Patent Application
20220285104
The present disclosure relates to an electrochemical device in which a positive electrode having a positive electrode material layer containing a conductive polymer and a negative electrode having a negative electrode material layer storing and releasing lithium ions are combined.
The electrochemical device that stores electric energy can be roughly classified into a high-capacitance electrochemical device performing charging and discharging by a faradaic reaction and a high-output electrochemical device performing charging and discharging by a non-faradaic reaction. As the high-capacitance electrochemical device, a lithium ion secondary battery has been getting a mainstream. On the other hand, a typical device as the high-output electrochemical device is an electric double layer capacitor.
In recent years, an electrochemical device having intermediate property between the lithium ion secondary battery and the electric double layer capacitor also attracts attention (refer to International Publication No. WO 2011/058748). For example, a lithium ion capacitor has a structure in which a positive electrode used in the electric double layer capacitor and a negative electrode used in the lithium ion secondary battery are combined, and has both property of the former and property of the latter. However, the positive electrode used for the electric double layer capacitor is a polarizable electrode and has a small capacity. Therefore, it is difficult in many cases to achieve a required high capacity as long as such a positive electrode is used.
On the other hand, it is investigated to use, as a positive electrode material, a conductive polymer which allows a faradaic reaction to proceed in association with the adsorption (doping) and desorption (dedoping) of the anion (refer to Unexamined Japanese Patent Publication No. S64-21873, Unexamined Japanese Patent Publication No. H01-132051, Unexamined Japanese Patent Publication No. 2014-123641). The positive electrode containing the conductive polymer has an adequately large capacity compared with a polarizable electrode and an adequately high output compared with a positive electrode used in a common lithium ion secondary battery.
In the adsorption and desorption of the anion, the conductive polymer does not greatly change its structure. Therefore, structural degradation of the conductive polymer is small. Thus, the conductive polymer is suitable for a long-life electrochemical device. Further, since the conductive polymer does not contain oxygen internally, a thermal runaway is unlikely to occur, and thus high safety can be expected.
An electrochemical device according to one aspect of the present disclosure include a positive electrode having a positive electrode material layer, a negative electrode having a negative electrode material layer, and a nonaqueous electrolytic solution having lithium ionic conductivity. The positive electrode material layer contains a conductive polymer doped with a first anion and a second anion. The negative electrode material layer stores and releases lithium ions. The second anion is more easily dedoped from the conductive polymer than the first anion. At an end period of charge of the electrochemical device, a number of moles M1 of the first anion and a number of moles M2 of the second anion respectively doped in the conductive polymer satisfy a relationship of M1<M2. At an end period of discharge of the electrochemical device, a number of moles M3 of the first anion and a number of moles M4 of the second anion respectively doped in the conductive polymer satisfy a relationship of M3>M4.
A method for manufacturing an electrochemical device according to another aspect of the present disclosure includes: a step of forming a positive electrode having a positive electrode material layer containing a conductive polymer; a step of forming a negative electrode having a negative electrode material layer storing and releasing lithium ions; and a step of immersing the positive electrode and the negative electrode in a nonaqueous electrolytic solution having lithium ionic conductivity. The step of forming a positive electrode includes: a step of polymerizing a polymerizable compound which is a raw material of the conductive polymer in a first solution containing a first anion so as to obtain the conductive polymer doped with the first anion; and a step of doping a second anion in the conductive polymer doped with the first anion in a second solution containing the second anion which is more easily dedoped from the conductive polymer than the first anion.
A method for manufacturing an electrochemical device according to another aspect of the present disclosure includes: a step of forming a positive electrode having a positive electrode material layer containing a conductive polymer; a step of forming a negative electrode having a negative electrode material layer storing and releasing lithium ions; and a step of immersing the positive electrode and the negative electrode in a nonaqueous electrolytic solution having lithium ionic conductivity. The step of forming a positive electrode includes a step of polymerizing a polymerizable compound which is a raw material of the conductive polymer in a first solution containing a first anion so as to obtain the conductive polymer doped with the first anion. The nonaqueous electrolytic solution contains a second anion which is more easily dedoped from the conductive polymer than the first anion. The step of immersing the positive electrode and the negative electrode in the nonaqueous electrolytic solution includes a step of doping the second anion in the conductive polymer doped with the first anion in the nonaqueous electrolytic solution.
