CN104167534B - A kind of method preparing cylinder 18650 lithium ion battery - Google Patents

A kind of method preparing cylinder 18650 lithium ion battery Download PDF

Info

Publication number
CN104167534B
CN104167534B CN201410383412.8A CN201410383412A CN104167534B CN 104167534 B CN104167534 B CN 104167534B CN 201410383412 A CN201410383412 A CN 201410383412A CN 104167534 B CN104167534 B CN 104167534B
Authority
CN
China
Prior art keywords
technological parameter
lithium ion
battery core
constant
ion battery
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.)
Active
Application number
CN201410383412.8A
Other languages
Chinese (zh)
Other versions
CN104167534A (en
Inventor
邓纶浩
刘国壮
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.)
Guangxi Zhuo Neng New Energy Technology Co Ltd
Original Assignee
Guangxi Zhuo Neng New Energy Technology Co Ltd
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 Guangxi Zhuo Neng New Energy Technology Co Ltd filed Critical Guangxi Zhuo Neng New Energy Technology Co Ltd
Priority to CN201410383412.8A priority Critical patent/CN104167534B/en
Publication of CN104167534A publication Critical patent/CN104167534A/en
Application granted granted Critical
Publication of CN104167534B publication Critical patent/CN104167534B/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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1391Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Abstract

The invention discloses a kind of method preparing cylinder 18650 lithium ion battery, battery core positive electrode is made up of following raw material by mass percentage: nickel cobalt lithium aluminate 95.5-98.8%, electrically conductive graphite 0-0.5%, conductive agent 0.5-2%, Kynoar 0.7-2.0%;Battery core negative material is made up of following raw material by mass percentage: graphite 94.5-97.5%, conductive carbon black 0-1.0%, sodium carboxymethyl cellulose 1-2%, butadiene-styrene rubber 1.5-2.5%.The preparation method of cylinder 18650 lithium ion battery that the present invention provides, there is low cost, capacity height 2800mAh, the feature of cycle performance superior (200 weeks conservation rates more than 80% of 0.5/0.5C), and the method there is the feature that efficiency is high and energy consumption is low that solvent usage amount is few, be coated with.

