Patent Application
20190189991
This Nonprovisional application claims priority under 35 U.S.C. § 119 on Patent Application No. 2017-243281 filed in Japan on Dec. 19, 2017, the entire contents of which are hereby incorporated by reference.
The present invention relates to a nonaqueous electrolyte secondary battery.
Nonaqueous electrolyte secondary batteries, particularly lithium-ion secondary batteries, have a high energy density, and are therefore in wide use as batteries for a personal computer, a mobile telephone, a portable information terminal, and the like. Such nonaqueous electrolyte secondary batteries have recently been developed as on-vehicle batteries.
For example, Patent Literature 1 discloses a nonaqueous electrolyte secondary battery including a separator for a nonaqueous electrolyte secondary battery (hereinafter referred to as a “nonaqueous electrolyte secondary battery separator”) which separator includes a polyolefin porous film. The polyolefin porous film has a nonaqueous electrolyte retaining property which has been controlled to a specific range such that (i) a diminution rate of diethyl carbonate dropped onto the polyolefin porous film is 15 sec/mg to 21 sec/mg, and (ii) a spot diameter of the diethyl carbonate 10 seconds after dropping is not less than mm. Patent Literature 1 discloses that such a nonaqueous electrolyte secondary battery exhibits a favorable discharge rate characteristic and cycle characteristic.
[Patent Literature 1]
Specification of Japanese Patent No. 6153992 (publication date: Jun. 28, 2017)
However, the above conventional nonaqueous electrolyte secondary battery has room for improvement in terms of restored discharge capacity after high-rate discharge.
An object of the present invention is to provide a nonaqueous electrolyte secondary battery having an excellent restored discharge capacity after high-rate discharge.
Embodiments of the present invention may include a nonaqueous electrolyte secondary battery as described in [1] to [6] below.
[1] A nonaqueous electrolyte secondary battery including:
a nonaqueous electrolyte secondary battery separator containing a polyolefin porous film;
a porous layer containing a polyvinylidene fluoride-based resin;
a positive electrode plate having a value in a range of 0.00 to 0.50, which value is represented by the following Formula (1); and
a negative electrode plate having a value in a range of 0.00 to 0.50, which value is represented by the following Formula (1):
|1−T/M| (1)
where T represents a distance at which a critical load is reached in a scratch test in which the positive electrode plate or the negative electrode plate is moved in a transverse direction under a constant load of 0.1 N, and M represents a distance at which a critical load is reached in a scratch test in which the positive electrode plate or the negative electrode plate is moved in a machine direction under a constant load of 0.1 N,
a diminution rate at which diethyl carbonate dropped onto the polyolefin porous film diminishes being in a range of 15 sec/mg to 21 sec/mg,
a spot diameter of diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the polyolefin porous film being not less than 20 mm,
the porous layer being provided between the nonaqueous electrolyte secondary battery separator and at least one of the positive electrode plate and the negative electrode plate,
the polyvinylidene fluoride-based resin containing an α-form polyvinylidene fluoride-based resin and a β-form polyvinylidene fluoride-based resin,
assuming that a sum of (i) an amount of the α-form polyvinylidene fluoride-based resin contained in the polyvinylidene fluoride-based resin and (ii) an amount of the β-form polyvinylidene fluoride-based resin contained in the polyvinylidene fluoride-based resin is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin being not less than 35.0 mol %,
the amount of the α-form polyvinylidene fluoride-based resin contained being calculated from (i) waveform separation of (α/2) observed at around −78 ppm in a 19F-NMR spectrum obtained from the porous layer and (ii) waveform separation of {(α/2)+β} observed at around −95 ppm in the 19F-NMR spectrum.
[2] The nonaqueous electrolyte secondary battery as described in [1], wherein the positive electrode plate contains a transition metal oxide.
[3] The nonaqueous electrolyte secondary battery as described in [1] or [2], wherein the negative electrode plate contains graphite.
[4] The nonaqueous electrolyte secondary battery as described in any one of [1] through [3], further including: another porous layer which is provided between (i) the nonaqueous electrolyte secondary battery separator and (ii) at least one of the positive electrode plate and the negative electrode plate.
[5] The nonaqueous electrolyte secondary battery as described in [4], wherein the another porous layer contains at least one resin selected from the group consisting of a polyolefin, a (meth)acrylate-based resin, a fluorine-containing resin (excluding a polyvinylidene fluoride-based resin), a polyamide-based resin, a polyester-based resin, and a water-soluble polymer.
[6] The nonaqueous electrolyte secondary battery as described in [5], wherein the polyamide-based resin is an aramid resin.
A nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention has an excellent restored discharge capacity after high-rate discharge.
The following description will discuss an embodiment of the present invention in detail. Note that numerical expressions such as “A to B” herein mean “not less than A and not more than B”.
A nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention includes: a nonaqueous electrolyte secondary battery separator containing a polyolefin porous film; a porous layer containing a polyvinylidene fluoride-based resin; a positive electrode plate having a value in a range of 0.00 to 0.50, which value is represented by the following Formula (1); and a negative electrode plate having a value in a range of 0.00 to 0.50, which value is represented by the following Formula (1):
|1−T/M| (1)
where T represents a distance at which a critical load is reached in a scratch test in which the positive electrode plate or the negative electrode plate is moved in a transverse direction (TD) under a constant load of 0.1 N, and M represents a distance at which a critical load is reached in a scratch test in which the positive electrode plate or the negative electrode plate is moved in a machine direction (MD) under a constant load of 0.1 N (these distances may be hereinafter referred to as “critical load distance”),
a diminution rate at which diethyl carbonate dropped onto the polyolefin porous film diminishes being in a range of 15 sec/mg to 21 sec/mg,
a spot diameter of diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the polyolefin porous film being not less than 20 mm,
the porous layer being provided between the nonaqueous electrolyte secondary battery separator and at least one of the positive electrode plate and the negative electrode plate,
the polyvinylidene fluoride-based resin containing an α-form polyvinylidene fluoride-based resin and a β-form polyvinylidene fluoride-based resin,
assuming that a sum of (i) an amount of the α-form polyvinylidene fluoride-based resin contained in the polyvinylidene fluoride-based resin and (ii) an amount of the β-form polyvinylidene fluoride-based resin contained in the polyvinylidene fluoride-based resin is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin being not less than 35.0 mol %,
the amount of the α-form polyvinylidene fluoride-based resin contained being calculated from (i) waveform separation of (α/2) observed at around −78 ppm in a 19F-NMR spectrum obtained from the porous layer and (ii) waveform separation of {(α/2)+β} observed at around −95 ppm in the 19F-NMR spectrum.
Note that a nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention includes not only the above-described positive electrode plate, negative electrode plate, nonaqueous electrolyte secondary battery separator, and porous layer, but also other component(s) such as a nonaqueous electrolyte.
<Nonaqueous Electrolyte Secondary Battery Separator>
A nonaqueous electrolyte secondary battery separator in accordance with an embodiment of the present invention includes a polyolefin porous film (hereinafter also referred to as “porous film”).
The porous film itself can be the nonaqueous electrolyte secondary battery separator. The porous film can also serve as a base material of a laminated separator for a nonaqueous electrolyte secondary battery (hereinafter referred to as a “nonaqueous electrolyte secondary battery laminated separator”) in which a porous layer (described later) is disposed. The porous film contains polyolefin-based resin as a main component and has a large number of pores therein, which pores are connected to one another, so that a gas and a liquid can pass through the porous film from one surface of the porous film to the other.
On at least one surface of the nonaqueous electrolyte secondary battery separator in accordance with an embodiment of the present invention, a porous layer containing a polyvinylidene fluoride-based resin (described later) can be disposed. In such a case, a laminated body obtained by disposing the porous layer on the at least one surface of the nonaqueous electrolyte secondary battery separator is herein also referred to as “nonaqueous electrolyte secondary battery laminated separator” or “laminated separator”. The nonaqueous electrolyte secondary battery separator in accordance with an embodiment of the present invention can further contain another layer in addition to the polyolefin porous film. Examples of the another layer encompass an adhesive layer, a heat-resistant layer, and a protective layer.
The polyolefin porous film contains a polyolefin-based resin at a proportion of not less than 50% by volume, preferably not less than 90% by volume, and more preferably not less than 95% by volume, relative to the whole porous film. The polyolefin-based resin more preferably contains a high molecular weight component having a weight-average molecular weight of 5×105 to 15×106. In particular, the polyolefin-based resin more preferably contains a high molecular weight component having a weight-average molecular weight of not less than 1,000,000 because such a polyolefin-based resin allows for an increase in strength of (i) the nonaqueous electrolyte secondary battery separator which is the porous film and (ii) the nonaqueous electrolyte secondary battery laminated separator which includes the porous film.
Examples of the polyolefin-based resin which is contained in the polyolefin porous film include, but are not particularly limited to, homopolymers (for example, polyethylene, polypropylene, and polybutene) and copolymers (for example, ethylene-propylene copolymer) produced through (co)polymerization of a monomer such as ethylene, propylene, 1-butene, 4-methyl-1-pentene, and 1-hexene (which are thermoplastic resins). Among the above examples, polyethylene is preferable as it is capable of preventing (shutting down) a flow of an excessively large electric current at a lower temperature. Examples of the polyethylene include low-density polyethylene, high-density polyethylene, linear polyethylene (ethylene-α-olefin copolymer), and ultra-high molecular weight polyethylene having a weight-average molecular weight of not less than 1,000,000. Among these examples, ultra-high molecular weight polyethylene having a weight-average molecular weight of not less than 1,000,000 is further preferable.
A thickness of the porous film can be decided as appropriate in view of (i) a thickness of a nonaqueous electrolyte secondary battery separator including the porous film and (ii) a thickness of a nonaqueous electrolyte secondary battery laminated separator (described later) including the porous film. The thickness of the porous film is preferably 4 μm to 40 μm, and more preferably 5 μm to 20 μm.
A weight per unit area of the porous film is decided as appropriate in view of strength, thickness, weight, and handleability of the nonaqueous electrolyte secondary battery separator including the porous film. Specifically, the porous film ordinarily has a mass per unit area of preferably 4 g/m2 to 20 g/m2, more preferably 5 g/m2 to 12 g/m2, so as to allow the battery, which includes a nonaqueous electrolyte secondary battery separator including the porous film, to have a higher weight energy density and a higher volume energy density.
The porous film has an air permeability of preferably 30 sec/100 mL to 500 sec/100 mL, more preferably 50 sec/100 mL to 300 sec/100 mL, in terms of Gurley values. The porous film having an air permeability which falls within these ranges allows a nonaqueous electrolyte secondary battery separator including the porous film to achieve sufficient ion permeability.
The porous film has a porosity of preferably 20% by volume to 80% by volume, more preferably 30% by volume to 75% by volume, so as to (i) retain a larger amount of electrolyte and (ii) obtain the function of reliably preventing (shutting down) a flow of an excessively large electric current at a lower temperature. Such a porosity is also preferable in terms of preventing an increase in resistance and a decrease in mechanical strength.
Further, the porous film has pores each having a pore size of preferably not larger than 0.3 μm, more preferably not larger than 0.14 μm so that (i) a nonaqueous electrolyte secondary battery separator including the porous film can have sufficient ion permeability and (ii) it is possible to prevent particles from entering the positive electrode or the negative electrode.
A diminution rate, at which diethyl carbonate (hereinafter also referred to as “DEC”) dropped on the porous film in accordance with an embodiment of the present invention diminishes, is in a range of 15 sec/mg to 21 sec/mg, preferably 16 sec/mg to 20 sec/mg, and more preferably 17 sec/mg to 19 sec/mg.
A diminution rate of the diethyl carbonate dropped on the porous film which is less than 15 sec/mg indicates that the porous film will have a poor liquid retention property in a nonaqueous electrolyte secondary battery including (i) a nonaqueous electrolyte secondary battery separator including the porous film or (ii) a laminated separator (described later) including the porous film. As a result, in a case where the nonaqueous electrolyte secondary battery is subjected to high-rate discharge, the inside of the nonaqueous electrolyte secondary battery will be prone to drying out, thus presenting the risk of deterioration of an electrode plate in the battery. A diminution rate of diethyl carbonate dropped on the porous film which is more than 21 sec/mg indicates that, in a nonaqueous electrolyte secondary battery including (i) a nonaqueous electrolyte secondary battery separator including the porous film or (ii) a laminated separator (described later) including the porous film, a fluid (an electrolyte such as DEC or a gas generated from an electrolyte in the battery during battery charge and discharge) will move at a slow speed in holes (voids) in the porous film. This causes the separator to have increased resistance to ion permeation (i.e. decreased ion permeability) as a result of (i) the battery drying out due to insufficient electrolyte supply to an electrode plate during high-rate discharge and (ii) the generated gas remaining in the voids. Consequently, deterioration of the electrode plate will progress excessively. As a result, there is a risk of a decrease in restored discharge capacity after high-rate discharge.
The “diminution rate of diethyl carbonate dropped on the polyolefin porous film” herein refers to a speed at which the DEC that has been dropped on the porous film evaporates, and is measured by the following method under the following measurement conditions.
Measurement conditions: atmospheric pressure; room temperature (approximately 25° C.); humidity of 60% to 70%; and air velocity of not more than 0.2 m/s.
(i) A square piece measuring 50 mm×50 mm is cut out from the porous film and then placed on a polytetrafluoroethylene (hereinafter, “PTFE”) plate. Then, the PTFE plate, on which the porous film is placed, is placed on an analytical balance, and then a zero point adjustment is carried out.
(ii) 20 μL of DEC is measured out with the use of a micropipette to which a pipette tip has been attached.
(iii) 20 μL of the DEC measured out in the step (ii) is dropped (a) from 5 mm above the porous film placed on the analytical balance (which has been subjected to zero point adjustment in the step (i)) and (b) toward a center part of the porous film, and then the reading of the analytical balance is taken, that is, a weight of the DEC is measured.
(iv) A length of time it takes for the weight of the DEC measured in the step (iii) to decrease from 15 mg to 5 mg is measured, and then the length of time thus measured is divided by the amount by which the weight of the DEC has changed (10 mg), so that the “diminution rate by which the diethyl carbonate dropped on the polyolefin porous film” (sec/mg) is calculated.
The porous film in accordance with an embodiment of the present invention is arranged so that a spot diameter of diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the porous film is not less than 20 mm, preferably not less than 21 mm, and more preferably not less than 22 mm. In addition, the spot diameter is preferably not more than 30 mm.
A spot diameter of the diethyl carbonate, 10 seconds after the diethyl carbonate is dropped on the porous film, which is less than 20 mm indicates that the DEC thus dropped is absorbed into the voids inside the porous film at a slow speed, and that the porous film has low affinity with an electrolyte (such as DEC). Therefore, in a nonaqueous electrolyte secondary battery including (i) a nonaqueous electrolyte secondary battery separator including the porous film or (ii) a laminated separator including the porous film, there is a reduction in a moving speed of an electrolyte such as DEC in the porous film, particularly a reduction in a speed at which the DEC is absorbed from an electrode mix layer into the inside of the porous film during high-rate discharge. At the same time, a decrease in permeation of the electrolyte into the inside of the porous film causes the amount of liquid retained in the porous film to decrease. This means that, as high-rate discharge is carried out, the electrolyte is easily depleted locally (i) at an interface between an electrode and the nonaqueous electrolyte secondary battery separator or the laminated separator (described later) and (ii) inside the porous base material. As a result, high-rate discharge can lead to an increase in a resistance value inside the nonaqueous electrolyte secondary battery, and thus there is a risk of a decrease in restored discharge capacity of the nonaqueous electrolyte secondary battery after high-rate discharge. Furthermore, a spot diameter of the diethyl carbonate, 10 seconds after the diethyl carbonate is dropped on the porous film, which is more than 30 mm indicates that, in a nonaqueous electrolyte secondary battery including (i) a nonaqueous electrolyte secondary battery separator including the porous film or (ii) a laminated separator including the porous film, an affinity between the porous film and the electrolyte becomes excessively high, and that the electrolyte can be therefore retained excessively in the porous film. As a result, during charging and discharging (particularly during high-rate discharge) the battery is prone to drying out due to insufficient electrolyte supply to an electrode, deterioration of an electrode plate can progress excessively, and thus there is a risk of a decrease in restored discharge capacity of the nonaqueous electrolyte secondary battery after high-rate discharge.
The “spot diameter of the diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the polyolefin porous film” herein means a diameter of a spot made by the dropped DEC remaining on the porous film after 10 seconds have passed since 20 μL of DEC was dropped on the porous film, and is measured by the following method under the following measurement conditions.
Measurement conditions: atmospheric pressure; room temperature (approximately 25° C.); humidity of 60% to 70%; and air velocity of not more than 0.2 m/s.
Measurement method: Steps similar to the steps (i) through (iii) in the above method of measuring the “diminution rate of the diethyl carbonate dropped on the polyolefin porous film” are carried out. Then, 20 μL of DEC is dropped (a) from 5 mm above the porous film and (b) toward a center part of the porous base material. Then, after 10 seconds pass, a diameter of a spot made by the dropped DEC remaining on the porous film is measured.
In a case where the porous layer and/or another layer is disposed on the porous film, physical property values of the porous film, which is included in the laminated body including the porous film and the porous layer and/or the another layer, can be measured after the porous layer or the another layer is removed from the laminated body. The porous layer or the another layer can be removed from the laminated body by, for example, a method of dissolving the resin of the porous layer or of the another layer with use of a solvent such as N-methylpyrrolidone or acetone for removal.
Note that in a case where, for example, there exists an adhering substance such as a resin powder and/or an inorganic matter on a surface of the porous film during measurement of the diminution rate of diethyl carbonate and the spot diameter, it is possible, as necessary, to (i) immerse the porous film, before the measurement, in an organic solvent such as DEC and/or water to clean and remove the adhering substance and the like and then (ii) carry out a pretreatment such as drying the solvent and the water.
The diminution rate of diethyl carbonate and the spot diameter can be controlled by, for example, setting a “T-die extrusion temperature” and a “heat fixation temperature after stretching” to respective specific ranges in a polyolefin porous film production method described later.
In a case where a porous layer containing polyvinylidene fluoride-based resin (described later) is to be formed on the nonaqueous electrolyte secondary battery separator, it is preferable to subject the nonaqueous electrolyte secondary battery separator to a hydrophilization treatment before applying a coating solution (described later) to the nonaqueous electrolyte secondary battery separator. Performing a hydrophilization treatment on the nonaqueous electrolyte secondary battery separator further facilitates the application of the coating solution and thus allows a more uniform porous layer to be formed. The hydrophilization treatment is effective in a case where water accounts for a high proportion of a solvent (dispersion medium) contained in the coating solution. Specific examples of the hydrophilization treatment include publicly known treatments such as (i) a chemical treatment involving an acid, an alkali, or the like, (ii) a corona treatment, and (iii) a plasma treatment. Among these hydrophilization treatments, the corona treatment is more preferable because the corona treatment makes it possible not only to hydrophilize the nonaqueous electrolyte secondary battery separator within a relatively short period of time, but also to hydrophilize only a surface and its vicinity of the nonaqueous electrolyte secondary battery separator so as to leave the inside of the nonaqueous electrolyte secondary battery separator unchanged in quality.
[Method of Producing Polyolefin Porous Film]
A method of producing a polyolefin resin composition in accordance with an embodiment of the present invention can include, for example: (i) the step of extruding a polyolefin resin composition, in a sheet-like shape, from a T-die at a specific T-die extrusion temperature; (ii) the step of carrying out heat fixation at a specific heat fixation temperature, so as to obtain a polyolefin porous film; and (iii) a further suitable step that can be included in a typical method for producing a polyolefin porous film. Examples of the suitable step include a step of adding a plasticizer to a resin such as polyolefin, forming a film, and then removing the plasticizer with the use of a suitable solvent, so that a porous base material is formed.
In a method of producing a polyolefin porous film, examples of a method for controlling the “diminution rate of diethyl carbonate dropped on the porous film” and the “spot diameter of the diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the polyolefin porous film” so as to be within the above-described ranges include a method of (i) controlling the temperature of the T-die when extruding the polyolefin resin composition in a sheet-like shape (i.e., controlling the T-die extrusion temperature) to a range of preferably 245° C. to 280° C. and more preferably 245° C. to 260° C. and (ii) controlling the heat fixation temperature to a range of preferably 100° C. to 125° C. and more preferably 100° C. to 120° C. Producing a polyolefin porous film by a method employing the above preferable conditions makes it possible to control (i) the electrolyte retention property of the resulting polyolefin porous film and (ii) the fluid moving speed in voids inside the resulting polyolefin porous film to preferable ranges. This makes it possible to produce a porous film in which (i) the diminution rate of diethyl carbonate dropped thereon is in a range of 15 sec/mg to 21 sec/mg and (ii) the spot diameter of the diethyl carbonate 10 seconds after dropping is not less than 20 mm.
[Porous Layer]
The porous layer in accordance with an embodiment of the present invention contains a polyvinylidene fluoride-based resin. The polyvinylidene fluoride-based resin contains a polyvinylidene fluoride-based resin having crystal form α (hereinafter also referred to as “α-form polyvinylidene fluoride-based resin”) and a polyvinylidene fluoride-based resin having crystal form β (hereinafter also referred to as “β-form polyvinylidene fluoride-based resin”). Assuming that a sum of (i) an amount of the α-form polyvinylidene fluoride-based resin and (ii) an amount of the β-form polyvinylidene fluoride-based resin is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin is not less than 35.0 mol %.
The amount of the α-form polyvinylidene fluoride-based resin contained is calculated from (i) waveform separation of (α/2) observed at around −78 ppm in a 19F-NMR spectrum obtained from the porous layer and (ii) waveform separation of {(α/2)+β} observed at around −95 ppm in the 19F-NMR spectrum.
The porous layer in accordance with an embodiment of the present invention contains a polyvinylidene fluoride-based resin (PVDF-based resin). The porous layer contains a large number of pores connected to one another, and thus allows a gas or a liquid to pass therethrough from one surface to the other.
In an embodiment of the present invention, the porous layer, as a member included in a nonaqueous electrolyte secondary battery, is provided between (i) the nonaqueous electrolyte secondary battery separator and (ii) at least one of the positive electrode plate and the negative electrode plate. The porous layer can be disposed on one surface or both surfaces of the nonaqueous electrolyte secondary battery separator. Alternatively, the porous layer can be disposed on an active material layer of at least one of the positive electrode plate and the negative electrode plate. Alternatively, the porous layer can be provided between the nonaqueous electrolyte secondary battery separator and at least one of the positive electrode plate and the negative electrode plate so as to be in contact with the nonaqueous electrolyte secondary battery separator and with the at least one of the positive electrode plate and the negative electrode plate. The porous layer, which is provided between the nonaqueous electrolyte secondary battery separator and at least one of the positive electrode plate and the negative electrode plate, can be a single layer or can be made up of two or more layers.
The porous layer is preferably an insulating porous layer. The resin which can be contained in the porous layer is preferably a resin that is insoluble in the electrolyte of the battery and that is electrochemically stable when the battery is in normal use. In a case where the porous layer is disposed on one surface of the porous film, the porous layer is disposed preferably on a surface of the porous film which surface faces the positive electrode plate of the nonaqueous electrolyte secondary battery, and more preferably on a surface of the porous film which surface is in contact with the positive electrode plate.
Examples of the PVDF-based resin include homopolymers of vinylidene fluoride; copolymers of vinylidene fluoride and other monomer(s) polymerizable with vinylidene fluoride; and mixtures of the above polymers. Examples of the monomers copolymerizable with vinylidene fluoride include hexafluoropropylene, tetrafluoroethylene, trifluoroethylene, trichloroethylene, and vinyl fluoride. The present invention can use (i) one kind of monomer or (ii) two or more kinds of monomers selected from above. The PVDF-based resin can be synthesized through emulsion polymerization or suspension polymerization.
The PVDF-based resin contains vinylidene fluoride at a proportion of ordinarily not less than 85 mol %, preferably not less than 90 mol %, more preferably not less than 95 mol %, further preferably not less than 98 mol %. A PVDF-based resin containing vinylidene fluoride at a proportion of not less than 85 mol % is more likely to allow a porous layer to have a mechanical strength against pressure and a heat resistance against heat during battery production.
The porous layer can also preferably contain two kinds of PVDF-based resins (that is, a first resin and a second resin below) that differ from each other in terms of, for example, the hexafluoropropylene content.
The first resin is (i) a vinylidene fluoride-hexafluoropropylene copolymer containing hexafluoropropylene at a proportion of more than 0 mol % and not more than 1.5 mol % or (ii) a vinylidene fluoride homopolymer.
The second resin is a vinylidene fluoride-hexafluoropropylene copolymer containing hexafluoropropylene at a proportion of more than 1.5 mol %.
A porous layer containing the two kinds of PVDF-based resins adheres better to an electrode than a porous layer not containing one of the two kinds of PVDF-based resins. Further, a porous layer containing the two kinds of PVDF-based resins adheres better to a nonaqueous electrolyte secondary battery separator (for example, the porous film), with the result of a higher peel strength between the two layers, than a porous layer not containing one of the two kinds of PVDF-based resins. A mass ratio of the first resin to the second resin is preferably in a range of 15:85 to 85:15.
The PVDF-based resin has a weight-average molecular weight of preferably 200,000 to 3,000,000. A PVDF-based resin having a weight-average molecular weight of not less than 200,000 tends to allow a porous layer to attain a mechanical property sufficient for the porous layer to endure a process of adhering the porous layer to an electrode, thereby allowing the porous layer and the electrode to adhere to each other sufficiently. Meanwhile, the PVDF-based resin which has a weight-average molecular weight of not more than 3,000,000 causes a coating solution, which is used to produce the porous layer, not to have a too high viscosity, and accordingly tends to be excellent in formability. The weight-average molecular weight of the PVDF-based resin is more preferably 200,000 to 2,000,000, further preferably 500,000 to 1,500,000.
The PVDF-based resin has a fibril diameter of preferably 10 nm to 1000 nm in view of the cycle characteristic of a nonaqueous electrolyte secondary battery containing the porous layer.
(Resin Other than PVDF-Based Resin)
The porous layer in accordance with an embodiment of the present invention may contain a resin other than the PVDF-based resin. Examples of the other resin include styrene-butadiene copolymers; homopolymers or copolymers of vinyl nitriles such as acrylonitrile and methacrylonitrile; and polyethers such as polyethylene oxide and polypropylene oxide.
(Filler)
The porous layer in accordance with an embodiment of the present invention may contain a filler. The filler may be an inorganic or organic filler. In a case where the porous layer in accordance with an embodiment of the present invention contains a filler, the filler is contained at a proportion of preferably not less than 1% by mass and not more than 99% by mass, more preferably not less than 10% by mass and not more than 98% by mass, with respect to the total amount of the polyvinylidene fluoride-based resin and the filler combined. Containing a filler allows the porous layer to have improved slidability and heat resistance, for example. The filler may be any inorganic or organic filler that is stable in a nonaqueous electrolyte and that is stable electrochemically. The filler preferably has a heat-resistant temperature of not lower than 150° C. to ensure safety of the battery.
The filler, such as the organic filler or the inorganic filler, can be a publicly known filler.
Examples of the organic filler include: crosslinked polymethacrylic acid esters such as crosslinked polyacrylic acid, crosslinked polyacrylic acid ester, crosslinked polymethacrylic acid, and crosslinked polymethyl methacrylate; fine particles of crosslinked polymers such as crosslinked polysilicone, crosslinked polystyrene, crosslinked polydivinyl benzene, a crosslinked product of a styrene-divinylbenzene copolymer, polyimide, a melamine resin, a phenol resin, and a benzoguanamine-formaldehyde condensate; and fine particles of heat-resistant polymers such as polysulfone, polyacrylonitrile, polyaramid, polyacetal, and thermoplastic polyimide.
Examples of the inorganic filler include metal hydroxides such as aluminum hydroxide, magnesium hydroxide, calcium hydroxide, chromium hydroxide, zirconium hydroxide, nickel hydroxide, and boron hydroxide; metal oxides such as alumina and zirconia, and hydrates thereof; carbonates such as calcium carbonate and magnesium carbonate; sulfates such as barium sulfate and calcium sulfate; and clay minerals such as calcium silicate and talc. The inorganic filler is preferably a metal hydroxide, a hydrate of a metal oxide, or a carbonate to improve the safety of the battery, for example, to impart fire retardance. The inorganic filler is preferably a metal oxide in terms of insulation and oxidation resistance.
The present invention may use (i) only one filler or (ii) two or more kinds of fillers in combination. Alternatively, the organic filler(s) and the inorganic filler(s) may be used in combination.
The porous layer for in accordance with an embodiment of the present invention has an average thickness of preferably 0.5 μm to 10 μm (per layer), more preferably 1 μm to 5 μm layer, in order to ensure (i) adhesion to an electrode and (ii) a high energy density.
A porous layer having a thickness of not less than 0.5 μm (per layer) is preferable because, in such a case, it is possible to (i) prevent an internal short circuit from occurring due to, for example, breakage of a nonaqueous electrolyte secondary battery and (ii) allow an amount of electrolyte retained in the porous layer to be sufficient.
A porous layer having a thickness of not more than 10 μm per layer is preferable for the following reasons. When a porous layer has such a thickness, an increase in resistance to permeation of lithium ions is inhibited in all areas of the nonaqueous electrolyte secondary battery laminated separator of the nonaqueous electrolyte secondary battery. This makes it possible to prevent deterioration of the positive electrode plate of the nonaqueous electrolyte secondary battery which occurs when charge-and-discharge cycles are repeated. As a result, it is possible to prevent deterioration of a rate characteristic and cycle characteristic. A porous layer having such a thickness is also preferable because it prevents an increase in distance between the positive and negative electrodes and therefore improves internal volume efficiency in a nonaqueous electrolyte secondary battery.
The porous layer in accordance with an embodiment of the present invention is preferably provided between (i) the nonaqueous electrolyte secondary battery separator and (ii) a positive electrode active material layer included in the positive electrode plate. Physical properties of the porous layer, which are described below, at least refer to physical properties of the porous layer which is provided between (i) a nonaqueous electrolyte secondary battery separator of a nonaqueous electrolyte secondary battery and (ii) a positive electrode active material layer included in a positive electrode plate of the nonaqueous electrolyte secondary battery.
The porous layer only needs to have a weight per unit area (per layer) which weight is determined as appropriate in view of the strength, thickness, weight, and handleability of a porous layer. Note, however, that the porous layer ordinarily has a weight per unit area (per layer) of preferably 0.5 g/m2 to 20 g/m2, more preferably 0.5 g/m2 to 10 g/m2, so as to allow a nonaqueous electrolyte secondary battery including the porous layer to have a higher weight energy density and a higher volume energy density. If the weight per unit area of the porous layer is beyond the above ranges, then the nonaqueous electrolyte secondary battery including the porous layer will be heavy.
A volume per square meter of a component(s) contained in the porous layer, i.e., a component volume per unit area (per layer) is preferably 0.5 cm3 to 20 cm3, more preferably 0.5 cm3 to 10 cm3.
The porous layer having a component volume per unit area that falls within the above numerical ranges allows a nonaqueous electrolyte secondary battery including the porous layer to have a higher weight energy density and a higher volume energy density. If the component volume per unit area of the porous layer is beyond the above ranges, then the nonaqueous electrolyte secondary battery will be heavy.
The component volume per unit area of the porous layer is calculated by the following method:
(1) The weight per unit area of each component of the porous layer is calculated by multiplying the weight per unit area of the porous layer by the weight concentration of the component (that is, the weight concentration in the porous layer).
(2) The weight per unit area of the component calculated in (1) is divided by the absolute specific gravity of the component. Then, the sum total of numerical values calculated is designated as the component volume per unit area of the B layer.
The porous layer has a porosity of preferably 20% by volume to 90% by volume, more preferably 30% by volume to 80% by volume, in order to achieve sufficient ion permeability. A pore size of each of pores of the porous layer is preferably not more than 3 μm, more preferably not more than 1 μm, and still more preferably not more than 0.5 μm, so that the porous layer and a nonaqueous electrolyte secondary battery laminated separator including the porous layer can have sufficient ion permeability.
The porous layer in accordance with an embodiment of the present invention has a surface roughness, in terms of a ten-point average roughness (Rz), of preferably 0.8 μm to 8.0 μm, more preferably 0.9 μm to 6.0 μm, and still more preferably 1.0 μm to 3.0 μm. The ten-point average roughness (Rz) is a value measured by a method in conformity with JIS B 0601-1994 (or Rzjis of JIS B 0601-2001). Specifically, Rz is a value measured with use of ET4000 (manufactured by Kosaka Laboratory Ltd.) with a measurement length of 1.25 mm, a measurement rate of 0.1 mm/sec, and a temperature and humidity of 25° C./50% RH.
The porous layer in accordance with an embodiment of the present invention has a coefficient of kinetic friction of preferably 0.1 to 0.6, more preferably 0.1 to 0.4, and still more preferably 0.1 to 0.3. The coefficient of kinetic friction is a value measured by a method in conformity with JIS K 7125. Specifically, in the present invention, a coefficient of kinetic friction is a value measured by use of Surface Property Tester (manufactured by Heidon).
<Crystal Forms of PVDF-Based Resin>
The PVDF-based resin contained in the porous layer used in an embodiment of the present invention contains an α-form polyvinylidene fluoride-based resin a β-form polyvinylidene fluoride-based resin. Assuming that a sum of (i) an amount of the α-form polyvinylidene fluoride-based resin contained in the PVDF-based resin and (ii) an amount of the β-form polyvinylidene fluoride-based resin contained in the PVDF-based resin is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin is not less than 35.0 mol %, preferably not less than 37.0 mol %, more preferably not less than 40.0 mol %, and still more preferably not less than 44.0 mol %. Further, the amount of the α-form polyvinylidene fluoride-based resin is preferably not more than 90.0 mol %.
A porous layer containing the α-form polyvinylidene fluoride-based resin in an amount falling within the above ranges is suitably used as a constituent member of a nonaqueous electrolyte secondary battery having an excellent ability to maintain a restored discharge capacity after high-rate discharge, particularly as a constituent member of a nonaqueous electrolyte secondary battery separator or as a constituent member of an electrode for a nonaqueous electrolyte secondary battery.
A nonaqueous electrolyte secondary battery generates heat during charge/discharge due to internal resistance. A greater current, i.e., a higher rate, correlates to a greater amount of heat generated. The α-form polyvinylidene fluoride-based resin has a melting point higher than that of the β-form polyvinylidene fluoride-based resin and is therefore less likely to undergo thermally induced plastic deformation than is the β-form polyvinylidene fluoride-based resin. It is known that the β-form polyvinylidene fluoride-based resin is more polarizable than the α-form polyvinylidene fluoride-based resin because the α-form polyvinylidene fluoride-based resin has a structure in which F atoms are arranged in one side of the structure.
According to the porous layer in accordance with an embodiment of the present invention, controlling a proportion of the α-form polyvinylidene fluoride-based resin contained in the PVDF-based resin of the porous layer to be not less than a certain value (not less than 35.0 mol %) makes the following possible: (i) to decrease, for example, deformation of an internal structure of the porous layer and blockage of voids, the deformation and the blockage occurring due to deformation of the PVDF-based resin as a result of heat generated during charge/discharge and particularly during high-rate operation and (ii) to prevent uneven distribution of Li ions, which uneven distribution occurs due to interaction between the Li ions and the PVDF-based resin. This consequently prevents a battery from deteriorating in performance.
The α-form polyvinylidene fluoride-based resin is arranged such that the PVDF-based resin is made of a polymer containing a PVDF skeleton. The PVDF skeleton has a conformation in which there are two or more consecutive chains of a steric structure in which, with respect to fluorine atoms (or hydrogen atoms) bonded to a main-chain carbon atom in a molecular chain of the skeleton, hydrogen (or fluorine) atoms bonded to a first adjacent carbon atom are in a trans position, and hydrogen (or fluorine) atoms bonded to a second (opposite) adjacent carbon atom are in a gauche position (positioned at an angle of 60°), the conformation being the following conformation:
(TGT
the molecular chain having the following type:
TGT
wherein dipole moments of C—F2 and C—H2 bonds have respective components perpendicular and parallel to the molecular chain.
The α-form polyvinylidene fluoride-based resin has characteristic peaks at around −95 ppm and around −78 ppm in its 19F-NMR spectrum.
The β-form polyvinylidene fluoride-based resin is arranged such that the PVDF-based resin is made of a polymer containing a PVDF skeleton. The PVDF skeleton has a conformation in which fluorine atoms and hydrogen atoms bonded to respective ones of two adjacent main-chain carbon atoms are positioned so as to form a trans configuration (TT-type conformation), that is, the fluorine atoms and the hydrogen atoms which are bonded to the respective ones of the two adjacent carbon atoms are positioned oppositely at an angle of 180°, as viewed in the direction of the carbon-carbon bond.
The β-form polyvinylidene fluoride-based resin may be arranged such that the polymer of the PVDF-based resin contains a PVDF skeleton that has a TT-type conformation in its entirety. The β-form polyvinylidene fluoride-based resin may alternatively be arranged such that a portion of the PVDF skeleton has a TT-type conformation and that the PVDF-based resin having β-form polyvinylidene fluoride-based resin has a molecular chain of the TT-type conformation in at least four consecutive PVDF monomeric units. In either case, (i) the carbon-carbon bond, in which the TT-type conformation constitutes a TT-type main chain, has a planar zigzag structure, and (ii) the respective dipole moments of C—F2 and C—H2 bonds each have a component perpendicular to the molecular chain.
The β-form polyvinylidene fluoride-based resin has characteristic peaks at around −95 ppm in its 19F-NMR spectrum.
(Method of Calculating Content Ratios of α-Form and β-Form Polyvinylidene Fluoride-Based Resins in PVDF-Based Resin)
Assuming that the sum of (i) the amount of the α-form polyvinylidene fluoride-based resin and (ii) the amount of the β-form polyvinylidene fluoride-based resin, each of which resins is contained in the porous layer in accordance with the an embodiment of present invention, is 100 mol %, a proportion of the amount of the α-form polyvinylidene fluoride-based resin and a proportion of the amount of the β-form PVDF-based resin can be calculated in the following manner from a 19F-NMR spectrum obtained from the porous layer. Specifically, the following calculation method, for example, can be employed.
(1) An 19F-NMR spectrum is measured from a porous layer containing a PVDF-based resin, under the following conditions.
Measurement device: AVANCE400 manufactured by Bruker Biospin
Measurement method: single-pulse method
Observed nucleus: 19F
Spectral bandwidth: 100 kHz
Pulse width: 3.0 s (90° pulse)
Pulse repetition time: 5.0 s
Reference material: C6F6 (external reference: −163.0 ppm)
Temperature: 22° C.
Sample rotation frequency: 25 kHz
(2) An integral value of a peak at around −78 ppm in the 19F-NMR spectrum obtained in (1) is calculated and is regarded as an α/2 amount.
(3) In a manner similar to (2) above, an integral value of a peak at around −95 ppm in the 19F-NMR spectrum obtained in (1) is calculated and is regarded as an {(α/2)+p} amount.
(4) Assuming that a sum of (i) an amount of an α-form polyvinylidene fluoride-based resin contained in the PVDF-based resin and (ii) an amount of a β-form polyvinylidene fluoride-based resin contained in the PVDF-based resin is 100 mol %, a ratio of the amount of the α-form polyvinylidene fluoride-based resin (hereinafter, also referred to as an “a ratio”) is calculated, from the integral values obtained in (2) and (3), in accordance with the following Formula (2).
α ratio (mol %)=[(integral value at around −78 ppm)×2/{(integral value at around −95 ppm)+(integral value at around −78 ppm)}]×100 (2)
(5) Assuming that a sum of (i) an amount of an α-form polyvinylidene fluoride-based resin contained in the PVDF-based resin and (ii) an amount of a β-form polyvinylidene fluoride-based resin contained in the PVDF-based resin is 100 mol %, a ratio of the amount of the β-form polyvinylidene fluoride-based resin (hereinafter also referred to as a “β ratio”) is calculated, from the α ratio obtained in (4), in accordance with the following Formula (3):
β ratio (mol %)=100 (mol %)−α ratio (mol %) (3)
[Nonaqueous Electrolyte Secondary Battery Laminated Separator]
A porous layer in accordance with an embodiment of the present invention can be provided to at least one surface of the nonaqueous electrolyte secondary battery separator so as to form a laminated body (nonaqueous electrolyte secondary battery laminated separator).
The nonaqueous electrolyte secondary battery laminated separator has a thickness of preferably 5.5 μm to 45 μm and more preferably 6 μm to 25 μm.
The nonaqueous electrolyte secondary battery laminated separator has an air permeability of preferably 30 sec/100 mL to 1000 sec/100 mL and more preferably 50 sec/100 mL to 800 sec/100 mL, in terms of Gurley values. Having an air permeability falling within the above ranges allows the nonaqueous electrolyte secondary battery laminated separator to have ion permeability sufficient for a separator.
[Porous Layer Production Method, Nonaqueous Electrolyte Secondary Battery Laminated Separator Production Method]
The porous layer in accordance with an embodiment of the present invention and the nonaqueous electrolyte secondary battery laminated separator in accordance with an embodiment of the present invention can be produced by any of various methods.
For example, in the case of the nonaqueous electrolyte secondary battery laminated separator, a porous layer containing a PVDF-based resin and optionally a filler is formed, through one of processes (1) through (3) described below, on a surface of a porous film which is to serve as a base material. In the case of the process (2) or (3), a porous layer which has been deposited is dried so as to remove the solvent. In the case of production of a porous layer containing a filler, the coating solution used in the processes (1) to (3) preferably contains a filler dispersed therein and a PVDF-based resin dissolved therein.
The coating solution for use in a method of producing the porous layer in accordance with an embodiment of the present invention can be prepared ordinarily by (i) dissolving, in a solvent, a resin to be contained in the porous layer and (ii) in a case where the coating solution is to contain a filler, dispersing the filler into the solvent.
(1) A process in which (i) a surface of a porous film is coated with a coating solution containing (a) fine particles of a PVDF-based resin to form a porous layer and optionally (b) fine particles of a filler and (ii) the surface of the porous film is dried to remove the solvent (dispersion medium) from the coating solution, so that the porous layer is formed.
(2) A process in which (i) a surface of a porous film is coated with the coating solution described in (1) and then (ii) the resultant porous film is immersed in a deposition solvent (which is a poor solvent for the PVDF-based resin), so that a porous layer is deposited.
(3) A process in which (i) a surface of a porous film is coated with a coating solution described in (1) and then (ii) the coating solution is made acidic with use of a low-boiling-point organic acid, so that a porous layer is deposited.
Examples of the solvent (dispersion medium) in the coating solution encompass N-methylpyrrolidone, N,N-dimethylacetamide, N,N-dimethylformamide, acetone, and water.
Preferable examples of the deposition solvent encompass isopropyl alcohol and t-butyl alcohol.
For the process (3), the low-boiling-point organic acid can be, for example, paratoluene sulfonic acid or acetic acid.
As appropriate, the coating solution can contain, as a component different from the resin and the filler, additive(s) such as a dispersing agent, a plasticizer, a surfactant, and/or a pH adjuster.
Examples of the base material other than the porous film encompass another film, a positive electrode plate, and a negative electrode plate.
The base material of the porous film etc. can be coated with coating solution by a conventionally publicly known method. Specific examples of such a method encompass a gravure coater method, a dip coater method, a bar coater method, and a die coater method.
(Method of Controlling Crystal Form of PVDF-Based Resin)
The crystal form of a PVDF-based resin contained in the porous layer in accordance with an embodiment of the present invention can be controlled with (i) drying conditions in the above-described method, such as (a) a drying temperature and (b) air velocity and air direction during drying and (ii) a deposition temperature in a case where a porous layer containing a PVDF-based resin is deposited with use of a deposition solvent or a low-boiling-point organic acid.
The drying conditions and the deposition temperature, for attaining the PVDF-based resin arranged such that, assuming that the sum of (i) the amount of the α-form polyvinylidene fluoride-based resin contained in the PVDF-based resin and (ii) the amount of the β-form polyvinylidene fluoride-based resin contained in the PVDF-based resin is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin is not less than 35.0 mol %, can be changed as appropriate by changing, for example, the method of producing the porous layer, the kind of solvent (dispersion medium) to be used, the kind of deposition solvent to be used, and/or and the low-boiling-point organic acid to be used.
In a case where the coating solution is simply dried as in the process (1), the drying conditions can be changed as appropriate by adjusting, for example, the amount of the solvent in the coating solution, the PVDF-based resin concentration in the coating solution, the amount of the filler (if contained), and/or the coating amount of the coating solution. In a case where a porous layer is to be formed through the process (1), it is preferable that (i) the drying temperature is 30° C. to 100° C., (ii) the direction of hot air for drying is perpendicular to a nonaqueous electrolyte secondary battery separator or electrode plate which has been coated with the coating solution, and (iii) the velocity of the hot air is 0.1 m/s to 40 m/s. Specifically, in a case where a coating solution to be applied contains N-methyl-2-pyrrolidone as the solvent for dissolving a PVDF-based resin, 1.0% by mass of a PVDF-based resin, and 9.0% by mass of alumina as an inorganic filler, the drying conditions are preferably adjusted so that (i) the drying temperature is 40° C. to 100° C., (ii) the direction of hot air for drying is perpendicular to a nonaqueous electrolyte secondary battery separator or electrode plate which has been coated with the coating solution, and (iii) the velocity of the hot air is 0.4 m/s to 40 m/s.
In a case where a porous layer is to be formed through the process (2), the deposition temperature is preferably −25° C. to 60° C., and the drying temperature is preferably 20° C. to 100° C. Specifically, in a case where a porous layer is to be formed through the process (2) with use of N-methylpyrrolidone as the solvent for dissolving a PVDF-based resin and isopropyl alcohol as the deposition solvent, it is preferable that (i) the deposition temperature is −10° C. to 40° C. and (ii) the drying temperature is 30° C. to 80° C.
(Another Porous Layer)
The nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention can contain another porous layer in addition to (i) the porous film and (ii) the porous layer containing the PVDF-based resin. The another porous layer need only be provided between (i) the nonaqueous electrolyte secondary battery separator and (ii) at least one of the positive electrode plate and the negative electrode plate. The porous layer and the another porous layer may be provided in any order with respect to the nonaqueous electrolyte secondary battery separator. In a preferable configuration, the porous film, the another porous layer, and the porous layer containing the PVDF-based resin are disposed in this order. In other words, the another porous layer is provided between the porous film and the porous layer containing the PVDF-based resin. In another preferable configuration, the another porous layer and the porous layer containing the PVDF-based resin are provided in this order on both surfaces of the porous film.
Examples of a resin which can be contained in the another porous layer in accordance with an embodiment of the present invention encompass: polyolefins; (meth)acrylate-based resins; fluorine-containing resins (excluding polyvinylidene fluoride-based resins); polyamide-based resins; polyimide-based resins; polyester-based resins; rubbers; resins with a melting point or glass transition temperature of not lower than 180° C.; water-soluble polymers; polycarbonate, polyacetal, and polyether ether ketone.
Among the above resins, polyolefins, (meth)acrylate-based resins, polyamide-based resins, polyester-based resins, and water-soluble polymers are preferable.
Preferable examples of the polyolefin encompass polyethylene, polypropylene, polybutene, and an ethylene-propylene copolymer.
Examples of the fluorine-containing resins encompass polytetrafluoroethylene, a vinylidene fluoride-hexafluoropropylene copolymer, a tetrafluoroethylene-hexafluoropropylene copolymer, a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer, a vinylidene fluoride-tetrafluoroethylene copolymer, a vinylidene fluoride-trifluoroethylene copolymer, a vinylidene fluoride-trichloroethylene copolymer, a vinylidene fluoride-vinyl fluoride copolymer, a vinylidene fluoride-hexafluoropropylene-tetrafluoroethylene copolymer, and an ethylene-tetrafluoroethylene copolymer. Particular examples of the fluorine-containing resins encompass fluorine-containing rubber having a glass transition temperature of not higher than 23° C.
Preferable examples of the polyamide-based resin encompass aramid resins such as aromatic polyamide and wholly aromatic polyamide.
Specific examples of the aramid resin encompass poly(paraphenylene terephthalamide), poly(metaphenylene isophthalamide), poly(parabenzamide), poly(metabenzamide), poly(4,4′-benzanilide terephthalamide), poly(paraphenylene-4,4′-biphenylene dicarboxylic acid amide), poly(metaphenylene-4,4′-biphenylene dicarboxylic acid amide), poly(paraphenylene-2,6-naphthalene dicarboxylic acid amide), poly(metaphenylene-2,6-naphthalene dicarboxylic acid amide), poly(2-chloroparaphenylene terephthalamide), a paraphenylene terephthalamide/2,6-dichloroparaphenylene terephthalamide copolymer, and a metaphenylene terephthalamide/2,6-dichloroparaphenylene terephthalamide copolymer. Among these aramid resins, poly(paraphenylene terephthalamide) is more preferable.
Preferable examples of the polyester-based resin encompass (i) aromatic polyesters such as polyarylate and (ii) liquid crystal polyesters.
Examples of the rubbers encompass a styrene-butadiene copolymer and a hydride thereof, a methacrylic acid ester copolymer, an acrylonitrile-acrylic acid ester copolymer, a styrene-acrylic acid ester copolymer, an ethylene propylene rubber, and polyvinyl acetate.
Examples of the resin with a melting point or a glass transition temperature of not lower than 180° C. encompass polyphenylene ether, polysulfone, polyether sulfone, polyphenylene sulfide, polyetherimide, polyamide imide, and polyether amide.
Examples of the water-soluble polymer encompass polyvinyl alcohol, polyethylene glycol, cellulose ether, sodium alginate, polyacrylic acid, polyacrylamide, and polymethacrylic acid.
Only one kind of these resins to be contained in the another porous layer can be used, or two or more kinds of these resins can be used in combination.
The other characteristics (e.g., thickness) of the another porous layer are similar to those (of the porous layer) described above, except that the porous layer contains the PVDF-based resin.
[Positive Electrode Plate]
A positive electrode plate in accordance with an embodiment of the present invention has a value in a range of 0.00 to 0.50, which value is represented by the following Formula (1). The positive electrode plate is ordinarily a sheet-shaped positive electrode plate including: (i) a positive electrode active material layer, constituted by a positive electrode mix containing a positive electrode active material, an electrically conductive agent, and a binding agent; and (ii) a positive electrode current collector supporting the positive electrode mix thereon. Note that the positive electrode plate may be configured such that the positive electrode current collector supports the positive electrode mix on both surfaces thereof or one of the surfaces thereof.
|1−T/M| (1)
In the above Formula (1), T represents a critical load distance in a transverse direction in a scratch test under a constant load of 0.1 N, and M represents a critical load distance in a machine direction in a scratch test under a constant load of 0.1 N.
The positive electrode active material is, for example, a material capable of being doped with and dedoped of lithium ions. Such a material is preferably a transition metal oxide. Examples of the transition metal oxide encompass lithium complex oxides containing at least one transition metal including, for example, V, Mn, Fe, Co, and Ni. Among such lithium complex oxides, (i) a lithium complex oxide having an α-NaFeO2 structure such as lithium nickelate and lithium cobaltate and (ii) a lithium complex oxide having a spinel structure such as lithium manganese spinel are preferable because such lithium complex oxides have a high average discharge potential. The lithium complex oxide may further contain any of various metallic elements, and is more preferably complex lithium nickelate.
Further, the complex lithium nickelate more preferably contains at least one metallic element selected from the group consisting of Ti, Zr, Ce, Y, V, Cr, Mn, Fe, Co, Cu, Ag, Mg, Al, Ga, In, and Sn at a proportion of 0.1 mol % to 20 mol % with respect to the sum of the number of moles of the at least one metallic element and the number of moles of Ni in the lithium nickelate. This is because such a complex lithium nickelate allows an excellent cycle characteristic when used in a high-capacity battery. An active material that contains Al or Mn and that contains Ni at a proportion of not less than 85%, further preferably not less than 90%, is particularly preferable because a nonaqueous electrolyte secondary battery including a positive electrode plate containing the above active material has an excellent cycle characteristic for use as a high-capacity battery.
Examples of the electrically conductive agent encompass carbonaceous materials such as natural graphite, artificial graphite, cokes, carbon black, pyrolytic carbons, carbon fiber, and a fired product of an organic polymer compound. It is possible to use (i) only one kind of the above electrically conductive agents or (ii) two or more kinds of the above electrically conductive agents in combination, for example, a mixture of artificial graphite and carbon black.
Examples of the binding agent encompass thermoplastic resins such as polyvinylidene fluoride, a copolymer of vinylidene fluoride, polytetrafluoroethylene, a tetrafluoroethylene-hexafluoropropylene copolymer, a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer, an ethylene-tetrafluoroethylene copolymer, a vinylidene fluoride-hexafluoropropylene copolymer, a vinylidene fluoride-hexafluoropropylene-tetrafluoroethylene copolymer, a thermoplastic polyimide, polyethylene, and polypropylene, as well as acrylic resin and styrene-butadiene-rubber. The binder functions also as a thickening agent.
The positive electrode mix may be prepared by, for example, a method of applying pressure to the positive electrode active material, the electrically conductive agent, and the binding agent on the positive electrode current collector or a method of using an appropriate organic solvent so that the positive electrode active material, the electrically conductive agent, and the binding agent are in a paste form.
Examples of the positive electrode current collector encompass electric conductors such as Al, Ni, and stainless steel. Among these, Al is preferable as it is easy to process into a thin film and less expensive.
The sheet-shaped positive electrode plate may be produced, that is, the positive electrode mix may be supported by the positive electrode current collector, through, for example, a method of applying pressure to the positive electrode active material, the electrically conductive agent, and the binding agent on the positive electrode current collector to form a positive electrode mix thereon or a method of (i) using an appropriate organic solvent so that the positive electrode active material, the electrically conductive agent, and the binding agent are in a paste form to provide a positive electrode mix, (ii) applying a coating of the positive electrode mix to the positive electrode current collector, (iii) drying the applied positive electrode mix to prepare a sheet-shaped positive electrode mix, and (iv) applying pressure to the sheet-shaped positive electrode mix so that the sheet-shaped positive electrode mix is firmly fixed to the positive electrode current collector.
[Negative Electrode Plate]
A negative electrode plate in accordance with an embodiment of the present invention has a value in a range of 0.00 to 0.50, which value is represented by the following Formula (1). The negative electrode plate is ordinarily a sheet-shaped positive electrode plate including: (i) a negative electrode active material layer, constituted by a negative electrode mix containing a negative electrode active material; and (ii) a negative electrode current collector supporting the negative electrode mix thereon. Note that the negative electrode plate may be configured such that the negative electrode current collector supports the negative electrode mix on both surfaces thereof or one of the surfaces thereof.
|1−T/M| (1)
In the above Formula (1), T represents a critical load distance in a transverse direction in a scratch test under a constant load of 0.1 N, and M represents a critical load distance in a machine direction in a scratch test under a constant load of 0.1 N.
The sheet-shaped negative electrode plate preferably contains an electrically conductive agent as described above and a binding agent as described above.
Examples of the negative electrode active material encompass (i) a material capable of being doped with and dedoped of lithium ions, (ii) a lithium metal, and (iii) a lithium alloy. Specific examples of the material encompass carbonaceous materials such as natural graphite, artificial graphite, cokes, carbon black, pyrolytic carbons, carbon fiber, and a fired product of an organic polymer compound; chalcogen compounds such as an oxide and a sulfide that are doped with and dedoped of lithium ions at an electric potential lower than that for the positive electrode plate; metals that can be alloyed with an alkali metal such as aluminum (Al), lead (Pb), tin (Sn), bismuth (Bi), and silicon (Si); cubic-crystal intermetallic compounds (for example, AlSb, Mg2Si, and NiSi2) of which an alkali metal is insertable into the lattice; and a lithium nitrogen compound such as Li3-xMxN (where M is a transition metal). Among the above negative electrode active materials, a carbonaceous material containing graphite is preferable because such a carbonaceous material has high electric potential flatness and low average discharge potential, and can thus be combined with a positive electrode plate to achieve a high energy density. A carbonaceous material containing a graphite material such as natural graphite or artificial graphite as a main component is more preferable. The negative electrode active material may alternatively be a mixture of graphite and silicon, preferably containing Si at a proportion of not less than 5%, more preferably not less than 10%, with respect to carbon (C) which constitutes the graphite.
The negative electrode mix may be prepared by, for example, a method of applying pressure to the negative electrode active material on the negative electrode current collector or a method of using an appropriate organic solvent so that the negative electrode active material is in a paste form.
Examples of the negative electrode current collector encompass Cu, Ni, and stainless steel. Among these, Cu is preferable as it is not easily alloyed with lithium in the case of a lithium-ion secondary battery in particular and is easily processed into a thin film.
The sheet-shaped negative electrode plate may be produced, that is, the negative electrode mix may be supported by the negative electrode current collector, through, for example, a method of applying pressure to the negative electrode active material on the negative electrode current collector to form a negative electrode mix thereon or a method of (i) using an appropriate organic solvent so that the negative electrode active material is in a paste form to provide a negative electrode mix, (ii) applying a coating of the negative electrode mix to the negative electrode current collector, (iii) drying the applied negative electrode mix to prepare a sheet-shaped negative electrode mix, and (iv) applying pressure to the sheet-shaped negative electrode mix so that the sheet-shaped negative electrode mix is firmly fixed to the negative electrode current collector. The above paste preferably includes the above electrically conductive agent and the binding agent.
(Scratch Test)
As illustrated in
(1) A measurement target object 3 (a positive electrode plate or a negative electrode plate) is cut into a piece of 20 mm×60 mm. Then, a diluted glue solution which has been obtained by diluting Arabic Yamato aqueous liquid glue (manufactured by YAMATO Co., Ltd.) with water by a 5-fold dilution factor is applied to an entire surface of a glass preparation (substrate 2) of 30 mm×70 mm so that the weight per unit area of the diluted glue solution is approximately 1.5 g/m2. The cut piece of the measurement target object 3 and the substrate 2 are bonded together via the diluted glue solution having been applied to the substrate 2. Thereafter, a resulting laminated material is dried at a temperature of 25° C. for 24 hours, so that a test sample is prepared. Note that the cut piece of the measurement target object 3 and the glass preparation (substrate 2) are to be bonded together with care so that no air bubble is made between the cut piece of the measurement target object 3 and the glass preparation. The test sample is prepared in a manner such that an active material layer (positive electrode active material layer or negative electrode active material layer) of the electrode plate (the measurement target object 3) is an upper surface that will come into contact with a diamond indenter 1 (described later).
(2) The test sample prepared in the step (1) is placed on a microscratch testing device (manufactured by CSEM Instruments). Then, while the diamond indenter 1 (in a conical shape having an apex angle of 120° and having a tip whose radius is 0.2 mm) of the testing device is applying a vertical load of 0.1 N to the test sample, a table of the testing device is moved by a distance of 10 mm in a transverse direction (TD) of the measurement target object at a speed of 5 mm/min. During the movement of the table, stress (force of friction) that occurs between the diamond indenter 1 and the test sample is measured.
(3) A line graph, which shows a relationship between a displacement of the stress measured in the step (2) and the distance of the movement of the table, is made. Then, based on the line graph, the following are calculated as illustrated in
(4) The direction of the movement of the table is changed to a machine direction (MD), and the above steps (1) through (3) are repeated. Then, the following are calculated: (i) a critical load value in the machine direction and (ii) the distance (critical load distance) in the machine direction between a starting point of measurement and a point where the critical load is obtained.
Note that any conditions and the like for the measurement in the scratch test other than the conditions described above are similar to those disclosed in JIS R 3255.
The term “MD” as used herein refers to a lengthwise direction of a positive electrode plate and a negative electrode plate, and the term “TD” as used herein refers to a direction orthogonal to the MD. Note, however, that in a case where a positive electrode plate or a negative electrode plate is squarely shaped, the MD is a direction which is parallel to one of the edges of the square, and the TD is a direction orthogonal to the MD.
The scratch test (i) models stress transfer inside an electrode active material layer (electrode active material particles (positive electrode active material particles or negative electrode active material particles)) due to expansion and shrinkage of the electrode a layer along with charge/discharge of a nonaqueous electrolyte secondary battery into which the electrode plate is incorporated, and (ii) measures and calculates uniformity of the stress transfer.
Further, in the scratch test, a measured critical load distance is affected by uniformity of a surface layer (electrode active material layer) of the electrode plate (measurement target object), the degree of alignment of particles present on a surface of the electrode active material layer of the electrode plate, the shape of the particles (e.g., aspect ratio of the particles), and the particle diameter of the particles.
Here, a positive electrode plate in accordance with an embodiment of the present invention has a value represented by the following Formula (1), which value is in a range of 0.00 to 0.50, preferably 0.00 to 0.47, and more preferably 0.00 to 0.45.
Further, a negative electrode plate in accordance with an embodiment of the present invention has a value represented by the following Formula (1), which value is in a range of 0.00 to 0.50, preferably 0.00 to 0.49, and more preferably 0.00 to 0.45:
|1−T/M| (1)
where T represents a critical load distance in a transverse direction in a scratch test under a constant load of 0.1 N, and M represents a critical load distance in a machine direction in a scratch test under a constant load of 0.1 N.
The values represented by the Formula (1) are each a value representing anisotropy of a critical load distance in a scratch test on each electrode plate. A value that is closer to zero indicates that the critical load distance is more isotropic.
Configuring the electrode plates in an embodiment of the present invention so that the value represented by Formula (1) is in a range of 0 to 0.50 makes it possible for the electrode active material layer contained in the electrode plates to isotropically follow expansion and shrinkage of the electrode active material which occurs with repetition of charge and discharge cycles. As such, even when the electrode active material expands and shrinks along with high-rate discharge, it is easy to maintain: (i) adhesiveness between electrode active material particles; (ii) adhesiveness between electrically conductive agent particles; (iii) adhesiveness between binder particles; (iv) adhesiveness between each of the materials of (i) through (iii) above; and (v) adhesiveness between the electrode active material layer and the current collector.
As such, even when the above expansion and shrinkage occurs, an electrode plate in accordance with an embodiment of the present invention is able to favorably maintain (i) adhesiveness between various members constituting the active material which deforms and (ii) adhesiveness between the members and the current collector. This prevents deterioration of the electrode plate which could otherwise occur along with repetition of charging and discharging. As a result, the electrode plate in accordance with an embodiment of the present invention makes it possible to improve restored discharge capacity after high-rate discharge of a nonaqueous electrolyte secondary battery.
A value represented by Formula (1) which falls outside the range of 0 to 0.50 (i.e., exceeds 0.50), indicates that a large degree of anisotropy exists between the transverse and machine directions at the critical load distances. An electrode plate having this large degree of anisotropy may have insufficient adhesiveness with the nonaqueous electrolyte secondary battery separator or nonaqueous electrolyte secondary battery laminated separator when high-rate discharge is carried out, and may have insufficient plane-direction-wise uniformity of electrode-to-electrode distance when high-rate discharge is carried out. As a result, a nonaqueous electrolyte secondary battery containing such an electrode plate will tend to suffer a decrease in restored discharge capacity after high-rate discharge.
In a nonaqueous electrolyte secondary battery including an electrode plate having the large degree of anisotropy, stress is transferred non-uniformly inside an electrode active material layer due to expansion and shrinkage of electrode active material particles along with high-rate discharge of the nonaqueous electrolyte secondary battery. This causes voids inside the electrode active material layer to have non-uniform diameters and to be distributed non-uniformly, and also causes stress inside the electrode active material layer to occur in a localized direction. As a result, high-rate discharge is accompanied by deterioration of the electrode plate due to disconnection of electrically conductive paths inside the electrode active material layer, separation of the electrode active material and the electrically conductive agent from the binding agent (binder), and a decrease in adhesiveness between the current collector and the electrode active material layer. As a result, such a nonaqueous electrolyte secondary battery tends to undergo a decrease in restored discharge capacity after high-rate discharge.
Examples of a method by which a value represented by Formula (1) is adjusted for an electrode plate (a positive electrode plate and a negative electrode plate) encompass: a method of adjusting a particle diameter of electrode active material particles, which serves as a material for an electrode plate, and/or an aspect ratio of the electrode active material particles; a method of applying a coating of an electrode mix (a positive electrode mix or a negative electrode mix) onto a current collector at a specific coating shear rate during formation of an electrode plate, to adjust an alignment property of electrode active material particles and/or a porosity of a resulting electrode active material layer; and a method of adjusting a ratio at which an electrode active material, an electrically conductive agent, and a binding agent, which are materials for an electrode plate, are mixed to control a composition ratio of a resulting electrode plate (electrode active material layer).
Among the above methods, preferable specific examples include controlling the particle diameter of the electrode active material particles to fall within a range of 1 μm to 30 μm, controlling the aspect ratio (long diameter to short diameter ratio) of the electrode active material particles to fall within a range of 1 to 5, controlling a coating line speed to fall within a range of 10 m/sec to 200 m/sec, controlling the porosity of the electrode plate (porosity of the electrode active material layer) to fall within a range of 10% to 50%, and controlling a proportion of an active material component present in a composition of an electrode plate to be equal to or greater than 80% by weight. By controlling the respective production conditions and the like described above to fall within suitable ranges, it is possible to suitably control a value represented by Formula (1) for an electrode plate to fall within a range of 0.00 to 0.50.
A porosity (ε) of an electrode active material layer can be calculated, by the following Formula (5), from a density p (g/m3) of an electrode active material layer, respective mass compositions (wt %) b1, b2, . . . bn of materials that constitute the electrode active material layer (e.g., a positive electrode active material, an electrically conductive material, and a binding agent), and respective real densities (g/m3) c1, c2, . . . cn of these materials. Note here that the real densities of the materials may be values as disclosed in literature or may be measured values obtained by a pycnometer method.
ε=1−{ρ×(b1/100)/c1+ρ×(b2/100)/c2+ . . . ρ×(bn/100)/cn}×100 (5)
[Nonaqueous Electrolyte]
A nonaqueous electrolyte, which can be contained in the nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention, is not limited to any particular one, provided that the nonaqueous electrolyte is that which is generally used in a nonaqueous electrolyte secondary battery. Examples of the nonaqueous electrolyte encompass a nonaqueous electrolyte prepared by dissolving a lithium salt in an organic solvent. Examples of the lithium salt encompass LiClO4, LiPF6, LiAsF6, LiSbF6, LiBF4, LiCF3SO3, LiN(CF3SO2)2, LiC(CF3SO2)3, Li2B10Cl10, lower aliphatic carboxylic acid lithium salt, and LiAlCl4. It is possible to use only one kind of the above lithium salts or two or more kinds of the above lithium salts in combination.
Examples of the organic solvent contained in the nonaqueous electrolyte encompass carbonates, ethers, esters, nitriles, amides, carbamates, sulfur-containing compounds, and fluorine-containing organic solvents obtained by introducing a fluorine group into any of these organic solvents. It is possible to use only one kind of the above organic solvents or two or more kinds of the above organic solvents in combination.
[Method of Producing Nonaqueous Electrolyte Secondary Battery]
The nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention can be produced by, for example, (i) forming a member for a nonaqueous electrolyte secondary battery (hereinafter referred to as a “nonaqueous electrolyte secondary battery member”) by disposing the positive electrode plate, the nonaqueous electrolyte secondary battery laminated separator, and the negative electrode plate in this order, (ii) placing the nonaqueous electrolyte secondary battery member in a container which is to serve as a housing of the nonaqueous electrolyte secondary battery, (iii) filling the container with the nonaqueous electrolyte, and then (iv) hermetically sealing the container while reducing pressure inside the container.
As described above, the nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention includes (i) the nonaqueous electrolyte secondary battery separator containing a polyolefin porous film, (ii) the porous layer, (iii) the positive electrode plate, and (iv) the negative electrode plate. In particular, the nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention satisfies the following requirements (i) through (iv):
(i) The polyvinylidene fluoride-based resin contained in the porous layer contains an α-form polyvinylidene fluoride-based resin and a β-form polyvinylidene fluoride-based resin, and assuming that a sum of (i) an amount of the α-form polyvinylidene fluoride-based resin contained in the polyvinylidene fluoride-based resin and (ii) an amount of the β-form polyvinylidene fluoride-based resin contained in the polyvinylidene fluoride-based resin is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin is not less than 35.0 mol %.
(ii) The positive electrode plate has a value in a range of 0.00 to 0.50, which value is represented as |1−T/M|.
(iii) The negative electrode plate has a value in a range of 0.00 to 0.50, which value is represented as |1−T/M|.
(iv) A diminution rate at which diethyl carbonate dropped onto the polyolefin porous film diminishes is in a range of 15 sec/mg to 21 sec/mg, and a spot diameter of diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the polyolefin porous film is not less than 20 mm.
In a nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention which satisfies the requirement (i), plastic deformation of the PVDF-based resin at a high temperature is prevented. This prevents the structural deformation and void blockage from occurring in the porous layer after charging and discharging. Furthermore, satisfying the requirements (ii) and (iii) allows the entirety of each electrode to easily isotropically follow expansion and shrinkage of the active material. As such, it is easy to maintain adhesiveness between components included in the electrode active material layer, as well as adhesiveness between the electrode active material layer and the current collector. Furthermore, satisfying the requirement (iv) controls, to a preferable range, liquid retention property of the polyolefin porous film with respect to a nonaqueous electrolyte, and controls, to a preferable range, fluid moving speed in the voids inside the polyolefin porous film.
As such, a nonaqueous electrolyte secondary battery which satisfies the above requirements (i) through (iv) exhibits the following: (a) because the porous layer has favorable structural stability after charging and discharging, the ion permeability of the porous layer is favorable; (b) because the fluid moving speed in the voids in the polyolefin porous film is controlled to a preferable range, movement of the nonaqueous electrolyte in the polyolefin porous film is favorable; and (c) because the above-described adhesiveness is easily maintained, deterioration of the nonaqueous electrolyte secondary battery which would be caused by charge and discharge cycles is prevented. Therefore, presumably, the restored capacity of the battery is improved even after high-rate discharge.
The present invention is not limited to the embodiments, but can be altered by a skilled person in the art within the scope of the claims. The present invention also encompasses, in its technical scope, any embodiment derived by combining technical means disclosed in differing embodiments.
The following description will discuss embodiments of the present invention in more detail with reference to Examples and Comparative Examples. Note, however, that the present invention is not limited to these Examples.
[Measurements]
Measurements in the Examples and Comparative examples were carried out in accordance with the following methods.
(Diminution Rate of Diethyl Carbonate Dropped on Polyolefin Porous Film)
For each of the Examples and Comparative Examples, a square piece measuring 50 mm×50 mm was cut out from the polyolefin porous film produced, and was then placed on a polytetrafluoroethylene (PTFE) plate under conditions of (i) atmospheric pressure, (ii) room temperature (approximately 25° C.), (iii) a humidity of 60% to 70%, and (iv) an air velocity of not more than 0.2 m/s. Then, the polytetrafluoroethylene (PTFE) plate on which the square piece had been placed was placed on an analytical balance (manufactured by Shimadzu Corporation, model: AUW220), and zero point adjustment was carried out. Then, diethyl carbonate (DEC) was measured out with the use of a micropipette (manufactured by Eppendorf, model: Reference, designed for 20 μL) to which a pipette tip (manufactured by Eppendorf; product name: Standard; yellow tip designed for 0.5 μL to 20 μL) had been attached. After the zero point adjustment was carried out, 20 μL of the DEC thus measured out was dropped from a from a height of 5 mm onto a center part of the polyolefin porous film, and then a change in weight was measured. Specifically, a length of time it took for the weight of the DEC to decrease from 15 mg to 5 mg (hereinafter referred to also as “evaporation time”) was measured. Then, the evaporation time thus measured was divided by the amount (10 mg) by which the weight of the DEC has changed, so as to obtain a value, which was considered to be the measured value of the “diminution rate”.
(Spot Diameter of Diethyl Carbonate 10 Seconds after Diethyl Carbonate is Dropped on Polyolefin Porous Film)
Under measurement conditions and by a measurement method similar to those for the measurement of the “diminution rate”, 20 μL of DEC, which had been measured out, was dropped from a height of 5 mm onto a center part of the polyolefin porous film produced in each of the Examples and Comparative Examples. After 10 seconds passed, a diameter of a spot made by the dropped DEC remaining on the polyolefin porous film was measured. The value obtained was considered to be a measured value of the “spot diameter”.
The “diminution rate” and the “spot diameter” of each of the polyolefin porous films produced in the Examples and Comparative Examples were measured three times. Three measured values of the “diminution rate” were averaged so as to calculate the ultimate “diminution rate”. Three measured values of the “spot diameter” were averaged so as to calculate the ultimate “spot diameter”.
(Amount of α-Form Polyvinylidene Fluoride-Based Resin)
In the Examples and Comparative Examples below, an amount (mol %) of the α-form polyvinylidene fluoride-based resin contained in the PVDF-based resin of each porous layer produced was measured via the procedure detailed in steps (1) to (4) of the section titled “(Method of calculating content ratios of α-form and β-form polyvinylidene fluoride-based resins in PVDF-based resin).” The measurement of the amount (mol %) of α-form polyvinylidene fluoride-based resin was carried out using a sample measuring 2 cm×5 cm, which was cut out from a nonaqueous electrolyte secondary battery laminated separator produced by providing the porous layer to one surface of the nonaqueous electrolyte secondary battery separator (polyolefin porous film) obtained in each Example and Comparative Example.
(Measurement of Porosity of Electrode Active Material Layer)
In Examples below, a porosity ε of the electrode active material layers (positive electrode active material layer and negative electrode active material layer) was measured via the following method.
First, from the electrode plate (positive electrode plate or negative electrode plate) was cut a piece having a size of 14.5 cm2 (4.5 cm×3 cm+1 cm×1 cm). The mass A1 g and thickness B1 μm of the piece of the electrode plate thus cut were measured. Thereafter, from the current collector (positive electrode current collector or negative electrode current collector) of the electrode plate was cut a piece having the same size as the piece of the electrode plate. The mass A2 g and thickness B2 μm of the piece of the current collector were measured. Using the measured values of A1, A2, B1, and B2, a density p of the electrode active material layer was calculated in accordance with the following Formula (4).
ρ=(A1−A2)/{(B1−B2)/10000×14.5} (4)
A porosity (ε) of an electrode active material layer was then calculated, in accordance with the following Formula (5), from the calculated density p of the electrode active material layer, respective mass compositions (wt %) b1, b2, . . . bn of materials that constitute the electrode active material layer (e.g., an electrode active material, an electrically conductive material, and a binding agent), and respective real densities (g/m3) c1, c2, . . . cn of these materials.
ε=1−{ρ×(b1/100)/c1+ρ×(b2/100)/c2+ . . . ρ×(bn/100)/cn}×100 (5)
For the positive electrode plate and negative electrode plate of each of the Examples and the Comparative Examples, the critical load value and the ratio of a critical load distance in a transverse direction to a critical load distance in a machine direction (T/M) were measured by in accordance with the steps (1) to (4) detailed in the section titled “(Scratch test)” above. Any conditions and the like for the measurement other than the conditions described in steps (1) to (4) are similar to those disclosed in JIS R 3255.
From this measured ratio of critical load distance in the transverse direction to the critical load distance in the machine direction, the values represented in Formula (1) (i.e., |1−T/M|) were calculated.
(Measurement of Restored Discharge Capacity after High-Rate Discharge)
(A) Initial Charge and Discharge
A new nonaqueous electrolyte secondary battery which had been produced in each of Examples and Comparative Examples and which had not been subjected to any charge-discharge cycle was subjected to four cycles of initial charge and discharge. Each of the four cycles of the initial charge and discharge was carried out at 25° C., at a voltage ranging from 4.1 V to 2.7 V, and at an electric current value of 0.2 C. Note here that “1 C” means an electric current value at which a battery rated capacity derived from a one-hour rate discharge capacity is discharged in one hour.
(B) High-Rate Discharge
Next, the nonaqueous electrolyte secondary battery which had been subjected to the initial charge and discharge was subjected to three cycles of charge and discharge (high-rate discharge). Each of the three cycles was carried out at 55° C., a constant charge electric current value of 1 C, and a constant discharge electric current value of 20 C. During the cycles, voltage ranged from 2.7 V to 4.2 V.
(C) Measurement of Restored Discharge Capacity after High-Rate Discharge
Next, the nonaqueous electrolyte secondary battery which had been subjected to the high-rate discharge was subjected to three more cycles of charge and discharge. Each of these three cycles was carried out at 55° C., a voltage ranging from 2.7 V to 4.2 V, a constant charge electric current value of 1 C, and a constant discharge electric current value of 0.2 C. A discharge capacity X was measured on the third of these cycles. The discharge capacity X was divided by the mass (unit: g) of the positive electrode active material, and a resulting value was used as the “restored discharge capacity after high-rate discharge”. The restored discharge capacity test described above involves a testing method to determine a degree of deterioration of the charging performance of the entire battery, and particularly a degree of deterioration of the charging performance of the electrodes, by measuring restored discharge capacity as observed in low-rate (0.2 C) discharge after high-rate discharge has been carried out.
[Production of Nonaqueous Electrolyte Secondary Battery Laminated Separator]
Ultra-high molecular weight polyethylene powder (GUR4032, manufactured by Ticona Corporation, weight-average molecular weight: 4,970,000) and polyethylene wax (FNP-0115, manufactured by Nippon Seiro Co., Ltd.) having a weight-average molecular weight of 1000 were mixed at a ratio of 70% by weight:30% by weight. Then, to 100 parts by weight of a mixture of the ultra-high molecular weight polyethylene and the polyethylene wax, the following were added: 0.4 parts by weight of antioxidant (Irg1010, manufactured by Ciba Specialty Chemicals Inc.), 0.1 parts by weight of antioxidant (P168, manufactured by Ciba Specialty Chemicals Inc.), and 1.3 parts by weight of sodium stearate. Then, calcium carbonate (manufactured by Maruo Calcium Co., Ltd.) having an average particle diameter of 0.1 pim was further added so as to account for 36% by volume of a total volume of the resultant mixture. Then, the resultant mixture while remaining a powder was mixed with the use of a Henschel mixer, so that a mixture 1 was obtained. Then, the mixture 1 was melted and kneaded with the use of a twin screw kneading extruder, so that a polyolefin resin composition 1 was obtained. Then, the polyolefin resin composition 1 was extruded in a sheet-like shape from a T-die which was set to 250° C. so as to obtain a sheet, and then the sheet was rolled with the use of a pair of rollers each having a surface temperature of 150° C., so that a rolled sheet 1 was prepared. Then, the rolled sheet 1 was immersed in an aqueous hydrochloric acid solution (containing 4 mol/L of hydrochloric acid and 0.5% by weight of a nonionic surfactant) so as to remove the calcium carbonate from the rolled sheet 1. Then, the resultant sheet was stretched with a stretch ratio of 6.2 times. Furthermore, the resultant sheet was subjected to heat fixation at 120° C. so that a polyolefin porous film 1 was obtained. Table 1 shows the results of the evaluation (diminution rate, spot diameter) of the polyolefin porous film 1.
An N-methyl-2-pyrrolidone (hereinafter referred to also as “NMP”) solution (available from Kureha Corporation; product name: L#9305, weight-average molecular weight: 1,000,000) containing a PVDF-based resin (polyvinylidene fluoride-hexafluoropropylene copolymer) was prepared as a coating solution. The coating solution was applied by a doctor blade method to the polyolefin porous film 1 so that the PVDF-based resin in the coating solution was applied in an amount of 6.0 g per square meter.
The porous film, to which the coating solution had been applied, was immersed in 2-propanol while a coating film thereof was wet with the solvent, and was then left to stand still at −10° C. for 5 minutes. This produced a laminated porous film 1. The laminated porous film 1 thus obtained was further immersed in other 2-propanol while the laminated porous film 1 was wet with the above immersion solvent, and was then left to stand still at 25° C. for 5 minutes. This produced a laminated porous film 1a. The laminated porous film 1a thus obtained was dried at 30° C. for 5 minutes. This produced a nonaqueous electrolyte secondary battery laminated separator 1. Table 1 shows the results of evaluation (amount of α-form polyvinylidene fluoride-based resin) of a porous layer 1 constituting the nonaqueous electrolyte secondary battery laminated separator 1.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
(Preparation of Positive Electrode Plate)
A positive electrode plate was obtained in which a layer of a positive electrode mix (a mixture of LiNi0.5Mn0.3Co0.2O2 having an average particle diameter (D50) of 4.5 μm based on volume, an electrically conductive agent, and PVDF (at a weight ratio of 92:5:3)) was applied on one surface of a positive electrode current collector (aluminum foil). In the positive electrode plate thus obtained, a positive electrode active material layer had a porosity of 40%.
The positive electrode plate was partially cut off so that a positive electrode active material layer was present in an area of 45 mm×30 mm and that this area was surrounded by an area with a width of 13 mm in which area no positive electrode active material layer was present. A portion thus cut was used as a positive electrode plate 1.
(Preparation of Negative Electrode Plate)
A negative electrode plate was obtained in which a layer of a negative electrode mix (a mixture of natural graphite having an average particle diameter (D50) of 15 μm based on volume, styrene-1,3-butadiene copolymer, and sodium carboxymethyl cellulose (at a weight ratio of 98:1:1)) was applied on one surface of a negative electrode current collector (copper foil). In the negative electrode plate thus obtained, a negative electrode active material layer had a porosity of 31%.
The negative electrode plate was partially cut off so that a negative electrode active material layer was present in an area of 50 mm×35 mm and that this area was surrounded by an area with a width of 13 mm in which area no negative electrode active material layer was present. A portion thus cut was used as a negative electrode plate 1.
(Assembling of Nonaqueous Electrolyte Secondary Battery)
With use of the positive electrode plate 1, the negative electrode plate 1, and the nonaqueous electrolyte secondary battery laminated separator 1, a nonaqueous electrolyte secondary battery was prepared by the following method.
The positive electrode plate 1, the nonaqueous electrolyte secondary battery laminated separator 1, and the negative electrode plate 1 were disposed (arranged) in this order in a laminate pouch. This produced a nonaqueous electrolyte secondary battery member 1. In so doing, the positive electrode plate 1 and the negative electrode plate 1 were arranged so that a main surface of the positive electrode active material layer of the positive electrode plate 1 was entirely included in a range of a main surface of the negative electrode active material layer of the negative electrode plate 1 (i.e., entirely overlapped with the main surface of the negative electrode active material layer of the negative electrode plate 1).
Subsequently, the nonaqueous electrolyte secondary battery member 1 was put into a bag which had been made, in advance, of a laminate of an aluminum layer and a heat seal layer. Then, 0.23 mL of nonaqueous electrolyte was put into the bag. The nonaqueous electrolyte had been prepared by dissolving LiPF6 in a mixed solvent in which ethylene carbonate, ethyl methyl carbonate, and diethyl carbonate were mixed at a ratio of 3:5:2 (volume ratio), so that a concentration of the LiPF6 would become 1 mol/L. The bag was then heat-sealed while the pressure inside the bag was reduced. This produced a nonaqueous electrolyte secondary battery 1.
Then, a restored discharge capacity after high-rate discharge of the nonaqueous electrolyte secondary battery 1 obtained by the above-described method was measured. Table 1 shows the measurement results.
[Production of Nonaqueous Electrolyte Secondary Battery Laminated Separator]
A polyolefin porous film 2 was obtained in the same manner as in Example 1, except that the heat fixation temperature was changed to 110° C. Table 1 shows the results of the evaluation (diminution rate, spot diameter) of the polyolefin porous film 2.
As in Example 1, the polyolefin porous film 2 was coated with the coating solution. The porous film, to which the coating solution had been applied, was immersed into 2-propanol while a coating film thereof was wet with the solvent, and was then left to stand still at 25° C. for 5 minutes. This produced a laminated porous film 2. The laminated porous film 2 thus obtained was further immersed in other 2-propanol while the laminated porous film 2 was wet with the above immersion solvent, and was then left to stand still at 25° C. for 5 minutes. This produced a laminated porous film 2a. The laminated porous film 2a thus obtained was dried at 65° C. for 5 minutes. This produced a nonaqueous electrolyte secondary battery laminated separator 2. Table 1 shows the results of evaluation (amount of α-form polyvinylidene fluoride-based resin) of a porous layer 2 constituting the nonaqueous electrolyte secondary battery laminated separator 2.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
A nonaqueous electrolyte secondary battery was prepared as in Example 1 except that the nonaqueous electrolyte secondary battery laminated separator 2 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 2.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 2 obtained by the above-described method, was measured. Table 1 shows the measurement results.
[Production of Nonaqueous Electrolyte Secondary Battery Laminated Separator]
A polyolefin porous film 3 was obtained in the same manner as in Example 1 except that (i) the amount of ultra-high molecular weight polyethylene powder (GUR4032, manufactured by Ticona Corporation) was set to 71.5 by weight %, (ii) the amount of polyethylene wax (FNP-0115, manufactured by Nippon Seiro Co., Ltd.) having a weight-average molecular weight of 1000 was set to 28.5 weight % by weight, (iii) the calcium carbonate (manufactured by Maruo Calcium Co., Ltd.) having an average particle diameter of 0.1 pim was added so as to account for 37% by volume of a total volume of the resultant mixture, (iv) the stretch ratio was set to 7.0 times, and (v) the heat fixation temperature was set to 123° C. Table 1 shows the results of the evaluation (diminution rate, spot diameter) of the polyolefin porous film 3.
As in Example 1, the polyolefin porous film 3 was coated with the coating solution. The porous film, to which the coating solution had been applied, was immersed into 2-propanol while a coating film thereof was wet with the solvent, and was then left to stand still at −5° C. for 5 minutes. This produced a laminated porous film 3. The laminated porous film 3 thus obtained was further immersed in other 2-propanol while the laminated porous film 3 was wet with the above immersion solvent, and was then left to stand still at 25° C. for 5 minutes. This produced a laminated porous film 3a. The laminated porous film 3a thus obtained was dried at 30° C. for 5 minutes. This produced a nonaqueous electrolyte secondary battery laminated separator 3. Table 1 shows the results of evaluation (amount of α-form polyvinylidene fluoride-based resin) of a porous layer 3 constituting the nonaqueous electrolyte secondary battery laminated separator 3.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that the nonaqueous electrolyte secondary battery laminated separator 3 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 3.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 3 obtained by the above-described method, was measured. Table 1 shows the measurement results.
(Preparation of Positive Electrode Plate)
A positive electrode plate was obtained in which a layer of a positive electrode mix (a mixture of LiCoO2 having an average particle diameter (D50) of 5 μm based on volume, an electrically conductive agent, and PVDF (at a weight ratio of 97:1.8:1.2)) was applied on one surface of a positive electrode current collector (aluminum foil). In the positive electrode plate thus obtained, a positive electrode active material layer had a porosity of 20%.
The positive electrode plate was partially cut off so that a positive electrode active material layer was present in an area of 45 mm×30 mm and that this area was surrounded by an area with a width of 13 mm in which area no positive electrode active material layer was present. A portion thus cut was used as a positive electrode plate 2.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that (i) the nonaqueous electrolyte secondary battery laminated separator 3 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1 and (ii) the positive electrode plate 2 was used as the positive electrode plate.
The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 4.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 4 obtained by the above-described method, was measured. Table 1 shows the measurement results.
(Preparation of Positive Electrode Plate)
A positive electrode plate was obtained in which a layer of a positive electrode mix (a mixture of LiNi0.33Mn0.33Co0.33O2 having an average particle diameter (D50) of 10 μm based on volume, an electrically conductive agent, and PVDF (at a weight ratio of 100:5:3)) was applied on one surface of a positive electrode current collector (aluminum foil). In the positive electrode plate thus obtained, a positive electrode active material layer had a porosity of 34%.
The positive electrode plate was partially cut off so that a positive electrode active material layer was present in an area of 45 mm×30 mm and that this area was surrounded by an area with a width of 13 mm in which area no positive electrode active material layer was present. A portion thus cut was used as a positive electrode plate 3.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that (i) the nonaqueous electrolyte secondary battery laminated separator 3 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1 and (ii) the positive electrode plate 3 was used as the positive electrode plate. The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 5.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 5 obtained by the above-described method, was measured. Table 1 shows the measurement results.
(Preparation of Negative Electrode Plate)
A negative electrode plate was obtained in which a layer of a negative electrode mix (a mixture of artificial graphite having an average particle diameter (D50) of 22 μm based on volume, styrene-1,3-butadiene copolymer, and sodium carboxymethyl cellulose (at a weight ratio of 98:1:1)) was applied on one surface of a negative electrode current collector (copper foil). In the negative electrode plate thus obtained, a negative electrode active material layer had a porosity of 35%.
The negative electrode plate was partially cut off so that a negative electrode active material layer was present in an area of 50 mm×35 mm and that this area was surrounded by an area with a width of 13 mm in which area no negative electrode active material layer was present. A portion thus cut was used as a negative electrode plate 2.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
The negative electrode plate 2 was used as a negative electrode plate. A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that the nonaqueous electrolyte secondary battery laminated separator 3 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 6.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 6 obtained by the above-described method, was measured. Table 1 shows the measurement results.
[Preparation of Porous Layer and Nonaqueous Electrolyte Secondary Battery Laminated Separator]
In N-methyl-2-pyrrolidone, a PVDF-based resin (manufactured by Arkema Inc.; product name “Kynar (registered trademark) LBG”; weight-average molecular weight of 590,000) was stirred and dissolved at 65° C. for 30 minutes so that a solid content would account for 10% by mass. A resultant solution was used as a binder solution. As a filler, alumina fine particles (manufactured by Sumitomo Chemical Co., Ltd.; product name “AKP3000”; silicon content: 5 ppm) was used. The alumina fine particles, the binder solution, and a solvent (N-methyl-2-pyrrolidone) were mixed together in the following proportion. That is, the alumina fine particles, the binder solution, and the solvent were mixed together so that (i) a resultant mixed solution would contain 10 parts by weight of the PVDF-based resin with respect to 90 parts by weight of the alumina fine particles and (ii) a solid content concentration (alumina fine particles+PVDF-based resin) of the mixed solution would account for 10% by weight. This produced a dispersion liquid. The dispersion liquid was used as a coating solution and applied by a doctor blade method to the polyolefin porous film 3 prepared in Example 3, so that the PVDF-based resin in the coating solution was applied in an amount of 6.0 g per square meter. The polyolefin porous film 3, to which the coating solution had been applied, was then dried at 65° C. for 5 minutes. This produced a nonaqueous electrolyte secondary battery laminated separator 4. The nonaqueous electrolyte secondary battery laminated separator 4 was dried such that (i) the direction of the hot air was perpendicular to the base material and (ii) the velocity of the hot air was 0.5 m/s. Table 1 shows the results of evaluation (amount of α-form polyvinylidene fluoride-based resin) of a porous layer 4 constituting the nonaqueous electrolyte secondary battery laminated separator 4.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that the nonaqueous electrolyte secondary battery laminated separator 4 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 7.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 7 obtained by the above-described method, was measured. Table 1 shows the measurement results.
[Preparation of Porous Layer and Nonaqueous Electrolyte Secondary Battery Laminated Separator]
A porous film, to which a coating solution had been applied, was obtained as in Example 3 and then was immersed in 2-propanol while a coating film thereof was wet with the solvent, and was then left to stand still at −78° C. for 5 minutes. This produced a laminated porous film 5. The laminated porous film 5 thus obtained was further immersed in other 2-propanol while the laminated porous film 5 was wet with the above immersion solvent, and was then left to stand still at 25° C. for 5 minutes. This produced a laminated porous film 5a. The laminated porous film 5a thus obtained was dried at 30° C. for 5 minutes. This produced a nonaqueous electrolyte secondary battery laminated separator 5. Table 1 shows the results of evaluation (amount of α-form polyvinylidene fluoride-based resin) of a porous layer 5 constituting the nonaqueous electrolyte secondary battery laminated separator 5.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that the nonaqueous electrolyte secondary battery laminated separator 5 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus prepared was used as a nonaqueous electrolyte secondary battery 8.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 8 obtained by the above-described method, was measured. Table 1 shows the measurement results.
(Preparation of Positive Electrode Plate)
A positive electrode plate was obtained in which a layer of a positive electrode mix (a mixture of LiMn2O4 having an average particle diameter (D50) of 8 μm based on volume, an electrically conductive agent, and PVDF (at a weight ratio of 100:5:3)) was applied on one surface of a positive electrode current collector (aluminum foil). In the positive electrode plate thus obtained, a positive electrode active material layer had a porosity of 51%.
The positive electrode plate was partially cut off so that a positive electrode active material layer was present in an area of 45 mm×30 mm and that this area was surrounded by an area with a width of 13 mm in which area no positive electrode active material layer was present. A portion thus cut was used as a positive electrode plate 4.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
The positive electrode plate 4 was used as a positive electrode plate. A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that the nonaqueous electrolyte secondary battery laminated separator 3 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus obtained was used as a nonaqueous electrolyte secondary battery 9.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 9 obtained by the above-described method, was measured. Table 1 shows the measurement results.
(Preparation of Negative Electrode Plate)
A negative electrode plate was obtained in which a layer of a negative electrode mix (a mixture of artificial spherocrystal graphite having an average particle diameter (D50) of 34 μm based on volume, an electrically conductive agent, and PVDF (at a weight ratio of 85:15:7.5)) was applied on one surface of a negative electrode current collector (copper foil). In the negative electrode plate thus obtained, a negative electrode active material layer had a porosity of 59%.
The negative electrode plate was partially cut off so that a negative electrode active material layer was present in an area of 50 mm×35 mm and that this area was surrounded by an area with a width of 13 mm in which area no negative electrode active material layer was present. A portion thus cut was used as a negative electrode plate 3.
[Preparation of Nonaqueous Electrolyte Secondary Battery]
The negative electrode plate 3 was used as a negative electrode plate. A nonaqueous electrolyte secondary battery was prepared in the same manner as in Example 1, except that the nonaqueous electrolyte secondary battery laminated separator 3 was used instead of the nonaqueous electrolyte secondary battery laminated separator 1. The nonaqueous electrolyte secondary battery thus obtained was used as a nonaqueous electrolyte secondary battery 10.
Then, a restored discharge capacity after high-rate discharge, of the nonaqueous electrolyte secondary battery 10 obtained by the above-described method, was measured. Table 1 shows the measurement results.
[Results]
As shown in Table 1, in a nonaqueous electrolyte secondary battery having a nonaqueous electrolyte secondary battery separator which contains a polyolefin porous film in which (i) a diminution rate of diethyl carbonate dropped on the polyolefin porous film is in a range of 15 sec/mg to 21 sec/mg and (ii) a spot diameter of the diethyl carbonate 10 seconds after the diethyl carbonate is dropped on the polyolefin porous film is not less than 20 mm, it is possible to further improve restored discharge capacity after high-rate discharge of the nonaqueous electrolyte secondary battery by configuring the battery to include (i) a porous layer between the polyolefin porous film and an electrode plate, the porous layer including an α-form polyvinylidene fluoride-based resin and a β-form polyvinylidene fluoride-based resin, assuming a sum of the amounts of the α-form and β-form polyvinylidene fluoride-based resins is 100 mol %, the amount of the α-form polyvinylidene fluoride-based resin being not less than 35.0 mol % and (ii) a positive electrode plate and a negative electrode plate, each of which has a value represented by Formula (1) which value is in a range of 0.00 to 0.50.
A nonaqueous electrolyte secondary battery in accordance with an embodiment of the present invention has an excellent restored discharge capacity after high-rate discharge and is suitable for use as (i) a battery for use in devices such as a personal computer, a mobile telephone, and a portable information terminal and (ii) an on-vehicle battery.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2017-243281 | Dec 2017 | JP | national |