According to the present disclosure, it is possible to attain an electrochemical device in which a positive electrode having a positive electrode material layer containing a conductive polymer and a negative electrode having a negative electrode material layer storing and releasing lithium ions are combined, the electrochemical device having excellent reliability and being able to charge and discharge stably over a long period.
In the conventional electrochemical device, in order to maintain high conductivity in the conductive polymer, it is necessary to stabilize anions with which the conductive polymer is doped. In the meanwhile, in order to stably repeat charging and discharging, it is necessary that internal resistance is kept low, and doping and dedoping of the anions in and from the conductive polymer can be easily performed.
An electrochemical device according to the present disclosure includes a positive electrode having a positive electrode material layer containing a conductive polymer doped with a first anion and a second anion, a negative electrode having a negative electrode material layer storing and releasing lithium ions, and a nonaqueous electrolytic solution having lithium ionic conductivity. The second anion is more easily dedoped from the conductive polymer than the first anion.
In the electrochemical device at the end of charge, a number of moles M1 of the first anion and a number of moles M2 of the second anion respectively doped in the conductive polymer are configured to satisfy a relationship of M1<M2 from the viewpoint of ensuring a high capacitance. In this time, M2/M1 is preferably 1 or more, and more preferably 3 or more. On the other hand, in the electrochemical device at the end of discharge, a number of moles M3 of the first anion and a number of moles M4 of the second anion respectively doped in the conductive polymer are configured to satisfy a relationship of M3>M4. This means that the second anion is mainly doped or dedoped in or from the conductive polymer in association with charging and discharging. In other words, the second anion mainly plays a role of exerting a faradaic reaction in association with charging and discharging.
Further, an amount of the first anion doped in the conductive polymer does not greatly vary in association with charging and discharging. The first anion plays a role of imparting conductivity to the conductive polymer. Therefore, a difference between M1 and M3 is small, and the difference between M1 and M3 (|M3−M1|) with respect to M1 is, for example, within ±10%.
The conductive polymer is preferably a π-conjugated polymer having a repeating unit containing a heteroatom. The heteroatom (nitrogen atom, sulfur atom, etc.) in the π-conjugated polymer tends to interact with an anion. It is thought that the anion adsorbs to or releases from the heteroatom in oxidation-reduction of the conductive polymer.
From the viewpoint of enhancing the stability of the first anion doped in the conductive polymer, a number of moles (Mx) of the first anion doped in the conductive polymer per mole of the heteroatom is preferably small during the time from an end period of charge to an end period of discharge. Mx is preferably, for example, 0.1 moles or less. However, when the Mx is too small, conductivity of the conductive polymer is lowered and internal resistance of the electrochemical device is increased. Therefore, Mx is preferably 0.001 moles or more, and more preferably 0.01 moles or more.
Herein, in the present disclosure, the end period of charge means a period being in a state in which a depth of discharge (ratio of a discharge amount to a capacitance at the time of full charge) of an electrochemical device is 10% or less. And a voltage between terminals at the time of charging before reaching this state is an end-of-charge voltage. Further, the end period of discharge means a period being in a state in which a depth of discharge of an electrochemical device is 90% or more. And a voltage between terminals at the time of discharging before reaching this state is an end-of-discharge voltage. The end-of-charge voltage and the end-of-discharge voltage can be defined according to a design of the electrochemical device so that the depth of discharge ranges from 0% to 10%, inclusive and 90% to 100%, inclusive, respectively. When the π-conjugated polymer is used as the conductive polymer, and a carbon material capable of insertion or desorption of the lithium ion is used as the negative electrode material, for example, the end-of-charge voltage is defined in a range from 3.7 V to 3.9 V, inclusive, and the end-of-discharge voltage is defined in a range from 2.0 V to 2.6 V, inclusive. When the π-conjugated polymer is used as the conductive polymer, and lithium titanate capable of insertion or desorption of the lithium ion is used as the negative electrode material, for example, the end-of-charge voltage is defined in a range from 2.4 V to 2.6 V, inclusive, and the end-of-discharge voltage is defined in a range from 1.6 V to 2.2 V, inclusive. That is, the end-of-charge voltage and the end-of-discharge voltage are determined by a combination of the positive electrode material and the negative electrode material.
