be as short as in Example 1. It was confirmed that the appearance of the positive electrode was good.
−実施例3−
実施例1に対して硫黄導入前の樹脂フィルムにおけるPEOの含有率を半分(樹脂フィルム質量の5wt%)とした。それ以外は実施例1と同様の方法によりアルカリ金属−硫黄電池用正極を作製した。スラリー中の硫黄の分散性は実施例1と同様に良好であった。
Example 3
Compared to Example 1, the PEO content in the resin film before introduction of sulfur was halved (5 wt% of the resin film mass). Otherwise, an alkali metal-sulfur battery positive electrode was produced in the same manner as in Example 1. The dispersibility of sulfur in the slurry was as good as in Example 1.
また、実施例3の方法によれば、1回の硫黄導入作業で大部分の硫黄を樹脂フィルムから多孔性導電材層中へと導入させることができたが、硫黄導入後に樹脂フィルムが一部崩れた状態で多孔性導電材層上に密着しており、導入後の樹脂フィルムが一部不均一にCNT電極の表面に残っていた。本実施例では、作業時間は実施例1と同程度に短くすることができたが、正極の外観は樹脂フィルムが局所的に崩れていたために実施例1に比べるとやや劣っていた。 In addition, according to the method of Example 3, a large part of sulfur could be introduced from the resin film into the porous conductive material layer by one sulfur introduction operation, but the resin film partially after the sulfur introduction. In the collapsed state, it was in close contact with the porous conductive material layer, and the resin film after introduction remained partially uneven on the surface of the CNT electrode. In this example, the working time could be shortened to the same extent as in Example 1, but the appearance of the positive electrode was slightly inferior to that in Example 1 because the resin film was locally broken.
−実施例4−
スラリーを作製する際に有機成分で修飾されていない硫黄を用い、硫黄導入前の樹脂フィルム中の樹脂の量は7wt%とした。また、バインダとなる樹脂として、PEOに代えてPTFEを用いた。スラリー作製の際には有機成分を含む硫黄と、PTFE粉末と、キシレンとを乳鉢で混練し、圧延することで樹脂フィルムを作製した。硫黄の導入は、実施例1と同様の方法により行った。実施例4の方法では、スラリー中の硫黄の分散性は良好であったが、実施例1と比べるとやや劣っていた。
Example 4
When producing the slurry, sulfur not modified with an organic component was used, and the amount of resin in the resin film before introduction of sulfur was 7 wt%. In addition, PTFE was used instead of PEO as the binder resin. At the time of slurry preparation, sulfur containing organic components, PTFE powder, and xylene were kneaded in a mortar and rolled to prepare a resin film. Sulfur was introduced in the same manner as in Example 1. In the method of Example 4, the dispersibility of sulfur in the slurry was good, but was slightly inferior to Example 1.
また、実施例4の方法によれば、硫黄導入作業後、樹脂フィルム中にわずかに硫黄が残存したが、1回の硫黄導入作業で大部分の硫黄を樹脂フィルムから多孔性導電材層中へと導入させることができた。本実施例では、作業時間は実施例1と同程度に短くすることができ、正極の外観も実施例1と同様に良好であった。 Further, according to the method of Example 4, a slight amount of sulfur remained in the resin film after the sulfur introduction work, but most of the sulfur was transferred from the resin film into the porous conductive material layer by one sulfur introduction work. It was possible to introduce. In this example, the working time could be shortened to the same extent as in Example 1, and the appearance of the positive electrode was as good as in Example 1.
−実施例5−
実施例5では、硫黄導入前の樹脂フィルムにおけるPEOの含有率を30%とした以外は実施例1と同様の方法により金属硫黄電池用正極を作製した。スラリー中の硫黄の分散性は実施例1と同様に良好であり、1回の硫黄導入作業で所定量の硫黄を樹脂フィルムから多孔性導電材層中へと導入させることができた。ただし、多孔性導電材層中に導入できた硫黄の量は実施例1、2の方法に比べると少なかった。
-Example 5
In Example 5, a positive electrode for a metal sulfur battery was produced in the same manner as in Example 1 except that the content of PEO in the resin film before introducing sulfur was 30%. The dispersibility of sulfur in the slurry was as good as in Example 1, and a predetermined amount of sulfur could be introduced from the resin film into the porous conductive material layer in one sulfur introduction operation. However, the amount of sulfur that could be introduced into the porous conductive material layer was small compared to the methods of Examples 1 and 2.
