CN103833620A - Sulfur-containing ionic liquid, and preparation method and application thereof - Google Patents
Sulfur-containing ionic liquid, and preparation method and application thereof Download PDFInfo
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Abstract
The invention relates to a sulfur-containing ionic liquid. The chemical structural formula of the ionic liquid is shown as the specification, wherein R is alkyl of C1-C4; Y<-> is CF3SO3<-> or CF3CO2<->. The sulfur-containing ionic liquid is completely formed by ions at room temperature or under a situation close to the room temperature, has the advantages of high electrical conductivity, low melting point, wide electrochemical window, no volatilization or inflammability, good thermal stability and no halogen impurities or toxicity, and can be applied to the field of preparation of supercapacitors or lithium ionic batteries with high specific capacity. Furthermore, the invention also relates to a preparation method and application of the sulfur-containing ionic liquid.
Description
[technical field]
The present invention relates to a kind of lithium-ion battery electrolytes field, relate in particular to a kind of sulfur-bearing class ionic liquid and preparation method thereof, also relate to a kind of electrolytic solution and compound method and lithium ion battery that uses this sulfur-bearing class ionic liquid simultaneously.
[background technology]
The advantage such as lithium ion battery has that capacity is high, memory-less effect, volume are little, lightweight and pollution-free.Volume with the ferric phosphate lithium cell of equal-specification capacity is 2/3 of lead-acid cell volume, and weight is 1/3 of lead-acid cell.Thereby be widely used in military field, device for mobile communication, computer and electromobile etc.The energy of storing of lithium ion battery increases with the rising of voltage, thereby the voltage that raising applies can increase substantially the specific energy of lithium ion battery.
But, the ionic liquid that adopts two-step approach to prepare inevitably all can be introduced halogens, these halogen impurities ions can cause the shortcomings such as the stability of ionic liquid reduces, and Melting point elevation and electrochemical window narrow, thereby are unfavorable for that it is applied to the electrolytic solution of lithium ion battery.
[summary of the invention]
Based on this, be necessary sulfur-bearing class ionic liquid providing a kind of not halogen-containing element and preparation method thereof.
A kind of sulfur-bearing class ionic liquid, chemical structural formula is as follows:
Wherein, R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
This sulfur-bearing class ionic liquid is in room temperature or approach under the condition of room temperature and be made up of ion completely, specific conductivity is high, fusing point is low, electrochemical window is wide, non-volatile, non-combustible, Heat stability is good and not contain halogen impurities nontoxic, particularly decomposition voltage is high, under high voltage condition, be difficult to decompose, thereby can be applied in ultracapacitor or the lithium ion battery field of manufacturing height ratio capacity.
A preparation method for sulfur-bearing class ionic liquid, comprises the steps:
Under inert atmosphere protection, dimethyl sulphide and alkylating reagent RY are added in organic solvent for 1: 1 in molar ratio～1.2: 1, the mass ratio of described organic solvent and described dimethyl sulphide is 0.8: 1～1.4: 1, be stirring reaction 5 hours～30 hours under 5 ℃～35 ℃ conditions in temperature, then remove excessive described dimethyl sulphide and described organic solvent, collect colourless liquid, after washing, vacuum-drying obtains sulfur-bearing class ionic liquid, described alkylating reagent RY is trifluoromethanesulfonic acid methyl esters, trifluoromethanesulfonic acid ethyl ester, trifluoromethanesulfonic acid propyl ester, trifluoromethanesulfonic acid butyl ester, trifluoro-acetate, Trifluoroacetic Acid Ethyl Ester, trifluoroacetic acid propyl ester or TAB, its chemical structural formula is as follows:
Wherein, R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
In a preferred embodiment, described organic solvent is chloroform, tetrahydrofuran (THF) or acetonitrile.
In a preferred embodiment, step is removed excessive described dimethyl sulphide and described organic solvent is specially: remove excessive dimethyl sulphide and described organic solvent by the mode of underpressure distillation, the condition of described underpressure distillation is that temperature is 80 ℃～150 ℃, and pressure is 0.1Pa～5Pa.
In a preferred embodiment, described washing step is specially: described vacuum drying step is specially, and vacuum drying temperature is 60 ℃～100 ℃, and vacuum tightness is 0.01MPa.
Above-mentioned preparation process adopts the large-scale industrial production that single stage method efficiency is high, pollution-free, be conducive to sulfur-bearing class ionic liquid.
