CN109742446A - A kind of lithium/thinly chloride battery electrolyte and preparation method thereof - Google Patents

A kind of lithium/thinly chloride battery electrolyte and preparation method thereof Download PDF

Info

Publication number
CN109742446A
CN109742446A CN201811570609.7A CN201811570609A CN109742446A CN 109742446 A CN109742446 A CN 109742446A CN 201811570609 A CN201811570609 A CN 201811570609A CN 109742446 A CN109742446 A CN 109742446A
Authority
CN
China
Prior art keywords
lithium
additive
addition
battery electrolyte
purification
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201811570609.7A
Other languages
Chinese (zh)
Other versions
CN109742446B (en
Inventor
裴广华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Zhongluman New Material Technology Co., Ltd.
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201811570609.7A priority Critical patent/CN109742446B/en
Priority to CN202010736012.6A priority patent/CN112072177A/en
Priority to CN202010737131.3A priority patent/CN112072178A/en
Publication of CN109742446A publication Critical patent/CN109742446A/en
Application granted granted Critical
Publication of CN109742446B publication Critical patent/CN109742446B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0567Liquid materials characterised by the additives
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0088Composites
    • H01M2300/0091Composites in the form of mixtures
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Inorganic Chemistry (AREA)
  • Primary Cells (AREA)

Abstract

The invention discloses a kind of lithium/thinly chloride battery electrolyte and preparation method thereof, the electrolyte includes thionyl chloride, electrolytic salt and additive, additive includes the first additive and Second addition, is somebody's turn to do the preparation method comprises the following steps: thionyl chloride is distilled, collection fraction;Electrolytic salt is weighed to be dissolved in thionyl chloride fraction;The purification of first additive;The purification of Second addition;The first additive of purifying and the Second addition of purifying are weighed, is added in the thionyl chloride solution of electrolytic salt to get lithium/thinly chloride battery electrolyte;The first additive and Second addition synergistic effect in lithium/thinly chloride battery electrolyte of the present invention, lithium/thinly chloride battery is set to achieve good discharge voltage and discharge capacity, the voltage delay phenomenon of lithium/thinly chloride battery is significantly improved, and there is preferable cycle performance and higher safety by lithium/thinly chloride battery prepared by the electrolyte.