Hereinafter, each constituent of the electrochemical device will be described in more detail.
The positive electrode has a positive electrode material layer in which an oxidation-reduction reaction involving doping and dedoping of the second anion is advanced. The positive electrode material layer is usually supported on a positive current collector. For example, a conductive sheet material is used for the positive current collector. As the sheet material, a metal foil, a metal porous body, a punching metal or the like is used. As a material of the positive current collector, aluminum, an aluminum alloy, nickel, titanium or the like can be used.
The positive electrode material layer contains a conductive polymer as a positive electrode active material. As the conductive polymer, a t-conjugated polymer is preferred, and polypyrrole, polythiophene, polyfuran, polyaniline, polythiophene vinylene, polypyridine, and derivatives thereof can be used. These conductive polymers may be used alone, or may be used in combination of two or more of the conductive polymers. A weight average molecular weight of the conductive polymer is not particularly limited and ranges, for example, from 1000 to 100000, inclusive.
In addition, the derivatives of polypyrrole, polythiophene, polyfuran, polyaniline and the like of the π-conjugated polymer mean polymers having, as a basic skeleton, polypyrrole, polythiophene, polyaniline, polythiophene vinylene, polypyridine and the like, respectively. For example, polythiophene derivative includes poly(3,4-ethylenedioxythiophene) (PEDOT) and the like.
The conductive polymer exerts excellent conductivity by doping a dopant. Herein, as described above, a conductive polymer is used which contains, as dopants, a first anion and a second anion with a predetermined balance at the end periods of charge and discharge.
The first anion is an anion which is relatively hardly dedoped from the conductive polymer, and is preferably an oxo acid anion not containing a halogen atom. Examples of the oxo acid anion not containing a halogen atom include a sulfate ion, a nitrate ion, a phosphate ion, a borate ion, a sulfonate ion, and the like. Examples of the sulfonate ion include a benzenesulfonate ion, methanesulfonic acid, toluenesulfonic acid, and the like. Among these oxo acid anions, a sulfate ion, a sulfonate ion and the like are preferred in that these tend to be stable in the conductive polymer. These ions may be used alone, or may be used in combination of two or more of the ions.
The first anion may be a polymer ion. Examples of a first anion of a polymer include ions of polyvinylsulfonic acid, polystyrenesulfonic acid, polyallylsulfonic acid, polyacrylsulfonic acid, polymethacrylsulfonic acid, poly(2-acrylamido-2-methylpropanesulfonic acid), polyisoprenesulfonic acid, and polyacrylic acid. These polymers may be a homopolymer or a copolymer of two or more monomers. These polymers may be used alone, or may be used in combination of two or more of these polymers. However, the first anion of a polymer is used, a number of moles of an anionic group (sulfonate group, acrylate group, etc.) is treated as a number of moles of the first anion.
The second anion may be an anion which is more easily dedoped from the conductive polymer than the first anion. Examples of the second anion include ClO4−, BF4−, PF6−, AlCl4−, SbF6−, SCN—, CF3SO3−, FSO3−, CF3CO2−, AsF6−, B10Cl10−, Cl—, Br—, I—, BCl4−, N(FSO2)2−, N(CF3SO2)2− and the like. Among these anions, oxo acid anions containing a halogen atom are preferred, and imide anion and the like are preferred. As the oxo acid anion containing a halogen atom, tetrafluoroborate anion (BF4−), hexafluorophosphate anion (PF6−), perchloric acid anion (ClO4−), fluorosulfate anion (FSO3−), and the like are preferred. As the imide anion, bis(fluorosulfonyl)imide anion (N(FSO2)2−) is preferred. These anions may be used alone, or may be used in combination of two or more of these anions.