Description

A kind of method preparing cylinder 18650 lithium ion battery
Technical field
The invention belongs to technical field of lithium ion, relate to a kind of cylinder 18650 lithium-ion electric The preparation method in pond.
Background technology
At present, the positive electrode of 18650-2800mAh model capacity battery core mostly uses gram volume 165mAh/g (voltage bound 4.35-2.75V), compactness 4.2g/cm3Cobalt acid lithium series Lithium-ion electric core, because the granule-morphology of cobalt acid lithium material and molecular structure property determine its Gram volume and compactness, existing material, in 18650 models of regulation, passes through lithium cobaltate cathode Compacting and the allotment of gram volume can produce the cylindrical electrical core of 2800mAh capacity;And in order to Reducing cost, part producer, in cobalt acid lithium, adds gram volume 175mAh/g, and (voltage is upper and lower Limit 4.35-2.75V), compactness is 3.9g/cm3Ternary material can also manufacture 2800mAh The cylindrical electrical core of capacity;But being because the restriction in model space, existing positive electrode can only be to make With pure cobalt acid lithium or mixing ternary manufacture.And use cobalt acid lithium or cobalt acid lithium to add ternary material and make Battery core for positive electrode has a disadvantage in that cost height, capacity low (2750mAh)), Cycle performance poor (100 weeks conservation rates more than 80% of 0.5/0.5C).
Summary of the invention
For the deficiencies in the prior art, an object of the present invention aims to provide a kind of cylinder 18650 lithium ion batteries, it has low cost, capacity high (2800mAh), cycle performance The feature of superior (200 weeks conservation rates more than 80% of 0.5/0.5C).
The two of the purpose of the present invention aim to provide the preparation of a kind of cylinder 18650 lithium ion battery Method, the method has the feature that efficiency is high and energy consumption is low that solvent usage amount is few, be coated with.
Realize the purpose of the present invention to reach by adopting the following technical scheme that:
A kind of method preparing cylinder 18650 lithium ion battery, the positive electrode of battery core be by by The following raw material composition of mass percent: nickel cobalt lithium aluminate 95.5-98.8%, electrically conductive graphite 0-0.5%, does not include other conductive agent 0.5-2% of electrically conductive graphite, Kynoar 0.7-2.0%, it is characterised in that sequentially include the following steps:
1) weigh raw material according to the formulation ratio of positive electrode and negative material, pass through double-planet Positive electrode, negative material are fabricated to anode sizing agent and cathode size by beater respectively;Wherein, Technological parameter: revolution 50Rpm, rotation 1700Rpm, time 3H;
2) use gap coating machine, anode sizing agent is coated on aluminium foil and makes water content < 0.12% Positive plate, cathode size is coated on Copper Foil and makes water content < 0.4% negative plate;Wherein, Technological parameter: temperature is set in 100-115 DEG C, speed 7-10 rice/min;
3) in humidity, < 60%RH, first by both positive and negative polarity pole piece difference in the environment of temperature 25 ± 5 DEG C After cutting and be welded into positive pole ear, negative lug, then with up-coiler by barrier film, anode pole piece, Cathode pole piece is wound into core, after outward appearance and short-circuit detecting are qualified, by upper insulating trip, volume After core, lower insulating trip stacking, be placed into a diameter of 18 ± 0.4mm, height is 68 ± 0.5mm Box hat, by inversion bonding machine, negative lug is weldingly connected with box hat, after slot rolling, Enter baking oven, under conditions of 85 ± 10 DEG C, toast 30 ± 10H, more entirely examine short circuit, qualified products Proceed to humidity < 2%RH, temperature 25 ± 5 DEG C glove box in, inject 5.3 ± 0.5g electrolyte, By on Laser Welding welding positive pole ear to block, then buckle well block and send into full envelope to box hat It is machined to 18650 standard battery cell of diameter 18mm, highly 65mm;
4) after 18650 standard battery cell being cleaned painting antirust oil, then 18650 standard battery cell are existed In the environment of temperature 25-45 DEG C after aging 36H, on be melted on formation cabinet, after terminating, By battery core first in the environment of temperature 40 ± 5 DEG C aging three days, then temperature 25 ± 5 DEG C Under environment aging four days, ageing process is wrapped PET, is then become by matching machine screening battery core Different voltage internal resistance class, by qualified battery core partial volume, finally by capacity > 2820mAh, FQC Outward appearance entirely examine qualified after battery core, prepare according to capacity 10mAh, voltage 3mV, internal resistance 2m Ω Group, OQC examines qualified rear shipment entirely.