−比較例1−
比較例1では、ふるいにかけた無修飾の硫黄をCNT電極の表面にふりかけ、さらに加熱することで硫黄をCNT内に導入した。しかしながら、1回あたりの硫黄導入量は最大でも多孔性導電材層の単位面積当たり2mg/cm2程度しか導入できず、5mg/cm2を導入するには最低3回は硫黄の導入作業を繰り返す必要があり、導入する硫黄量の制御も非常に困難であった。正極の外観は良好であった。
-Comparative Example 1-
In Comparative Example 1, unmodified sulfur that had been sieved was sprinkled on the surface of the CNT electrode, and further heated to introduce sulfur into the CNT. However, the maximum amount of sulfur introduced per time is only 2 mg / cm 2 per unit area of the porous conductive material layer, and the introduction of sulfur is repeated at least three times to introduce 5 mg / cm 2. Therefore, it was very difficult to control the amount of sulfur introduced. The appearance of the positive electrode was good.
−比較例2−
比較例2では、濃度8wt%で硫黄を含む二硫化炭素溶液を作製し、CNT電極を当該溶液に浸漬後、引き上げて乾燥することで正極を作製した。CNTが金属箔から剥離することが多く、複数の正極を作製したが、電極として使用可能な正極は少数であった。また、CNTの剥離のために硫黄の導入作業は1回しか行わなかった。また、多孔性導電材層に導入できた硫黄の量は実施例1〜5に比べて少なかった。
-Comparative Example 2-
In Comparative Example 2, a carbon disulfide solution containing sulfur at a concentration of 8 wt% was prepared, and the CNT electrode was immersed in the solution, and then pulled up and dried to prepare a positive electrode. CNT often peeled from the metal foil and produced a plurality of positive electrodes, but there were only a few positive electrodes that could be used as electrodes. Also, the introduction of sulfur was performed only once for CNT peeling. Moreover, the amount of sulfur that could be introduced into the porous conductive material layer was smaller than in Examples 1-5.
−比較例3−
比較例3では、硫黄を密閉容器中で加熱昇華し、昇華した硫黄をCNT電極に触れさせた後、CNT電極を冷却することで硫黄の導入を試みた。しかしながら、硫黄の導入量を5mg/cm2程度まで大きくするのには10回以上の導入処理を要し、多くの時間が必要であった。導入量の制御も非常に困難であった。
-Comparative Example 3-
In Comparative Example 3, sulfur was heated and sublimated in a sealed container, and the sublimated sulfur was brought into contact with the CNT electrode, and then the introduction of sulfur was attempted by cooling the CNT electrode. However, in order to increase the amount of sulfur introduced to about 5 mg / cm 2 , 10 or more introduction treatments were required, and a lot of time was required. Control of the amount introduced was also very difficult.
−比較例4−
比較例4では、硫黄を加圧しペレット状に成型することを試みたが、成型は可能なものの非常に脆く作業性は悪かった。CNT電極上にペレットを載せることができた場合は1回のみ硫黄の導入作業を行えたが、ペレットが崩れてしまい、CNT電極にペレットを載せることができない場合もあった。従って、硫黄導入性の良否を判断することができなかった。
<正極の作製方法の判定基準及び評価結果>
表1に、実施例1〜5及び比較例1〜4の方法を評価した結果を示す。
-Comparative Example 4-
In Comparative Example 4, an attempt was made to pressurize sulfur and mold it into a pellet. However, although it could be molded, it was very brittle and the workability was poor. When the pellet could be placed on the CNT electrode, the sulfur was introduced only once, but the pellet collapsed and sometimes the pellet could not be placed on the CNT electrode. Therefore, it was not possible to judge whether the sulfur introduction property was good or bad.
<Judgment criteria and evaluation results of positive electrode manufacturing method>
In Table 1, the result of having evaluated the method of Examples 1-5 and Comparative Examples 1-4 is shown.
表1に示す「量」の項目は、乾燥後、硫黄導入前の樹脂フィルムにおける樹脂の含有率を示す。その他の項目と判定基準は下記の通りとした。 The item “Amount” shown in Table 1 indicates the resin content in the resin film after drying and before introduction of sulfur. Other items and criteria were as follows.