The negative electrode has a negative electrode material layer in which an oxidation-reduction reaction involving storing and releasing of the lithium ion is advanced. The negative electrode material layer is usually supported on a negative current collector. For example, a conductive sheet material is used for the negative current collector. As the sheet material, a metal foil, a metal porous body, a punching metal or the like is used. As a material of the negative current collector, copper, a copper alloy, nickel, stainless steel or the like can be used.
For the negative electrode material layer, a material which electrochemically stores and releases lithium ions is used as the negative electrode active material. Examples of such a material include a carbon material, a metal compound, an alloy, a ceramic material and the like. As the carbon material, graphite, non-graphitizable carbon (hard carbon), and easily graphitizable carbon (soft carbon) are preferred, and graphite and hard carbon are particularly preferred. Examples of the metal compound include silicon oxide, tin oxide and the like. Examples of the alloy include a silicon alloy, a tin alloy and the like. Examples of the ceramic material include lithium titanate, lithium manganate, and the like. These materials may be used alone, or may be used in combination of two or more of these materials. Among these materials, a carbon material can achieve low potential of the negative electrode, and thus is preferred.
The negative electrode material layer preferably contains a conducting agent, a binder and the like beside the negative electrode active material. Examples of the conducting agent include carbon black, carbon fibers, and the like. Examples of the binder include a fluorine resin, an acrylic resin, a rubber material, a cellulose derivative, and the like. Examples of the fluorine resin include polyvinylidene fluoride, polyterafluoroethylene, terafluoroethylene-hexafluoropropylene copolymer, and the like. Examples of the acrylic resin include polyacrylic acid, acrylic acid-methacrylic acid copolymer, and the like. Examples of the rubber material include a styrene-butadiene rubber, and examples of the cellulose derivative include carboxymethyl cellulose.
The lithium ion is preferably pre-doped in the negative electrode in advance. Thereby, a potential of the negative electrode is lowered, and therefore a difference in potential between the positive electrode and the negative electrode (that is, a voltage) is increased and energy density of the electrochemical device is improved.
Pre-doping of lithium ions in the negative electrode is advanced, for example, by forming a metal lithium film serving as a supply source of a lithium ion on the surface of the negative electrode material layer, and impregnating the negative electrode having the metal lithium film with the nonaqueous electrolytic solution having lithium ionic conductivity. In this time, the lithium ion is eluted in the nonaqueous electrolytic solution from the metal lithium film and the eluted lithium ion is stored in the negative electrode active material. For example, when graphite or hard carbon is used as the negative electrode active material, lithium ions are inserted in the interlayer of the graphite or the fine pores of the hard carbon. An amount of lithium ion to be pre-doped can be controlled by a mass of the metal lithium film.
A method of forming the metal lithium film on the surface of the negative electrode material layer may be a method of bonding a metal lithium foil to the negative electrode material layer, or may be a method of depositing a lithium film on the surface of the negative electrode material layer applying a vapor phase method. The vapor phase method is, for example, a method of using a vacuum deposition apparatus, and a thin film of metal lithium can be formed by evaporating metal lithium in an apparatus in which a degree of vacuum is enhanced and depositing the metal lithium on the surface of the negative electrode material layer.
The nonaqueous electrolytic solution having lithium ionic conductivity includes a lithium salt and a nonaqueous solvent in which the lithium salt is dissolved. In this time, when a salt containing the second anion is used as the lithium salt, it becomes possible to reversibly repeat doping and dedoping of the second anion in and from the positive electrode. On the other hand, lithium ions derived from the lithium salt are stored in the negative electrode.
Examples of the lithium salt include LiClO4, LiBF4, LiPF6, LiAlCl4, LiSbF6, LiSCN, LiCF3SO3, LiFSO3, LiCF3CO2, LiAsF6, LiB10Cl10, LiCl, LiBr, LiI, LiBCl4, LiN(FSO2)2, LiN(CF3SO2)2 and the like. These lithium compounds may be used alone, or may be used in combination of two or more of these lithium compounds. Among these lithium compounds, at least one selected from the group consisting of lithium salts having the oxo acid anion containing a halogen atom which is suitable for the second anion and lithium salts having the imide anion, are preferably used. A concentration of the lithium salt in the nonaqueous electrolytic solution may range, for example, from 0.2 mol/L to 4 mol/L, inclusive and is not particularly limited.