The formulation Design Principle of positive electrode:
1, during the effect of nickel cobalt lithium aluminate is battery core charge and discharge process, the composition of lithium ion is produced, Embody the material of battery core capacity;Regulation is to reserve enough ratios in 95.5-98.8% scope Example is to conductive agent and binding agent, and less than 95.5, battery core capacity is difficult to design and reaches 2800, greatly Big in the 98.8 easy sheddings of battery core pole piece or battery core internal resistance.
2, the effect of electrically conductive graphite be pole piece to roller during, soften pole piece.Regulation is at 0-0.5% Scope, is to effectively pole piece toughness be improved with it more than 0, but more than 0.5 impact The design of battery core capacity, and battery core pole piece toughness also will not increase with its dosage and change.
3, the effect of conductive agent is to play conduction electronic action in pole piece.Regulation is at 0.5-2.0% Scope, setting value reduces the internal resistance of pole piece more than 0.5 for sufficient conductive agent, gives full play to Active matter gram volume, is to reserve more space to active matter less than 2, and increases dosage also It is helpless to active matter gram volume play.
4, Kynoar effect is binding agent, is attached on by positive electrode on long-pending fluid aluminium foil Face.Specifying in 0.7-2.0% scope, design load is the binding agent in order to there be abundance more than 0.7 Material above is sticked to above aluminium foil, it is ensured that processing characteristics and the material capacity of pole piece are sent out Wave, less than 2 in order to reserve more space to active matter, and increase dosage and be also helpless to active matter Gram volume plays, and also can increase battery core internal resistance, affect battery core volumetric properties.
Preferably, its negative material is made up of following raw material by mass percentage: graphite 94.5-97.5%, conductive carbon black 0-1.0%, sodium carboxymethyl cellulose 1-2%, butadiene-styrene rubber 1.5-2.5%.
Preferably, in step 1) positive electrode formula in independent add that to account for positive electrode total The oxalic acid of the 0.1-1% of amount.The alkalescence of ternary can be neutralized, reduce slurry water suction, strengthen slurry The mobility of material, promotes the stability of coating, ensures the Capacity uniformity of battery core, grass after coating Acid decomposes, does not affect material prescription ratio and the combination property of battery core.
Preferably, step 4) in, the technological parameter of chemical conversion is as follows: upper voltage limit: 4350mV, Constant current: 140mA, time: 120min;Upper voltage limit: 4350mV, constant current constant voltage: 560mA, Time: 420min, terminates electric current: 28mA.
Preferably, step 4) in, also include that the processing procedure singly filled is as follows:
The first step: constant-current constant-voltage charging, technological parameter is: upper voltage limit 4350mV, electric current 1700mA, time 300min, terminate electric current 28mA;
Second step: shelve, technological parameter is: time 5min;
3rd step: constant-current discharge, technological parameter is: lower voltage limit 2750mV, discharge current 1400mA, time 150min;
4th step: shelve, technological parameter is: time 5min;
5th step: constant-current charge, technological parameter is: upper voltage limit 4350mV, electric current 1400mA, Time 40min
6th step: constant-current charge, technological parameter is: upper voltage limit 4350mV, electric current 560mA, Time 20min.
Preferably, step 3) in, described block be 17.5*3.9mm containing PTC and CID Block.
The beneficial effects of the present invention is:
1, the present invention is reformed by formula and ternary improved properties is (by promoting nickel cobalt lithium aluminate Gram volume is to 192mAh/g (voltage bound 4.35-2.75V), compactness to 3.6g/cm3)。 Existing cobalt acid lithium or cobalt acid lithium are added the high cost of ternary, capacity low (2750mAh), circulation The positive pole system of poor performance (100 weeks conservation rates more than 80% of 0.5/0.5C), replaces with completely Pure ternary (nickel cobalt lithium aluminate) low cost, capacity high (2800mAh), cycle performance are superior The positive pole system of (200 weeks conservation rates more than 80% of 0.5/0.5C), negative pole graphite (active matter Main material) content is substantially improved 95.5% by original 93.8%, and so can be in 18650 models Load more active component in the space that battery core is quantitative and make the battery core of more capacity, and battery core Performance meet national requirements.Therefore, the present invention is by 18650-2800mAh model capacity lithium The capacity of ion battery battery core is risen to by existing 0.2/0.2C dischargeable capacity 2750mAh More than 2800mAh, cycle performance superior (200 weeks conservation rates more than 80% of 0.5/0.5C). Because the unit price of nickel cobalt aluminum is: 180,000 yuan/ton, gram volume is: 192mAh/g;Cobalt acid Lithium unit price is: 18.5 ten thousand yuan/ton, and gram volume is: 165mAh/g;According to the 2800mAh set, Polynary cost is 2.62 yuan/PCS, and cobalt acid lithium cost is: 3.14 yuan/PCS.Every price is raw Produce cost and reduce by more than 0.5 yuan.