Meanwhile, be also necessary to provide a kind of electrolytic solution and compound method and lithium ion battery that uses above-mentioned difficult decomposition, the good ionic liquid of stability.
A kind of electrolytic solution, comprises sulfur-bearing class ionic liquid, lithium salts and organic solvent,
Wherein, the structural formula of described sulfur-bearing class ionic liquid is as follows:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -;
Described lithium salts is 1: 20～1: 10 with the quality of described organic solvent than scope;
Described sulfur-bearing class ionic liquid is 1: 10～1: 1 with the quality of described organic solvent than scope.
In a preferred embodiment, described organic solvent is the mixing solutions of NSC 11801, propylene carbonate and Methyl ethyl carbonate, and wherein, the volume ratio of described NSC 11801, propylene carbonate and Methyl ethyl carbonate is 1～3: 1: 3～7.
A compound method for electrolytic solution, comprises the steps:
Under inert atmosphere protection, get NSC 11801, the volume ratio of propylene carbonate and Methyl ethyl carbonate is 1～3: 1: 3～7 mix as organic solvent, the ratio that than scope is in described sulfur-bearing class ionic liquid and the quality of described organic solvent adds sulfur-bearing class ionic liquid in described organic solvent, be to be uniformly mixed under 20 ℃～50 ℃ conditions in temperature, then add lithium salts, described lithium salts is LiBF4, lithium hexafluoro phosphate, trifluoromethanesulfonic acid lithium or two (trimethyl fluoride sulfonyl) imine lithium, described lithium salts is 1: 20～1: 10 with the quality of described organic solvent than scope, obtain described electrolytic solution, wherein, the structural formula of described sulfur-bearing class ionic liquid is as follows:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
The electrolytic conductivity that contains sulfur-bearing class ionic liquid is high, fusing point is low, the decomposition voltage of Heat stability is good and not halogen-containing impurity, particularly electrolytic solution is high, can be widely used in the preparation field of lithium ion battery, obtains the lithium ion battery of high-energy-density.Meanwhile, its process for preparation is simple, uses raw material cheap and easy to get, can large-scale industrial production.
A kind of lithium ion battery, the electrolytic solution of described lithium ion battery comprises the ionic liquid with following structure:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
By test, use the above-mentioned lithium ion battery that contains sulfur-bearing class ionic liquid to there is higher charging/discharging voltage, and under high charge-discharge voltage conditions, electrolytic solution is highly stable.
[accompanying drawing explanation]
Fig. 1 is the preparation method's of the prepared sulfur-bearing class of embodiment of the present invention ionic liquid schema;
Fig. 2 is the preparation method's of the prepared sulfur-bearing class of embodiment of the present invention ion electrolytic solution schema;
[embodiment]
Mainly in conjunction with specific embodiments sulfur-bearing class ionic liquid and its preparation method and application is described in further detail below.
The sulfur-bearing class ionic liquid of present embodiment, chemical structural formula is as follows:
Wherein, R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
This sulfur-bearing class ionic liquid is in room temperature or approach under the condition of room temperature and be made up of ion completely, specific conductivity is high, fusing point is low, electrochemical window is wide, non-volatile, non-combustible, Heat stability is good and not halogen-containing impurity nontoxic, particularly decomposition voltage is high, under high voltage condition, be difficult to decompose, thereby can be applied in ultracapacitor or the lithium ion battery field of manufacturing height ratio capacity.
A preparation method for above-mentioned sulfur-bearing class ionic liquid, preparation flow is as follows:
Wherein RY is trifluoromethanesulfonic acid methyl esters, trifluoromethanesulfonic acid ethyl ester, trifluoromethanesulfonic acid propyl ester, trifluoromethanesulfonic acid butyl ester, trifluoro-acetate, Trifluoroacetic Acid Ethyl Ester, trifluoroacetic acid propyl ester or TAB; R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
Specifically comprise the steps:
Step S1: under inert atmosphere protection; dimethyl sulphide and alkylating reagent RY are added in organic solvent for 1: 1 in molar ratio～1.2: 1; the mass ratio of described organic solvent and described dimethyl sulphide is 0.8: 1～1.4: 1, is stirring reaction 5 hours～30 hours under 5 ℃～35 ℃ conditions in temperature.