硫黄導入回数:所定の量の硫黄を導入するのに要した硫黄導入回数を示す。ただし、繰り返しの導入作業ができない場合は導入回数は1回とした。導入回数が1回の場合を○(良)、2回を△(可)、3回以上を×(不可)と判定した。ただし、1回しか導入作業ができず、所定量(5mg/cm2)の硫黄を導入できない場合(比較例2)の判定は×(不可)とした。 Number of sulfur introductions: Indicates the number of sulfur introductions required to introduce a predetermined amount of sulfur. However, if repeated introduction work is not possible, the number of introductions is set to one. A case where the number of introductions was 1 was judged as ◯ (good), 2 times as Δ (possible), and 3 times or more as x (impossible). However, when the introduction work could be performed only once and a predetermined amount (5 mg / cm 2 ) of sulfur could not be introduced (Comparative Example 2), the determination was x (impossible).
作業性:導入回数の少なさ及び作業に要した時間の短さを実施例1を基準に評価した。具体的には、導入に要する時間が30分以内の場合を○(良)、30分を越え、60分以下の場合を△(可)、60分を越えた場合を×(不可)とした。。 Workability: The number of introductions and the short time required for the work were evaluated based on Example 1. Specifically, when the time required for introduction is within 30 minutes, ○ (good), when it exceeds 30 minutes, when it is 60 minutes or less, △ (possible), and when it exceeds 60 minutes, × (impossible). . .
硫黄導入性:多孔性導電材層に導入できた硫黄の分布量に基づいて判断した。硫黄が移動した後の樹脂フィルム、または硫黄が導入された箇所の痕跡がCNT電極表面のほぼ全面にあるものを○(良)、一部偏りがあるものを△(可)、不均一にあるものを×(不可)と判定した。 Sulfur introduction property: Judged based on the distribution amount of sulfur introduced into the porous conductive material layer. The resin film after the sulfur has moved, or the trace of the portion where the sulfur has been introduced is almost entirely on the surface of the CNT electrode. Things were judged as x (impossible).
分散性:スラリー中での硫黄の分散性を目視により観察して評価を行った。硫黄が均一に分散している場合を○(良)、分散性がやや劣り、一部凝集物が見られるが樹脂フィルムを作製する際に問題を生じない場合を△(可)、樹脂フィルムの作製が困難な程度に硫黄の分散性が良くない場合を×(不可)とした。 Dispersibility: Evaluation was made by visually observing the dispersibility of sulfur in the slurry. ○ (good) when the sulfur is uniformly dispersed, △ (possible) when the dispersibility is slightly inferior and some aggregates are seen but no problem occurs when the resin film is produced. The case where the dispersibility of sulfur was not so good as to be difficult to produce was determined as x (impossible).
正極の外観:作製できた正極を目視により確認した結果を示す。樹脂フィルムを使用する場合、樹脂フィルムがCNT電極のほぼ全面を覆っていれば良好と判断する。樹脂フィルムを使用しない場合は、硫黄導入の痕跡がほぼ全面にあるか、偏っていないか等を基準にして判断する。外観上問題が見られない場合は○(良)、一部で樹脂フィルムが崩れている等、外観上多少の問題はあっても作成された正極が、電極として機能できる場合には△(可)、CNTが剥離する等外観上に問題があり、且つ作製された正極が電極として機能できない場合には×(不可)と判定した。 Appearance of positive electrode: The result of visual confirmation of the produced positive electrode is shown. When using a resin film, it is judged that the resin film is good if it covers almost the entire surface of the CNT electrode. When the resin film is not used, the judgment is made based on whether there is a trace of sulfur introduction on the entire surface or whether it is not biased. ○ (good) when there is no problem in appearance, or △ (possible if the created positive electrode can function as an electrode, even if there are some problems in appearance such as the resin film is partially broken. ), There was a problem in appearance such as separation of CNT, and when the produced positive electrode could not function as an electrode, it was determined as x (impossible).
総合評価:すべての項目が○(良)評価である場合には◎(優)判定とし、△(可)判定が2つ以下で残りが○(良)判定である場合には○(可)判定とした。×(不可)の項目が1つでもある場合、又は△(可)判定が3つ以上である場合には×(不可)判定とした。 Comprehensive evaluation: If all items are ○ (good) evaluation, it is judged as ◎ (excellent), and if there are 2 or less △ (good) decisions and the rest is ○ (good), ○ (good) Judgment was made. When there was at least one item of x (impossible), or when there were three or more △ (possible) determinations, an x (impossible) determination was made.
表1に示すように、本実施形態の製造方法を用いた実施例1〜5では、総合評価がいずれも○(可)以上であり、作業性が良好で且つ多孔性導電材層に十分な量の硫黄を導入できることが確認できた。 As shown in Table 1, in Examples 1 to 5 using the manufacturing method of the present embodiment, the overall evaluation is all ◯ (possible) or more, the workability is good, and the porous conductive material layer is sufficient. It was confirmed that an amount of sulfur could be introduced.