2, in the preparation method of the present invention, the solvent usage amount of dispensing, by original 33%, reduces To 30%, (slurry solvent content reduces the improved efficiency 3% of coating, and during coating, pole piece is easily done Dry), coating temperature, by original average 120 DEG C, is reduced to present 115 DEG C, and energy consumption drops Low by 4%.In step 1 in the preparation method of the present invention) positive electrode formula in independent add Account for the oxalic acid of the 0.1-1% of positive electrode total amount, the alkalescence of ternary can be neutralized, reduce slurry Water suction, the mobility of enhancing slurry, promote the stability of coating, ensures that the capacity of battery core is consistent Property, oxalic acid decomposes after coating, do not affect material prescription ratio and the combination property of battery core.
Detailed description of the invention
Below in conjunction with embodiment, the present invention is illustrated
Embodiment 1:
A kind of method preparing cylinder 18650 lithium ion battery, including be made up of positive electrode Positive plate and the negative plate being made up of negative material.
Its positive electrode is made up of following raw material by mass percentage: nickel cobalt lithium aluminate 96.8%, electrically conductive graphite 0.30%, conductive agent 1.40%, Kynoar (PVDF) 1.50%.
Its negative material is made up of following raw material by mass percentage: graphite 95.5%, SP (conductive carbon black) 1.0%, CMC (sodium carboxymethyl cellulose) 1.5%, SBR (fourth Benzene rubber) 2.0%.
Described conductive agent is CNT (CNT), CNC (carbon nano tube compound material) or SP (conductive carbon black).Described electrically conductive graphite is KS-6 (crystalline flake graphite).
Prepare specifically comprising the following steps that of cylinder 18650 lithium ion battery
1) raw material is weighed according to the formulation ratio of above-mentioned positive electrode and negative material, by double Positive electrode, negative material are fabricated to anode sizing agent and cathode size by planet beater respectively; Wherein, technological parameter: revolution 50Rpm, rotation 1700Rpm, time 3H;
2) use gap coating machine, anode sizing agent is coated on aluminium foil and makes water content < 0.12% Positive plate, cathode size is coated on Copper Foil and makes water content < 0.4% negative plate;Wherein, Technological parameter: temperature is set in 100-115 DEG C, speed 7-10 rice/min;
3) in humidity, < 60%RH, first by both positive and negative polarity pole piece difference in the environment of temperature 25 ± 5 DEG C After cutting and be welded into positive pole ear, negative lug, (the most extremely aluminium strip, negative pole is nickel strap or plating Nickel steel band), then with up-coiler, barrier film, anode pole piece, cathode pole piece are wound into core, will After outward appearance and short-circuit detecting are qualified, after upper insulating trip, core, lower insulating trip stacking, It is placed into the box hat of a diameter of 18 ± 0.4mm, highly 68 ± 0.5mm, by inversion bonding machine Negative lug is weldingly connected with box hat, after slot rolling, enters baking oven, at 85 ± 10 DEG C Under the conditions of toast 40H, more entirely examine short circuit, qualified products proceed to humidity < 2%RH, temperature 25 ± 5 DEG C Glove box in, inject 5.3 ± 0.5g electrolyte, by Laser Welding welding positive pole ear to cover On cap, described block is the block containing PTC and CID of 17.5*3.9mm, then buckles well lid Cap is machined to 18650 standard electric of diameter 18mm, highly 65mm to the full envelope of feeding on box hat Core;
4) after 18650 standard battery cell being cleaned painting antirust oil, then 18650 standard battery cell are existed In the environment of temperature 25-45 DEG C after aging 36H, on be melted on formation cabinet, after terminating, By battery core first in the environment of temperature 40 ± 5 DEG C aging three days, then temperature 25 ± 5 DEG C Under environment aging four days, ageing process is wrapped PET, is then become by matching machine screening battery core Different voltage internal resistance class, by qualified battery core partial volume, finally by capacity > 2820mAh, FQC Outward appearance entirely examine qualified after battery core, prepare according to capacity 10mAh, voltage 3mV, internal resistance 2m Ω Group, OQC examines qualified rear shipment entirely.