Wherein, alkylating reagent RY is trifluoromethanesulfonic acid methyl esters, trifluoromethanesulfonic acid ethyl ester, trifluoromethanesulfonic acid propyl ester, trifluoromethanesulfonic acid butyl ester, trifluoro-acetate, Trifluoroacetic Acid Ethyl Ester, trifluoroacetic acid propyl ester or TAB.
Wherein, organic solvent is chloroform, tetrahydrofuran (THF) or acetonitrile.
Step S2: then remove excessive described dimethyl sulphide and described organic solvent, collect colourless liquid.
Wherein, the concrete step of removing excessive described dimethyl sulphide and described organic solvent is to remove excessive dimethyl sulphide and described organic solvent by the mode of underpressure distillation, the condition of described underpressure distillation is that temperature is 80 ℃～150 ℃, and pressure is 0.1Pa～5Pa.
Step S3: after washing, it is as follows that vacuum-drying obtains its chemical structural formula of sulfur-bearing class ionic liquid:
Wherein, vacuum drying temperature is 60 ℃～100 ℃, and vacuum tightness is 0.01MPa;
Wherein, R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
Wherein, the mode of washing is for adopting methyl tertiary butyl ether 50ml repetitive scrubbing more than 3 times.
The large-scale industrial production that above-mentioned preparation process efficiency is high, pollution-free, be conducive to sulfur-bearing class ionic liquid.
Meanwhile, the present invention also provides a kind of electrolytic solution and compound method and lithium ion battery that uses above-mentioned difficult decomposition, the good ionic liquid of stability.
The electrolytic solution of one embodiment comprises sulfur-bearing class ionic liquid, lithium salts and organic solvent,
Wherein, the structural formula of sulfur-bearing class ionic liquid is as follows:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -;
Described lithium salts is 1: 20～1: 10 with the quality of described organic solvent than scope;
Described sulfur-bearing class ionic liquid is 1: 10～1: 1 with the quality of described organic solvent than scope.
Organic solvent is preferably the mixing solutions of NSC 11801, propylene carbonate and Methyl ethyl carbonate, and wherein, the volume ratio of described NSC 11801, propylene carbonate and Methyl ethyl carbonate is 1～3: 1: 3～7.
With reference to the accompanying drawings 2, the process for preparation of this electrolytic solution, comprises the steps:
Step S4: under inert atmosphere protection; the volume ratio of getting NSC 11801, propylene carbonate and Methyl ethyl carbonate is 1～3: 1: 3～7 mix as organic solvent; the ratio that than scope is in described sulfur-bearing class ionic liquid and the quality of described organic solvent adds sulfur-bearing class ionic liquid in described organic solvent; be to be uniformly mixed under 20 ℃～50 ℃ conditions in temperature
Step S5: then add lithium salts, described lithium salts is LiBF4, lithium hexafluoro phosphate, trifluoromethanesulfonic acid lithium or two (trimethyl fluoride sulfonyl) imine lithium, described lithium salts is 1: 20～1: 10 with the quality of described organic solvent than scope, obtain described electrolytic solution, wherein, the structural formula of described sulfur-bearing class ionic liquid is as follows:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
The electrolytic conductivity that contains sulfur-bearing class ionic liquid is high, fusing point is low, Heat stability is good and not contain the decomposition voltage of halogen impurities, particularly electrolytic solution high, can be widely used in the preparation field of lithium ion battery, obtains the lithium ion battery of high-energy-density.Meanwhile, its process for preparation is simple, uses raw material cheap and easy to get, can large-scale industrial production.
The electrolytic solution of the lithium ion battery of one embodiment comprises the ionic liquid with following structure:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
By test, use and above-mentionedly contain the lithium ion battery that sulfur-bearing class ionic liquid prepares and there is higher charging/discharging voltage, and under high charge-discharge voltage conditions, electrolytic solution is highly stable.
Be below specific embodiment part:
In following examples, contain atmosphere of inert gases take nitrogen and argon atmosphere as representative.
Embodiment 1:
In the flask of 500mL, add respectively 70g chloroform, (68.3g, 1.1mol) dimethyl sulphide, (164.1g, 1.0mol) trifluoromethanesulfonic acid methyl esters, under nitrogen atmosphere, be warming up to 25 ℃, stirring reaction 20 hours.Leave standstill cooling, it is 100 ℃ in temperature, pressure is to carry out underpressure distillation under the condition of 3.0Pa, remove excessive reactant, collecting colourless liquid 50ml methyl tertiary butyl ether repetitive scrubbing three times, is then 80 ℃ in temperature, and vacuum tightness is under 0.01MPa condition, to carry out vacuum-drying, obtain colourless liquid trimethylsulfonium fluoroform sulphonate, productive rate 87%.
Its hydrogen spectrum data are as follows:
1H?NMR(CDCl
3，400MHz，ppm)：3.24(s，9H)
Under inert atmosphere protection; take out 10g; trimethylsulfonium fluoroform sulphonate; then add wherein the mixed solvent of 50g NSC 11801 (EC), propylene carbonate (PC) and Methyl ethyl carbonate (EMC); wherein; volume ratio between NSC 11801, propylene carbonate and Methyl ethyl carbonate is 2: 1: 5, and is heated to 40 ℃ and is uniformly mixed, and then adds 3.5g LiBF4 (LiBF
4), continue stirring it is all dissolved, thereby obtain object ion liquid electrolyte.
Embodiment 2:
In the flask of 500mL, add respectively 50g tetrahydrofuran (THF), (62.1g, 1.0mol) dimethyl sulphide, (178.1g, 1.0mol) trifluoromethanesulfonic acid ethyl ester, under nitrogen atmosphere, be warming up to 10 ℃, stirring reaction 30 hours.Leave standstill cooling, it is 80 ℃ in temperature, pressure is to carry out underpressure distillation under the condition of 0.1Pa, remove excessive reactant, collecting colourless liquid 50ml methyl tertiary butyl ether repetitive scrubbing three times, is then 60 ℃ in temperature, and vacuum tightness is under 0.01MPa condition, to carry out vacuum-drying, obtain colourless liquid dimethyl ethyl sulfonium fluoroform sulphonate, productive rate 88%.
Its hydrogen spectrum data are as follows:
1H?NMR(CDCl
3，400MHz，ppm)：3.38(m，2H)，3.25(s，6H)，2.29(s，3H).
Under inert atmosphere protection; take out 10g dimethyl ethyl sulfonium fluoroform sulphonate; then add wherein the mixed solvent of 100g NSC 11801 (EC), propylene carbonate (PC) and Methyl ethyl carbonate (EMC); wherein; volume ratio between NSC 11801, propylene carbonate and Methyl ethyl carbonate is 1: 1: 3; and be heated to 20 ℃ and be uniformly mixed, then add 5.0g lithium hexafluoro phosphate (LiPF
6), continue stirring it is all dissolved, thereby obtain object ion liquid electrolyte.
Embodiment 3
In the flask of 500mL, add respectively 89g acetonitrile, (74.5g, 1.2mol) dimethyl sulphide, (156.1g, 1.0mol) trifluoroacetic acid propyl ester, under nitrogen atmosphere, be warming up to 35 ℃, stirring reaction 5 hours.Leave standstill cooling, it is 150 ℃ in temperature, pressure is to carry out underpressure distillation under the condition of 5.0Pa, remove excessive reactant, collecting colourless liquid 50ml methyl tertiary butyl ether repetitive scrubbing three times, is then 100 ℃ in temperature, and vacuum tightness is under 0.01MPa condition, to carry out vacuum-drying, obtain colourless liquid dimethyl propyl sulfonium trifluoroacetate, productive rate 90%.
Its hydrogen spectrum data are as follows:
1H?NMR(CDCl
3，400MHz，ppm)：3.53(m，2H)，3.25(s，6H)，2.88(m，2H)，0.96(t，3H)
Under inert atmosphere protection; take out 10g dimethyl propyl sulfonium trifluoroacetate; then add wherein the mixed solvent of 10g NSC 11801 (EC), propylene carbonate (PC) and Methyl ethyl carbonate (EMC); wherein; volume ratio between NSC 11801, propylene carbonate and Methyl ethyl carbonate is 3: 1: 7; and be heated to 50 ℃ and be uniformly mixed, then add 1.0g trifluoromethanesulfonic acid lithium (LiSO
3cF
3), continue stirring it is all dissolved, thereby obtain object ion liquid electrolyte.