Examples of the nonaqueous solvent include cyclic carbonates such as ethylene carbonate, propylene carbonate, and butylene carbonate; chain carbonates such as dimethyl carbonate, diethyl carbonate, and ethyl methyl carbonate; aliphatic carboxylate esters such as methyl formate, methyl acetate, methyl propionate, and ethyl propionate; lactones such as γ-butyrolactone and γ-valerolactone; chain ethers such as 1,2-dimethoxyethane (DME), 1,2-diethoxyethane (DEE) and ethoxymethoxyethane (EME); cyclic ethers such as tetrahydrofuran and 2-methyltetrahydrofuran; dimethylsulfoxide, 1,3-dioxolane, formamide, acetamide, dimethylformamide, dioxolane, acetonitrile, propionitrile, nitromethane, ethylmonoglyme, trimethoxymethane, sulfolane, methyl sulfolane, 1,3-propanesultone or the like can be used. These compounds may be used alone, or may be used in combination of two or more of these compounds.
An additive may be contained in the nonaqueous electrolytic solution, and contained in the nonaqueous solvent as required. For example, unsaturated carbonate such as vinylene carbonate, vinyl ethylene carbonate, and divinyl ethylene carbonate may be added as an additive for forming a coating having high lithium ionic conductivity on the surface of the negative electrode.
A group of electrodes in laminate type or wound type is formed by laminating a positive electrode and a negative electrode with a separator interposed between the positive electrode and the negative electrode or by winding a belt-shaped positive electrode and a belt-shaped negative electrode with a separator interposed between the positive electrode and the negative electrode. As a material of the separator, a nonwoven fabric made of cellulose fiber, a nonwoven fabric made of glass fiber, a microporous membrane made of polyolefin, a fabric cloth, a nonwoven fabric or the like is preferably used. A thickness of the separator is, for example, 10 μm to 300 μm, inclusive, and preferably 10 μm to 40 μm, inclusive.
Next, one example of a method for manufacturing an electrochemical device will be described. In the following examples, it is easy to control a quantitative balance between the first anion and the second anion respectively doped in the conductive polymer. However, the method for manufacturing an electrochemical device is not limited to the following examples.
The conductive polymer contained in the positive electrode material layer of the positive electrode is synthesized by polymerizing a polymerizable compound (monomer) serving as a raw material of the conductive polymer. Synthesis of the conductive polymer may be performed by electrolytic polymerization or may be performed by chemical polymerization. In this time, the conductive polymer doped with first anions can be obtained by polymerizing the monomer in the first solution containing the first anions. For example, a conductive sheet material (e.g., metal foil) is prepared as a positive current collector, the positive current collector and the counter electrode are immersed in the first solution. By applying a current between the positive current collector as an anode and the counter electrode, a film of a conductive polymer doped with the first anions is formed so as to cover at least part of the surface of the positive current collector.
The first solution is formed by dissolving a supporting electrolyte containing the first anion in a solvent. As the solvent, water may be used, but the nonaqueous solvent may be used in consideration of a solubility of a monomer. As the nonaqueous solvent, alcohols such as ethyl alcohol, methyl alcohol, isopropyl alcohol, ethylene glycol and propylene glycol are preferably used. As the supporting electrolyte, a conjugated acid of the first anion or an alkali metal salt containing the first anion (sodium salt, potassium salt, etc.) may be used. Specifically, an acid aqueous solution formed by dissolving sulfuric acid, sodium sulfate, phosphoric acid, dibasic sodium phosphate or the like is preferably used as the first solution. It is preferred that the first solution is controlled so as to have a pH ranging from 0 to 4, inclusive, and a temperature ranging from 0° C. to 45° C., inclusive. A current density is not particularly limited; however, preferably it ranges from 1 mA/cm2 to 100 mA/cm2, inclusive. It is preferred to dissolve a polymerizable compound (monomer) in the first solution at a concentration ranging from 0.1 mol/L to 3 mol/L, inclusive. A concentration of the first anion ranges preferably from 0.1 mol/L to 5 mol/L, inclusive.