In step 1) positive electrode formula in independent interpolation account for positive electrode total amount The oxalic acid of 0.1-0.5%.The alkalescence of ternary can be neutralized, reduce slurry water suction, strengthen slurry Mobility, promotes the stability of coating, ensures the Capacity uniformity of battery core, and after coating, oxalic acid is subject to Thermal decomposition, does not affect material prescription ratio and the combination property of battery core.
Step 4) technological parameter of described chemical conversion is as follows: the technological parameter of chemical conversion is as follows: the upper limit Voltage: 4350mV, constant current: 140mA, time: 120min;Upper voltage limit: 4350mV, Constant current constant voltage: 560mA, time: 420min, terminate electric current: 28mA.
Step 4) the described processing procedure singly filled is as follows:
The first step: constant-current constant-voltage charging, technological parameter is: upper voltage limit 4350mV, electric current 1700mA, time 300min, terminate electric current 28mA;
Second step: shelve, technological parameter is: time 5min;
3rd step: constant-current discharge, technological parameter is: lower voltage limit 2750mV, discharge current 1400mA, time 150min;
4th step: shelve, technological parameter is: time 5min;
5th step: constant-current charge, technological parameter is: upper voltage limit 4350mV, electric current 1400mA, Time 40min
6th step: constant-current charge, technological parameter is: upper voltage limit 4350mV, electric current 560mA, Time 20min.
Preferably, step 3) described block is the lid containing PTC and CID of 17.5*3.9mm Cap.
Embodiment 2:
The feature of the present embodiment is:
Its positive electrode is made up of following raw material by mass percentage: nickel cobalt lithium aluminate 98.8%, electrically conductive graphite 0%, conductive agent 0.5%, Kynoar (PVDF) 0.7%.
Its negative material is made up of following raw material by mass percentage: graphite 97.5%, SP (conductive carbon black) 0%, CMC (sodium carboxymethyl cellulose) 1%, SBR (butylbenzene rubber Glue) 1.5%.
Other are same as in Example 1.
Embodiment 3:
The feature of the present embodiment is:
Its positive electrode is made up of following raw material by mass percentage: nickel cobalt lithium aluminate 95.5%, electrically conductive graphite 0.5%, conductive agent 2%, Kynoar (PVDF) 2.0%.
Its negative material is made up of following raw material by mass percentage: graphite 94.5%, SP (conductive carbon black) 1.0%, CMC (sodium carboxymethyl cellulose) 2%, SBR (butylbenzene Rubber) 2.5%.
Other are same as in Example 1.
Embodiment 4:
The feature of the present embodiment is:
Its positive electrode is made up of following raw material by mass percentage: nickel cobalt lithium aluminate 95.9%, electrically conductive graphite 0.1%, conductive agent 2%, Kynoar (PVDF) 2.0%.
Its negative material is made up of following raw material by mass percentage: graphite 94.9%, SP (conductive carbon black) 0.1%, CMC (sodium carboxymethyl cellulose) 2%, SBR (butylbenzene Rubber) 2.5%.
Other are same as in Example 1.
Comparative example 1:
The positive electrode of conventional 18650-2800mAh model capacity battery core and negative material Concrete formula is shown in Table 1.
Table 1 conventional cathode material and the formula table of negative material
By above contrast embodiments of the invention 1 and comparative example 1, prove the present invention clearly Embodiment 1 formula positive pole ternary (nickel cobalt lithium aluminate) content is substantially improved by original 94% To 97.4%, reformed by formula and ternary improved properties (gram volume promotes, and compacting strengthens) Existing cobalt acid lithium or cobalt acid lithium are added the high cost of ternary, capacity low (2750mAh), circulation The positive pole system of poor performance (100 weeks conservation rates more than 80% of 0.5/0.5C), replaces with completely Pure ternary (nickel cobalt lithium aluminate) low cost, capacity high (2800mAh), cycle performance are superior The positive pole system of (200 weeks conservation rates more than 80% of 0.5/0.5C), negative pole graphite (active matter Main material) content is substantially improved 95.5% by original 93.8%, and so can be in 18650 models Load more active component in the space that battery core is quantitative and make the battery core of more capacity, and battery core Performance meet national requirements.
Above-described embodiment is only currently preferred case study on implementation, it is impossible to limit the present invention with this Scope required for protection, it is any that those skilled in the art is done on the basis of the present invention Unsubstantiality and replace belong to the scope of protection of present invention.

