Patent Application
20120058393
1. Field of the Invention
The present invention relates to a battery and an energy system.
2. Description of the Background Art
Leveling in electric power demands that vary between day and night or vary depending on the season (load leveling) has recently been desired and a sodium-sulfur battery has increasingly been used as electric energy charge and discharge means.
For example, according to Japanese Patent Laying-Open No. 2007-273297, a sodium-sulfur battery is a secondary battery in which molten sodium metal representing a negative-electrode active material and molten sulfur representing a positive-electrode active material are separated from each other by a β-alumina solid electrolyte having selective permeability with respect to sodium ions, and it has such excellent characteristics as having energy density higher than other secondary batteries, realizing compact facilities, hardly likely to cause self-discharge, and achieving high battery efficiency and facilitated maintenance (see paragraph [0002] of Japanese Patent Laying-Open No. 2007-273297).
In addition, according to Japanese Patent Laying-Open No. 2007-273297, cells (electric cells) of the sodium-sulfur batteries are connected in series to form a string, such strings are connected in parallel to form a module, and such modules are connected in series to form a module row. Arrangement of such modules rows in parallel as a whole is used as a main component of an electric power storage system connected to an electric power system or the like with an AC/DC converter and a transformer (see paragraph [0003] of Japanese Patent Laying-Open No. 2007-273297).
The sodium-sulfur battery, however, should normally be operated at a high temperature from 280 to 360° C. (see paragraph [0004] of Japanese Patent Laying-Open No. 2007-273297).
Therefore, as described above, if arrangement of the sodium-sulfur battery module rows in parallel as a whole is used as the main component of the electric power storage system of a large-scale energy system, it takes several days to increase a temperature of the sodium-sulfur battery to the high operating temperature above and hence it takes an immense time until the electric power storage system is driven.
Meanwhile, a lithium ion secondary battery is also famous as a secondary battery high in energy density and low in operating temperature. As well known, however, the lithium ion secondary battery contains a liquid of a combustible organic compound as an electrolytic solution and hence it is low in safety and there is a problem also of lithium resources.
In view of the circumstances above, an object of the present invention is to provide a battery achieving high safety and high energy density, operable at a low temperature, and containing sodium abundant in resources, as well as an energy system including the battery.
The present invention is directed to a battery including a positive electrode, a negative electrode mainly composed of sodium, and an electrolyte provided between the positive electrode and the negative electrode, the electrolyte is molten salt containing anions expressed with chemical formula (I) below and cations of metal,
R1 and R2 in the chemical formula (I) independently represent fluorine atom or fluoroalkyl group, and the cations of metal contain at least one of at least one type of cations of alkali metal and at least one type of cations of alkaline-earth metal.
Here, in the battery according to the present invention, preferably, the positive electrode contains a metal or a metal compound expressed with chemical formula (II) below,
NaxM1yM2zM3w (II)
in the chemical formula (II), M1 represents any one type of Fe (iron), Ti (titanium), Cr (chromium), and Mn (manganese), M2 represents any one of PO4 (phosphorous tetroxide) and S (sulfur), M3 represents any one of F (fluorine) and O (oxygen), a composition ratio x of Na (sodium) is a real number satisfying relation of 0≦x≦2, a composition ratio y of M1 is a real number satisfying relation of 0≦y≦1, a composition ratio z of M2 is a real number satisfying relation of 0≦z≦2, a composition ratio w of M3 is a real number satisfying relation of 0≦w≦3, and relation of x+y>0 and relation of z+w>0 are satisfied.
In addition, in the battery according to the present invention, the positive electrode preferably further contains a conductive additive.
In addition, in the battery according to the present invention, the positive electrode preferably further contains a binder.
In addition, in the battery according to the present invention, the cations of metal are preferably potassium ions and/or sodium ions.
In addition, the present invention is directed to an energy system including an electric energy generation apparatus for generating electric energy, a secondary battery capable of being charged with the electric energy generated by the electric energy generation apparatus and capable of discharging the charged electric energy, and a line for electrically connecting the electric energy generation apparatus and the secondary battery to each other, the secondary battery includes a positive electrode, a negative electrode mainly composed of sodium, and an electrolyte provided between the positive electrode and the negative electrode, the electrolyte is molten salt containing anions expressed with chemical formula (I) below and cations of metal,
R1 and R2 in the chemical formula (I) independently represent fluorine atom or fluoroalkyl group, and the cations of metal contain at least one of at least one type of cations of alkali metal and at least one type of cations of alkaline-earth metal.
According to the present invention, a battery achieving high safety and high energy density, operable at a low temperature, and containing sodium abundant in resources, as well as an energy system including the battery can be provided.
The foregoing and other objects, features, aspects and advantages of the present invention will become more apparent from the following detailed description of the present invention when taken in conjunction with the accompanying drawings.
An embodiment of the present invention will be described hereinafter. In the drawings of the present invention, the same or corresponding elements have the same reference characters allotted.
<Battery>
While lower pan 2b is covered with upper lid 2a, for example, upper lid 2a and lower pan 2b are fixed by a fixing member (not shown) such as a bolt and a nut.
In addition, an electrically insulating sealing material 9a such as an O-ring is provided around a peripheral portion of upper lid 2a, and an electrically insulating sealing material 9b such as an O-ring is also provided around a peripheral portion of lower pan 2b. Thus, a space between upper lid 2a and lower pan 2b is hermetically sealed and upper lid 2a and lower pan 2b are electrically isolated from each other.
It is noted that a current collector electrically connected to upper lid 2a may be provided in an upper portion of upper lid 2a, and a current collector electrically connected to lower pan 2b may be provided in a lower portion of lower pan 2b.
Here, separator 8 is immersed in an electrolyte composed of molten salt containing anions expressed in the chemical formula (I) below and cations of metal, and the electrolyte composed of the molten salt is in contact with both of negative electrode 3 and positive electrode 4.
Here, in the chemical formula (I) above, R1 and R2 independently represent fluorine atom or fluoroalkyl group. R1 and R2 may represent the same substance or may represent different substances respectively.
Examples of anions expressed in chemical formula (I) above include such anions that R1 and R2 in chemical formula (I) above both represent fluorine atoms (F), such anions that R1 and R2 both represent trifluoromethyl groups (CF3), and such anions that R1 represents fluorine atom (F) and R2 represents trifluoromethyl group (CF3).
Examples of the molten salt contained in the electrolyte include molten salt containing anions expressed with the chemical formula (I) above and at least one of at least one type of cations of alkali metal and at least one type of cations of alkaline-earth metal.
The present inventors have found as a result of dedicated studies that the molten salt above has a low melting point and use of such molten salt for an electrolyte for the battery can lead to significant lowering in an operating temperature of the battery as compared with 280 to 360° C. of a sodium-sulfur battery.
In addition, if the molten salt above is used for the electrolyte for the battery, owing to incombustibility of the molten salt, a battery achieving high safety and high energy density can be obtained.
Here, from a point of view of operating battery 1 at a lower temperature, such anions expressed in the chemical formula (I) above that R1 and R2 both represent F, that is, bis(fluorosulfonyl)imide ions (FSI−; hereinafter may also be referred to as “FSI ions”), and/or R1 and R2 both represent CF3, that is, bis(trifluoromethylsulfonyl)imide ions (TFSI−; hereinafter may also be referred to as “TFSI ions”), are preferably used.
Therefore, from a point of view of operating battery 1 at a lower temperature, as the molten salt to be used for the electrolyte, simple salt of molten salt MFSI, simple salt of molten salt MTFSI, a mixture of two or more types of simple salt of molten salt MFSI, a mixture of two or more types of simple salt of molten salt MTFSI, or a mixture of one or more type of simple salt of molten salt MFSI and one or more type of simple salt of molten salt MTFSI, that contains FSI ions and/or TFSI ions as anions and contains ions of M representing any one type of alkali metal and alkaline-earth metal as cations is preferably used.
In particular, since the mixture of simple salt of molten salt MFSI, the mixture of simple salt of molten salt MTFSI, and the mixture of one or more type of simple salt of molten salt MFSI and one or more type of simple salt of molten salt MTFSI are composed of two or more types of simple salt of the molten salt, they are further preferred in that a melting point can remarkably be lower than the melting point of the simple salt of the molten salt and hence an operating temperature of battery 1 can remarkably be lowered.
Strictly speaking, it is inappropriate to refer to FSI ions and TFSI ions without imino group as imide, however, they have already widely been referred to as such these days and hence such names are also used herein as trivial names.
Meanwhile, at least one type selected from the group consisting of lithium (Li), sodium (Na), potassium (K), rubidium (Rb), and cesium (Cs) may be used as the alkali metal.
In addition, at least one type selected from the group consisting of beryllium (Be), Mg (magnesium), calcium (Ca), strontium (Sr), and barium (Ba) may be used as the alkaline-earth metal.
Therefore, any one type of simple salt selected from the group consisting of LiFSI, NaFSI, KFSI, RbFSI, CsFSI, Be(FSI)2, Mg(FSI)2, Ca(FSI)2, Sr(FSI)2, and Ba(FSI)2 may be used as the simple salt of molten salt MFSI.
In addition, any one type of simple salt selected from the group consisting of LiTFSI, NaTFSI, KTFSI, RbTFSI, CsTFSI, Be(TFSI)2, Mg(TFSI)2, Ca(TFSI)2, Sr(TFSI)2, and Ba(TFSI)2 may be used as the simple salt of molten salt MTFSI.
Moreover, a mixture of two or more types of simple salt selected from the group consisting of LiFSI, NaFSI, KFSI, RbFSI, CsFSI, Be(FSI)2, Mg(FSI)2, Ca(FSI)2, Sr(FSI)2, and Ba(FSI)2 may be used as the mixture of the simple salt of molten salt MFSI.
Further, a mixture of two or more types of simple salt selected from the group consisting of LiTFSI, NaTFSI, KTFSI, RbTFSI, CsTFSI, Be(TFSI)2, Mg(TFSI)2, Ca(TFSI)2, Sr(TFSI)2, and Ba(TFSI)2 may be used as the mixture of the simple salt of molten salt MTFSI.
Furthermore, a mixture of one or more type of simple salt selected from the group consisting of LiFSI, NaFSI, KFSI, RbFSI, CsFSI, Be(FSI)2, Mg(FSI)2, Ca(FSI)2, Sr(FSI)2, and Ba(FSI)2 and one or more type of simple salt selected from the group consisting of LiTFSI, NaTFSI, KTFSI, RbTFSI, CsTFSI, Be(TFSI)2, Mg(TFSI)2, Ca(TFSI)2, Sr(TFSI)2, and Ba(TFSI)2 may be used as the mixture of one or more type of the simple salt of molten salt MFSI and one or more type of the simple salt of molten salt MTFSI.
Among others, from a point of view of lowering in an operating temperature of the battery, binary-system molten salt composed of a mixture of NaFSI and KFSI (hereinafter referred to as “NaFSI—KFSI molten salt”) or binary-system molten salt composed of a mixture of NaFSI and NaTFSI (hereinafter referred to as “NaFSI—NaTFSI molten salt”) is preferably used for the electrolyte.
In particular, a mole ratio between Na cations and K cations ((the number of moles of K cations)/(the number of moles of Na cations+the number of moles of K cations)) in the NaFSI—KFSI molten salt is preferably not smaller than 0.4 and not larger than 0.7, and more preferably not smaller than 0.5 and not larger than 0.6. When the mole ratio between Na cations and K cations ((the number of moles of K cations)/(the number of moles of Na cations+the number of moles of K cations)) in the NaFSI—KFSI molten salt is not smaller than 0.4 and not larger than 0.7, in particular not smaller than 0.5 and not larger than 0.6, it is likely that the operating temperature of the battery can be as low as 90° C. or less.
When molten salt composed of the mixture of the simple salt of the molten salt above is used for the electrolyte of the battery, from a point of view of a lower operating temperature of the battery, the molten salt preferably has a composition close to such a composition that two or more types of molten salt exhibit eutectic (eutectic composition), and the molten salt most preferably has a eutectic composition.
In addition, organic cations may be contained in the electrolyte composed of the molten salt above. In this case, it is likely that the electrolyte can have high conductivity and the operating temperature of the battery can be low.
Here, for example, alkyl imidazole-type cations such as 1-ethyl-3-methylimidazolium cations, alkyl pyrrolidinium-type cations such as N-ethyl-N-methylpyrrolidinium cations, alkylpyridinium-type cations such as 1-methyl-pyridinium cations, quaternary ammonium-type cations such as trimethylhexyl ammonium cations, and the like can be used as the organic cations.
In addition, as shown in
Here, for example, a metal or a metal compound allowing intercalation of M of the molten salt serving as the electrolyte can be used as metal or metal compound 5, and among others, a metal or a metal compound expressed with the chemical formula (II) below is preferably contained. In this case, a battery achieving excellent charge and discharge cycle characteristics and high energy density can be obtained.
NaxM1yM2zM3w (II)
In the chemical formula (II) above, M1 represents any one type of Fe, Ti, Cr, and Mn, M2 represents any one of PO4 and S, and M3 represents any one of F and O.
In the chemical formula (II) above, a composition ratio x of Na is a real number satisfying relation of 0≦x≦2, a composition ratio y of M1 is a real number satisfying relation of 0≦y≦1, a composition ratio z of M2 is a real number satisfying relation of 0≦z≦2, a composition ratio w of M3 is a real number satisfying relation of 0≦w≦3, and relation of x+y>0 and relation of z+w>0 are satisfied.
For example, at least one type selected from the group consisting of NaCrO2, TiS2, NaMnF3, Na2FePO4F, NaVPO4F, and Na0.44MnO2 is preferably used as the metal compound expressed with the chemical formula (II) above.
Among others, NaCrO2 is preferably used as the metal compound expressed with the chemical formula (II) above. When NaCrO2 is used as metal compound 5, it is likely that battery 1 achieving excellent charge and discharge cycle characteristics and high energy density can be obtained.
Meanwhile, an additive made of a conductive material can be used as conductive additive 6 without particularly limited, however, conductive acetylene black is preferably used among others. When conductive acetylene black is used as conductive additive 6, it is likely that battery 1 achieving excellent charge and discharge cycle characteristics and high energy density can be obtained.
In addition, the content of conductive additive 6 in positive electrode 4 is preferably not higher than 40 mass % of positive electrode 4, and more preferably not lower than 5 mass % and not higher than 20 mass %. When the content of conductive additive 6 in positive electrode 4 is not higher than 40 mass %, in particular not lower than 5 mass % and not higher than 20 mass %, it is more likely that battery 1 achieving excellent charge and discharge cycle characteristics and high energy density can be obtained. It is noted that conductive additive 6 does not necessarily have to be contained in positive electrode 4 if positive electrode 4 has conductivity.
Meanwhile, any binder capable of securely adhering metal or metal compound 5 and conductive additive 6 to each other can be used as binder 7 without particularly limited, however, polytetrafluoroethylene (PTFE) is preferably used among others. When polytetrafluoroethylene (PTFE) is used as binder 7, it is likely that metal compound 5 composed of NaCrO2 and conductive additive 6 composed of acetylene black can more firmly be adhered to each other.
The content of binder 7 in positive electrode 4 is preferably not higher than 40 mass % of positive electrode 4, and more preferably not lower than 1 mass % and not higher than 10 mass %. When the content of binder 7 in positive electrode 4 is not higher than 40 mass %, in particular not lower than 1 mass % and not higher than 10 mass %, it is further likely that metal or metal compound 5 and conductive additive 6 can more firmly be adhered to each other while conductivity of positive electrode 4 is suitable. It is noted that binder 7 does not necessarily have to be contained in positive electrode 4.
Battery structured as above can be used as a secondary battery capable of being charged and discharging through electrode reaction as shown in formulae (III) and (IV) below.
Negative electrode 3: Na→←Na++e− (the right direction indicates discharge reaction and the left direction indicates charge reaction) (III)
Positive electrode 4: NaCrO2→←xNa++xe−+Na1-xCrO2 (the right direction indicates charge reaction and the left direction indicates discharge reaction) (IV)
Alternatively, battery 1 can also be used as a primary battery.
Battery 1 serving as an electric cell has been described above, however, a plurality of batteries 1 that are electric cells may electrically be connected in series, to thereby form a string, and a plurality of such strings may electrically be connected in parallel, to thereby form a module.
An electric cell of battery 1 structured as above as well as a string and a module of the electric cells can suitably be used, for example, as an electric energy charge and discharge apparatus in an energy system as will be described later.
<Energy System>
Here, secondary batteries 100a, 100b, 100c, 100d, and 100e constituted of electric cells of batteries 1 above or strings or modules obtained by electrically connecting a plurality of the electric cells are each used as a charge and discharge apparatus of electric energy generated in an energy system according to the embodiment structured as shown in
For example, electric energy generated in wind-power generation in a wind farm 10, which is a large-scale wind plant, is sent from wind farm 10 through a line 21 to secondary battery 100a, which is charged as it receives the electric energy.
Then, the electric energy charged in secondary battery 100a is discharged from secondary battery 100a and sent through a line 22 to a power line 11. Thereafter, the electric energy is sent from power line 11 through a line 23 to a substation 12, which sends the electric energy through a line 24 to secondary battery 100b. Secondary battery 100b is charged as it receives the electric energy sent from substation 12 through line 24.
Meanwhile, electric energy generated in photovoltaic power generation by a solar battery module 18 provided in a plant is sent through a line 29 to secondary battery 100e, which is charged as it receives the electric energy.
Meanwhile, electric energy generated by using a fuel gas, ammonia, VOC (a volatile organic compound), or the like in a gas power plant 20 provided in the plant and electric energy generated in fuel cell facilities 19 provided outside the plant are sent through respective lines 26 and 27 to secondary battery 100e, which is charged as it receives the electric energy.
Then, the electric energy charged in secondary battery 100e is discharged from secondary battery 100e through a line 28 and used as electric power 17 for operating the plant.
Meanwhile, electric energy charged in secondary battery 100b is discharged from secondary battery 100b through a line 25 and used as electric power 17 for operating the plant or sent through line 25 to secondary battery 100c, which is charged therewith.
Meanwhile, electric energy generated in photovoltaic power generation by mega solar facilities 13, which are large-scale photovoltaic power generation facilities, is sent through line 25 and used as electric power 17 for operating the plant or sent through line 25 to secondary battery 100c, which is charged therewith.
Meanwhile, electric energy charged in secondary battery 100c is discharged from secondary battery 100c through a line 30 to a power station 14, which is charged therewith. The electric energy charged in power station 14 is sent through a line 31 to a car 15 such as a hybrid car or an electric car and used as electric power for driving car 15.
Meanwhile, the electric energy charged in secondary battery 100c is discharged from secondary battery 100c and sent through a line 32 to secondary battery 100d within car 15, and secondary battery 100d is charged therewith. Then, the electric energy charged in secondary battery 100d is discharged from secondary battery 100d and used as electric power 16 for driving car 15.
In the energy system structured as shown in
Therefore, the energy system including these secondary batteries also achieves high safety and can generate a large amount of electric energy for efficient use thereof. In addition, since an immense time such as several days until the energy system is driven is not required, an energy system having excellent characteristics can be achieved.
In the energy system structured as shown in
(i) Fabrication of Electrolyte
Initially, KFSI (manufactured by Daiichi Kogyo Seiyaku Co., Ltd.) and NaClO4 (manufactured by Aldrich: purity 98%) were measured in a glove box filled with an argon atmosphere such that they are equal in moles, and thereafter each of KFSI and NaClO4 was dissolved in acetonitrile and stirred for 30 minutes for mixing and reaction as shown in the following chemical equation (V).
KFSI+NaClO4→NaFSI+KClO4 (V)
Then, KClO4 precipitated in a solution after reaction above was removed through vacuum filtration, and thereafter the solution after removal of KClO4 was introduced in a vacuum container made of Pyrex (trademark), that was evacuated for two days at 333K using a vacuum pump to remove acetonitrile.
Then, thionyl chloride was added to the substance obtained after removal of acetonitrile, which was stirred for three hours for reaction as shown in the following chemical equation (VI) in order to remove moisture.
H2O+SOCl2→2HCl+SO2 (VI)
Thereafter, washing with dichloromethane was performed three times to remove thionyl chloride, and thereafter the substance obtained after removal of thionyl chloride was introduced in a PFA tube, which was evacuated for two days at 323K by using a vacuum pump in order to remove dichloromethane. Thus, white powdery NaFSI was obtained.
Then, NaFSI powders obtained as above and KFSI (manufactured by Daiichi Kogyo Seiyaku Co., Ltd.) powders were measured in a glove box filled with an argon atmosphere such that a mole ratio between NaFSI and KFSI was set to NaFSI:KFSI=0.45:0.55, and mixed together to thereby fabricate a powder mixture. Thereafter, the powder mixture was heated to 57° C. or higher, which is the melting point of the powder mixture, so as to melt the same, thus fabricating NaFSI—KFSI molten salt.
(ii) Fabrication of Positive Electrode
Initially, Na2CO3 (manufactured by Wako Pure Chemical Industries, Ltd.) and Cr2O3 (manufactured by Wako Pure Chemical Industries, Ltd.) were mixed at a mole ratio of 1:1, and thereafter the mixture was formed in a pellet shape and fired for five hours at a temperature of 1223K in an argon stream, to thereby obtain NaCrO2.
Then, NaCrO2 obtained as above, acetylene black and PTFE were mixed and kneaded at a mass ratio of 80:15:5, and thereafter compression bonding thereof onto an Al mesh was performed to thereby fabricate a positive electrode.
(iii) Fabrication of Battery
Initially, the positive electrode fabricated as above was set on the lower pan, with the Al mesh side of the positive electrode facing the lower pan made of Al.
Then, glass mesh was immersed in the NaFSI—KFSI molten salt fabricated as above in a glove box filled with an argon atmosphere, so as to set the glass mesh impregnated with the NaFSI—KFSI molten salt on the positive electrode.
Then, a negative electrode made of sodium metal was set on the glass mesh above, and the upper lid made of stainless was set on the negative electrode.
Thereafter, the bolt and the nut were used to fix the upper lid and the lower pan, to thereby fabricate the battery according to Example 1.
(iv) Evaluation
The battery according to Example 1 fabricated as above was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 80° C., a charge start voltage of 2.5 V and a discharge start voltage of 3.5 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 1.
As shown in Table 1, the discharge capacity of the battery according to Example 1 after 10 cycles was 74 (mA·h/g).
A battery according to Example 2 was fabricated as in Example 1 except that NaCrO2 for the positive electrode was replaced with commercially available TiS2.
The battery according to Example 2 was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 80° C., a charge start voltage of 1.9 V and a discharge start voltage of 2.4 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 1.
As shown in Table 1, the discharge capacity of the battery according to Example 2 after 10 cycles was 115 (mA·h/g).
A battery according to Example 3 was fabricated as in Example 1 except that NaCrO2 for the positive electrode was replaced with commercially available FeF3.
The battery according to Example 3 was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 80° C., a charge start voltage of 2.7 V and a discharge start voltage of 4.1 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 1.
As shown in Table 1, the discharge capacity of the battery according to Example 3 after 10 cycles was 125 (mA·h/g).
A battery according to Example 4 was fabricated as in Example 1 except that NaFSI—NaTFSI molten salt was fabricated by using NaTFSI powders instead of KFSI powders and the NaFSI—NaTFSI molten salt was employed instead of the NaFSI—KFSI molten salt. It is noted that a method of fabricating NaTFSI powders will be described later.
The battery according to Example 4 was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 80° C., a charge start voltage of 2.5 V and a discharge start voltage of 3.5 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 1.
As shown in Table 1, the discharge capacity of the battery according to Example 4 after 10 cycles was 76 (mA·h/g).
As shown in Table 1, it was confirmed that the batteries according to Examples 1 to 4 were batteries achieving high energy density at such a low operating temperature of 80° C.
In addition, the batteries according to Examples 1 to 4 achieved high safety, because incombustible NaFSI—KFSI molten salt or NaFSI—NaTFSI molten salt was used for the electrolyte.
(i) Fabrication of Electrolyte
Initially, HTFSI (manufactured by Morita Chemical Industries Co., Ltd.: purity 99% or higher) and Na2CO3 (manufactured by Wako Pure Chemical Industries, Ltd.: purity 99.5%) were measured in a glove box filled with an argon atmosphere such that a mole ratio between HTFSI and Na2CO3 was set to HTFSI:Na2CO3=2:1, and thereafter each of HTFSI and Na2CO3 was dissolved in ethanol and stirred for 30 minutes for mixing and reaction as shown in the following chemical equation (VII).
2HTFSI+Na2CO3→2NaTFSI+CO2+H2O (VII)
Then, ethanol was roughly removed by stirring this mixture for several hours by using a rotary evaporator. The resultant substance was introduced in a vacuum container made of Pyrex (trademark), that was evacuated for 24 hours at 353K, for 24 hours at 373K, and for 24 hours at 403K using a vacuum pump in order to remove ethanol for drying, thus obtaining white powdery NaTFSI.
Meanwhile, HTFSI (manufactured by Morita Chemical Industries Co., Ltd.: purity 99% or higher) and Cs2CO3 (manufactured by Aldrich: purity 99.9%) were measured in a glove box filled with an argon atmosphere such that a mole ratio between HTFSI and Cs2CO3 was set to HTFSI:Cs2CO3=2:1, and thereafter each of HTFSI and Cs2CO3 was dissolved in ethanol and stirred for 30 minutes for mixing and reaction as shown in the following chemical equation (VIII).
2HTFSI+Cs2CO3→2CsTFSI+CO2+H2O (VIII)
Then, ethanol was roughly removed by stirring this mixture for several hours by using a rotary evaporator. The resultant substance was introduced in a vacuum container made of Pyrex (trademark), that was evacuated for 24 hours at 353K, for 24 hours at 373K, and for 24 hours at 403K using a vacuum pump in order to remove ethanol for drying, thus obtaining white powdery CsTFSI.
Then, NaTFSI powders and CsTFSI powders obtained as above were measured in a glove box filled with an argon atmosphere such that a mole ratio between NaTFSI and CsTFSI was set to NaTFSI:CsTFSI=0.1:0.9, and mixed together to thereby fabricate a powder mixture. Thereafter, the powder mixture was heated to 110° C. or higher, which is the melting point of the powder mixture, so as to melt the same, thus fabricating NaTFSI-CsTFSI molten salt.
(ii) Fabrication of Positive Electrode
As in Example 1, NaCrO2, acetylene black and PTFE were mixed and kneaded at a mass ratio of 80:15:5, and thereafter compression bonding thereof onto an Al mesh was performed to thereby fabricate a positive electrode.
(iii) Fabrication of Battery
Initially, the positive electrode fabricated as above was set on the lower pan, with the Al mesh side of the positive electrode facing the lower pan made of Al.
Then, glass mesh was immersed in the NaTFSI-CsTFSI molten salt fabricated as above in a glove box filled with an argon atmosphere, to set the glass mesh impregnated with the NaTFSI-CsTFSI molten salt on the positive electrode.
Then, a negative electrode made of sodium metal was set on the glass mesh above, and the upper lid made of stainless was set on the negative electrode.
Thereafter, the bolt and the nut were used to fix the upper lid and the lower pan, to thereby fabricate the battery according to Example 5.
(iv) Evaluation
The battery according to Example 5 fabricated as above was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 150° C., a charge start voltage of 2.3 V and a discharge start voltage of 3.1 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 2.
As shown in Table 2, the discharge capacity of the battery according to Example 5 after 10 cycles was 100 (mA·h/g).
A battery according to Example 6 was fabricated as in Example 5 except that NaCrO2 for the positive electrode was replaced with commercially available TiS2.
Then, the battery according to Example 6 was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 150° C., a charge start voltage of 1.8 V and a discharge start voltage of 2.5 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 2.
As shown in Table 2, the discharge capacity of the battery according to Example 6 after 10 cycles was 125 (mA·h/g).
A battery according to Example 7 was fabricated as in Example 5 except that NaCrO2 for the positive electrode was replaced with commercially available FeF3.
Then, the battery according to Example 7 was subjected to charge and discharge tests of 10 cycles under such conditions as an operating temperature of 150° C., a charge start voltage of 2.6 V and a discharge start voltage of 4.0 V, and a discharge capacity after 10 cycles was measured. The results are as shown in Table 2.
As shown in Table 2, the discharge capacity of the battery according to Example 7 after 10 cycles was 135 (mA·h/g).
As shown in Table 2, it was confirmed that the batteries according to Examples 5 to 7 were batteries achieving high energy density at such a low operating temperature of 150° C.
In addition, the batteries according to Examples 5 to 7 achieved high safety, because incombustible NaTFSI-CsTFSI molten salt was used for the electrolyte.
Although the present invention has been described and illustrated in detail, it is clearly understood that the same is by way of illustration and example only and is not to be taken by way of limitation, the scope of the present invention being interpreted by the terms of the appended claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2009-222854 | Sep 2009 | JP | national |
This is a continuation of application Serial No. PCT/JP2010/054640 filed Mar. 18, 2010, the contents of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/JP2010/054640 | Mar 2010 | US |
| Child | 13219167 | US |