Embodiment 4:
In the flask of 500mL, add respectively 95.6g chloroform, (68.3g, 1.1mol) dimethyl sulphide, (170.1g, 1.0mol) TAB, under nitrogen atmosphere, be warming up to 5 ℃, stirring reaction 30 hours.Leave standstill cooling, it is 120 ℃ in temperature, pressure is to carry out underpressure distillation under the condition of 4.0Pa, remove excessive reactant, collecting colourless liquid 50ml methyl tertiary butyl ether repetitive scrubbing three times, is then 90 ℃ in temperature, and vacuum tightness is under 0.01MPa condition, to carry out vacuum-drying, obtain colourless liquid dimethylbutyl sulfonium trifluoroacetate, productive rate 85%.
Its hydrogen spectrum data are as follows:
1H?NMR(CDCl
3，400MHz，ppm)：3.53(m，2H)，3.25(s，6H)，2.88(m，4H)，0.96(t，3H).
Under inert atmosphere protection; take out 10g dimethylbutyl sulfonium trifluoroacetate; then add wherein the mixed solvent of 30g NSC 11801 (EC), propylene carbonate (PC) and Methyl ethyl carbonate (EMC); wherein; volume ratio between NSC 11801, propylene carbonate and Methyl ethyl carbonate is 2: 1: 6; and be heated to 30 ℃ and be uniformly mixed; then add 2.2g bis-(trimethyl fluoride sulfonyl) imine lithium (LiTFSI); continue stirring it is all dissolved, thereby obtain object ion liquid electrolyte.
Application Example
Electrolytic solution in application above-described embodiment 1～4 is assembled into lithium ion battery
Take 0.9g LiCoO
2, 0.5g acetylene black and 0.5g PVDF, and add 20g NMP, fully stir and make it to become the slurry mixing.Then by its blade coating on the aluminium foil cleaning through ethanol, under the vacuum of 0.01MPa, 80 ℃ are dried to constant weight, and are pressed into LiCoO in 10MPa pressure lower roll
2electrode, and be cut into anode electrode disk, pp barrier film, lithium sheet is as negative pole.In the glove box that is full of argon gas, the electrolytic solution electrolytic solution in pp barrier film and above-described embodiment 1～4 is placed between positive and negative electrode, on stamping machine, button cell is made in sealing.
In the voltage range of 2.5～4.2V, utilize charge-discharge test instrument to carry out 0.05C charge-discharge test to the lithium ion battery assembling in the present embodiment, its performance data is listed in the table below:
| Embodiment | 1 | 2 | 3 | 4 |
| First discharge specific capacity mAh/g | 117 | 120 | 105 | 110 |
| Discharging efficiency | 95％ | 96％ | 93％ | 95％ |
As can be seen from the table, the prepared il electrolyte of the embodiment of the present invention is suitable for the electrolytic solution of lithium ion battery, and assembled lithium ion battery has good specific storage and efficiency for charge-discharge while being applied to electrolytic solution.
The above embodiment has only expressed several embodiment of the present invention, and it describes comparatively concrete and detailed, but can not therefore be interpreted as the restriction to the scope of the claims of the present invention.It should be pointed out that for the person of ordinary skill of the art, without departing from the inventive concept of the premise, can also make some distortion and improvement, these all belong to protection scope of the present invention.Therefore, the protection domain of patent of the present invention should be as the criterion with claims.
Claims (10)
1. a sulfur-bearing class ionic liquid, is characterized in that, chemical structural formula is as follows:
Wherein, R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
2. a preparation method for sulfur-bearing class ionic liquid, is characterized in that, comprises the steps:
Under inert atmosphere protection, dimethyl sulphide and alkylating reagent RY are added in organic solvent for 1: 1 in molar ratio～1.2: 1, the mass ratio of described organic solvent and described dimethyl sulphide is 0.8: 1～1.4: 1, be stirring reaction 5 hours～30 hours under 5 ℃～35 ℃ conditions in temperature, then remove excessive described dimethyl sulphide and described organic solvent, collect colourless liquid, after washing, vacuum-drying obtains sulfur-bearing class ionic liquid, wherein, described alkylating reagent RY is trifluoromethanesulfonic acid methyl esters, trifluoromethanesulfonic acid ethyl ester, trifluoromethanesulfonic acid propyl ester, trifluoromethanesulfonic acid butyl ester, trifluoro-acetate, Trifluoroacetic Acid Ethyl Ester, trifluoroacetic acid propyl ester or TAB, its chemical structural formula is as follows:
Wherein, R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
3. the preparation method of sulfur-bearing class ionic liquid as claimed in claim 2, is characterized in that, described organic solvent is chloroform, tetrahydrofuran (THF) or acetonitrile.