Claims (6)

1. the method preparing cylinder 18650 lithium ion battery, the positive electrode of battery core be by Following raw material composition by mass percentage: nickel cobalt lithium aluminate 95.5-98.8%, electrically conductive graphite 0-0.5%, does not include other conductive agent 0.5-2% of electrically conductive graphite, Kynoar 0.7-2.0%, it is characterised in that sequentially include the following steps:
1) weigh raw material according to the formulation ratio of positive electrode and negative material, pass through double-planet Positive electrode, negative material are fabricated to anode sizing agent and cathode size by beater respectively;Wherein, Technological parameter: revolution 50Rpm, rotation 1700Rpm, time 3H;
2) use gap coating machine, anode sizing agent is coated on aluminium foil and makes water content < 0.12% Positive plate, cathode size is coated on Copper Foil and makes water content < 0.4% negative plate;Wherein, Technological parameter: temperature is set in 100-115 DEG C, speed 7-10 rice/min;
3) in humidity, < 60%RH, first by both positive and negative polarity pole piece difference in the environment of temperature 25 ± 5 DEG C After cutting and be welded into positive pole ear, negative lug, then with up-coiler by barrier film, anode pole piece, Cathode pole piece is wound into core, after outward appearance and short-circuit detecting are qualified, by upper insulating trip, volume After core, lower insulating trip stacking, be placed into a diameter of 18 ± 0.4mm, height is 68 ± 0.5mm Box hat, by inversion bonding machine, negative lug is weldingly connected with box hat, after slot rolling, Enter baking oven, under conditions of 85 ± 10 DEG C, toast 30 ± 10H, more entirely examine short circuit, qualified products Proceed to humidity < 2%RH, temperature 25 ± 5 DEG C glove box in, inject 5.3 ± 0.5g electrolyte, By on Laser Welding welding positive pole ear to block, then buckle well block and send into full envelope to box hat It is machined to 18650 standard battery cell of diameter 18mm, highly 65mm;
4) after 18650 standard battery cell being cleaned painting antirust oil, then 18650 standard battery cell are existed In the environment of temperature 25-45 DEG C after aging 36H, on be melted on formation cabinet, after terminating, By battery core first in the environment of temperature 40 ± 5 DEG C aging three days, then temperature 25 ± 5 DEG C Under environment aging four days, ageing process is wrapped PET, is then become by matching machine screening battery core Different voltage internal resistance class, by qualified battery core partial volume, finally by capacity > 2820mAh, FQC Outward appearance entirely examine qualified after battery core, prepare according to capacity 10mAh, voltage 3mV, internal resistance 2m Ω Group, OQC examines qualified rear shipment entirely.
The method preparing cylinder 18650 lithium ion battery the most according to claim 1, its It is characterised by: its negative material is made up of following raw material by mass percentage: graphite 94.5-97.5%, conductive carbon black 0-1.0%, sodium carboxymethyl cellulose 1-2%, butadiene-styrene rubber 1.5-2.5%.
The method preparing cylinder 18650 lithium ion battery the most according to claim 1, its Be characterised by: in step 1) positive electrode formula in independent interpolation account for positive electrode total amount The oxalic acid of 0.1-1%.
The method preparing cylinder 18650 lithium ion battery the most according to claim 1, its It is characterised by: step 4) in, the technological parameter of chemical conversion is as follows: upper voltage limit: 4350mV, Constant current: 140mA, time: 120min;Upper voltage limit: 4350mV, constant current constant voltage: 560mA, Time: 420min, terminates electric current: 28mA.
The method preparing cylinder 18650 lithium ion battery the most according to claim 1, its It is characterised by: step 4) in, also include that the processing procedure singly filled is as follows:
The first step: constant-current constant-voltage charging, technological parameter is: upper voltage limit 4350mV, electric current 1700mA, time 300min, terminate electric current 28mA;
Second step: shelve, technological parameter is: time 5min;
3rd step: constant-current discharge, technological parameter is: lower voltage limit 2750mV, discharge current 1400mA, time 150min;
4th step: shelve, technological parameter is: time 5min;
5th step: constant-current charge, technological parameter is: upper voltage limit 4350mV, electric current 1400mA, Time 40min
6th step: constant-current charge, technological parameter is: upper voltage limit 4350mV, electric current 560mA, Time 20min.
The method preparing cylinder 18650 lithium ion battery the most according to claim 1, its Be characterised by: step 3) in, described block be 17.5*3.9mm containing PTC's and CID Block.
CN201410383412.8A 2014-08-06 2014-08-06 A kind of method preparing cylinder 18650 lithium ion battery Active CN104167534B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410383412.8A CN104167534B (en) 2014-08-06 2014-08-06 A kind of method preparing cylinder 18650 lithium ion battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410383412.8A CN104167534B (en) 2014-08-06 2014-08-06 A kind of method preparing cylinder 18650 lithium ion battery