Description

A kind of lithium/thinly chloride battery electrolyte and preparation method thereof
Technical field
The present invention relates to technical field of lithium ion, specifically a kind of lithium/thinly chloride battery electrolyte and its preparation Method.
Background technique
Lithium/thinly chloride (Li/SOCl2) battery be one kind using lithium as anode, carbon makees cathode carrier, anhydrous tetrachloro-lithium aluminate Thionyl chloride (SOCl2) solution makees the lithium battery of electrolyte.Lithium/thinly chloride battery is high with specific energy, specific power is big, puts The characteristics such as piezoelectric voltage is steady, storage life is long, in aerospace, underawater ordnance, navigation equipment, geological prospecting, instrument and meter etc. It is all widely used in military and civilian industry.Lithium/thinly chloride battery is specific energy and specific power in current battery field A kind of highest battery.The overall reaction mechanism of lithium/thinly chloride battery are as follows: 4Li+2SOCl2→4LiCl+S+SO2, sulphur and dioxy Change sulphur to be dissolved in excessive thionyl chloride electrolyte, and during electric discharge, due to generating sulfur dioxide, has to a certain degree Pressure generate.During storage, cathode of lithium is contacted once with electrolyte, just generates LiCl with thionyl chloride electrolysis qualitative response, Cathode of lithium is the protection by the LiCl film being formed thereon.This passivating film is beneficial to extend the storage life of battery, but It can cause voltage delay when discharging and starting, the battery after long-term storage, discharges, voltage is stagnant at low ambient temperatures at high temperature Phenomenon is especially apparent afterwards.
In order to eliminate lithium/thinly chloride battery voltage delay phenomenon, the afflux form for improving cathode and anode is mostly used greatly, Or improve the impurity content and molar concentration of electrolyte, to reduce the internal resistance of cell;Electronic component is installed additional in inside battery or outside, Battery is set to be in weak discharge state, to weaken the formation of passivating film;In cathode and electrolyte add metal phthalocyanine compound or The modes such as sulfide, to improve voltage delay performance.The above method some can improve to a certain extent lithium/thinly chloride electricity Certain performances in pond, but some then it weakens lithium/thinly chloride using the capacity of " sacrifice " lithium/thinly chloride battery as cost The other performance of battery.
Electrolyte is one of the three elements for forming lithium/thinly chloride battery, hair of the physicochemical property to battery material performance It waves and plays a crucial role, develop the electrolyte material to match with cathode and anode material and mean a great.
Summary of the invention
It is existing to solve the purpose of the present invention is to provide a kind of lithium/thinly chloride battery electrolyte and preparation method thereof The problems in technology.
To achieve the above object, the invention provides the following technical scheme:
A kind of lithium/thinly chloride battery electrolyte, including thionyl chloride, electrolytic salt and additive, the thionyl of electrolytic salt The molar concentration of solutions of chlorine is 0.1-1mol/L, and the quality of additive is the 0.01-0.5% of electrolyte gross mass.Additive adds It is very little to enter amount, does not have the phenomenon that mitigating cell voltage lag, the additional amount of additive is too many, it will affect the gram volume of material, And it causes to waste, does not have the phenomenon that mitigating cell voltage lag.
As optimization, additive includes the first additive and Second addition, the structural formula of the first additive are as follows:
Wherein, X is halogen;R1For itrile group, amido, hydroxyl or nitro;R2、R3It is hydrogen, monosubstituted or polysubstituted C1-C6 alkane Base, aryl, C1-C6 alkoxy or halogenated C1-C6 alkoxy;R4For C1-C6 alkyl or the C1- being mono-or polysubstituted with halogens C6 alkyl.
As optimization, the structural formula of Second addition are as follows:
Wherein, X1For halogen;R11、R21、R31It is C1-C10 alkyl, halogenated C1-C10 alkyl, C1-C10 alkoxy or halogenated C1-C10 alkoxy;R41For it is unsubstituted or or by the alkyl-substituted heterocycle of C1-C6, O, N, S element are contained on the heterocycle One of or it is a variety of.
As optimization, electrolytic salt is bis- (fluorine sulphonyl) imine lithiums, di-oxalate lithium borate, trifluoromethanesulfonic acid lithium, three (trifluoros Sulfonyloxy methyl) lithium methide, lithium hexafluoro phosphate, three oxalic acid lithium phosphates, difluoro dioxalic acid lithium phosphate, one in tetrafluoro oxalic acid lithium phosphate Kind is a variety of.Li/SOCl2The major defect of battery is its voltage delay phenomenon, this phenomenon especially after high temperature storage, It shows even more serious when using at normal temperature again, causes Li/SOCl2The reason of cell voltage lags is mainly in battery system Tetrachloro-lithium aluminate (LiAlCl is used4) electrolytic salt, the electrolyte solution containing this salt generates spontaneous change in lithium anode Learn reaction, product LiCl, and LiCl is covered in the form of a film on lithium anode surface hampers lithium and electrolyte solution Contact, eventually leads to voltage delay, and the present invention replaces tetrachloro-lithium aluminate (LiAlCl using above-mentioned electrolytic salt4) electrolytic salt The phenomenon that preparing lithium/thinly chloride battery electrolyte, can effectively mitigating cell voltage lag.
As optimization, the quality of the first additive is the 0.005-0.3% of electrolyte gross mass, the quality of Second addition For the 0.005-0.2% of electrolyte gross mass.
A kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) thionyl chloride is distilled, collects fraction;
(2) it weighs electrolytic salt to be placed in thionyl chloride fraction obtained by step (1), constant volume obtains the sulfurous of electrolytic salt Solution of acid chloride;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, then Leaching liquor is distilled, the first additive, the first additive of purifying obtained by drying are obtained;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to heating interior by feeding inlet, using the first fused salt heating rod and the second fused salt heating rod to molten Salt is heated;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe behind the door and is vacuumized by vacuum pump, and the purification of Second addition is completed after a period of time;
(5) Second addition for the purifying that the first additive and step (4) for weighing the purifying that step (3) obtains obtain, then It is added in the thionyl chloride solution of step (2) obtained electrolytic salt, is stirred continuously until being completely dissolved to get lithium/Asia Chlorosulfuric acid battery electrolyte.
