JP5679260B2 - Composite composed of sulfur and conductive polymer - Google Patents
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本発明は、繊維状の硫黄とそれを取り囲むように存在する導電性ポリマーよりなる複合体であって、電池の正極活物質として有用な複合体に関する。 The present invention relates to a composite composed of fibrous sulfur and a conductive polymer existing so as to surround it, and is useful as a positive electrode active material of a battery.
近年、急速な携帯電子機器や電気自動車の普及に伴い、高容量で繰り返し充放電可能な二次電池が要求され、開発が盛んに行われている。なかでもリチウム電池が、軽量で高出力が期待されることから、特に注目されている。現在、リチウム電池としては、正極にLiCoO2やLiMn2O4など、負極にはカーボンや金属リチウムが用いられているケースが多いが、負極カーボンの場合、電気容量が300−370mAh/g、リチウムの場合、3830mAh/gであるのに対して、正極のLiCoO2やLiMn2O4の電気容量は、110−140mAh/g程度であり、正極材料の開発が望まれている。 In recent years, with the rapid spread of portable electronic devices and electric vehicles, secondary batteries that can be repeatedly charged and discharged with high capacity are required and are actively developed. Among them, lithium batteries are particularly attracting attention because they are expected to be lightweight and have high output. At present, as lithium batteries, there are many cases where LiCoO 2 or LiMn 2 O 4 is used for the positive electrode and carbon or metallic lithium is used for the negative electrode, but in the case of the negative electrode carbon, the electric capacity is 300-370 mAh / g, lithium In this case, the electric capacity of LiCoO 2 and LiMn 2 O 4 of the positive electrode is about 110-140 mAh / g, whereas it is 3830 mAh / g, and development of a positive electrode material is desired.
一方高エネルギー密度電池の正極としては、硫黄が着目されている。硫黄はLi2Sまでリチウムと完全に反応すると仮定した場合、2600Wh/gの理論エネルギー密度と1672mAh/gの理論的に高い容量を有している。さらに硫黄は毒性が低く、資源も豊富であるため、安価であるという利点もある。 On the other hand, sulfur has attracted attention as a positive electrode of a high energy density battery. Sulfur has a theoretical energy density of 2600 Wh / g and a theoretically high capacity of 1672 mAh / g, assuming complete reaction with lithium up to Li 2 S. Furthermore, sulfur has the advantage of being inexpensive because it has low toxicity and is rich in resources.
しかしながら、硫黄は反応性に乏しく、また絶縁体であるため、正極活物質に用いるためには、硫黄の活性を高め、更に導電性を付与する必要がある。そこで、これらの欠点を補うため、開発が多くなされており、例えば金属ナトリウムを負極とし、硫黄を正極とする二次電池として、硫黄の活性を高めるために、作動温度を300℃以上とする提案がなされている。このような高温下での作動を改良するナトリウム/硫黄電池として、混合物全体の重量に対して50〜70重量%の硫黄、15〜30重量%の炭素、15〜20重量%のポリエチレンオキサイドの混合物を正極として用い、負極をナトリウム又はナトリウム含有炭素或いはナトリウム酸化物として、電解液にナトリウム塩を含むグリミド(grymid)溶液を用いることで、常温作動のナトリウム/硫黄電池(特許文献1)が提案されている。 However, since sulfur is poor in reactivity and is an insulator, in order to be used for the positive electrode active material, it is necessary to increase the activity of sulfur and to impart conductivity. Therefore, in order to compensate for these drawbacks, many developments have been made. For example, as a secondary battery using metallic sodium as a negative electrode and sulfur as a positive electrode, a proposal to increase the operating temperature to 300 ° C. or higher in order to increase the activity of sulfur. Has been made. As a sodium / sulfur battery for improving the operation at such a high temperature, a mixture of 50 to 70% by weight of sulfur, 15 to 30% by weight of carbon, and 15 to 20% by weight of polyethylene oxide based on the weight of the whole mixture. As a positive electrode, a negative electrode as sodium or sodium-containing carbon or sodium oxide, and a glymid solution containing a sodium salt as an electrolyte, a sodium / sulfur battery operating at room temperature has been proposed (Patent Document 1). ing.