Publications (2)

Publication Number Publication Date
CN104167534A CN104167534A (en) 2014-11-26
CN104167534B true CN104167534B (en) 2016-08-17

Family

ID=51911262

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410383412.8A Active CN104167534B (en) 2014-08-06 2014-08-06 A kind of method preparing cylinder 18650 lithium ion battery

Country Status (1)

Country Link
CN (1) CN104167534B (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104900921A (en) * 2015-04-03 2015-09-09 深圳市博力康电池有限公司 Technology for producing high magnification power cylinder lithium ion battery
CN105185986A (en) * 2015-08-14 2015-12-23 江苏腾方新能源科技有限公司 High-capacity cylindrical 18650 lithium-ion battery and preparation method thereof
CN105261796A (en) * 2015-09-23 2016-01-20 深圳市博力康电池有限公司 Preparation method of quickly fully-charged cylindrical power lithium-ion battery cell
CN105336961A (en) * 2015-11-30 2016-02-17 四川北方硝化棉股份有限公司 Lithium battery anode and preparation method thereof
CN106252569B (en) * 2016-08-31 2019-03-01 天津市捷威动力工业有限公司 A kind of high volume energy density extended-life lithium ion battery of high voltage and preparation method thereof
CN107037365A (en) * 2016-11-16 2017-08-11 上海中兴派能能源科技股份有限公司 A kind of measuring method of power lithium cell electric core
CN108054425B (en) * 2017-12-09 2020-02-21 珠海聚碳复合材料有限公司 Preparation method of novel high-rate ternary nickel-cobalt-aluminum power battery
CN108258236B (en) * 2018-01-15 2021-04-30 江西省汇亿新能源有限公司 18650 cylindrical lithium battery with high specific capacity and long cycle life and preparation method thereof
CN108281639A (en) * 2018-01-31 2018-07-13 山东德朗能新能源科技有限公司 A kind of long-life nickle cobalt lithium manganate cylindrical lithium ion battery production method
CN109860510A (en) * 2019-01-16 2019-06-07 广西师范大学 A kind of nickle cobalt lithium manganate physical mixed lithium manganese phosphate is the battery preparation method of positive electrode
CN112599840A (en) * 2020-12-14 2021-04-02 广西卓能新能源科技有限公司 High-rate and high-specific-energy lithium ion battery and preparation method thereof
CN114864874B (en) * 2022-05-12 2024-03-12 陈钦湘 Preparation method of positive plate of lithium battery, positive plate and lithium ion battery