As optimization, a kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) thionyl chloride is placed in flask, heating is distilled, and 70-80 DEG C of fraction is collected;Thionyl chloride is distilled It is the purpose for playing purification;
(2) electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned dissolving electrolyte salt sulfurous obtained by step (1) In acyl chlorides fraction, constant volume is carried out, obtains the thionyl chloride solution for the electrolytic salt that molar concentration is 0.1-1mol/L;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, then Leaching liquor is distilled, the first additive, the first additive of purifying obtained by drying are obtained;The temperature of extraction is 30-45 DEG C, The time of extraction is 1-4h, and the distillation is carried out at 40-80 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device: the method for purification Process flow is short, easy to operate, and the purity of the Second addition after purification is greater than 99%;
(a) fused salt is added to heating interior by feeding inlet, using the first fused salt heating rod and the second fused salt heating rod to molten Salt is heated, and temperature is made to reach 200-250 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.03-0.08KPa behind the door, completes Second addition by 6-15h Purification;Silica gel mainly plays decolorization;
(5) Second addition for the purifying that the first additive and step (4) for weighing the purifying that step (3) obtains obtain, then It is added in the thionyl chloride solution of step (2) obtained electrolytic salt, is stirred continuously until being completely dissolved to get lithium/Asia Chlorosulfuric acid battery electrolyte.
First additive and Second addition are purified, impurity is reduced, utilizes the electricity of lithium/thinly chloride made from them Pond electrolyte can more effectively mitigate the phenomenon that cell voltage lag.
As optimization, the sodium nitrite of quality and the mixtures of potassium nitrite such as the fused salt in step (a) is.
As optimization, leaching liquor is transferred in oscillator before distillation by step in (3), is shaken at 100-300r/min 30-60min.The purpose of concussion is that mix the first additive with acetone more uniform.
As optimization, step (1), step (2) and step (3) be in relative humidity≤0.5-1% dry environment into Row operation.The effect of lithium/thinly chloride battery electrolyte and water is very fierce, or even very micro water is also easy to occur therewith Effect generates HCl gas, heavy corrosion is caused, so to carry out experimental implementation in dry environment when preparing electrolyte.
Compared with prior art, the beneficial effects of the present invention are:
First is that the first additive and Second addition synergistic effect in lithium/thinly chloride battery electrolyte of the present invention have preferably The passivation of anti-thionyl chloride characteristic, the first additive and Second addition pass through cathode activity object in lithium/thinly chloride battery The effect of matter thionyl chloride, it is suppressed that the formation of lithium metal anode surface " passivating film " achieves lithium/thinly chloride battery good Good discharge voltage and discharge capacity, significantly improves the voltage delay phenomenon of lithium/thinly chloride battery.
Second is that the first additive and Second addition in lithium/thinly chloride battery electrolyte of the present invention have preferable resist Nucleophillic attack ability, the two synergistic effect can effectively inhibit Li2The loss of O stabilizes the structure of lithium-rich anode material, effectively slow Solved the generation of cell voltage hysteresis, at the same lithium/thinly chloride battery electrolyte of the invention have good in oxidation resistance and Non-ignitable characteristic, therefore there is preferable cycle performance and higher safety by lithium/thinly chloride battery prepared by the electrolyte Property.
Third is that the preparation method of lithium/thinly chloride battery electrolyte of the present invention is simple, and easy to operate, formula science, raw material It is at low cost, it is practical, it has a wide range of applications.
Fourth is that being distilled in the preparation method of lithium/thinly chloride battery electrolyte of the present invention to thionyl chloride, to first Additive and Second addition are purified, and keep the impurity content for the lithium/thinly chloride battery electrolyte being prepared less, electricity The performance for solving liquid is more excellent.
Specific embodiment
The following is a clear and complete description of the technical scheme in the embodiments of the invention, it is clear that described embodiment Only a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, the common skill in this field Art personnel every other embodiment obtained without making creative work belongs to the model that the present invention protects It encloses.
Embodiment 1:
A kind of lithium/thinly chloride battery electrolyte, including thionyl chloride, bis- (fluorine sulphonyl) imine lithiums and additive, electrolytic salt The molar concentration of thionyl chloride solution be 0.1mol/L, the quality of additive is the 0.01% of electrolyte gross mass, additive packet The first additive and Second addition are included, wherein the quality of the first additive is the 0.005% of electrolyte gross mass, the second addition The quality of agent is the 0.005% of electrolyte gross mass.
The structural formula of first additive are as follows:
Wherein, X Cl;R1For itrile group;R2、R3It is hydrogen;R4For methyl.
The structural formula of Second addition are as follows:
Wherein, X1For Cl;R11、R21、R31It is methyl;R41For pyrrole heterocyclic base.
A kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) under the dry environment of relative humidity≤0.5%, thionyl chloride is placed in flask, heating is distilled, and collects 70 DEG C fraction;
(2) under the dry environment of relative humidity≤0.5%, electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned electrolysis Matter salt is dissolved in thionyl chloride fraction obtained by step (1), carries out constant volume, obtains the electrolysis that molar concentration is 0.1mol/L The thionyl chloride solution of matter salt;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, will Leaching liquor is transferred in oscillator, 30min is shaken at 100r/min, then distill to leaching liquor, is removed acetone, is obtained first Additive crude extract finally removes supernatant, the first additive of purifying obtained by drying;The temperature of extraction is 30 DEG C, extraction Time is 1h, and distillation is carried out at 40 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to the mixing for the sodium nitrites and potassium nitrite of quality such as heating is indoor, and fused salt is by feeding inlet Object heats fused salt using the first fused salt heating rod and the second fused salt heating rod, temperature is made to reach 200 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.03KPa behind the door, and the purification of Second addition is completed by 6h;