4. the preparation method of sulfur-bearing class ionic liquid as claimed in claim 2, it is characterized in that, step is removed excessive described dimethyl sulphide and described organic solvent is specially: remove excessive dimethyl sulphide and described organic solvent by the mode of underpressure distillation, the condition of described underpressure distillation is that temperature is 80 ℃～150 ℃, and pressure is 0.1Pa～5Pa.
5. the preparation method of sulfur-bearing class ionic liquid as claimed in claim 2, is characterized in that, described vacuum drying step is specially, and vacuum drying temperature is 60 ℃～100 ℃, and vacuum tightness is 0.01MPa.
6. an electrolytic solution, is characterized in that, comprises sulfur-bearing class ionic liquid, lithium salts and organic solvent,
Wherein, the structural formula of described sulfur-bearing class ionic liquid is as follows:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -;
Described lithium salts is 1: 20～1: 10 with the quality of described organic solvent than scope;
Described sulfur-bearing class ionic liquid is 1: 10～1: 1 with the quality of described organic solvent than scope.
7. electrolytic solution as claimed in claim 6, it is characterized in that, described organic solvent is the mixing solutions of NSC 11801 propylene carbonate and Methyl ethyl carbonate, and wherein, the volume ratio of described NSC 11801, propylene carbonate and Methyl ethyl carbonate is 1～3: 1: 3～7.
8. electrolytic solution as claimed in claim 6, is characterized in that, described lithium salts is LiBF4, lithium hexafluoro phosphate, trifluoromethanesulfonic acid lithium or two (trimethyl fluoride sulfonyl) imine lithium.
9. a compound method for electrolytic solution, is characterized in that, comprises the steps:
Under inert atmosphere protection, get NSC 11801, the volume ratio of propylene carbonate and Methyl ethyl carbonate is 1～3: 1: 3～7 mix as organic solvent, the ratio that than scope is in described sulfur-bearing class ionic liquid and the quality of described organic solvent adds sulfur-bearing class ionic liquid in described organic solvent, be to be uniformly mixed under 20 ℃～50 ℃ conditions in temperature, then add lithium salts, described lithium salts is LiBF4, lithium hexafluoro phosphate, trifluoromethanesulfonic acid lithium or two (trimethyl fluoride sulfonyl) imine lithium, described lithium salts is 1: 20～1: 10 with the quality of described organic solvent than scope, obtain described electrolytic solution, wherein, the structural formula of described sulfur-bearing class ionic liquid is as follows:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
10. a lithium ion battery, is characterized in that, the electrolytic solution of described lithium ion battery comprises the ionic liquid with following structure:
R is that carbonatoms is 1～4 alkyl, Y
-for CF
3sO
3 -or CF
3cO
2 -.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006070545A1 (en) * | 2004-12-27 | 2006-07-06 | National Institute Of Advanced Industrial Science And Technology | Ionic liquid |
| CN101160325A (en) * | 2005-04-15 | 2008-04-09 | 巴斯福股份公司 | Cellulose solutions in ionic liquids |
| WO2012042004A1 (en) * | 2010-09-30 | 2012-04-05 | Basf Se | Li-based anode with ionic liquid polymer gel |
-
2012
- 2012-11-26 CN CN201210485297.6A patent/CN103833620A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006070545A1 (en) * | 2004-12-27 | 2006-07-06 | National Institute Of Advanced Industrial Science And Technology | Ionic liquid |
| CN101160325A (en) * | 2005-04-15 | 2008-04-09 | 巴斯福股份公司 | Cellulose solutions in ionic liquids |
| WO2012042004A1 (en) * | 2010-09-30 | 2012-04-05 | Basf Se | Li-based anode with ionic liquid polymer gel |
Non-Patent Citations (2)
| Title |
|---|
| 房少华等: "新型离子液体电解质的合成及在锂二次电池中的应用研究", 《中国博士学位论文全文数据库 工程科技Ⅱ辑》, 30 April 2011 (2011-04-30), pages 6 - 7 * |
| 罗世春等: "新型含不对称锍阳离子室温离子液体在锂离子电池中的应用研究", 《化学世界》, 31 December 2006 (2006-12-31) * |
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Application publication date: 20140604 |