Next, a second anion is doped in the conductive polymer doped with the first anions in a second solution containing the second anions. For example, the positive current collector having a film of the conductive polymer doped with the first anion and the current collector are immersed in the second solution. By applying a potential more noble than that of the counter electrode to the positive current collector, the second anion is further doped in the film of the conductive polymer doped with the first anion. Thereby, it is possible to form a positive electrode material layer containing a conductive polymer doped with first anions and second anions in a state of being supported on the positive current collector.
The second solution is formed by dissolving a supporting electrolyte containing the second anion in a solvent. As the solvent, water may be used, but the nonaqueous solvent is used when the second anion is unstable in water. As the supporting electrolyte, a conjugated acid of the second anion or an alkali metal salt containing the second anion (sodium salt, potassium salt, lithium salt, etc.) may be used. As the second solution, a nonaqueous electrolytic solution containing the second anion which is used for an electrochemical device described later may be used. The supporting electrolyte at this time is a lithium salt dissolved in the nonaqueous electrolytic solution. With respect to conditions in doping the second anion, a temperature of the second solution is preferably controlled so as to be a range from 40° C. to 80° C., inclusive. A potential to be applied to the positive current collector may be a range from 3.5 V to 4.2 V, inclusive, with respect to the metal lithium. A concentration of the second anion is preferably a range from 0.1 mol/L to 4 mol/L, inclusive.
As described above, by doping the first anion and the second anion in the conductive polymer so as to separate a step of doping of the first anion and a step of doping of the second anion which are performed as different steps from each other, it is easy to control a quantitative balance between the first anion and the second anion.
In addition, in the above described step of synthesizing the conductive polymer, the electrolytic polymerization is performed, but the conductive polymer may be synthesized by the chemical polymerization. And the first anion may be doped in the conductive polymer after synthesizing a conductive polymer not containing the first anion.
When the second anion is doped in the conductive polymer doped with the first anions in the nonaqueous electrolytic solution, a group of electrodes may be assembled before the step of doping the second anion is performed, and then the group of electrodes may be housed in a case of the electrochemical device together with the nonaqueous electrolytic solution. In this case, by applying a charge voltage to the group of electrodes so that a positive potential becomes higher, the second anion is doped in the conductive polymer. On the other hand, part of the lithium ions is further doped in the negative electrode. Therefore, considering an amount of the second anion to be doped in the conductive polymer, a concentration of the lithium salt contained in the nonaqueous electrolytic solution is preferably set to a range from 0.1 mol/L to 4 mol/L, inclusive.
The step of removing part of the first anion from the conductive polymer doped with the first anion may be performed prior to the step of doping the second anion in the conductive polymer. Thereby, a site of the conductive polymer in which the second anion contributing to charging and discharging can be doped is increased. Therefore, an electrochemical device having a higher capacitance can be attained. Further, by removing part of the first anion, it becomes easy to allow part of the second anion to remain in a state of being doped in the conductive polymer at the end period of discharge. Furthermore, when part of the first anion is removed, the first anion doped in the conductive polymer in a relatively unstable state is easily removed earlier. It is thought that the first anion remaining in a state of being doped in the conductive polymer without being removed is able to still keep on stably remaining in the conductive polymer.
The step of removing part of the first anion can be performed subsequent to the step of synthesizing the conductive polymer doped with the first anions. For example, by applying the reverse current which brings the positive current collector into a cathode between the counter electrode and the positive current collector in a state of being immersed in the first solution, the positive current collector having a film of the conductive polymer doped with the first anion, the conductive polymer is reduced and part of the first anion is dedoped. Also, it is possible to dedope the first anion by similarly applying the reverse current in a solution different from the first solution. A current density (I1) of the reverse current is preferably lower than a current density (I0) at the time of synthesizing the conductive polymer doped with the first anion, and I1 is preferably controlled so as to be a range from 5% to 50% of I0, inclusive. In this time, when the conductive polymer is a π-conjugated polymer containing a heteroatom, it is preferred to reduce the conductive polymer until a number of moles (Mx) of the first anion per mole of the heteroatom becomes 0.1 moles or less.
The negative electrode material layer of the negative electrode is formed, for example, by preparing a negative electrode mixture paste as a mixture of a negative electrode active material, a conducting agent, a binder and a dispersing medium, and applying the negative electrode mixture paste onto the positive current collector. For the dispersing medium, water, N-methyl-2-pyrrolidone (NMP) or the like is preferably used. Thereafter, an applied film is preferably pressed between rollers in order to enhance strength of the negative electrode material layer.
A step of pre-doping lithium ions in the negative electrode may be performed before assembling the group of electrodes, or pre-doping may be advanced after housing the group of electrodes in a case of the electrochemical device together with the nonaqueous electrolytic solution. In the latter case, the metal lithium film is previously formed on the surface of the negative electrode, and then the group of electrodes may be prepared.
(iii) Step of Immersing a Group of Electrodes in Nonaqueous Electrolytic Solution
The group of electrodes is housed in, for example, a bottomed case having an opening together with the nonaqueous electrolytic solution. Thereafter, the opening is blocked with a sealing body to complete an electrochemical device.
Group of electrodes 10 is a wound body as shown in
In the exemplary embodiment described above, a wound electrochemical device having a cylindrical shape has been described. The application range of the present disclosure, however, is not limited to the wound electrochemical device and can also be applied to a square or a laminate type electrochemical device.
Hereinafter, the present disclosure will be described in more detail with reference to examples; however, the present disclosure is not to be considered to be limited to the examples.
An aluminum foil having a thickness of 30 μm was prepared as a positive current collector. On the other hand, as a first solution, a solution containing aniline at concentration of 1 mol/L and sulfuric acid at concentration of 2 mol/L was prepared. The first solution was adjusted to a pH of 0.6 and a temperature of 25° C.
A positive current collector and a stainless steel counter electrode were immersed in the first solution. And then electrolytic polymerization at a current density of 10 mA/cm2 for 20 minutes was conducted to deposit a film of a conductive polymer (polyaniline) doped with sulfate ions (SO42−) as the first anion on both entire front surface and entire back surface of the positive current collector.
The positive current collector having the film of the conductive polymer doped with sulfate ions and the counter electrode were taken out from the first solution, and then immersed in a 0.1 mol/L sulfuric acid aqueous solution. Next, a reverse current of a current density of 1 mA/cm2 was applied between the positive current collector and the stainless steel counter electrode for 20 minutes. Thereby, the conductive polymer was reduced to dedope part of the sulfate ions that have been doped in the conductive polymer. In this manner, a conductive polymer film doped with a predetermined amount of first anions was formed. A thickness of the conductive polymer film was 60 μm at each of the front surface and the back surface of the positive current collector. The conductive polymer film was adequately washed with water, and then subjected to vacuum drying at 100° C. for 12 hours.
A copper foil having a thickness of 20 μm was prepared as a negative current collector. On the other hand, carbon paste was prepared by kneading mixed powder and water at a weight ratio of 40:60. The mixed powder was a mixture of hard carbon of 97 parts by mass, carboxy cellulose of 1 part by mass, and styrene butadiene rubber of 2 parts by mass. The carbon paste was applied on both surfaces of the negative current collector and dried to obtain a negative electrode having a negative electrode material layer with a thickness of 35 μm on each of both surfaces. Next, a metal lithium foil was attached to the negative electrode material layer. An amount of the metal lithium foil was calculated so that a negative potential in the nonaqueous electrolytic solution after completion of pre-doping is 0.2 V or less with respect to metal lithium.
After a lead tab was connected to each of the positive electrode and the negative electrode, as shown in
Vinylene carbonate of 0.2% by mass was added to a mixture of propylene carbonate and dimethyl carbonate at a volume ratio of 1:1 to prepare a nonaqueous solvent. LiPF6 was dissolved in the resulting nonaqueous solvent in a concentration of 2 mol/L to prepare a nonaqueous electrolytic solution having hexafluorophosphate anions (PF6−) as the second anion.
The group of electrodes and the nonaqueous electrolytic solution were housed in a bottomed case having an opening. And an electrochemical device as shown in
An electrochemical device (A2) was prepared in the same manner as in Example 1 except that in the preparation of the positive electrode material layer, the condition of reducing the conductive polymer by the reverse current was changed a condition of reducing at a current density of 2 mA/cm2 for 15 minutes.
An electrochemical device (B1) was prepared in the same manner as in Example 1 except that in the preparation of the positive electrode material layer, the condition of reducing the conductive polymer by the reverse current was changed to a condition of reducing at a current density of 5 mA/cm2 for 120 minutes.
An electrochemical device (B2) was prepared in the same manner as in Example 1 except that in the preparation of the positive electrode material layer, an operation of removing part of the first anion, that is, reducing the conductive polymer by the reverse current was not carried out.
An electrochemical device (B3) was prepared in the same manner as in Example 1 except that an operation of heating at 60° C. for 24 hours while applying a charge voltage of 3.6 V between a terminal of a positive electrode and a terminal of a negative electrode, that is, doping of the second anion in the conductive polymer was not carried out.
Immediately after completion of the electrochemical device at the time when a voltage between terminals was 3.2 V, the electrochemical device was disassembled. The positive electrode was taken out from the electrochemical device, and an amount of the dopant contained in the positive electrode material layer was measured. From an amount of the first anion (SO42−) at this time, a number of moles (Mx) of the first anion per mole of the heteroatom (i.e., nitrogen atom) in polyaniline (that is, per mole of polyaniline) was determined. Similarly, a number of moles (My) of the second anion (PF6−) per mole of the heteroatom was determined.
Similarly, also in an electrochemical device at the end of charge which was charged until the voltage between terminals reached 3.8 V, an amount of the dopant contained in the positive electrode material layer was measured. And a number of moles of the first anion per mole of the heteroatom as M1 and a number of moles of the second anion per mole of the heteroatom as M2 were obtained.
Similarly, also in an electrochemical device at the end of discharge which was discharged until the voltage between terminals reached 2.5 V, an amount of the dopant contained in the positive electrode material layer was measured. And a number of moles of the first anion per mole of the heteroatom as M3 and a number of moles of the second anion per mole of the heteroatom as M4 were obtained.
An amount of sulfate ion (SO42−) was determined by measuring a concentration of the sulfate ion in an absorbing solution by ion chromatography, the absorbing solution being made by absorbing a gas generated in burning the positive electrode material layer. An amount of hexafluorophosphate anion (PF6−) was determined by measuring a P (phosphorus) concentration of a solution by inductively coupled plasma (ICP) atomic emission spectrometry, the solution being made by dissolving the positive electrode material layer in a mixed acid (mixture of hydrochloric acid and nitric acid) by heating, allowing to cool, separating an insoluble matter by filtration to define a volume.
An initial capacity (C0) and internal resistance (R0) of the electrochemical device were measured. Then, the electrochemical device was kept at 60° C. for 1000 hours while applying a charge voltage of 3.5 V. After that, a capacitance (C1) and internal resistance (R1) of the electrochemical device were measured.
Table 1 shows results of the above evaluation.
From Table 1, it became apparent that an electrochemical device excellent in both of initial characteristics and characteristics after keeping can be realized by satisfying both relationships of M1<M2 and M3>M4.
The electrochemical device according to the present disclosure can be suitably applied to use which has a higher capacitance than that of the electric double layer capacitor and the lithium ion capacitor, and requires a higher output than that of the lithium ion secondary battery.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-232340 | Nov 2015 | JP | national |
This application is a continuation of U.S. patent application Ser. No. 15/977,001, filed on May 11, 2018, which is a continuation of the PCT International Application No. PCT/JP2016/004724 filed on Oct. 27, 2016, which claims the benefit of foreign priority of Japanese patent application No. 2015-232340 filed on Nov. 27, 2015, the contents all of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 15977001 | May 2018 | US |
| Child | 17553035 | US | |
| Parent | PCT/JP2016/004724 | Oct 2016 | US |
| Child | 15977001 | US |