また、硫黄の微粉体と炭素の微粉体とをメカノケミカルフュージョン法により緊密一体化した複合体を正極とする提案(特許文献2)などが提案されている。 In addition, a proposal (Patent Document 2) is proposed in which a composite in which sulfur fine powder and carbon fine powder are closely integrated by a mechanochemical fusion method is used as a positive electrode.
しかしながら、300℃もの高温下に作動する電池では装置の大型化や安定性に欠けるなどの不便があり、硫黄と炭素等とを混合する正極にあっては硫黄以外の不純物の混合割合が多くなること及び繰り返し充放電することにより硫黄化合物が電解液中に溶出し、次第に出力が低下するという欠点があった。そこで硫黄を正極活物質として高エネルギー密度で長期間安定的に作用する正極材料の開発が期待されていたのである。 However, a battery that operates at a high temperature of 300 ° C. has inconveniences such as an increase in size and lack of stability, and in a positive electrode that mixes sulfur and carbon, the mixing ratio of impurities other than sulfur increases. In addition, the sulfur compound is eluted in the electrolytic solution due to repeated charging and discharging, and the output is gradually reduced. Therefore, development of a positive electrode material that functions stably for a long time at a high energy density using sulfur as a positive electrode active material has been expected.
本発明は硫黄を正極活物質とする場合の上記問題点に鑑み、より効率的で且つ安定性の高い硫黄を含む正極材料を開発し、提案するものである。 The present invention develops and proposes a cathode material containing sulfur that is more efficient and highly stable in view of the above-described problems when sulfur is used as a cathode active material.
本発明の第1の態様は、繊維状硫黄に導電性ポリマーとなるモノマーを吸着させた後、重合させることを特徴とする実質的に硫黄と導電性ポリマーよりなる複合体である。 A first aspect of the present invention is a composite substantially consisting of sulfur and a conductive polymer, characterized in that a monomer that becomes a conductive polymer is adsorbed on fibrous sulfur and then polymerized.
また、本発明の第2の態様は、前記導電性ポリマーを5〜30重量%含むことを特徴とする第1の態様に記載の実質的に硫黄と導電性ポリマーよりなる複合体である。 Moreover, the 2nd aspect of this invention is a composite_body | complex substantially consisting of sulfur and a conductive polymer as described in the 1st aspect characterized by including 5-30 weight% of said conductive polymers.
更に本発明の第3の態様は、前記繊維状硫黄は、平均直径50μm以下、好ましくは10〜30μmよりなる不繊布である第1の態様又は第2の態様に記載の実質的に硫黄と導電性ポリマーよりなる複合体である。 Further, according to a third aspect of the present invention, the fibrous sulfur is a non-woven cloth having an average diameter of 50 μm or less, preferably 10 to 30 μm, and is substantially electrically conductive with sulfur according to the first aspect or the second aspect. It is a composite made of a functional polymer.
更に本発明の第4の態様は、導電性ポリマーとなるモノマーがピロールであり、導電性ポリマーがポリピロールである第1の態様乃至第3の態様のいずれかに記載の実質的に硫黄と導電性ポリマーよりなる複合体である。 Further, according to a fourth aspect of the present invention, substantially the sulfur and the conductive material according to any one of the first to third aspects, wherein the monomer to be a conductive polymer is pyrrole and the conductive polymer is polypyrrole. It is a composite made of a polymer.
また、本発明の第5の態様は、繊維状硫黄が溶融電界紡糸法により作製されていることを特徴とする第1の態様乃至第4の態様のいずれかに記載の実質的に硫黄と導電性ポリマーよりなる複合体である。 According to a fifth aspect of the present invention, the sulfur and the conductive material according to any one of the first to fourth aspects are characterized in that the fibrous sulfur is produced by a melt electrospinning method. It is a composite made of a functional polymer.