(5) under the dry environment of relative humidity≤0.5%, the first additive and step of the purifying that step (3) obtains are weighed (4) Second addition of the purifying obtained is then added in the thionyl chloride solution of step (2) obtained electrolytic salt, It is stirred continuously until being completely dissolved to get lithium/thinly chloride battery electrolyte.
Embodiment 2:
A kind of lithium/thinly chloride battery electrolyte, including thionyl chloride, di-oxalate lithium borate and additive, the Asia of electrolytic salt The molar concentration of sulfonyl solutions of chlorine is 0.4mol/L, and the quality of additive is the 0.1% of electrolyte gross mass, and additive includes the One additive and Second addition, wherein the quality of the first additive is the 0.05% of electrolyte gross mass, the matter of Second addition Amount is the 0.05% of electrolyte gross mass.
The structural formula of first additive are as follows:
Wherein, X Br;R1For amido;R2、R3It is chloromethyl;R4For ethyl.
The structural formula of Second addition are as follows:
Wherein, X1For Br;R11、R21、R31It is chloromethyl;R41For furans heterocycle.
A kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) under the dry environment of relative humidity≤0.6%, thionyl chloride is placed in flask, heating is distilled, and collects 72 DEG C fraction;
(2) under the dry environment of relative humidity≤0.6%, electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned electrolysis Matter salt is dissolved in thionyl chloride fraction obtained by step (1), carries out constant volume, obtains the electrolysis that molar concentration is 0.4mol/L The thionyl chloride solution of matter salt;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, will Leaching liquor is transferred in oscillator, 35min is shaken at 150r/min, then distill to leaching liquor, is removed acetone, is obtained first Additive crude extract finally removes supernatant, the first additive of purifying obtained by drying;The temperature of extraction is 32 DEG C, extraction Time is 1.5h, and distillation is carried out at 50 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to the mixing for the sodium nitrites and potassium nitrite of quality such as heating is indoor, and fused salt is by feeding inlet Object heats fused salt using the first fused salt heating rod and the second fused salt heating rod, temperature is made to reach 210 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.04KPa behind the door, and the purification of Second addition is completed by 8h;
(5) under the dry environment of relative humidity≤0.6%, the first additive and step of the purifying that step (3) obtains are weighed (4) Second addition of the purifying obtained is then added in the thionyl chloride solution of step (2) obtained electrolytic salt, It is stirred continuously until being completely dissolved to get lithium/thinly chloride battery electrolyte.
Embodiment 3:
A kind of lithium/thinly chloride battery electrolyte, including thionyl chloride, trifluoromethanesulfonic acid lithium and additive, the Asia of electrolytic salt The molar concentration of sulfonyl solutions of chlorine is 0.6mol/L, and the quality of additive is the 0.2% of electrolyte gross mass, and additive includes the One additive and Second addition, wherein the quality of the first additive is the 0.1% of electrolyte gross mass, the matter of Second addition Amount is the 0.2% of electrolyte gross mass.
The structural formula of first additive are as follows:
Wherein, X I;R1For hydroxyl;R2、R3It is phenyl;R4For chloromethyl.
The structural formula of Second addition are as follows:
Wherein, X1For I;R11、R21、R31It is methoxyl group;R41For thiophene heterocycle.
A kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) under the dry environment of relative humidity≤0.7%, thionyl chloride is placed in flask, heating is distilled, and collects 74 DEG C fraction;
(2) under the dry environment of relative humidity≤0.7%, electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned electrolysis Matter salt is dissolved in thionyl chloride fraction obtained by step (1), carries out constant volume, obtains the electrolysis that molar concentration is 0.6mol/L The thionyl chloride solution of matter salt;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, will Leaching liquor is transferred in oscillator, 40min is shaken at 200r/min, then distill to leaching liquor, is removed acetone, is obtained first Additive crude extract finally removes supernatant, the first additive of purifying obtained by drying;The temperature of extraction is 34 DEG C, extraction Time is 2h, and distillation is carried out at 60 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to the mixing for the sodium nitrites and potassium nitrite of quality such as heating is indoor, and fused salt is by feeding inlet Object heats fused salt using the first fused salt heating rod and the second fused salt heating rod, temperature is made to reach 220 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.05KPa behind the door, and the purification of Second addition is completed by 10h;
(5) under the dry environment of relative humidity≤0.7%, the first additive and step of the purifying that step (3) obtains are weighed (4) Second addition of the purifying obtained is then added in the thionyl chloride solution of step (2) obtained electrolytic salt, It is stirred continuously until being completely dissolved to get lithium/thinly chloride battery electrolyte.
Embodiment 4:
A kind of lithium/thinly chloride battery electrolyte, including thionyl chloride, three (trimethyl fluoride sulfonyl) lithium methides, lithium hexafluoro phosphate And additive, the molar concentration of the thionyl chloride solution of electrolytic salt are 0.8mol/L, the quality of additive is the total matter of electrolyte The 0.4% of amount, additive includes the first additive and Second addition, wherein the quality of the first additive is electrolyte gross mass 0.2%, the quality of Second addition is the 0.2% of electrolyte gross mass.
The structural formula of first additive are as follows:
Wherein, X F;R1For nitro;R2、R3It is methoxyl group;R4For propyl.
The structural formula of Second addition are as follows:
Wherein, X1For F;R11、R21、R31It is chloromethoxy;R41For 3- picoline heterocycle.
A kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) under the dry environment of relative humidity≤0.8%, thionyl chloride is placed in flask, heating is distilled, and collects 78 DEG C fraction;
(2) under the dry environment of relative humidity≤0.8%, electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned electrolysis Matter salt is dissolved in thionyl chloride fraction obtained by step (1), carries out constant volume, obtains the electrolysis that molar concentration is 0.8mol/L The thionyl chloride solution of matter salt;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, will Leaching liquor is transferred in oscillator, 50min is shaken at 250r/min, then distill to leaching liquor, is removed acetone, is obtained first Additive crude extract finally removes supernatant, the first additive of purifying obtained by drying;The temperature of extraction is 40 DEG C, extraction Time is 3h, and distillation is carried out at 70 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to the mixing for the sodium nitrites and potassium nitrite of quality such as heating is indoor, and fused salt is by feeding inlet Object heats fused salt using the first fused salt heating rod and the second fused salt heating rod, temperature is made to reach 240 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.07KPa behind the door, and the purification of Second addition is completed by 12h;
(5) under the dry environment of relative humidity≤0.8%, the first additive and step of the purifying that step (3) obtains are weighed (4) Second addition of the purifying obtained is then added in the thionyl chloride solution of step (2) obtained electrolytic salt, It is stirred continuously until being completely dissolved to get lithium/thinly chloride battery electrolyte.
Embodiment 5:
A kind of lithium/thinly chloride battery electrolyte, including thionyl chloride, three oxalic acid lithium phosphates, difluoro dioxalic acid lithium phosphate and add Add agent, the molar concentration of the thionyl chloride solution of electrolytic salt is 1mol/L, and the quality of additive is electrolyte gross mass 0.5%, additive includes the first additive and Second addition, wherein the quality of the first additive is electrolyte gross mass 0.3%, the quality of Second addition is the 0.2% of electrolyte gross mass.
The structural formula of first additive are as follows:
Wherein, X Cl;R1For amido;R2、R3It is tolyl;R4For chloroethyl.
The structural formula of Second addition are as follows:
Wherein, X1For Cl;R11、R21、R31It is chloropropyl;R41For 2- chlorine furans heterocycle.
A kind of preparation method of lithium/thinly chloride battery electrolyte, the preparation method the following steps are included:
(1) under the dry environment of relative humidity≤1%, thionyl chloride is placed in flask, heating is distilled, and collects 80 DEG C Fraction;
(2) under the dry environment of relative humidity≤1%, electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned electrolyte Salt is dissolved in thionyl chloride fraction obtained by step (1), carries out constant volume, obtains the electrolytic salt that molar concentration is 1mol/L Thionyl chloride solution;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, will Leaching liquor is transferred in oscillator, 60min is shaken at 300r/min, then distill to leaching liquor, is removed acetone, is obtained first Additive crude extract finally removes supernatant, the first additive of purifying obtained by drying;The temperature of extraction is 45 DEG C, extraction Time is 4h, and distillation is carried out at 80 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to the mixing for the sodium nitrites and potassium nitrite of quality such as heating is indoor, and fused salt is by feeding inlet Object heats fused salt using the first fused salt heating rod and the second fused salt heating rod, temperature is made to reach 250 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.08KPa behind the door, and the purification of Second addition is completed by 15h;
(5) under relative humidity≤0.5-1% dry environment, the first additive and step of the purifying that step (3) obtains are weighed (4) Second addition of the purifying obtained is then added in the thionyl chloride solution of step (2) obtained electrolytic salt, It is stirred continuously until being completely dissolved to get lithium/thinly chloride battery electrolyte.
Comparative example:
Commercially available lithium/thinly chloride battery electrolyte is using the thionyl chloride solution of tetrachloro-lithium aluminate as electrolyte, and thionyl chloride was both It is solvent is positive active material again, electrolytic salt is tetrachloro-lithium aluminate, lithium salt 1.7mol/L.
Effect example:
Make lithium/thinly chloride battery:
At room temperature by graphite positive electrode, conductive agent carbon black (SP), bonding agent Kynoar (PVDF) according to 8:1:1 ratio Example is homogenized, and solvent is n-methyl-2-pyrrolidone (NMP), and solid content 25% is evenly applied to the aluminium foil of 0.02mm thickness On, by drying, roll-in, cut-parts, carbon electrode film is made;
Anode is used uniformly carbon electrode film, and cathode uses metal lithium electrode, and electrolyte successively uses the embodiment of the present invention 1 to 5 Electrolyte in obtained lithium/thinly chloride battery electrolyte and comparative example produces lithium/thinly chloride battery respectively, 3.87V carries out charge-discharge test with 0.05C circulation 200 weeks, to battery, and test result is shown in Table 1, between 0.025-2C Under any multiplying power, charge-discharge test is carried out to battery, test result is shown in Table 2.
1 battery of table carries out charge-discharge performance test result
From the test data of table 1 it is found that the battery of lithium/thinly chloride battery electrolyte obtained by the embodiment of the present invention 1 to 5 fills After discharge cycles 200 weeks, capacity retention ratio 90% or more, up to 93.7%, electric discharge average voltage be respectively 3.36V, 3.34V, 3.32V, 3.35V, 3.37, and after the battery charging and discharging of comparative example lithium/thinly chloride battery electrolyte recycles 200 weeks, Capacity retention ratio is 76.3%, electric discharge average voltage be 3.12V, the results showed that using lithium obtained by the embodiment of the present invention 1 to 5/ The cycle performance of the battery of thionyl chloride battery electrolyte is better than the battery of comparative example lithium/thinly chloride battery electrolyte, and Voltage delay phenomenon is also obviously improved.
Battery carries out charge-discharge performance test result under 2 different multiplying of table
From the test data of table 2 it is found that the battery of lithium/thinly chloride battery electrolyte obtained by the embodiment of the present invention 1 is put down Platform voltage and capacity are above the platform voltage of the battery of comparative example lithium/thinly chloride battery electrolyte, the results showed that using this The battery of lithium/thinly chloride battery electrolyte obtained by inventive embodiments 1 has good discharge voltage and discharge capacity.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie In the case where without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power Benefit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent elements of the claims Variation is included within the present invention.

Claims (10)

1. a kind of lithium/thinly chloride battery electrolyte, it is characterised in that: described including thionyl chloride, electrolytic salt and additive The molar concentration of the thionyl chloride solution of electrolytic salt is 0.1-1mol/L, and the quality of the additive is electrolyte gross mass 0.01-0.5%。
2. a kind of lithium/thinly chloride battery electrolyte according to claim 1, which is characterized in that the additive includes First additive and Second addition, the structural formula of first additive are as follows:
Wherein, X is halogen;R1For itrile group, amido, hydroxyl or nitro;R2、R3It is hydrogen, monosubstituted or polysubstituted C1-C6 alkane Base, aryl, C1-C6 alkoxy or halogenated C1-C6 alkoxy;R4For C1-C6 alkyl or the C1- being mono-or polysubstituted with halogens C6 alkyl.
3. a kind of lithium/thinly chloride battery electrolyte according to claim 2, which is characterized in that the Second addition Structural formula are as follows:
Wherein, X1For halogen;R11、R21、R31It is C1-C10 alkyl, halogenated C1-C10 alkyl, C1-C10 alkoxy or halogenated C1- C10 alkoxy;R41For it is unsubstituted or or by the alkyl-substituted heterocycle of C1-C6, containing in O, N, S element on the heterocycle It is one or more.
4. a kind of lithium/thinly chloride battery electrolyte according to any one of claim 1 to 3, it is characterised in that: described Electrolytic salt be bis- (fluorine sulphonyl) imine lithiums, di-oxalate lithium borate, trifluoromethanesulfonic acid lithium, three (trimethyl fluoride sulfonyl) lithium methides, One of lithium hexafluoro phosphate, three oxalic acid lithium phosphates, difluoro dioxalic acid lithium phosphate, tetrafluoro oxalic acid lithium phosphate are a variety of.
5. a kind of lithium/thinly chloride battery electrolyte according to claim 4, it is characterised in that: first additive Quality be electrolyte gross mass 0.005-0.3%, the quality of the Second addition is the 0.005- of electrolyte gross mass 0.2%。
6. a kind of preparation method of lithium/thinly chloride battery electrolyte, which is characterized in that the preparation method the following steps are included:
Thionyl chloride is distilled, fraction is collected;
It weighs electrolytic salt to be placed in thionyl chloride fraction obtained by step (1), constant volume obtains the thionyl chloride of electrolytic salt Solution;
The purification of first additive: extracting the first additive using acetone, obtains the first additive leaching liquor, then to leaching Extract is distilled, and the first additive, the first additive of purifying obtained by drying are obtained;
The purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to heating interior by feeding inlet, using the first fused salt heating rod and the second fused salt heating rod to molten Salt is heated;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe behind the door and is vacuumized by vacuum pump, and the purification of Second addition is completed after a period of time;
(5) Second addition for the purifying that the first additive and step (4) for weighing the purifying that step (3) obtains obtain, then It is added in the thionyl chloride solution of step (2) obtained electrolytic salt, is stirred continuously until being completely dissolved to get lithium/Asia Chlorosulfuric acid battery electrolyte.
7. a kind of preparation method of lithium/thinly chloride battery electrolyte according to claim 6, which is characterized in that the system Preparation Method the following steps are included:
(1) thionyl chloride is placed in flask, heating is distilled, and 70-80 DEG C of fraction is collected;
(2) electrolytic salt is weighed, under inert atmosphere conditions, by above-mentioned dissolving electrolyte salt sulfurous obtained by step (1) In acyl chlorides fraction, constant volume is carried out, obtains the thionyl chloride solution for the electrolytic salt that molar concentration is 0.1-1mol/L;
The purification of (3) first additives: extracting the first additive using acetone, obtains the first additive leaching liquor, then Leaching liquor is distilled, the first additive, the first additive of purifying obtained by drying are obtained;The temperature of the extraction is 30- 45 DEG C, the time of the extraction is 1-4h, and the distillation is carried out at 40-80 DEG C by the way of vacuum distillation;
(4) purification of Second addition: the purification of Second addition is purified using sublimation purification device:
(a) fused salt is added to heating interior by feeding inlet, using the first fused salt heating rod and the second fused salt heating rod to molten Salt is heated, and temperature is made to reach 200-250 DEG C;
(b) Second addition is fitted into distillation charging boat, in Second addition upper berth silica gel, is then placed in cylindrical tube, closes Closed end passes through vacuum cooled pipe by vacuum pump suction to 0.03-0.08KPa behind the door, completes Second addition by 6-15h Purification;
The Second addition for the purifying that the first additive and step (4) for weighing the purifying that step (3) obtains obtain, is then added Into the thionyl chloride solution of step (2) obtained electrolytic salt, it is stirred continuously until being completely dissolved to get lithium/thionyl Chlorine battery electrolyte.
8. a kind of preparation method of lithium/thinly chloride battery electrolyte according to claim 6 or 7, it is characterised in that: institute Stating fused salt in step (a) sodium nitrite of quality and the mixture of potassium nitrite such as is.
9. a kind of preparation method of lithium/thinly chloride battery electrolyte according to claim 8, it is characterised in that: described Leaching liquor is transferred in oscillator before distillation by step in (3), shakes 30-60min at 100-300r/min.
10. a kind of preparation method of lithium/thinly chloride battery electrolyte according to claim 9, it is characterised in that: described Step (1), step (2) and step (3) are operated in relative humidity≤0.5-1% dry environment.
CN201811570609.7A 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte and preparation method thereof Active CN109742446B (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN201811570609.7A CN109742446B (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte and preparation method thereof
CN202010736012.6A CN112072177A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte
CN202010737131.3A CN112072178A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811570609.7A CN109742446B (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte and preparation method thereof

Related Child Applications (2)

Application Number Title Priority Date Filing Date
CN202010736012.6A Division CN112072177A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte
CN202010737131.3A Division CN112072178A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte

Publications (2)

Publication Number Publication Date
CN109742446A true CN109742446A (en) 2019-05-10
CN109742446B CN109742446B (en) 2020-09-08

Family

ID=66360901

Family Applications (3)

Application Number Title Priority Date Filing Date
CN202010737131.3A Pending CN112072178A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte
CN201811570609.7A Active CN109742446B (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte and preparation method thereof
CN202010736012.6A Pending CN112072177A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN202010737131.3A Pending CN112072178A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN202010736012.6A Pending CN112072177A (en) 2018-12-21 2018-12-21 Lithium/thionyl chloride battery electrolyte

Country Status (1)

Country Link
CN (3) CN112072178A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115863534A (en) * 2022-12-29 2023-03-28 武汉昊诚锂电科技股份有限公司 Lithium-ion battery positive plate and preparation device and preparation process thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4307160A (en) * 1980-12-17 1981-12-22 The United States Of America As Represented By The Secretary Of The Navy Lithium-thionyl chloride battery with niobium pentachloride electrolyte
US4309490A (en) * 1976-10-08 1982-01-05 Honeywell Inc. Long life thionyl chloride cell
US4355086A (en) * 1981-10-01 1982-10-19 Honeywell Inc. Lithium thionyl chloride battery
CN101102000A (en) * 2007-07-17 2008-01-09 中国地质大学(武汉) Lithium thionyl chloride battery electrolyte and its making method
CN104835971A (en) * 2015-03-25 2015-08-12 武汉孚安特科技有限公司 A preparing method of an electrolyte of a lithium-thionyl chloride cell
CN106129467A (en) * 2016-08-31 2016-11-16 襄阳艾克特电池科技股份有限公司 A kind of lithium thionyl chloride battery electrolyte manufacture method
CN106169608A (en) * 2016-08-31 2016-11-30 襄阳艾克特电池科技股份有限公司 A kind of lithium thionyl chloride battery electrolyte manufacture method