これに対し、CNT電極上に直接硫黄をふりかけた場合や、二硫化炭素を溶媒として用いた場合、昇華させた硫黄を導入する方法では、十分な量の硫黄を多孔性導電材層に導入することができなかった。また、比較例1、3、4に係る方法に比べて実施例1〜5の方法では作業性が良好であることも確認できた。
<リチウム硫黄二次電池の評価>
−実施例6−
実施例1と同様の方法で作製した正極を用いたリチウム硫黄二次電池を作製した。正極の平面形状は直径14mmの円形とした。多孔性導電材層の単位面積当たりの硫黄導入量は8.7mg/cm2とした。
On the other hand, when sulfur is sprinkled directly on the CNT electrode or when carbon disulfide is used as a solvent, a method of introducing sublimated sulfur introduces a sufficient amount of sulfur into the porous conductive material layer. I couldn't. It was also confirmed that the workability of the methods of Examples 1 to 5 was better than the methods according to Comparative Examples 1, 3, and 4.
<Evaluation of lithium-sulfur secondary battery>
-Example 6
A lithium-sulfur secondary battery using a positive electrode produced in the same manner as in Example 1 was produced. The planar shape of the positive electrode was a circle having a diameter of 14 mm. The amount of sulfur introduced per unit area of the porous conductive material layer was 8.7 mg / cm 2 .
負極として直径15mm、厚さ400μmのLi-Al合金箔(Alの濃度が20vol%)を用い、セパレータとしてセルガード♯2400(セルガード社製)を用いた。電解液としては、1M LiTFSIの1,2−ジメトキシエタン(DME)/1,3−ジオキソラン(DOL)=90vol%/10vol%溶液に3wt%のLiNO3を加えたものを100μL使用した。公知の方法によりこれらの材料を用いてCR2032型のコイン電池を作製し、リチウム−硫黄二次電池の特性を評価した。 A Li—Al alloy foil (Al concentration of 20 vol%) having a diameter of 15 mm and a thickness of 400 μm was used as the negative electrode, and Celgard # 2400 (manufactured by Celgard) was used as the separator. As an electrolytic solution, 100 μL of 1M LiTFSI in which 1,2-dimethoxyethane (DME) / 1,3-dioxolane (DOL) = 90 vol% / 10 vol% was added with 3 wt% LiNO 3 was used. A CR2032-type coin battery was manufactured using these materials by a known method, and the characteristics of the lithium-sulfur secondary battery were evaluated.
測定の際は、0.77mA(0.50mA/cm2)の定電流で充放電を行い、カット電圧は放電1.5V、充電2.8Vとした。 During the measurement, charging / discharging was performed at a constant current of 0.77 mA (0.50 mA / cm 2 ), and the cut voltage was set to discharge 1.5V and charge 2.8V.
図3は、実施例6に係るリチウム硫黄二次電池の充放電プロファイルを示す図である。縦軸は測定電圧を示し、横軸は比容量を示す。 FIG. 3 is a diagram showing a charge / discharge profile of the lithium-sulfur secondary battery according to Example 6. The vertical axis represents the measured voltage, and the horizontal axis represents the specific capacity.
同図に示す結果から、本実施形態に係る方法で作製した正極を用いれば、硫黄重量あたり1100mA/gを超える高い電気容量で良好な充放電が行えることが確認できた。 From the results shown in the figure, it was confirmed that if the positive electrode produced by the method according to this embodiment was used, good charge / discharge could be performed with a high electric capacity exceeding 1100 mA / g per sulfur weight.
以上説明したように、本明細書に開示されたアルカリ金属−硫黄電池用正極及びその製造方法は、リチウム−硫黄二次電池等のアルカリ金属−硫黄電池に適用される。 As described above, the alkali metal-sulfur battery positive electrode and the manufacturing method thereof disclosed in this specification are applied to alkali metal-sulfur batteries such as lithium-sulfur secondary batteries.
1 リチウム−硫黄二次電池
3 正極層
5 樹脂フィルム
7 多孔性導電材層
9 硫黄
10 導電材
11 集電体
13 セパレータ
15 負極層
17 電解液
1 Lithium-sulfur secondary battery
3 Positive electrode layer
5 Resin film
7 Porous conductive material layer
9 Sulfur
10 Conductive material
11 Current collector
13 Separator
15 Negative electrode layer
17 Electrolyte
Claims (10)
前記多孔性導電材層の前記空隙内に保持された硫黄と、
前記多孔性導電材層の少なくとも一部に直接載置された樹脂フィルムとを備えており、
前記樹脂フィルムの質量は、前記多孔性導電材層に導入された硫黄原子の質量に対し、15wt%未満であるアルカリ金属−硫黄電池用正極。 A porous conductive material layer composed of a plurality of conductive materials and having voids formed between the plurality of conductive materials;
Sulfur retained in the voids of the porous conductive material layer;
A resin film placed directly on at least a part of the porous conductive material layer ,
The positive electrode for an alkali metal-sulfur battery in which the mass of the resin film is less than 15 wt% with respect to the mass of sulfur atoms introduced into the porous conductive material layer .
前記導電材は、前記集電体の平面に対して垂直に配向したカーボンナノチューブであることを特徴とする請求項1〜3のうちいずれか1つに記載のアルカリ金属−硫黄電池用正極。 A current collector having a plane on which the porous conductive material layer is formed;
The positive electrode for an alkali metal-sulfur battery according to any one of claims 1 to 3 , wherein the conductive material is a carbon nanotube oriented perpendicular to a plane of the current collector.
前記多孔性導電材層における前記カーボンナノチューブの密度は1×108 本/cm2以上1×1012 本/cm2以下であり、100μm以上1000μm以下の長さを有することを特徴とする請求項4に記載のアルカリ金属−硫黄電池用正極。 The current collector is a metal foil;
The density of the carbon nanotube in the porous conductive material layer is 1 × 10 8 pieces / cm 2 or more and 1 × 10 12 pieces / cm 2 or less, and has a length of 100 μm or more and 1000 μm or less. 4. The positive electrode for an alkali metal-sulfur battery according to 4 .
リチウムイオンを吸蔵及び放出する材料を含む負極と、
前記アルカリ金属−硫黄電池用正極と前記負極との間に満たされた、リチウムイオン伝導性を持つ電解液と、
前記電解液中で前記アルカリ金属−硫黄電池用正極と前記負極との間を絶縁するセパレータとを備えているリチウム−硫黄二次電池。 A positive electrode for an alkali metal-sulfur battery according to any one of claims 1 to 7 ,
A negative electrode comprising a material that occludes and releases lithium ions;
An electrolyte having lithium ion conductivity filled between the positive electrode for an alkali metal-sulfur battery and the negative electrode;
A lithium-sulfur secondary battery comprising a separator for insulating between the positive electrode for an alkali metal-sulfur battery and the negative electrode in the electrolytic solution.
前記多孔性導電材層の少なくとも一部上に硫黄を含む樹脂フィルムを直接載置する工程と、
前記樹脂フィルムに含まれる硫黄を前記多孔性導電材層中に挿入させる工程とを備えているアルカリ金属−硫黄電池用正極の製造方法。 A step of preparing a current collector composed of a plurality of conductive materials and having a porous conductive material layer formed on the upper surface with a gap between the plurality of conductive materials;
Directly placing a resin film containing sulfur on at least a portion of the porous conductive material layer;
A method for producing a positive electrode for an alkali metal-sulfur battery, comprising a step of inserting sulfur contained in the resin film into the porous conductive material layer.
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| US14/955,137 US10050265B2 (en) | 2014-12-18 | 2015-12-01 | Positive electrode having sulfur contained in pores between nanocarbon structures, alkali metal-sulfur battery including the same, and method of preparing the positive electrode |
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| KR102468500B1 (en) * | 2018-07-02 | 2022-11-17 | 주식회사 엘지에너지솔루션 | A sulfur-carbon complex, positive eletrode for lithium-sulfur battery and lithium-sulfur battery comprising the same |
| KR102763149B1 (en) * | 2018-11-22 | 2025-02-07 | 주식회사 엘지에너지솔루션 | Lithium-sulfur secondary battery |
| KR102940359B1 (en) | 2018-12-13 | 2026-03-18 | 주식회사 엘지에너지솔루션 | Lithium-sulfur secondary battery |
| US12021224B2 (en) | 2018-11-22 | 2024-06-25 | Lg Energy Solution, Ltd. | Lithium-sulfur secondary battery |
| KR102663586B1 (en) * | 2018-12-17 | 2024-05-03 | 주식회사 엘지에너지솔루션 | Lithium-sulfur secondary battery |
| WO2020149659A1 (en) | 2019-01-16 | 2020-07-23 | 주식회사 엘지화학 | Lithium secondary battery |
| KR102781566B1 (en) * | 2019-01-16 | 2025-03-17 | 주식회사 엘지에너지솔루션 | Lithium secondary battery |
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