本発明は、硫黄を繊維状とし得るという新知見に基づき、特に電界紡糸技術によりナノオーダー乃至ミクロンオーダーの直径を有する繊維とすることができ、これに導電性ポリマーとなるモノマーを吸着させた後重合して主として繊維表面を薄い導電性ポリマー皮膜で、被覆することにより、絶縁体である硫黄の活性を助長し、導電性を付与することが可能となり、高密度のエネルギーを与える電池の正極材料とすることができるのである。 The present invention is based on the new knowledge that sulfur can be made into a fiber, and can be made into a fiber having a nano-order to micron-order diameter by an electrospinning technique, after adsorbing a monomer serving as a conductive polymer to the fiber. By covering the fiber surface mainly with a thin conductive polymer film by polymerization, it is possible to promote the activity of sulfur, which is an insulator, to provide conductivity, and to provide a positive electrode material for a battery that provides high-density energy. It can be.
また本発明にあっては、繊維の表面に導電性皮膜が形成されているため、硫黄化合物の電解液への流出が抑えられるため、充放電の繰り返しに対しても出力の減少や電圧の低下などは少なく、安定して作用するものである。 Further, in the present invention, since a conductive film is formed on the surface of the fiber, the outflow of the sulfur compound to the electrolytic solution is suppressed, so that the output is reduced and the voltage is lowered even with repeated charge and discharge. There are few etc. and it works stably.
本発明のポイントは、硫黄を繊維状、特に極細繊維状に成形し得るという知見を得たことにある。従来硫黄又は、硫黄化合物の表面積を増大し、活性な電極物質とする試みは、一般に硫黄を微粒化することであり、これらを導電性物質である炭素で継ぎ合わせる方法が奨められていた。この場合、硫黄粒子の全表面を覆う炭素の量が多くなり、実用的な正極とするには炭素が50%程度混合されることになる。しかるに本発明にあっては細い繊維状とするため、その側面方向だけを被覆すればよいため、同様の効果を得るための導電性物質の量を減ずることが可能となる。このため正極活物質としての複合体中の硫黄割合を多くすることができる。 The point of the present invention is that it has been found that sulfur can be formed into a fibrous form, particularly an ultrafine fiber form. Conventionally, an attempt to increase the surface area of sulfur or a sulfur compound to make it an active electrode material is generally to atomize sulfur, and a method of joining them with carbon which is a conductive material has been recommended. In this case, the amount of carbon covering the entire surface of the sulfur particles is increased, and about 50% of carbon is mixed for a practical positive electrode. However, in the present invention, since it is made into a thin fiber shape, it is only necessary to cover the side direction, so the amount of the conductive material for obtaining the same effect can be reduced. For this reason, the sulfur ratio in the composite as the positive electrode active material can be increased.
更に本発明にあっては、導電性ポリマーとなるモノマーを繊維状硫黄に吸着させるため、硫黄の表面や繊維の割れ目等に均一に付着させることが可能となり、しかも極めて薄い層状となっているため、これを重合することにより、薄い導電性ポリマーの皮膜とすることができるのである。このように、薄い被膜を形成させることで、電解液の浸み込みは容易となり、しかもLi2Sn(nは硫黄原子の数、一般に8以下)で表わされる硫黄化合物の電解液への溶出が抑制されるという利点を有する。 Furthermore, in the present invention, since the monomer that becomes the conductive polymer is adsorbed on the fibrous sulfur, it can be uniformly attached to the surface of the sulfur or the fissures of the fiber, and the layer is extremely thin. By polymerizing this, a thin conductive polymer film can be formed. In this way, by forming a thin film, it is easy for the electrolytic solution to penetrate, and elution of the sulfur compound represented by Li 2 Sn (where n is the number of sulfur atoms, generally 8 or less) into the electrolytic solution. Has the advantage of being suppressed.
本発明において、繊維状の硫黄の形状は特に限定されない。一般に繊維の直径は、細い程表面積は大きくなり、且つ導電率は5.0×10−16Ω−1
・m−1と低く、絶縁体である硫黄の反応性や電子の移動性は確保されるが、繊維としての強度も減少し、取扱が不便になる。一般に繊維の直径は、平均50μm以下とするのがよく、取扱や加工の面から10μm以上好ましくは、平均20〜30μm程度である。
In the present invention, the shape of fibrous sulfur is not particularly limited. In general, the smaller the fiber diameter, the larger the surface area and the electrical conductivity is 5.0 × 10 −16 Ω −1.
・ As low as m −1 , the reactivity of sulfur, which is an insulator, and the mobility of electrons are ensured, but the strength as a fiber is reduced and handling becomes inconvenient. In general, the diameter of the fiber is preferably 50 μm or less on average, and is 10 μm or more, preferably about 20 to 30 μm on average in terms of handling and processing.
また、繊維の長さは特に制限されない。一般に不織布のマット状として用いられる場合が多く、1〜30cm、好ましくは20〜30cmである。 Further, the length of the fiber is not particularly limited. Generally, it is often used as a non-woven mat, and is 1 to 30 cm, preferably 20 to 30 cm.
これらの繊維の製造方法は、何ら制限されないが、一般に溶融し、ノズルから押し出して作ることができる。すなわち、硫黄の融点は112.8℃(α硫黄)〜119.6℃(γ硫黄)であるが、195℃までは粘度が増加し、更に高温では再び減少する。そこで、溶融紡糸は、180〜250℃、好ましくは190〜220℃程度で行うことができる。好ましい紡糸方法の一つは、電界紡糸方法である。 Although the manufacturing method of these fibers is not limited at all, it can generally be melted and extruded from a nozzle. That is, the melting point of sulfur is 112.8 ° C. (α sulfur) to 119.6 ° C. (γ sulfur), but the viscosity increases up to 195 ° C. and decreases again at higher temperatures. Therefore, melt spinning can be performed at 180 to 250 ° C., preferably about 190 to 220 ° C. One preferred spinning method is the electrospinning method.
溶融電界紡糸装置の概細を図1に示す。図中、シリンジ中に硫黄を入れ加熱して、ニードル(針)とコレクター(集電体)の間に印加した電圧により、電圧がしきい値を超えると、電荷の反発力が溶融硫黄の表面張力に打ち勝って電荷を帯びた噴流が発生し、電場内で噴流は伸長して非常に細いファイバーを形成し、コレクター上に堆積する。溶融電界紡糸法における条件としては、通常溶融電界紡糸温度が180〜250℃の場合、ニードル〜コレクター間の距離は、過度に短い場合には、ニードル〜コレクター間で放電が起こり紡糸が出来ないことがあり、過度に長い場合には、ファイバーを引っ張る静電引力が小さくなることで紡糸が出来ないことがあるので、前記距離は、4cm〜10cmとするのが好ましい。また、印加電圧は、過度に低い場合には、静電引力が小さくなることで紡糸が出来ないことがあり、過度に高い場合には、ニードル〜コレクター間で放電が起こり紡糸が出来ないことがあるので、前記印加電圧は8kV〜10kVとすることが好ましい。なお、周囲条件(主に湿度)の変化により放電の起こり易さが変化し、湿度20%以下と低い条件が好まれるが、この場合、湿度10〜50%程度の条件において紡糸可能である。 An outline of the melt electrospinning apparatus is shown in FIG. In the figure, when sulfur is charged in the syringe and heated, and the voltage exceeds the threshold value due to the voltage applied between the needle and the collector (current collector), the repulsive force of the charge causes the surface of the molten sulfur A charged jet is generated by overcoming the tension, and the jet stretches in the electric field to form very thin fibers, which are deposited on the collector. As conditions in the melt electrospinning method, when the melt electrospinning temperature is usually 180 to 250 ° C., if the distance between the needle and the collector is excessively short, electric discharge occurs between the needle and the collector and spinning cannot be performed. If the length is excessively long, spinning may not be possible because the electrostatic attraction force that pulls the fiber becomes small. Therefore, the distance is preferably 4 cm to 10 cm. In addition, when the applied voltage is excessively low, spinning may not be possible because the electrostatic attractive force is small, and when it is excessively high, discharge may occur between the needle and the collector and spinning may not be possible. Therefore, the applied voltage is preferably 8 kV to 10 kV. It should be noted that the ease of occurrence of discharge varies with changes in ambient conditions (mainly humidity), and conditions with a humidity as low as 20% or less are preferred. In this case, spinning is possible under conditions of a humidity of about 10 to 50%.
かくして、直径ナノサイズ〜ミクロンサイズの硫黄繊維が得られる。この場合、繊維の平均直径は、溶融硫黄の粘度、印加する電圧及びニードル〜コレクター間の距離により、ほぼ決めることができる。従って、数度程度の試行錯誤により、繊維状硫黄の直径を決めることができる。 Thus, sulfur fibers having a diameter of nanometer to micron size are obtained. In this case, the average diameter of the fiber can be almost determined by the viscosity of the molten sulfur, the applied voltage, and the distance between the needle and the collector. Therefore, the diameter of fibrous sulfur can be determined by trial and error of several degrees.
図2に電圧を印加しながら押し出し調製した硫黄繊維(a)と溶融電界紡糸による硫黄繊維(b)(ニードル〜コレクター間6cm、印加電圧10kV、溶融温度200℃)のSEM写真を示す。 FIG. 2 shows SEM photographs of sulfur fiber (a) prepared by extrusion while applying voltage and sulfur fiber (b) obtained by melt electrospinning (6 cm between needle and collector, applied voltage 10 kV, melting temperature 200 ° C.).
一般に電池の正極とする場合、該溶融紡糸の堆積は集電体上に行われる、集電体としては板状、網状、凹凸状の金属、例えば、銅、白金、鉄、ニッケル等であるが、炭素であってもよい。また正極活物質と集電体との接触を考慮して、後述する導電性ポリマーの一部が集電体を被覆していてもよい。 In general, when a positive electrode of a battery is used, the melt spinning is performed on a current collector, and the current collector is a plate-like, net-like, or uneven metal, for example, copper, platinum, iron, nickel, etc. Carbon may also be used. In consideration of the contact between the positive electrode active material and the current collector, a part of the conductive polymer described later may cover the current collector.
次に、繊維状の硫黄は、導電性ポリマーで一体化されるが、該導電性ポリマーは、まず、モノマーを繊維状硫黄に吸着させ、この吸着したモノマーを硫黄上で重合させることにより薄い被膜を形成させる必要がある。 Next, the fibrous sulfur is integrated with a conductive polymer. The conductive polymer first adsorbs the monomer to the fibrous sulfur and polymerizes the adsorbed monomer on the sulfur to form a thin film. Need to be formed.
導電性ポリマー用モノマーとしては周知のモノマーを使用し得る。例えば、ポリパラフェニレン、ポリピロール、ポリアニリン、ポリチオフェンなどを形成するモノマー等である。中でも、ピロールが重合の容易性や得られる皮膜の状態から特に好ましい。 A well-known monomer can be used as a monomer for conductive polymers. For example, monomers that form polyparaphenylene, polypyrrole, polyaniline, polythiophene, and the like. Among these, pyrrole is particularly preferable from the viewpoint of ease of polymerization and the state of the obtained film.
繊維状の硫黄に上記モノマーを吸着させる方法は、繊維状硫黄を、そのまま又は、場合によっては集電体上に堆積させた不織布状物をそのまま、モノマー溶液又は、モノマーガス中に入れることによって達成される。この場合、あらかじめ重合触媒中で処理し、あらかじめ触媒を付着させておいてもよいし、またモノマーを吸着させた後、触媒で処理することもできる。また場合によっては紫外線照射や加熱によって重合させることも可能となる。 The method for adsorbing the monomer to fibrous sulfur is achieved by placing fibrous sulfur as it is or, in some cases, a non-woven fabric deposited on a current collector as it is in a monomer solution or monomer gas. Is done. In this case, the treatment may be performed in advance in a polymerization catalyst and the catalyst may be attached in advance, or the monomer may be adsorbed and then treated with the catalyst. In some cases, polymerization can be performed by ultraviolet irradiation or heating.
なお、触媒処理により、重合を行う場合は、あらかじめ触媒を吸着した後、モノマー中に入れるより、あらかじめモノマーを吸着させた後、触媒で処理する方がモノマーの重合量を制御し易いので好ましい。 In the case where the polymerization is performed by the catalyst treatment, it is preferable to adsorb the monomer in advance and then treat with the catalyst after the catalyst is adsorbed in advance because the amount of monomer polymerization can be controlled more easily.
また、繊維状硫黄を導電性ポリマーで被覆した後、或いは導電性ポリマーの形成時にヨウ素等導電性ポリマーの導電性を高める物質をドープすることも好ましい場合がある。 It may also be preferable to dope a substance that enhances the conductivity of the conductive polymer such as iodine after coating the fibrous sulfur with the conductive polymer or during the formation of the conductive polymer.
図3に繊維状硫黄にヨウ素を触媒して用い、ピロールを重合させて得た実質的に硫黄と導電性ポリマーの複合体のSEM写真を示す。図中(1’)、(2’)はそれぞれ次の表1に示す条件による。
FIG. 3 shows an SEM photograph of a composite of substantially sulfur and a conductive polymer obtained by polymerizing pyrrole using iodine as a catalyst for fibrous sulfur. In the figure, (1 ') and (2') are based on the conditions shown in Table 1 below.
として覆い内部間際にも浸透して重合していることがわかる。
本発明により得られる、電気化学的性能を見るため、酸化還元電位及び電流量をサイクリックボルタンメトリ(CV)測定を行った結果の一例を図4に示す。図4では、3.5ボルトからスタートし、1〜4.5ボルトを10サイクル行った図である。第一サイクル目においては、2.0、2.8ボルトにわずかな還元反応に伴うピークが見られるが、5サイクル目以降では、多少の還元ピーク電位のシフトはあるものの、2.5〜3.5ボルトと高い電位で還元ピークが見られる。更に還元電流もサイクル数と共に増大し、10サイクル目においても還元電流は大きな値を維持している。これらの要因としては、本発明の複合体が、絶縁体である硫黄繊維へ導電性ポリマーが緊密に付加し、導電経路が確立され、硫黄の酸化還元反応の進行が助長されているものと理解される。
以下に実施例を示す。
FIG. 4 shows an example of results obtained by performing cyclic voltammetry (CV) measurement of the oxidation-reduction potential and the current amount in order to see the electrochemical performance obtained by the present invention. In FIG. 4, it is a figure which started from 3.5 volts and performed 1 to 4.5 volts for 10 cycles. In the first cycle, a slight peak due to the reduction reaction is observed at 2.0 and 2.8 volts, but after the fifth cycle, there is a slight shift in the reduction peak potential, but 2.5-3. A reduction peak is seen at a high potential of .5 volts. Further, the reduction current increases with the number of cycles, and the reduction current maintains a large value even at the 10th cycle. As for these factors, it is understood that the composite of the present invention is that the conductive polymer is closely added to the sulfur fiber as an insulator, the conductive path is established, and the progress of the sulfur redox reaction is promoted. Is done.
Examples are shown below.
(繊維状硫黄の製造)
(1)溶融電界紡糸装置
ステンレス針(内径0.7mm)を装着した3mlガラスシリンジ[MITSUBA株式会社]へ、変圧器[YAMABISHI株式会社 TYPE S−130−10]に接続したシリコンコードヒータ(1.5m)[相互理化化学硝子製作所株式会社 SKH−0151]を巻きつけた。収集板としてステンレス板(9×9cm)を用いた。電圧を印加した際にステンレス針が正に、収集板コレクターが負に帯電するよう高圧電源装置[松定プレシジョン株式会社]を接続した。コードヒータの温度は、被接触温度センサ[タスコジャパン株式会社 THI−303F]およびセンサ電源付ディジタルメータリレー[タスコジャパン株式会社 TAT−806A]によって測定、制御した。溶融電界紡糸に用いた装置の概略図を図1に示す。
(2)繊維状硫黄の作製
調製法としては、硫黄粉末をガラスシリンジへ加えた後、シリコンコードヒータによってガラスシリンジを200℃まで加熱した。その後、ステンレス針および収集板へ電圧を印加することで、収集板上の硫黄の溶融電界紡糸を行った。最適な紡糸条件を探索するために、印加電圧、ステンレス針の針先から集電体までの距離をそれぞれ変化させて紡糸を行う。
(Manufacture of fibrous sulfur)
(1) Melt electrospinning apparatus A silicon cord heater (1. 5m) [Reciprocal Chemical Glass Manufacturing Co., Ltd. SKH-0151] was wound. A stainless steel plate (9 × 9 cm) was used as a collecting plate. A high voltage power supply [Matsusada Precision Co., Ltd.] was connected so that the stainless steel needle was positively charged and the collector collector was negatively charged when voltage was applied. The temperature of the cord heater was measured and controlled by a contact temperature sensor [Tasco Japan Co., Ltd. THI-303F] and a sensor-powered digital meter relay [Tasco Japan Co., Ltd. TAT-806A]. A schematic diagram of an apparatus used for melt electrospinning is shown in FIG.
(2) Preparation of fibrous sulfur As a preparation method, after adding sulfur powder to a glass syringe, the glass syringe was heated to 200 degreeC with the silicon cord heater. Thereafter, a voltage was applied to the stainless needle and the collecting plate to perform melt electrospinning of sulfur on the collecting plate. In order to search for optimum spinning conditions, spinning is performed by changing the applied voltage and the distance from the tip of the stainless needle to the current collector.
なお電気化学的測定(CV)を行うため、電極とするための集電体として、白金メッシュ(3×20mm)を収集板状に載置した。紡糸条件を表2にまとめて示す。 In order to perform electrochemical measurement (CV), a platinum mesh (3 × 20 mm) was placed in a collecting plate shape as a current collector for forming an electrode. The spinning conditions are summarized in Table 2.
なお、ステンレス針の針先から収集板あるいは集電体までの距離を紡糸距離と表記する。 The distance from the tip of the stainless needle to the collecting plate or current collector is expressed as the spinning distance.
また、硫黄を溶融電界紡糸した直後(b)、2日後(c)、5日後(d)のファイバーおよび硫黄粉末(a)のXRDスペクトルを図5に示す。硫黄粉末のXRDスペクトルでは2θ=22−23゜に見られたピークが紡糸した直後の硫黄ファイバーでは消失し、新たに2θ=20,24°付近に、硫黄粉末では見られなかったピークが出現した。したがって、溶融電界紡糸法によって作製した硫黄ファイバーは、ポリマー硫黄の結晶構造で紡糸されたことがわかる。しかし、硫黄ファイバーを作製してから2日後,5日後のXRDスペクトルでは、紡糸した直後のファイバーで見られた2θ=20,24°付近のピークは再び消失し、硫黄粉末と同じXRDスペクトルとなった。これらのことより、紡糸直後のファイバーの結晶構造は不安定であり、時間が経つと単体硫黄の安定な結晶構造として知られるα硫黄へと変化する。
(3)導電性ポリマー(ポリピロール)の被覆
iodine(ヨウ素)吸着後のPyrrole(ピロール;Py)接触によるポリピロール(PPy)重合:
表2の条件3で作製した硫黄ファイバーを用いて、PPyの被覆を行った。各条件を表3に示す。Ptメッシュ(5mm×3mm)上へ硫黄を溶融紡糸したもの(Pt/S)を、iodineの入ったガラスセル中に静置してArガスで脱気後、暗所、50℃(オイルバス中)でiodineをファイバーへ所定時間吸着させた(Pt/S/iodine)。その後、Pt/S/iodineをPyの入ったガラスセル中へ移し、Arガスで脱気後、50℃(オイルバス中)でPyと所定時間接触させた。重合後50℃、24h減圧乾燥を行った。生成したPPy量/(S+PPy)量(%)を表3に示す。
FIG. 5 shows XRD spectra of the fiber and sulfur powder (a) immediately after melt electrospinning of sulfur (b), 2 days later (c), and 5 days later (d). In the XRD spectrum of the sulfur powder, the peak observed at 2θ = 22-23 ° disappeared in the sulfur fiber immediately after spinning, and a new peak appeared in the vicinity of 2θ = 20,24 ° that was not found in the sulfur powder. . Therefore, it can be seen that the sulfur fiber produced by the melt electrospinning method was spun with a crystal structure of polymer sulfur. However, in the XRD spectrum two days and five days after the production of the sulfur fiber, the peak near 2θ = 20,24 ° seen in the fiber immediately after spinning disappears again, and the same XRD spectrum as the sulfur powder is obtained. It was. For these reasons, the crystal structure of the fiber immediately after spinning is unstable, and changes to α sulfur, which is known as a stable crystal structure of elemental sulfur, over time.
(3) Coating of conductive polymer (polypyrrole) Polypyrrole (PPy) polymerization by Pyrolele (pyrrole; Py) contact after adsorption of iodine (iodine):
Using the sulfur fiber produced under Condition 3 in Table 2, coating with PPy was performed. Table 3 shows each condition. Sulfur melt-spun (Pt / S) on a Pt mesh (5 mm x 3 mm) (Pt / S) is placed in a glass cell containing iodine and degassed with Ar gas. ), Iodine was adsorbed to the fiber for a predetermined time (Pt / S / iodine). Thereafter, Pt / S / iodine was transferred into a glass cell containing Py, deaerated with Ar gas, and then contacted with Py at 50 ° C. (in an oil bath) for a predetermined time. After the polymerization, drying was performed under reduced pressure at 50 ° C. for 24 hours. Table 3 shows the amount of PPy produced / (S + PPy) amount (%).
表2の条件3で作製した硫黄ファイバーを用いて、PPyの被覆を行った。各条件を表4に示す。Pt/SをPyの入ったガラスセル中に静置してArガスで脱気後、暗所、50℃(オイルバス中)でPyをファイバーへ所定時間吸着させた(Pt/S/Py)。その後Pt/S/Pyをiodineの入ったガラスセル中へ移し、Arガスで脱気後、暗所、50℃(オイルバス中)でiodineと所定時間吸着させた。重合後50℃、24h減圧乾燥を行った。生成したPPy量/(S+PPy)量(%)を表4に示す。
Using the sulfur fiber produced under Condition 3 in Table 2, coating with PPy was performed. Table 4 shows each condition. Pt / S was allowed to stand in a glass cell containing Py, degassed with Ar gas, and then Py was adsorbed to the fiber for a predetermined time in a dark place at 50 ° C. (in an oil bath) (Pt / S / Py). . Thereafter, Pt / S / Py was transferred into a glass cell containing iodine, degassed with Ar gas, and adsorbed with iodine in a dark place at 50 ° C. (in an oil bath) for a predetermined time. After the polymerization, drying was performed under reduced pressure at 50 ° C. for 24 hours. The amount of PPy produced / (S + PPy) amount (%) is shown in Table 4.
(4)電気化学的挙動
サイクリックボルタンメトリ(CV)測定:
表2の3に示す繊維状硫黄を用い、下記表5に示す条件で導電性ポリマーを被覆した電極の電気化学的挙動を調査するためにCV測定を行った。また比較のために、硫黄繊維を白金メッシュ上へ堆積し、その後50℃で24時間減圧乾燥を行うことで、硫黄電極を作製した。なお、この硫黄電極をSf電極と表記する。測定には電気化学システム[北斗電工株式会社 HZ−5000]を使用した。全ての電極に対して電位走査範囲1.0V−4.5V、走査速度1mVs−1とし、恒温槽[東京理科器械株式会社 EYELA MG−2300]中でセルの温度を30℃で一定に保ち測定を行った。
(4) Electrochemical behavior Cyclic voltammetry (CV) measurement:
In order to investigate the electrochemical behavior of the electrode coated with the conductive polymer under the conditions shown in Table 5 below using the fibrous sulfur shown in 3 of Table 2, CV measurement was performed. For comparison, a sulfur electrode was prepared by depositing sulfur fibers on a platinum mesh and then drying under reduced pressure at 50 ° C. for 24 hours. This sulfur electrode is referred to as an Sf electrode. The electrochemical system [Hokuto Denko Co., Ltd. HZ-5000] was used for the measurement. Measurement was performed with a potential scanning range of 1.0 V to 4.5 V and a scanning speed of 1 mVs −1 for all the electrodes, and the cell temperature was kept constant at 30 ° C. in a thermostatic chamber [Tokyo Science Instruments EYELA MG-2300]. Went.
なお、これらの操作は全てアルゴン雰囲気下、グローブボックス中で行った。 All these operations were performed in a glove box under an argon atmosphere.
また、電解質は1モルLiPF6/プロピレンカーボネート−ジエチルカーボネート(容積比1:1)とする。またCV測定グラフの図の番号をそれぞれ表5に示す。 The electrolyte is 1 mol LiPF 6 / propylene carbonate-diethyl carbonate (volume ratio 1: 1). Table 5 shows the numbers of the CV measurement graphs.
Claims (5)
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| US12424617B2 (en) | 2015-03-12 | 2025-09-23 | University Of Pittsburgh-Of The Commonwealth System Of Higher Education | Electro-spun sulfur wire for fabricating mattes of lithium sulfur batteries |
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