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4309490A (en) * 1976-10-08 1982-01-05 Honeywell Inc. Long life thionyl chloride cell
US4307160A (en) * 1980-12-17 1981-12-22 The United States Of America As Represented By The Secretary Of The Navy Lithium-thionyl chloride battery with niobium pentachloride electrolyte
US4355086A (en) * 1981-10-01 1982-10-19 Honeywell Inc. Lithium thionyl chloride battery
CN101102000A (en) * 2007-07-17 2008-01-09 中国地质大学(武汉) Lithium thionyl chloride battery electrolyte and its making method
CN104835971A (en) * 2015-03-25 2015-08-12 武汉孚安特科技有限公司 A preparing method of an electrolyte of a lithium-thionyl chloride cell
CN106129467A (en) * 2016-08-31 2016-11-16 襄阳艾克特电池科技股份有限公司 A kind of lithium thionyl chloride battery electrolyte manufacture method
CN106169608A (en) * 2016-08-31 2016-11-30 襄阳艾克特电池科技股份有限公司 A kind of lithium thionyl chloride battery electrolyte manufacture method

Also Published As

Publication number Publication date
CN112072177A (en) 2020-12-11
CN109742446B (en) 2020-09-08
CN112072178A (en) 2020-12-11

Similar Documents

Publication Publication Date Title
CN105826607B (en) A kind of electrolyte and the lithium ion battery including the electrolyte
CN108306048A (en) A kind of lithium-ion battery electrolytes and its lithium ion battery of preparation
CN106356562A (en) Electrolyte for ternary cathode material lithium ion battery and ternary cathode material lithium ion battery
CN105731399A (en) Preparation method of difluoro-sulfonyl imide lithium
JP2018530852A (en) Electrolytic solution for high voltage lithium ion battery, its preparation method and its application
CN106058319B (en) One kind has the electrolyte and the preparation method and application thereof of polyanionic functional group
CN105390742A (en) High-voltage lithium-ion battery electrolyte as well as preparation method and application thereof
CN103560270B (en) A kind of electrolyte for lithium ion battery
CN107011371A (en) A kind of siliceous glyoxaline ion liquid and its preparation method and application
CN103035947A (en) Novel electrolyte of lithium-ion battery and preparation method thereof
CN107845831B (en) A kind of electrolyte for lithium-sulfur cell
CN106129473A (en) A kind of nonaqueous electrolytic solution of silicon-based anode lithium ion battery
CN108281700A (en) A kind of electrolyte and preparation method with use the secondary lithium-sulfur battery of the electrolyte
WO2023217091A1 (en) Electrolyte additive, battery electrolyte and use thereof
CN107819152A (en) A kind of reference electrolyte and preparation method that can improve lithium-sulfur cell cycle performance
CN103539168B (en) The purification process of lithium hexafluoro phosphate
Liu et al. Research progress on preparation and purification of fluorine-containing chemicals in lithium-ion batteries
CN105449139A (en) Method for solving high-temperature flatulence of lithium titanate negative lithium-ion battery
CN109742446A (en) A kind of lithium/thinly chloride battery electrolyte and preparation method thereof
CN107180998B (en) A kind of electrolyte and lithium ion battery
CN103996873B (en) The lithium ion battery nonaqueous electrolytic solution of coupling BTR918 graphite cathode
CN110627742B (en) Preparation method and purification method of compound containing at least one cyclic ligand structure
CN108767315A (en) A kind of electrolysis additive, lithium battery electrolytes and lithium ion battery
CN105633463B (en) A kind of electrolyte of lithium-ion secondary battery suitable for low temperature environment electric discharge
CN109346763B (en) Electrolyte and lithium ion battery

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information

Address after: 215000 LongLi and Building 1201, No. 59 Suli Road, Wuzhong District, Suzhou City, Jiangsu Province

Applicant after: Pei Guanghua

Address before: 325600 Xuyang Road, Yueqing City, Wenzhou City, Zhejiang Province, Confidence in Platinum Bay 1205

Applicant before: Pei Guanghua

CB02 Change of applicant information
TA01 Transfer of patent application right

Effective date of registration: 20200812

Address after: 325600 No.531 Danxia Road, Leqing City, Wenzhou City, Zhejiang Province

Applicant after: YUEQING HUAZUN ELECTRIC Co.,Ltd.

Address before: 215000 LongLi and Building 1201, No. 59 Suli Road, Wuzhong District, Suzhou City, Jiangsu Province

Applicant before: Pei Guanghua

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20220811

Address after: No. 66, Xingyu Road, Haiyu Town, Changshu City, Suzhou City, Jiangsu Province 215000

Patentee after: Jiangsu Zhongluman New Material Technology Co., Ltd.

Address before: 325600 No.531 Danxia Road, Yueqing City, Wenzhou City, Zhejiang Province

Patentee before: YUEQING HUAZUN ELECTRIC Co.,Ltd.

TR01 Transfer of patent right