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101399368A (en) * 2007-09-24 2009-04-01 董兴国 Electric core used for secondary lithium battery and preparation
CN102185157A (en) * 2011-03-22 2011-09-14 宁波海锂子新能源有限公司 Production process of waterborne positive lithium ion battery
CN103151513A (en) * 2013-03-13 2013-06-12 山东神工海特电子科技有限公司 High-performance ternary power battery and preparation method of high-performance ternary power battery
CN103682415A (en) * 2012-09-19 2014-03-26 万向电动汽车有限公司 High-energy-density lithium ion battery and preparation technology thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101399368A (en) * 2007-09-24 2009-04-01 董兴国 Electric core used for secondary lithium battery and preparation
CN102185157A (en) * 2011-03-22 2011-09-14 宁波海锂子新能源有限公司 Production process of waterborne positive lithium ion battery
CN103682415A (en) * 2012-09-19 2014-03-26 万向电动汽车有限公司 High-energy-density lithium ion battery and preparation technology thereof
CN103151513A (en) * 2013-03-13 2013-06-12 山东神工海特电子科技有限公司 High-performance ternary power battery and preparation method of high-performance ternary power battery

Also Published As

Publication number Publication date
CN104167534A (en) 2014-11-26

Similar Documents

Publication Publication Date Title
CN104167534B (en) A kind of method preparing cylinder 18650 lithium ion battery
CN104022278B (en) A kind of cylindrical lithium ion battery battery core and preparation method thereof
CN102354751B (en) Formula and preparation method of high energy storage lead-acid battery lead paste
CN106129365A (en) A kind of high security iron manganese phosphate lithium battery
CN105226285B (en) A kind of porous Si-C composite material and preparation method thereof
CN102324494B (en) Lithium iron phosphate / nano-powder tube oxide composite cathode material and preparation method thereof
CN102104144B (en) Method for preparing lithium iron phosphate compound anode material
CN105845928A (en) Lithium-ion power battery and preparation method thereof
WO2016206548A1 (en) Preparation method for lithium battery high-voltage modified negative electrode material
CN110600696A (en) Quick-charging type long-circulation cylindrical lithium ion battery with high low-temperature discharge capacity
CN105932253B (en) SiO2@SnO2Clad structure ion cathode material lithium and its preparation method and application
CN103682304A (en) Lithium-rich solid solution anode composite and preparation method thereof, lithium ion battery anode plate and lithium ion battery
CN108461804A (en) A kind of 18650-3800mAh lithium batteries and preparation method thereof
CN103928668B (en) Lithium ion battery and preparation method of anode material thereof
CN103682415A (en) High-energy-density lithium ion battery and preparation technology thereof
WO2024087388A1 (en) Secondary battery and electrical device
WO2024087383A1 (en) Secondary battery and electric device
CN102299365B (en) Lithium ion battery preventing overdischarge and battery pack thereof
CN103531776B (en) The lithium ion battery and its positive electrode and chemical synthesizing method of high security extra long life
CN105513827B (en) A kind of (LMO NCM AC)/(LTO AC) hybrid battery capacitance electrode material and electrode slice
CN103022417A (en) Anode material of lithium-ion cell
CN104157877A (en) Lithium ion battery electrical core and preparation method thereof
CN106784992A (en) A kind of power lithium titanate battery and preparation method thereof
CN102227031A (en) Lithium ion battery with high-rate discharge characteristic
WO2023087209A1 (en) Electrochemical device and electronic device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant