Patent Publication Number: US-2022238870-A1

Title: Lithium secondary battery and method for measuring state of charge of same

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This application is a continuation application of PCT/JP2020/033090 filed Sep. 1, 2020, which claims priority to Japanese Patent Application No. 2019-209921 filed Nov. 20, 2019, the entire contents all of which are incorporated herein by reference. 
    
    
     BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     The present invention relates to a lithium secondary battery and a method for measuring the state of charge of the lithium secondary battery. 
     2. Description of the Related Art 
     A lithium secondary battery using lithium cobaltate LiCoO 2  (which will be hereinafter referred to as LCO) as a positive electrode active material and lithium titanate Li 4 Ti 5 O 12  (which will be hereinafter referred to as LTO) as a negative electrode active material is widely known. For example, Patent Literature 1 (JP4439456B) discloses a battery pack comprising a plurality of non-aqueous electrolyte batteries each using a positive electrode (so-called coated positive electrode) produced by applying a slurry containing LCO powder, a binder, and a conductive additive, followed by drying, and a negative electrode (that is, a coated negative electrode) produced by applying a slurry containing an LTO negative electrode, a binder, and a conductive additive, followed by drying. It is known that such a battery has a stable voltage with respect to a change in capacity as compared with a battery using carbon as a negative electrode. For example, it is known that the battery exhibits an extremely flat voltage behavior in the charge/discharge curve of the LTO negative electrode over a wide capacity range. 
     Meanwhile, a coated positive electrode contains a relatively large amount (e.g., about 10% by weight) of components (such as binders and conductive additives) that do not contribute to the capacity, resulting in a low packing density of the lithium complex oxide as a positive electrode active material. Accordingly, the powder-dispersed positive electrode should be greatly improved from the viewpoint of the capacity and charge/discharge efficiency. Some attempts have been made to improve the capacity and charge/discharge efficiency by positive electrodes or layers of positive electrode active material composed of lithium complex oxide sintered plate. In this case, since the positive electrode or the layer of positive electrode active material contains no binder or conductive agent, high capacity and satisfactory charge/discharge efficiency can be expected due to a high packing density of lithium complex oxide. For example, Patent Literature 2 (JP5587052B) discloses a positive electrode including a positive electrode current collector and a positive electrode active material layer connected to the positive electrode current collector with a conductive bonding layer therebetween. The positive electrode active material layer is composed of a lithium complex oxide sintered plate, and the sintered plate has a thickness of 30 μm or more, a porosity of 3 to 30%, and an open pore rate of 70% or more. Further, Patent Literature 3 (WO2017/146088) discloses use of an oriented sintered plate including a plurality of primary grains composed of lithium complex oxide such as lithium cobaltate (LiCoO 2 ), the plurality of primary grains being oriented at an average orientation angle of over 0° and 30° or less to the plate face in the positive electrode plate, as a positive electrode of a lithium secondary battery including a solid electrolyte. 
     Meanwhile, use of a titanium-containing sintered plate as a negative electrode has been also proposed. For example, Patent Literature 4 (JP2015-185337A) discloses a lithium secondary battery using a lithium titanate (Li 4 Ti 5 O 12 ) sintered body as a positive electrode or a negative electrode. However, this lithium secondary battery is an all-solid battery having a solid electrolyte layer between a positive electrode and a negative electrode and is not a secondary battery using a non-aqueous electrolytic solution. 
     CITATION LIST 
     Patent Literature 
     Patent Literature 1: JP4439456B 
     Patent Literature 2: JP5587052B 
     Patent Literature 3: WO2017/146088 
     Patent Literature 4: JP2015-185337A 
     SUMMARY OF THE INVENTION 
     In the case of using lithium secondary batteries as a battery pack, the battery voltage is generally monitored in order to know how much battery capacity is left (that is, remaining capacity). However, in the case of a lithium secondary battery using an LCO positive electrode and an LTO negative electrode, as disclosed in Patent Literature 1, it is difficult to monitor the remaining capacity since the change in voltage according to the remaining capacity is minute, which has been a problem. 
     The inventors have now found that it is possible to provide a lithium secondary battery in which the resistance value changes greatly depending on the state of charge (SOC) by adopting a configuration including a predetermined positive electrode layer composed of a lithium complex oxide sintered body (e.g., LCO sintered body) and a predetermined negative electrode layer composed of a titanium-containing sintered body (e.g., LTO sintered body). 
     Accordingly, an object of the present invention is to provide a lithium secondary battery capable of providing a lithium secondary battery in which the resistance value changes greatly depending on the state of charge (SOC) while using a lithium complex oxide positive electrode such as LCO and a titanium-containing oxide negative electrode such as LTO. 
     According to an aspect of the present invention, there is provided a lithium secondary battery comprising:
         a positive electrode layer composed of a lithium complex oxide sintered body and having a thickness of 70 μm or more;   a negative electrode layer composed of a titanium-containing sintered body and having a thickness of 70 μm or more;   a separator interposed between the positive electrode layer and the negative electrode layer;   an electrolyte with which at least the separator is impregnated; and   an outer package comprising a closed space, the closed space accommodating the positive electrode layer, the negative electrode layer, the separator, and the electrolyte,   wherein the lithium secondary battery has a property that the resistance value decreases as the state of charge (SOC) increases from 10% to 80%.       

     According to another aspect of the present invention, there is provided a method for measuring the state of charge of a lithium secondary battery, comprising:
         providing the lithium secondary battery that has been charged;   measuring the resistance value of the charged lithium secondary battery; and   applying the resistance value to the correlation between the resistance value and the state of charge (SOC) of 10 to 80% measured in advance for the same type of lithium secondary battery to determine the state of charge (SOC) corresponding to the resistance value.       

    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a schematic sectional view of an example of the lithium secondary battery of the present invention. 
         FIG. 2  is a SEM image showing an example of a cross section perpendicular to the layer face of an oriented positive electrode layer. 
         FIG. 3  is an EBSD image in the cross section of the oriented positive electrode layer shown in  FIG. 2 . 
         FIG. 4  is an area-based histogram showing the distribution of orientation angles of primary grains in the EBSD image shown in  FIG. 3 . 
         FIG. 5  is a graph showing the relationship between the state of charge (SOC) and the resistance value measured in Example B1. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     Lithium Secondary Battery 
       FIG. 1  schematically shows an example of the lithium secondary battery of the present invention. A lithium secondary battery  10  shown in  FIG. 1  is in a form of coin-shaped battery, but the present invention is not limited to this and may be a battery in another form. The lithium secondary battery  10  includes a positive electrode layer  12 , a negative electrode layer  16 , a separator  20 , an electrolytic solution  22 , and an outer package  24 . The positive electrode layer  12  is composed of a lithium complex oxide sintered body and has a thickness of 70 μm or more. The negative electrode layer  16  is composed of a titanium-containing sintered body and has a thickness of 70 μm or more. The separator  20  is interposed between the positive electrode layer  12  and the negative electrode layer  16 . At least the separator  20  (typically, the positive electrode layer  12 , the negative electrode layer  16 , and the separator  20 ) is impregnated with the electrolytic solution  22 . The outer package  24  includes a closed space, and the closed space accommodates the positive electrode layer  12 , the negative electrode layer  16 , the separator  20 , and the electrolytic solution  22 . Then, the lithium secondary battery  10  has a property that the resistance value decreases (preferably continuously) as the state of charge (SOC) increases from 10% to 80%. In this way, it is possible to provide the lithium secondary battery  10  in which the resistance value changes greatly (preferably continuously) depending on the state of charge (SOC) by adopting the configuration including the predetermined positive electrode layer  12  composed of a lithium complex oxide sintered body (e.g., LCO sintered body) and the predetermined negative electrode layer  16  composed of a titanium-containing sintered body (e.g., LTO sintered body). 
     As described above, in the case of using lithium secondary batteries as a battery pack, the battery voltage is generally monitored in order to know the remaining capacity. However, in the case of a lithium secondary battery using an LCO positive electrode and an LTO negative electrode as disclosed in Patent Literature 1, it is difficult to monitor the remaining capacity since the change in voltage depending on the remaining capacity is minute, which has been a problem. In this regard, the lithium secondary battery  10  according to the present invention has a property that the resistance value decreases as the state of charge (SOC) increases from 10% to 80% and therefore can solve the aforementioned problem conveniently. The mechanism by which the resistance value changes depending on the state of charge is not clear, but it is considered as follows, referring to LTO, which is a typical example of the constituent material of the negative electrode layer  16 , as an example. That is, during charging and discharging of LTO, the reaction proceeds with the coexistence of two phases, a high-resistance phase (Li 4 Ti 5 O 12 ) and a low-resistance phase (Li 7 Ti 5 O 12 ). The resistance increases in the state of charge where the proportion of the high-resistance phase increases (that is, when the state of charge is low). Then, it is considered that, in the case where the positive electrode layer  12  and the negative electrode layer  16  each have a large thickness, as described above, the contribution rate of other resistance components becomes sufficiently low, thereby enabling detection of the resistance change in the battery according to the resistance change in LTO. This is a phenomenon peculiar to ceramic sintered plate electrodes that conduct electrons inside the sintered body without using conductive additives. In the case of using a conventional coated electrode, which contains a large amount of conductive additives, a desired conductivity can be ensured due to the conductive additives, even if the proportion of the high-resistance phase increases. Therefore, the aforementioned phenomenon cannot be seen. 
     That is, the lithium secondary battery  10  according to the present invention can preferably measure the state of charge by measuring the resistance value of the lithium secondary battery charged and applying the resistance value measured to the correlation between the resistance value and the state of charge (SOC) of 10 to 80% measured in advance for the same type of lithium secondary battery to determine the state of charge (SOC) corresponding to the resistance value. That is, a preferable aspect of the present invention provides a method for measuring the state of charge of a lithium secondary battery, the method comprising the steps of: i) providing a charged lithium secondary battery, ii) measuring the resistance value of the charged lithium secondary battery, iii) applying the resistance value to the correlation between the resistance value and the state of charge (SOC) of 10 to 80% measured in advance for the same type of lithium secondary battery to determine the state of charge (SOC) corresponding to the resistance value. 
     For performing the measurement more reliably, the lithium secondary battery  10  desirably has a large change in resistance value when the state of charge (SOC) is in the range of 10 to 80%. Specifically, the lithium secondary battery  10  preferably satisfies the relationship of 0.30≤R 50 /R 10 ≤0.85, 0.30≤R 80 /R 50 ≤0.85, and 0.20≤R 80 /R 10 ≤0.70, more preferably 0.35≤R 50 /R 10 ≤0.80, 0.35≤R 80 /R 50 ≤0.80, and 0.25≤R 80 /R 10 ≤0.65, further preferably 0.40≤R 50 /R 10 ≤0.75, 0.40≤R 80 /R 50 ≤0.75, and 0.30≤R 80 /R 10 ≤0.60, wherein R 10 , R 50  and R 80  represent the resistance values of the lithium secondary battery at an SOC of 10%, 50%, and 80%, respectively. Since satisfying such a relationship allows the resistance value to decrease more significantly as the SOC increases from 10% to 80%, the SOC can be measured more accurately based on the correlation with the resistance value. 
     The C/A, which is the ratio of the capacity C of the positive electrode layer  12  with respect to the capacity A of the negative electrode layer  16  is preferably 1.1 or more, more preferably 1.10 to 2.5, further preferably 1.15 to 2.0, particularly preferably 1.15 to 1.5. The capacity A of the negative electrode layer  16  and the capacity C of the positive electrode layer  12  can be measured according to the procedures described in Examples below. The C/A falling within such a range (together with the thickness of each of the positive electrode layer  12  and the negative electrode layer  16 ) enables a change in resistance of the battery corresponding to the change in resistance of the titanium-containing sintered body such as LTO to be detected more effectively. For achieving such a C/A, the ratio Tc/Ta of the thickness Tc of the positive electrode layer  12  to the thickness Ta of the negative electrode layer  16  is preferably 0.50 to 2.00, more preferably 0.55 to 1.90, further preferably 0.60 to 1.80, particularly preferably 0.65 to 1.70, most preferably 0.70 to 1.50. 
     The positive electrode layer  12  is composed of a lithium complex oxide sintered body. The fact that the positive electrode layer  12  is composed of a sintered body means that the positive electrode layer  12  contains no binder or conductive agent. This is because, even if a binder is contained in a green sheet, the binder disappears or burns out during firing. Since the positive electrode layer  12  contains no binder, there is an advantage that deterioration of the positive electrode due to the electrolytic solution  22  can be avoided. The lithium complex oxide constituting the sintered body is particularly preferably lithium cobaltite (typically, LiCoO 2 , which may be hereinafter abbreviated as LCO). Various lithium complex oxide sintered plates or LCO sintered plates are known, and those disclosed in Patent Literature 2 (JP5587052A) and Patent Literature 3 (WO2017/146088) can be referred to, for example. 
     According to a preferable aspect of the present invention, the positive electrode layer  12 , that is, the lithium complex oxide sintered plate is an oriented positive electrode layer including a plurality of primary grains composed of lithium complex oxide, the plurality of primary grains being oriented at an average orientation angle of over 0° and 30° or less to the layer face of the positive electrode layer.  FIG. 2  shows an example of a SEM image in a cross section perpendicular to the layer face of the oriented positive electrode layer  12 , and  FIG. 3  shows an electron backscatter diffraction (EBSD: Electron Backscatter Diffraction) image in a cross section perpendicular to the layer face of the oriented positive electrode layer  12 . Further,  FIG. 4  shows an area-based histogram showing the distribution of orientation angles of primary grains  11  in the EBSD image shown in  FIG. 3 . In the EBSD image shown in  FIG. 3 , the discontinuity of crystal orientation can be observed. In  FIG. 3 , the orientation angle of each primary grain  11  is indicated by the shading of color. A darker color indicates a smaller orientation angle. The orientation angle is a tilt angle formed by plane (003) of the primary grains  11  to the layer face direction. In  FIGS. 2 and 3 , the points shown in black within the oriented positive electrode layer  12  represent pores. 
     The oriented positive electrode layer  12  is an oriented sintered body composed of the plurality of primary grains  11  bound to each other. The primary grains  11  are each mainly in the form of a plate but may include rectangular, cubic, and spherical grains. The cross-sectional shape of each primary grain  11  is not particularly limited and may be a rectangular shape, a polygonal shape other than the rectangular shape, a circular shape, an elliptical shape, or a complex shape other than above. 
     The primary grains  11  are composed of a lithium complex oxide. The lithium complex oxide is an oxide represented by Li x MO 2  (where 0.05&lt;×&lt;1.10 is satisfied, M represents at least one transition metal, and M typically contains one or more of Co, Ni, and Mn). The lithium complex oxide has a layered rock-salt structure. The layered rock-salt structure refers to a crystalline structure in which lithium layers and transition metal layers other than lithium are alternately stacked with oxygen layers interposed therebetween, that is, a crystalline structure in which transition metal ion layers and single lithium layers are alternately stacked with oxide ions therebetween (typically, an α-NaFeO 2  structure, i.e., a cubic rock-salt structure in which transition metal and lithium are regularly disposed in the [111] axis direction). Examples of the lithium complex oxide include Li x CoO 2  (lithium cobaltate), Li x NiO 2  (lithium nickelate), Li x MnO 2  (lithium manganate), Li x NiMnO 2  (lithium nickel manganate), Li x NiCoO 2  (lithium nickel cobaltate), Li x CoNiMnO 2  (lithium cobalt nickel manganate), and Li x CoMnO 2  (lithium cobalt manganate), particularly preferably Li x CoO 2  (lithium cobaltate, typically LiCoO 2 ). The lithium complex oxide may contain one or more elements selected from Mg, Al, Si, Ca, Ti, V, Cr, Fe, Cu, Zn, Ga, Ge, Sr, Y, Zr, Nb, Mo, Ag, Sn, Sb, Te, Ba, Bi, and W. 
     As shown in  FIGS. 3 and 4 , the average of the orientation angles of the primary grains  11 , that is, the average orientation angle is over 0° and 30° or less. This brings various advantages as follows. First, since each primary grain  11  lies in a direction inclined from the thickness direction, the adhesion between the primary grains can be improved. As a result, the lithium ion conductivity between a certain primary grain  11  and each of other primary grains  11  adjacent to the primary grain  11  on both sides in the longitudinal direction can be improved, so that the rate characteristic can be improved. Secondly, the rate characteristic can be further improved. This is because, when lithium ions move in and out, the oriented positive electrode layer  12  expands and contracts smoothly since the oriented positive electrode layer  12  expands and contracts more in the thickness direction than in the layer face direction, as described above, and thus the lithium ions also move in and out smoothly. Further, in the case where the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  constitute one integrated sintered plate as a whole, which is a preferable aspect to be described below, since the expansion and contraction of the oriented positive electrode layer  12  following the inflow and outflow of lithium ions are predominant in the direction perpendicular to the layer face, stress is less likely to occur at the bonding interface between the oriented positive electrode layer  12  and the ceramic separator  20 , thereby making it easy to maintain good bonding at the interface. 
     The average orientation angle of the primary grains  11  is obtained by the following method. First, three horizontal lines that divide the oriented positive electrode layer  12  into four equal parts in the thickness direction and three vertical lines that divide the oriented positive electrode layer  12  into four equal parts in the layer face direction are drawn in an EBSD image of a rectangular region of 95 μm×125 μm observed at a magnification of 1000 times, as shown in  FIG. 3 . Next, the average orientation angle of the primary grains  11  is obtained by arithmetically averaging the orientation angles of all the primary grains  11  intersecting at least one of the three horizontal lines and the three vertical lines. The average orientation angle of the primary grains  11  is preferably 30° or less, more preferably 25° or less, from the viewpoint of further improving the rate characteristics. From the viewpoint of further improving the rate characteristics, the average orientation angle of the primary grains  11  is preferably 2° or more, more preferably 5° or more. 
     As shown in  FIG. 4 , the orientation angles of the primary grains  11  may be widely distributed from 0° to 90°, but most of them are preferably distributed in the region of over 0° and 30° or less. That is, when a cross section of the oriented sintered body constituting the oriented positive electrode layer  12  is analyzed by EBSD, the total area of the primary grains  11  with an orientation angle of over 0° and 30° or less to the layer face of the oriented positive electrode layer  12  (which will be hereinafter referred to as low-angle primary grains) out of the primary grains  11  contained in the cross section analyzed is preferably 70% or more, more preferably 80% or more, with respect to the total area of the primary grains  11  contained in the cross section (specifically, 30 primary grains  11  used for calculating the average orientation angle). Thereby, the proportion of the primary grains  11  with high mutual adhesion can be increased, so that the rate characteristic can be further improved. Further, the total area of grains with an orientation angle of 20° or less among the low-angle primary grains is more preferably 50% or more with respect to the total area of 30 primary grains  11  used for calculating the average orientation angle. Further, the total area of grains with an orientation angle of 10° or less among the low-angle primary grains is more preferably 15% or more with respect to the total area of 30 primary grains  11  used for calculating the average orientation angle. 
     Since the primary grains  11  are each mainly in the form of a plate, the cross section of each primary grain  11  extends in a predetermined direction, typically in a substantially rectangular shape, as shown in  FIGS. 2 and 3 . That is, when the cross section of the oriented sintered body is analyzed by EBSD, the total area of the primary grains  11  with an aspect ratio of 4 or more in the primary grains  11  contained in the cross section analyzed is preferably 70% or more, more preferably 80% or more, with respect to the total area of the primary grains  11  contained in the cross section (specifically, 30 primary grains  11  used for calculating the average orientation angle). Specifically, in the EBSD image as shown in  FIG. 3 , the mutual adhesion between the primary grains  11  can be further improved by above, as a result of which the rate characteristic can be further improved. The aspect ratio of each primary grain  11  is a value obtained by dividing the maximum Feret diameter of the primary grain  11  by the minimum Feret diameter. The maximum Feret diameter is the maximum distance between two parallel straight lines that interpose the primary grain  11  therebetween on the EBSD image in observation of the cross section. The minimum Feret diameter is the minimum distance between two parallel straight lines that interpose the primary grain  11  therebetween on the EBSD image. 
     The mean diameter of the plurality of primary grains constituting the oriented sintered body is preferably 5 μm or more. Specifically, the mean diameter of the 30 primary grains  11  used for calculating the average orientation angle is preferably 5 μm or more, more preferably 7 μm or more, further preferably 12 μm or more. Thereby, since the number of grain boundaries between the primary grains  11  in the direction in which lithium ions conduct is reduced, and the lithium ion conductivity as a whole is improved, the rate characteristic can be further improved. The mean diameter of the primary grains  11  is a value obtained by arithmetically averaging the equivalent circle diameters of the primary grains  11 . An equivalent circle diameter is the diameter of a circle having the same area as each primary grain  11  on the EBSD image. 
     The positive electrode layer  12  preferably includes pores. The electrolytic solution can penetrate into the sintered body by the sintered body including pores, particularly open pores, when the sintered body is integrated into a battery as a positive electrode plate. As a result, the lithium ion conductivity can be improved. This is because there are two types of conduction of lithium ions within the sintered body: conduction through constituent grains of the sintered body; and conduction through the electrolytic solution within the pores, and the conduction through the electrolytic solution within the pores is overwhelmingly faster. 
     The positive electrode layer  12 , that is, the lithium complex oxide sintered body preferably has a porosity of 20 to 60%, more preferably 25 to 55%, further preferably 30 to 50%, particularly preferably 30 to 45%. The stress relief effect by the pores and the increase in capacity can be expected, and the mutual adhesion between the primary grains  11  can be further improved, so that the rate characteristics can be further improved. The porosity of the sintered body is calculated by polishing a cross section of the positive electrode layer with CP (cross-section polisher) polishing, thereafter observing the cross section at a magnification of 1000 times with SEM, and binarizing the SEM image obtained. The average equivalent circle diameter of pores formed inside the oriented sintered body is not particularly limited but is preferably 8 μm or less. The smaller the average equivalent circle diameter of the pores, the mutual adhesion between the primary grains  11  can be improved more. As a result, the rate characteristic can be improved more. The average equivalent circle diameter of the pores is a value obtained by arithmetically averaging the equivalent circle diameters of  10  pores on the EBSD image. An equivalent circle diameter is the diameter of a circle having the same area as each pore on the EBSD image. Each of the pores formed inside the oriented sintered body is preferably an open pore connected to the outside of the positive electrode layer  12 . 
     The positive electrode layer  12 , that is, the lithium complex oxide sintered body preferably has a mean pore diameter of 0.1 to 10.0 μm, more preferably 0.2 to 5.0 μm, further preferably 0.25 to 3.0 μm. Within such a range, stress concentration is suppressed from occurring locally in large pores, and the stress is easily released uniformly in the sintered body. 
     The thickness of the positive electrode layer 12 is 70 μm or more, preferably 70 to 800 μm, more preferably 70 to 600 μm, further preferably 80 to 500 μm, particularly preferably 90 to 450 μm. The thickness within such a range can improve the energy density of the lithium secondary battery  10  by increasing the capacity of the active material per unit area together with suppressing the deterioration of the battery characteristics (particularly, the increase of the resistance value) due to repeated charging/discharging. 
     The negative electrode layer  16  is composed of a titanium-containing sintered body. The titanium-containing sintered body preferably contains lithium titanate Li 4 Ti 5 O 12  (which will be hereinafter referred to as LTO) or niobium titanium complex oxide Nb 2 TiO 7 , more preferably LTO. LTO is typically known to have a spinel structure but can have other structures during charging and discharging. For example, the reaction of LTO proceeds in the two-phase coexistence of Li 4 Ti 5 O 12  (spinel structure) and Li 7 Ti 5 O 12  (rock salt structure) during charging and discharging. Accordingly, the structure of LTO is not limited to the spinel structure. 
     The fact that the negative electrode layer  16  is composed of a sintered body means that the negative electrode layer  16  contains no binder or conductive agent. This is because, even if a binder is contained in a green sheet, the binder disappears or burns out during firing. Since the negative electrode layer contains no binder, high capacity and good charge/discharge efficiency can be achieved by high packing density of the negative electrode active material (for example, LTO or Nb 2 TiO 7 ). The LTO sintered body can be produced according to the method described in Patent Literature 4 (JP2015-185337A). 
     The negative electrode layer  16 , that is, the titanium-containing sintered body has a structure that a plurality (namely, a large number) of primary grains are bonded. Accordingly, these primary grains are preferably composed of LTO or Nb 2 TiO 7 . Further, a material with high insulation in a charged state and high conductivity in a discharged state is preferable in the present invention. In other words, a material in which the valence of Ti is close to tetravalent in a charged state and is trivalent in a discharged state is preferable. Examples of other materials include TiO 2 . 
     The thickness of the negative electrode layer 16 is 70 μm or more, preferably 70 to 800 μm, more preferably 70 to 700 μm, further preferably 80 to 600 μm, particularly preferably 90 to 550 μm. It is considered that, as the thickness of the negative electrode layer  16  increases, it is easier to achieve a battery with high capacity and high energy density, and the contribution rate of other resistance components decreases furthermore, thereby making it easier to detect a change in resistance of the battery corresponding to the resistance change of the negative electrode layer  16 . The thickness of the negative electrode layer  16  is determined by measuring the distance between the two substantially parallel faces of the layer, for example, when the cross section of the negative electrode layer  16  is observed by SEM (scanning electron microscopy). 
     The primary grain size that is the average grain size of the plurality of primary grains forming the negative electrode layer  16  is preferably 1.2 μm or less, more preferably 0.02 to 1.2 μm, further preferably 0.05 to 0.7 μm. Within such a range, the lithium ion conductivity and the electron conductivity are easily compatible with each other, which contributes to improving the rate performance. 
     The negative electrode layer  16  preferably includes pores. The electrolytic solution can penetrate into the sintered body by the sintered body including pores, particularly open pores, when the sintered body is integrated into a battery as a negative electrode layer. As a result, the lithium ion conductivity can be improved. This is because there are two types of conduction of lithium ions within the sintered body: conduction through constituent grains of the sintered body; and conduction through the electrolytic solution within the pores, and the conduction through the electrolytic solution within the pores is overwhelmingly faster. 
     The negative electrode layer  16  preferably has a porosity of 20 to 60%, more preferably 30 to 55%, further preferably 35 to 50%. Within such a range, the lithium ion conductivity and the electron conductivity are easily compatible with each other, which contributes to improving the rate performance. 
     The negative electrode layer  16  has a mean pore diameter of 0.08 to 5.0 μm, preferably 0.1 to 3.0 μm, more preferably 0.12 to 1.5 μm. Within such a range, the lithium ion conductivity and the electron conductivity are easily compatible with each other, which contributes to improving the rate performance. 
     The separator  20  is preferably a separator made of cellulose, polyolefin, polyimide, polyester (e.g., polyethylene terephthalate (PET)), or ceramic. A separator made of cellulose is advantageous since it is inexpensive and has excellent heat resistance. Further, being different from widely used polyolefin separators having poor heat resistance, a separator made of polyimide, polyester (e.g., polyethylene terephthalate (PET)), or cellulose has not only excellent heat resistance of itself but also excellent wettability to γ-butyrolactone (GBL), which is an electrolytic solution component having excellent heat resistance. Accordingly, in the case of using an electrolytic solution containing GBL, the electrolytic solution can be sufficiently penetrated into the separator (without repelling). Meanwhile, a separator made of ceramic is advantageous in that it, of course, has excellent heat resistance and can be produced as one integrated sintered plate together with the positive electrode layer  12  and the negative electrode layer  16  as a whole. In the case of a ceramic separator, the ceramic constituting the separator is preferably at least one selected from MgO, Al 2 O 3 , ZrO 2 , SiC, Si 3 N 4 , AlN, and cordierite, more preferably at least one selected from MgO, Al 2 O 3 , and ZrO 2 . 
     The ceramic separator  20  is a microporous film made of ceramic. The ceramic separator  20  is advantageous in that it, of course, has excellent heat resistance and can be produced as one integrated sintered plate together with the positive electrode layer  12  and the negative electrode layer  16  as a whole. The ceramic separator  20  preferably has a thickness of 3 to 40 μm, more preferably 5 to 35 μm, further preferably 10 to 30 μm. The ceramic separator  20  preferably has a porosity of 30 to 85%, more preferably 40 to 80%. The ceramic separator  20  may contain a glass component for improving the adhesion to the positive electrode layer  12  and the negative electrode layer  16 . In this case, the content ratio of the glass component in the ceramic separator  20  is preferably 0.1 to 50 wt %, more preferably 0.5 to 40 wt %, further preferably 0.5 to 30 wt %, with respect to the total weight of the ceramic separator  20 . The addition of the glass component to the ceramic separator  20  is preferably performed by adding glass frit to the raw material powder of the ceramic separator. However, if the desired adhesion of the ceramic separator  20  to the positive electrode layer  12  and the negative electrode layer  16  can be ensured, the glass component is not particularly required to be contained in the ceramic separator  20 . 
     According to a preferable aspect of the present invention, the separator  20  is a ceramic separator, and the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  form one integrated sintered plate as a whole, whereby the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  are bonded together. That is, the three layers of the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  are preferably bonded together without resorting to other bonding methods such as adhesives. Here, to “form one integrated sintered plate as a whole” means that green sheets having a three-layer structure composed of a positive electrode green sheet providing the positive electrode layer  12 , a separator green sheet providing the ceramic separator  20 , and a negative electrode green sheet providing the negative electrode layer  16  are fired, so that each layer is sintered. Therefore, if the green sheets with a three-layer structure before firing are punched into a predetermined shape (such as a coin shape and a chip shape) using a punching die, the displacement between the positive electrode layer  12  and the negative electrode layer  16  in the integrated sintered plate in the final form is supposed not to exist at all. That is, the end face of the positive electrode layer  12  and the end face of the negative electrode layer  16  are aligned, so that the capacity can be maximized. Alternatively, even if such a displacement is present, the integrated sintered plate is suitable for processing such as laser processing, cutting, and polishing. Therefore, the end face may be finished to minimize or eliminate such a displacement. In any case, the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  are bonded together, as long as they form an integrated sintered plate, the displacement between the positive electrode layer  12  and the negative electrode layer  16  never occurs afterwards. The high discharge capacity, as expected (that is, close to the theoretical capacity), can be achieved by minimizing or eliminating the displacement between the positive electrode layer  12  and the negative electrode layer  16 . Further, it is considered that, since the integrated sintered plate has a three-layer structure including the ceramic separator, waviness or warpage is less likely to occur (that is, the flatness is excellent), and therefore variations in the distance between the positive and negative electrodes are less likely to occur (that is, the distance is uniform), as compared with a single positive electrode plate and a single negative electrode plate that are each produced as one sintered plate, thereby contributing to improving the charge/discharge cycle performance. For example, the area displacement ratio between the positive electrode layer  12  and the negative electrode layer  16  is preferably less than 1%, more preferably less than 0.5%, further preferably 0%. The area displacement ratio between the positive electrode layer  12  and the negative electrode layer  16  is defined as a value (%) calculated based on the formula: [(S p +S n )/S pn ]×100, wherein the area of the region where the positive electrode layer  12  and the negative electrode layer  16  overlap each other is referred to as S pn , the area of the region where the positive electrode layer  12  protrudes from the negative electrode layer  16  is referred to as S p , and the area of the region where the negative electrode layer  16  protrudes from the positive electrode layer  12  is referred to as S n . Further, the lithium secondary battery  10  preferably has a ratio of the discharge capacity to the theoretical capacity of 99% or more, more preferably 99.5% or more, further preferably 100%. 
     The electrolytic solution  22  is not specifically limited, and commercially available electrolytic solutions for lithium batteries such as a solution obtained by dissolving a lithium salt (e.g., LiPF 6 ) in a non-aqueous solvent such as an organic solvent (e.g., a mixed solvent of ethylene carbonate (EC) and methyl ethyl carbonate (MEC), a mixed solvent of ethylene carbonate (EC) and diethyl carbonate (DEC), or a mixed solvent of ethylene carbonate (EC) and ethyl methyl carbonate (EMC)) may be used. 
     In the case of forming a lithium secondary battery having excellent heat resistance, the electrolytic solution  22  preferably contains lithium borofluoride (LiBF 4 ) in a non-aqueous solvent. In this case, the non-aqueous solvent is preferably at least one selected from the group consisting of γ-butyrolactone (GBL), ethylene carbonate (EC) and propylene carbonate (PC), more preferably a mixed solvent composed of EC and GBL, a single solvent composed of PC, a mixed solvent composed of PC and GBL, or a single solvent composed of GBL, particularly preferably a mixed solvent composed of EC and GBL or a single solvent composed of GBL. The non-aqueous solvent has an increased boiling point by containing γ-butyrolactone (GBL), which considerably improves the heat resistance. From such a viewpoint, the volume ratio of EC:GBL in the EC and/or GBL containing non-aqueous solvent is preferably 0:1 to 1:1 (GBL ratio: 50 to 100% by volume), more preferably 0:1 to 1:1.5 (GBL ratio: 60 to 100% by volume), further preferably 0:1 to 1:2 (GBL ratio: 66.6 to 100% by volume), particularly preferably 0:1 to 1:3 (GBL ratio: 75 to 100% by volume). The lithium borofluoride (LiBF 4 ) to be dissolved in the non-aqueous solvent is an electrolyte having a high decomposition temperature, which also considerably improves the heat resistance. The LiBF 4  concentration in the electrolytic solution 22 is preferably 0.5 to 2 mol/L, more preferably 0.6 to 1.9 mol/L, further preferably 0.7 to 1.7 mol/L, particularly preferably 0.8 to 1.5 mol/L. 
     The electrolytic solution  22  may further contain vinylene carbonate (VC) and/or fluoroethylene carbonate (FEC) and/or vinyl ethylene carbonate (VEC) as additives. Both VC and FEC have excellent heat resistance. Accordingly, a SEI film having excellent heat resistance can be formed on the surface of the negative electrode layer  16  by the electrolytic solution  22  containing such additives. 
     Further, a solid electrolyte or a polymer electrolyte may be used instead of the electrolytic solution  22  (in other words, a solid electrolyte and a polymer electrolyte can be used as an electrolyte, other than the electrolytic solution  22 ). In such a case, at least the inside of the pores of the separator  20  is preferably impregnated with the electrolyte, as in the case of the electrolytic solution  22 . The impregnation method is not specifically limited, but examples thereof include a method of melting the electrolyte and infiltrating it into the pores of the separator  20  and a method of pressing the green compact of the electrolyte against the separator  20 . 
     The outer package  24  includes a closed space, and the closed space accommodates the positive electrode layer  12 , the negative electrode layer  16 , the separator  20 , and the electrolytic solution  22 . The outer package  24  may be appropriately selected corresponding to the type of the lithium secondary battery  10 . For example, in the case where the lithium secondary battery is in a form of coin-shaped battery as shown in  FIG. 1 , the outer package  24  typically includes the positive electrode can  24   a,  the negative electrode can  24   b,  and the gasket  24   c,  and the positive electrode can  24   a  and the negative electrode can  24   b  are crimped via the gasket  24   c  to form the closed space. The positive electrode can  24   a  and the negative electrode can  24   b  can be made of metals such as stainless steel and are not specifically limited. The gasket  24   c  can be an annular member made of an insulating resin such as polypropylene, polytetrafluoroethylene, and PFA resin and is not particularly limited. 
     Further, in the case where the lithium secondary battery is in a form of chip battery that can be incorporated in a card, it is preferable that the outer package is a resin substrate, and the battery elements (that is, the positive electrode layer  12 , the negative electrode layer  16 , the separator  20 , and the electrolytic solution  22 ) are embedded in the resin substrate. For example, the battery elements may be sandwiched by a pair of resin films, and it is preferable that the resin films are bonded together by an adhesive, or the resin films are thermally fused together by hot pressing. 
     The lithium secondary battery  10  preferably further includes a positive electrode current collector  14  and/or a negative electrode current collector  18 . The positive electrode current collector  14  and the negative electrode current collector  18  are not specifically limited but are preferably metal foils such as copper foils and aluminum foils. The positive electrode current collector  14  is preferably interposed between the positive electrode layer  12  and the outer package  24  (e.g., the positive electrode can  24   a ), and the negative electrode current collector  18  is preferably interposed between the negative electrode layer  16  and the outer package  24  (e.g., the negative electrode can  24   b ). Further, a positive side carbon layer  13  is preferably provided between the positive electrode layer  12  and the positive electrode current collector  14  for reducing the contact resistance. Likewise, a negative side carbon layer  17  is preferably provided between the negative electrode layer  16  and the negative electrode current collector  18  for reducing the contact resistance. Both the positive side carbon layer  13  and the negative side carbon layer  17  are preferably composed of a conductive carbon and may be formed, for example, by applying a conductive carbon paste by screen printing or the like. 
     Method for Producing Integrated Sintered Plate 
     The integrated sintered plate with a three-layer structure of the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  may be produced by any method but is preferably produced by (1) preparation green sheets corresponding to the respective three layers and (2) laminating the green sheets, followed by pressure bonding and firing. 
     (1) Preparation of Various Green Sheets 
     (1a) Preparation of Positive Electrode Green Sheet 
     A lithium complex oxide-containing green sheet as a positive electrode green sheet can be prepared, as follows. A raw material powder composed of lithium complex oxide is prepared. The powder preferably comprises pre-synthesized platy particles (e.g., LiCoO 2  platy particles) having a composition of LiMO 2  (M as described above). The volume-based D50 particle diameter of the raw material powder is preferably 0.3 to 30 μm. For example, the LiCoO 2  platy particles can be produced as follows. Co 3 O 4  powder and Li 2 CO 3  powder as raw materials are mixed and fired (500 to 900° C., 1 to 20 hours) to synthesize LiCoO 2  powder. The resultant LiCoO 2  powder is milled into a volume-based D50 particle diameter of 0.2 μm to 10 μm with a pot mill to yield platy LiCoO 2  particles capable of conducting lithium ions along the faces of the plate. Such LiCoO 2  particles are also produced by a procedure involving grain growth in a green sheet from LiCoO 2  powder slurry and crushing the green sheet, or a procedure involving synthesis of platy crystals, such as a flux process, a hydrothermal synthesis process, a single crystal growth process using a melt, and a sol gel process. The resultant LiCoO 2  particles are readily cleaved along cleavage planes. The LiCoO 2  particles may be cleaved by crushing to produce LiCoO 2  platy particles. 
     The platy particles may be independently used as raw material powder, or a mixed powder of the platy powder and another raw material powder (for example, Co 3 O 4  particles) may be used as a raw material powder. In the latter case, it is preferred that the platy powder serves as template particles for providing orientation, and another raw material powder (e.g., Co 3 O 4  particles) serves as matrix particles that can grow along the template particle. In this case, the raw powder is preferably composed of a mixed powder in a ratio of template particles to matrix particles of 100:0 to 3:97. When the Co 3 O 4  raw material powder is used as the matrix particles, the volume-based D50 particle diameter of the Co 3 O 4  raw material powder may be any value, for example, 0.1 to 1.0 μm, and is preferably smaller than the volume-based D50 particle diameter of LiCoO 2  template particles. The matrix particles may also be produced by heating a Co(OH) 2  raw material at 500° C. to 800° C. for 1 to 10 hours. In addition to Co 3 O 4 , Co(OH) 2  particles may be used, or LiCoO 2  particles may be used as the matrix particles. 
     When the raw material powder is composed of 100% of LiCoO 2  template particles, or when LiCoO 2  particles are used as matrix particles, a large (e.g., 90 mm×90 mm square) flat LiCoO 2  sintered layer can be yielded by firing. Although the mechanism is not clear, since synthesis of LiCoO 2  does not proceed in a firing process, a change in volume or local unevenness of the shape probably does not occur.  0052  The raw material powder is mixed with a dispersive medium and any additive (e.g., binder, plasticizer, and dispersant) to form a slurry. A lithium compound (e.g., lithium carbonate) in an excess amount of about 0.5 to 30 mol % other than LiMO 2  may be added to the slurry to promote grain growth and compensate for a volatile component in a firing process described later. The slurry preferably contains no pore-forming agent. The slurry is defoamed by stirring under reduced pressure, and the viscosity is preferably adjusted into 4000 to 10000 cP. The resultant slurry is formed into a sheet to give a green sheet containing lithium complex oxide. The sheet is preferably formed by a forming procedure capable of applying a shear force to platy particles (for example, template particles) in the raw material powder. Through this process, the primary grains can have a mean tilt angle of over 0° and 30° or less to the sheet face. The forming procedure capable of applying a shear force to platy particles suitably includes a doctor blade process. The thickness of the green sheet containing the lithium complex oxide may be appropriately selected so as to give the above desired thickness after firing. 
     (1b) Preparation of Negative Electrode Green Sheet 
     A titanium-containing green sheet as a negative electrode green sheet may be produced by any method. For example, a LTO-containing green sheet can be prepared, as follows. First, raw material powder (LTO powder) composed of lithium titanate Li 4 Ti 5 O 12  is prepared. Commercially available or newly synthesized LTO powder may be used as the raw material powder. For example, powder obtained by hydrolyzing a mixture of titanium tetraisopropoxy alcohol and isopropoxy lithium may be used, or a mixture containing lithium carbonate, titania, or the like may be fired. The raw material powder preferably has a volume-based D50 particle size of 0.05 to 5.0 μm, more preferably 0.1 to 2.0 μm. A larger particle size of the raw material powder tends to increase the size of the pores. Further, in the case where the particle size of the raw material is large, milling (such as pot milling, bead milling, and jet milling) may be performed to a desired particle size. The raw material powder is mixed with a dispersive medium and any additive (e.g., binder, plasticizer, and dispersant) to form a slurry. A lithium compound (e.g., lithium carbonate) in an excess amount of about 0.5 to 30 mol % other than LiMO 2  may be added to the slurry to promote grain growth and compensate for a volatile component in a firing process described later. The slurry preferably contains no pore-forming agent. The slurry is defoamed by stirring under reduced pressure, and the viscosity is preferably adjusted into 4000 to 10000 cP. The resultant slurry is formed into a LTO-containing green sheet. The sheet can be formed by any known process and is preferably formed by a doctor blade process. The thickness of the LTO-containing green sheet may be appropriately selected so as to give the above desired thickness after firing. 
     (1c) Preparation of Separator Green Sheet 
     A separator green sheet can be prepared, as follows. First, at least one ceramic powder selected from MgO, Al 2 O 3 , ZrO 2 , SiC, Si 3 N 4 , AlN, and cordierite is prepared. Glass frit may be added to the ceramic powder. The raw material powder preferably has a volume-based D50 particle size of 0.05 to 20 μm, more preferably 0.1 to 10 μm. A larger particle size of the raw material powder tends to increase the size of the pores. Further, in the case where the particle size of the raw material is large, milling (such as pot milling, bead milling, and jet milling) may be performed to a desired particle size. The raw material powder is mixed with a dispersive medium and any additive (e.g., binder, plasticizer, and dispersant) to form a slurry. The slurry preferably contains no pore-forming agent. The slurry is defoamed by stirring under reduced pressure, and the viscosity is preferably adjusted into 4000 to 10000 cP. The resultant slurry is formed into a separator green sheet. The sheet can be formed by any known process and is preferably formed by a doctor blade process. The thickness of the separator green sheet may be appropriately selected so as to give the above desired thickness after firing. 
     (2) Lamination, Pressure Bonding, and Firing of Green Sheets 
     Then, the positive electrode green sheet, the separator green sheet, and the negative electrode green sheet are sequentially stacked, and the laminate obtained is pressed so that the green sheets are pressure-bonded together. The pressing may be performed by a known method and is not specifically limited but is preferably performed by CIP (cold isostatic pressing). The pressing pressure is preferably 10 to 5000 kgf/cm 2 , more preferably 50 to 3000 kgf/cm 2 . The green sheet laminate thus pressure-bonded is preferably punched into a desired shape (such as a coin shape and a chip shape) or size using a punching die. Thereby, the displacement between the positive electrode layer  12  and the negative electrode layer  16  can be eliminated in the integrated sintered plate in the final form. As a result, the end face of the positive electrode layer  12  and the end face of the negative electrode layer  16  are aligned, so that the battery capacity can be maximized. 
     The green sheet laminate obtained is placed on a setter. The setter is made of ceramics, preferably zirconia or magnesia. The setter is preferably embossed. The green sheet disposed on the setter is put into a sheath. The sheath is made of ceramics, preferably alumina. Then, the green sheet in this state is degreased, as needed, and fired to obtain an integrated sintered plate. The degreasing is preferably performed at 300 to 600° C. for 0.5 to 20 hours. Further, the firing is preferably performed at 650 to 900° C. for 0.01 to 20 hours, more preferably at 700 to 850° C. for 0.5 to 10 hours. The heating rate during firing is preferably 50 to 1500° C./h, more preferably 200 to 1300° C./h. In particular, this heating rate is preferably employed in a temperature rising process from 600 to 900° C., more preferably from 600 to 800° C. Thus, an integrated sintered plate having a three-layer structure of the positive electrode layer  12 , the ceramic separator  20 , and the negative electrode layer  16  is obtained. In the case where the punching process is not performed at the stage of the green sheet laminate, a displacement between the positive electrode layer  12  and the negative electrode layer  16  can occur in the integrated sintered plate in the final form. In this case, the end face of the integrated sintered plate is preferably finished by a technique such as laser processing, cutting, and polishing, to minimize or eliminate the displacement. As a result, the end face of the positive electrode layer  12  and the end face of the negative electrode layer  16  are aligned, so that the battery capacity can be maximized. 
     EXAMPLES 
     The invention will be illustrated in more detail by the following examples. In the following examples, LiCoO 2  will be abbreviated as “LCO”, and Li 4 Ti 5 O 12  will be abbreviated as “LTO”. 
     Examples A1 to A6 
     Hereinafter, Reference Examples demonstrating that batteries using an integrated sintered plate have more excellent performance than assembled batteries using no integrated sintered plate are shown. 
     Example A1 (Reference) 
     (1) Preparation of LCO Green Sheet (Positive Electrode Green Sheet) 
     First, Co 3 O 4  powder (manufactured by SEIDO CHEMICAL INDUSTRY CO., LTD.) and Li 2 CO 3  powder (manufactured by THE HONJO CHEMICAL CORPORATION) weighed to a molar ratio Li/Co of 1.01 were mixed, and thereafter the mixture was kept at 780° C. for 5 hours. The resultant powder was milled into a volume-based D50 of 0.4 μm with a pot mill to yield powder composed of platy LCO particles. The resultant LCO powder (100 parts by weight), a dispersive medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by SEKISUI CHEMICAL CO., LTD.) (10 parts by weight), a plasticizer (di-2-ethylhexyl phthalate (DOP), manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant mixture was defoamed by stirring under reduced pressure to prepare a LCO slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into a LCO green sheet onto a PET film by a doctor blade process. The thickness of the LCO green sheet was adjusted to 60 μm after firing. 
     (2) Preparation of LTO Green Sheet (Negative Electrode Green Sheet) 
     First, LTO powder (volume-based D50 particle size: 0.06 μm, manufactured by Sigma-Aldrich Japan) (100 parts by weight), a dispersive medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by SEKISUI CHEMICAL CO., LTD.) (20 parts by weight), a plasticizer (di-2-ethylhexyl phthalate (DOP), manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant negative electrode raw material mixture was defoamed by stirring under reduced pressure to prepare a LTO slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into a LTO green sheet onto a PET film by a doctor blade process. The thickness of the LTO green sheet was adjusted to 70 μm after firing. 
     (3) Preparation of MgO Green Sheet (Separator Green Sheet) 
     Magnesium carbonate powder (manufactured by Konoshima Chemical Co., Ltd.) was heated at 900° C. for 5 hours to obtain MgO powder. The resultant MgO powder and glass frit (CK0199, manufactured by Nippon Frit Co., Ltd. (currently, TAKARA STANDARD CO., LTD.)) were mixed at a weight ratio of 4:1. The resultant mixed powder (volume-based D50 particle size: 0.4 μm) (100 parts by weight), a dispersive medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by SEKISUI CHEMICAL CO., LTD.) (20 parts by weight), a plasticizer (di-2-ethylhexyl phthalate (DOP), manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant raw material mixture was defoamed by stirring under reduced pressure to prepare a slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into a separator green sheet onto a PET film by a doctor blade process. The thickness of the separator green sheet was adjusted to 25 μm after firing. 
     (4) Lamination, Pressure Bonding, and Firing 
     The LCO green sheet (positive electrode green sheet), the MgO green sheet (separator green sheet), and the LTO green sheet (negative electrode green sheet) were sequentially stacked, and the resultant laminate was pressed by CIP (cold isostatic pressing) at 200 kgf/cm 2  so that the green sheets were pressure-bonded together. The laminate thus pressure-bonded was punched into a circular plate with a diameter of 10 mm using a punching die. The resultant laminate in a form of circular plate was degreased at 600° C. for 5 hours, then heated to 800° C. at 1000° C./h, and kept for 10 minutes to fire, followed by cooling. Thus, one integrated sintered plate including three layers of a positive electrode layer (LCO sintered layer), a ceramic separator (MgO separator), and a negative electrode layer (LTO sintered layer) was obtained. 
     (5) Production of Lithium Secondary Battery 
     The coin-shaped lithium secondary battery  10  as schematically shown in  FIG. 1  was produced as follows. 
     (5a) Adhesion of Negative Electrode Layer and Negative Electrode Current Collector with Conductive Carbon Paste 
     Acetylene black and polyimide amide were weighed to a mass ratio of 3:1 and mixed with an appropriate amount of NMP (N-methyl-2-pyrrolidone) as a solvent, to prepare a conductive carbon paste as a conductive adhesive. The conductive carbon paste was screen-printed on an aluminum foil as a negative electrode current collector. The integrated sintered body produced in (4) above was disposed so that the negative electrode layer was located within an undried printing pattern (that is, a region coated with the conductive carbon paste), followed by vacuum drying at 60° C. for 30 minutes, to produce a structure with the negative electrode layer and the negative electrode current collector bonded via the negative side carbon layer. The negative side carbon layer had a thickness of 10 μm. 
     (5b) Preparation of Positive Electrode Current Collector with Carbon Layer 
     Acetylene black and polyimide amide were weighed to a mass ratio of 3:1 and mixed with an appropriate amount of NMP (N-methyl-2-pyrrolidone) as a solvent, to prepare a conductive carbon paste. The conductive carbon paste was screen-printed on an aluminum foil as a positive electrode current collector, followed by vacuum drying at 60° C. for 30 minutes, to produce a positive electrode current collector with a positive side carbon layer formed on a surface. The positive side carbon layer had a thickness of 5 μm. 
     (5c) Assembling of Coin-Shaped Battery 
     The positive electrode current collector, the positive side carbon layer, the integrated sintered plate (the LCO positive electrode layer, the MgO separator, and the LTO negative electrode layer), the negative side carbon layer, and the negative electrode current collector were accommodated between the positive electrode can and the negative electrode can, which would form a battery case, so as to be stacked in this order from the positive electrode can toward the negative electrode can, and an electrolytic solution was filled therein. Thereafter, the positive electrode can and the negative electrode can were crimped via a gasket to be sealed. Thus, the coin cell-shaped lithium secondary battery  10  with a diameter of 12 mm and a thickness of 1.0 mm was produced. At this time, the electrolytic solution was a solution of LiBF4 (1.5 mol/L) in a mixed organic solvent of ethylene carbonate (EC) and γ-butyrolactone (GBL) at 1:3 (volume ratio). 
     (6) Evaluation 
     The LCO sintered layer (positive electrode layer), the LTO sintered layer (negative electrode layer), and the MgO separator (ceramic separator) synthesized in Procedure (4) above and the coin-shaped lithium secondary battery manufactured in Procedure (5) were evaluated for various properties as shown below. 
     Average Orientation Angle of Primary Grains 
     The LCO sintered layer was polished with a cross-section polisher (CP) (IB-15000CP, manufactured by JEOL Ltd.), and the resultant cross section of the positive electrode layer (cross section perpendicular to the layer face of the positive electrode layer) was subjected to the EBSD measurement at a 1000-fold field of view (125 μm×125 μm) to give an EBSD image. This EBSD measurement was performed using a Schottky field emission scanning electron microscope (model JSM-7800F, manufactured by JEOL Ltd.). For all grains identified in the resultant EBSD image, the angles defined by the (003) planes of the primary grains and the layer face of the positive electrode layer (that is, the tilt of the crystal orientation from the (003) planes) is determined as a tilt angle. The mean value of the angles was determined as an average orientation angle of the primary grains. 
     Layer Thickness 
     The LCO and LTO sintered layers and the MgO separator were polished with a cross-section polisher (CP) (IB-15000CP, manufactured by JEOL Ltd.), and the resultant cross sections were observed with SEM (JSM6390LA, manufactured by JEOL Ltd.) to determine the thickness of the positive electrode layer, the negative electrode layer, and the separator. 
     Porosity 
     The LCO or LTO sintered layer and the MgO separator were polished with a cross-section polisher (CP) (IB-15000CP, manufactured by JEOL Ltd.), and the resultant cross section of the positive electrode layer or the negative electrode layer was observed with SEM (JSM6390LA, manufactured by JEOL Ltd.) at a 1000-fold field of view (125 μm×125 μm). The SEM image was subjected to an image analysis, the area of all pores was divided by the area of the positive electrode or the negative electrode, and the resultant value was multiplied by 100 to calculate the porosity (%). 
     Mean Pore Diameter 
     The mean pore diameter of the LCO or LTO sintered layer was measured by a mercury intrusion method using a mercury porosimeter (Autopore IV 9510, manufactured by Shimadzu Corporation). 
     Area Displacement Ratio Between Positive and Negative Electrodes 
     The area displacement ratio between the positive electrode layer and the negative electrode layer in the battery was calculated. Specifically, the area displacement ratio (%) between the positive and negative electrodes was calculated based on the formula: [(S p +S n )/S pn ]×100 by measuring the area S pn  of the region where the positive electrode layer and the negative electrode layer overlap each other, the area S p  of the region where the positive electrode layer protrudes from the negative electrode layer, and the area S n  of the region where the negative electrode layer protrudes from the positive electrode layer. The areas S pn , S p , and S n  were measured and calculated by determining the shape from both sides of each sample using a 3D shape measuring machine (VR3000, manufactured by KEYENCE CORPORATION). 
     Discharge Capacity/Theoretical Capacity Ratio 
     The discharge capacity of the battery was measured by the following procedures. That is, the battery was charged at a constant voltage of 2.7 V and then discharged at a discharge rate of 0.2 C to measure the initial capacity, and the resultant initial capacity was employed as a discharge capacity. Then, the discharge capacity was divided by the theoretical capacity and multiplied by 100, to obtain a discharge capacity/theoretical capacity ratio (%). 
     The theoretical capacity of the battery was calculated by the following procedures. First, the area of each layer of integrated sintered plate was calculated by the shape measurement, and the thickness and porosity of each layer of the integrated sintered plate were calculated from the cross-section SEM, to calculate the effective volumes of the positive electrode layer and the negative electrode layer from the values obtained. The true specific gravity of each constituent of the positive electrode layer and the negative electrode layer was calculated based on JIS standard R1634, and the weight values of the positive electrode layer and the negative electrode layer were calculated. The theoretical capacity value of each of the positive electrode layer and the negative electrode layer was calculated by multiplying the weight of each active material thus obtained by the capacity per weight of the material (described in the battery handbook), and the lower value was employed as the theoretical capacity value of the battery. 
     Pulse Cycle Capacity Retention Rate 
     The pulse cycle capacity retention rate (constant voltage charge cycle performance) of the battery was measured by the following procedures. First, the battery was charged at a constant voltage of 2.7 V and discharged at a discharge rate of 0.2 C to measure the initial capacity. Then, a total of 100 charge/discharge cycles including 100 times of charging at a constant voltage of 2.7 V and discharging at a current of 20 mA for 0.5 seconds were conducted. Finally, the battery was charged at a constant voltage of 2.7 V and discharged at 0.2 C, to measure the capacity after cycles. The capacity after cycles measured was divided by the initial capacity and multiplied by 100, to determine the pulse cycle capacity retention rate (%). 
     Example A2 (Reference) 
     An integrated sintered plate and a battery were prepared and evaluated for the various properties as in Example A1 except that 1) the thickness of the LCO green sheet was increased so that the thickness of the positive electrode layer was 100 μm, and 2) the thickness of the LTO green sheet was increased so that the thickness of the negative electrode layer was 120 μm. 
     Example A3 (Reference) 
     An integrated sintered plate and a battery were prepared and evaluated for the various properties as in Example A1 except that 1) the thickness of the LCO green sheet was increased so that the thickness of the positive electrode layer was 200 μm, and 2) the thickness of the LTO green sheet was increased so that the thickness of the negative electrode layer was 240 μm. 
     Example A4 (Reference) 
     An integrated sintered plate and a battery were prepared and evaluated for the various properties as in Example A1 except that 1) the thickness of the LCO green sheet was increased so that the thickness of the positive electrode layer was 400 μm, and 2) the thickness of the LTO green sheet was increased so that the thickness of the negative electrode layer was 480 μm. 
     Example A5 (Reference) 
     An integrated sintered plate and a battery were prepared and evaluated for the various properties as in Example A4 except that the mean pore diameter of the positive electrode layer was adjusted to 0.25 μm. 
     Example A6 (Reference) 
     (1) Production of Positive Electrode Plate 
     (1a) Preparation of LCO Green Sheet 
     First, Co 3 O 4  powder (manufactured by SEIDO CHEMICAL INDUSTRY CO., LTD.) and Li 2 CO 3  powder (manufactured by THE HONJO CHEMICAL CORPORATION) weighed to a molar ratio Li/Co of 1.01 were mixed, and thereafter the mixture was kept at 780° C. for 5 hours. The resultant powder was milled and crushed into a volume-based D50 of 0.4 μm with a pot mill to obtain powder composed of platy LCO particles. The resultant LCO powder (100 parts by weight), a dispersive medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by Sekisui Chemical Co., Ltd.) (10 parts by weight), a plasticizer (di-2-ethylhexyl phthalate (DOP), manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant mixture was defoamed by stirring under reduced pressure to prepare an LCO slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into an LCO green sheet onto a PET film by a doctor blade process. The dried thickness of the LCO green sheet was 220 μm. 
     (1b) Preparation of LCO Sintered Plate 
     The LCO green sheet was separated from the PET film, and was cut into a 50 mm square. The cut piece was placed on the center of a bottom magnesia setter (dimensions: 90 mm square, height: 1 mm). A porous magnesia setter as the top setter was placed on the LCO sheet. The LCO sheet disposed between the setters was placed into an alumina sheath of a 120 mm square (manufactured by Nikkato Co., Ltd.). At this time, the alumina sheath was not tightly sealed, and was covered with a lid with a gap of 0.5 mm. The stack obtained was heated to 600° C. at a heating rate of 200° C./h and degreased for 3 hours, then heated to 820° C. at 200° C./h, and held for 20 hours for firing. After the firing, the fired laminate was cooled to room temperature, and was removed from the alumina sheath. Thus, the LCO sintered plate with a thickness of 200 μm was yielded as a positive electrode plate. The positive electrode plate obtained was cut into a circular shape with a diameter of 10 mm using a laser processing machine, to obtain a positive electrode plate. 
     (2) Production of Negative Electrode Plate 
     (2a) Preparation of LTO Green Sheet 
     First, LTO powder (volume-based D50 particle size 0.06 μm, manufactured by Sigma-Aldrich Japan) (100 parts by weight), a dispersion medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by SEKISUI CHEMICAL CO., LTD.) (20 parts by weight), a plasticizer (DOP: Di(2-ethylhexyl)phthalate, manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant negative electrode raw material mixture was defoamed by stirring under reduced pressure to prepare a LTO slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into a LTO green sheet onto a PET film by a doctor blade process. The thickness of the LTO green sheet after drying and firing was adjusted to 240 μm. 
     (2b) Firing of LTO Green Sheet 
     The green sheet obtained was cut out into a 25-mm square with a cutter knife and disposed on an embossed zirconia setter. The green sheet on the setter was put into an alumina sheath and kept at 500° C. for 5 hours. Thereafter, the temperature was raised at a heating rate of 200° C./h, to perform firing at 765° C. for 5 hours. The LTO sintered plate obtained was cut into a circular shape with a diameter of 10.5 mm using a laser processing machine, to obtain a negative electrode plate. 
     (3) Production of Coin-Shaped Lithium Secondary Battery 
     The coin-shaped lithium secondary battery  10  as schematically shown in  FIG. 1  was produced as follows. 
     (3a) Adhesion of Negative Electrode Plate and Negative Electrode Current Collector with Conductive Carbon Paste 
     Acetylene black and polyimide amide were weighed to a mass ratio of 3:1 and mixed with an appropriate amount of NMP (N-methyl-2-pyrrolidone) as a solvent, to prepare a conductive carbon paste. The conductive carbon paste was screen-printed on an aluminum foil as a negative electrode current collector. The negative electrode plate produced in (2) above was disposed within an undried printing pattern (that is, a region coated with the conductive carbon paste), followed by vacuum drying at 60° C. for 30 minutes, to produce a negative electrode structure with the negative electrode plate and the negative electrode current collector bonded via a negative side carbon layer. The negative side carbon layer had a thickness of 10 μm. 
     (3b) Preparation of Positive Electrode Current Collector with Carbon Layer 
     Acetylene black and polyimide amide were weighed to a mass ratio of 3:1 and mixed with an appropriate amount of NMP (N-methyl-2-pyrrolidone) as a solvent, to prepare a conductive carbon paste. The conductive carbon paste was screen-printed on an aluminum foil as a positive electrode current collector, followed by vacuum drying at 60° C. for 30 minutes, to produce a positive electrode current collector with a positive side carbon layer formed on a surface. The positive side carbon layer had a thickness of 5 μm. 
     (3c) Assembling of Coin-Shaped Battery 
     The positive electrode current collector, the carbon layer, the LCO positive electrode plate, a cellulose separator, the LTO negative electrode plate, the carbon layer, and the negative electrode current collector were accommodated between the positive electrode can and the negative electrode can, which would form a battery case, so as to be stacked in this order from the positive electrode can toward the negative electrode can, and an electrolytic solution was filled therein. Thereafter, the positive electrode can and the negative electrode can were crimped via a gasket to be sealed. Thus, the coin cell-shaped lithium secondary battery  10  with a diameter of 12 mm and a thickness of 1.0 mm was produced. At this time, the electrolytic solution was a solution of LiBF 4  (1.5 mol/L) in a mixed organic solvent of ethylene carbonate (EC) and γ-butyrolactone (GBL) at 1:3. 
     (4) Evaluation 
     The LCO sintered plate (positive electrode plate) prepared in Procedure (1b), the LTO sintered plate (negative electrode plate) prepared in Procedure (2b), and the coin-shaped lithium secondary battery manufactured in Procedure (3) were evaluated for various properties as in Example A1. 
     Evaluation Results 
     Tables 1 and 2 show the evaluation results for Examples A1 to A6. 
     
       
         
           
               
               
               
               
               
             
               
                 TABLE 1 
               
             
            
               
                   
               
               
                   
                 Configuration 
                   
                   
                   
               
               
                   
                 of positive 
                 Positive electrode layer 
                   
                 Separator 
               
            
           
           
               
               
               
               
               
               
               
               
               
               
               
            
               
                   
                 electrode/ 
                   
                   
                   
                   
                 Mean 
                   
                 Mean 
                   
                   
               
               
                   
                 separator/ 
                   
                 Average 
                   
                   
                 pore 
                 Negative electrode layer 
                 pore 
                   
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
               
               
               
               
            
               
                   
                 negative 
                   
                 orientation 
                 Thickness 
                 Porosity 
                 diameter 
                   
                 Thickness 
                 Porosity 
                 diameter 
                   
                 Thickness 
               
               
                   
                 electrode 
                 Type 
                 angle 
                 (μm) 
                 (%) 
                 (μm) 
                 Type 
                 (μm) 
                 (%) 
                 (μm) 
                 Type 
                 (μm) 
               
               
                   
               
            
           
           
               
               
               
               
               
               
               
               
               
               
               
               
               
            
               
                 Example 
                 Integrated 
                 LCO 
                 16° 
                 60 
                 45 
                 0.8 
                 LTO 
                 70 
                 50 
                 0.2 
                 MgO 
                 25 
               
               
                 A1* 
                 sintered 
                 sintered 
                   
                   
                   
                   
                 sintered 
                   
                   
                   
                   
                   
               
               
                   
                 plate 
                 body 
                   
                   
                   
                   
                 body 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated 
                 LCO 
                 16° 
                 100 
                 45 
                 0.8 
                 LTO 
                 120 
                 50 
                 0.2 
                 MgO 
                 25 
               
               
                 A2* 
                 sintered 
                 sintered 
                   
                   
                   
                   
                 sintered 
                   
                   
                   
                   
                   
               
               
                   
                 plate 
                 body 
                   
                   
                   
                   
                 body 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated 
                 LCO 
                 16° 
                 200 
                 45 
                 0.8 
                 LTO 
                 240 
                 50 
                 0.2 
                 MgO 
                 25 
               
               
                 A3* 
                 sintered 
                 sintered 
                   
                   
                   
                   
                 sintered 
                   
                   
                   
                   
                   
               
               
                   
                 plate 
                 body 
                   
                   
                   
                   
                 body 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated 
                 LCO 
                 16° 
                 400 
                 45 
                 0.8 
                 LTO 
                 480 
                 50 
                 0.2 
                 MgO 
                 25 
               
               
                 A4* 
                 sintered 
                 sintered 
                   
                   
                   
                   
                 sintered 
                   
                   
                   
                   
                   
               
               
                   
                 plate 
                 body 
                   
                   
                   
                   
                 body 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated 
                 LCO 
                 16° 
                 400 
                 45 
                 0.25 
                 LTO 
                 480 
                 50 
                 0.2 
                 MgO 
                 25 
               
               
                 A5* 
                 sintered 
                 sintered 
                   
                   
                   
                   
                 sintered 
                   
                   
                   
                   
                   
               
               
                   
                 plate 
                 body 
                   
                   
                   
                   
                 body 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Assembled 
                 LCO 
                 Random 
                 200 
                 38 
                 0.8 
                 LTO 
                 240 
                 38 
                 0.2 
                 Cellulose 
                 25 
               
               
                 A6* 
                   
                 sintered 
                   
                   
                   
                   
                 sintered 
                   
                   
                   
                   
                   
               
               
                   
                   
                 body 
                   
                   
                   
                   
                 body 
               
               
                   
               
               
                 Symbol * represents a reference example. 
               
               
                 *LCO represents LiCoO 2 , and LTO represents Li 4 Ti 5 O 12 . 
               
            
           
         
       
     
     
       
         
           
               
               
               
             
               
                   
                 TABLE 2 
               
             
            
               
                   
                   
               
               
                   
                   
                 Properties 
               
            
           
           
               
               
               
               
               
            
               
                   
                   
                 Area displacement  
                 Discharge  
                 Pulse cycle  
               
               
                   
                   
                 ratio between  
                 capacity/ 
                 capacity 
               
               
                   
                   
                 positive and 
                 theoretical  
                 retention 
               
               
                   
                   
                 negative  
                 capacity 
                 rate 
               
               
                   
                   
                 electrodes (%) 
                 ratio (%) 
                 (%) 
               
               
                   
                   
               
            
           
           
               
               
               
               
               
            
               
                   
                 Example A1* 
                 0 
                 100 
                 99 
               
               
                   
                 Example A2* 
                 0 
                 100 
                 99 
               
               
                   
                 Example A3* 
                 0 
                 100 
                 98 
               
               
                   
                 Example A4* 
                 0 
                 100 
                 96 
               
               
                   
                 Example A5* 
                 0 
                 100 
                 96 
               
               
                   
                 Example A6* 
                 5 
                 97 
                 94 
               
               
                   
                   
               
               
                   
                 Symbol * represents a reference example. 
               
            
           
         
       
     
     Examples B1 to B7 
     Hereinafter, specific examples of the lithium secondary battery according to the present invention and the battery of a comparative aspect are shown. 
     Example B1 
     (1) Production of Positive Electrode Plate 
     Co 3 O 4  powder (manufactured by SEIDO CHEMICAL INDUSTRY CO., LTD.) weighed to a molar ratio Li/Co of 1.02 and Li 2 CO 3  powder (manufactured by THE HONJO CHEMICAL CORPORATION) were mixed and kept at 750° C. for 5 hours. The resultant powder was milled with a pot mill to a volume-based D50 of 0.4 μm, to obtain LiCoO 2  powder. The resultant LiCoO 2  powder (100 parts by weight), a dispersive medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by SEKISUI CHEMICAL CO., LTD.) (10 parts by weight), a plasticizer (di-2-ethylhexyl phthalate (DOP), manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant mixture was defoamed by stirring under reduced pressure to prepare an LiCoO 2  slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into an LiCoO 2  green sheet onto a PET film by a doctor blade process. The dried thickness of the LiCoO 2  green sheet was 80 μm. The green sheet obtained was cut out into a 25-mm square with a cutter knife and disposed on a magnesia setter. The green sheet on the setter was put into an alumina sheath and kept at 500° C. for 5 hours. Thereafter, the temperature was raised at a heating rate of 200° C./h, to perform firing at 800° C. for 5 hours. An Au film (thickness: 100 nm) as a current collecting layer was formed by sputtering on the surface of the resultant LCO sintered plate in contact with the setter and then laser-processed into a circular shape with a diameter of 17 mm. 
     (2) Production of Negative Electrode Plate 
     The LTO powder (volume-based D50 particle size: 0.6 μm, manufactured by ISHIHARA SANGYO KAISHA, LTD.) (100 parts by weight), a dispersive medium (toluene:isopropanol=1:1) (100 parts by weight), a binder (polyvinyl butyral: Product No. BM-2, manufactured by SEKISUI CHEMICAL CO., LTD.) (20 parts by weight), a plasticizer (di-2-ethylhexyl phthalate (DOP), manufactured by Kurogane Kasei Co., Ltd.) (4 parts by weight), and a dispersant (product name: RHEODOL SP-O30, manufactured by Kao Corporation) (2 parts by weight) were mixed. The resultant negative electrode raw material mixture was defoamed by stirring under reduced pressure to prepare a LTO slurry with a viscosity of 4000 cP. The viscosity was measured with an LVT viscometer manufactured by Brookfield. The slurry prepared was formed into a LTO green sheet onto a PET film by a doctor blade process. The thickness of the LTO green sheet after drying and firing was adjusted to 70 μm. The green sheet obtained was cut out into a 25-mm square with a cutter knife and disposed on a magnesia setter. The green sheet on the setter was put into an alumina sheath and kept at 500° C. for 5 hours. Thereafter, the temperature was raised at a heating rate of 200° C./h, to perform firing at 800° C. for 5 hours. An Au film (thickness: 100 nm) as a current collecting layer was formed by sputtering on the surface of the resultant LTO sintered plate in contact with the setter and then laser-processed into a circular shape with a diameter of 17 mm. 
     (3) Production and Evaluation of Battery 
     Using the positive electrode plate and the negative electrode plate obtained as a positive electrode layer and a negative electrode layer, a battery was produced with the same configuration as in Example A6. For the battery obtained, the capacity ratio was calculated, and the resistance ratio was measured, according to the procedures shown below. The results were as shown in Table 3. 
     Capacity Ratio 
     The actual electric capacity (mAh) of the positive electrode layer at 25° C. per 1 cm 2  of the area of the positive electrode layer  12  was determined as the capacity C of the positive electrode layer (LCO sintered layer)  12 . The actual electric capacity was an electric capacity when charging at a constant current and a constant voltage with a current of 0.2 C and a potential of 4.25 V for lithium metals was performed for 10 hours, and then discharging at a constant current with a current of 0.2 C was performed until the potential for lithium metals reached 3.0 V. Meanwhile, the actual electric capacity (mAh) of the negative electrode layer 16 at 25° C. per 1 cm 2  of the area of the negative electrode layer  16  was determined as capacity A of the negative electrode layer (LTO sintered layer)  16 . The actual electric capacity was an electric capacity when charging at a constant current and a constant voltage with a current of 0.2 C and a potential of 0.8 V for lithium metals was performed for 10 hours, and then discharging at a constant current with a current of 0.2 C was performed until the potential for lithium metals reached 2.0 V. Finally, the ratio of the capacity C of the positive electrode layer  12  with respect to the capacity A of the negative electrode layer  16  was calculated as the C/A ratio. 
     Resistance Ratio 
     i) Measurement of SOC 
     The battery obtained was charged and discharged at 0.05 C, and the capacity of the battery obtained was taken as a theoretical capacity. The states in which 10%, 50%, and 80% of the capacity were charged were respectively defined as SOC 10%, SOC 50%, and SOC 80%. 
     ii) Resistivity measurement 
     The battery was Charged and discharged so as to be in the SOC states of SOC 10%, SOC 50%, and SOC 80%, and the resistance of 1 Hz of the battery obtained in each state was measured by the AC impedance method and taken as R10, R50, and R80, respectively. The R50/R10 was calculated by dividing R50 by R10, the R80/R50 was calculated by dividing R80 by R50, and the R80/R10 was calculated by dividing R80 by R10, respectively. 
     The resistance value at each SOC measured in Example B1 was as shown in  FIG. 5 . 
     Example B2 
     A battery was produced and evaluated in the same manner as in Example B1 except that the thickness of the negative electrode was changed to 90 μm. 
     Example B3 
     A battery was produced and evaluated in the same manner as in Example B1 except that the thickness of the positive electrode layer was changed to 200 μm, and the thickness of the negative electrode was changed to 240 μm. 
     Example B4 
     A battery was produced in the same manner as in Example A3 except that the electrode size was changed to a diameter of 17 mm. The battery produced was evaluated in the same manner as in Example B1. 
     Example B5 
     A battery was produced and evaluated in the same manner as in Example B4 except that the thickness of the positive electrode layer was changed to 420 μm, and the thickness of the negative electrode layer was changed to 500 μm. 
     Example B6 
     A battery was produced and evaluated in the same manner as in Example B4 except that the thickness of the positive electrode layer was changed to 600 μm, and the thickness of the negative electrode layer was changed to 500 μm. 
     Example B7 (Comparison) 
     A battery was produced and evaluated in the same manner as in Example B4 except that a commercially available LCO coated electrode (manufactured by Hachiyama Co., Ltd.) was used as a positive electrode layer instead of the LCO sintered plate, and a commercially available LTO coated electrode (manufactured by Hachiyama Co., Ltd.) was used as a negative electrode layer instead of the LTO sintered plate. These coated electrodes were prepared by applying a paste containing an electrode active material, followed by drying, and were not sintered plates. 
     
       
         
           
               
               
               
               
               
             
               
                 TABLE 3 
               
             
            
               
                   
               
               
                   
                 Configuration of positive 
                 Thickness of 
                   
                   
               
               
                   
                 electrode/separator/ 
                 negative electrode 
                   
                 Resistance ratio 
               
            
           
           
               
               
               
               
               
               
               
            
               
                   
                 negative electrode 
                 layer (μm) 
                 C/A 
                 R 50 /R 10   
                 R 80 /R 50   
                 R 80 /R 10   
               
               
                   
               
            
           
           
               
               
               
               
               
               
               
            
               
                 Example 
                 Assembled 
                 70 
                 0.95 
                 0.81 
                 0.82 
                 0.66 
               
               
                 B1 
                 (Sintered plate electrode) 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Assembled 
                 90 
                 1.2 
                 0.77 
                 0.78 
                 0.60 
               
               
                 B2 
                 (Sintered plate electrode) 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Assembled 
                 240 
                 1.2 
                 0.72 
                 0.74 
                 0.53 
               
               
                 B3 
                 (Sintered plate electrode) 
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated sintered plate 
                 240 
                 1.2 
                 0.69 
                 0.69 
                 0.48 
               
               
                 B4 
                   
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated sintered plate 
                 500 
                 1.2 
                 0.56 
                 0.63 
                 0.35 
               
               
                 B5 
                   
                   
                   
                   
                   
                   
               
               
                 Example 
                 Integrated sintered plate 
                 500 
                 1.5 
                 0.55 
                 0.62 
                 0.34 
               
               
                 B6 
                   
                   
                   
                   
                   
                   
               
               
                 Example 
                 Coated electrode 
                 500 
                 1.2 
                 0.94 
                 0.94 
                 0.88 
               
               
                 B7* 
               
               
                   
               
               
                 Symbol * represents a comparative example.