WO2003077348A1 - A rechargeable lithium-ion power battery and manufacture method of the same - Google Patents

A rechargeable lithium-ion power battery and manufacture method of the same Download PDF

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Publication number
WO2003077348A1
WO2003077348A1 PCT/CN2003/000170 CN0300170W WO03077348A1 WO 2003077348 A1 WO2003077348 A1 WO 2003077348A1 CN 0300170 W CN0300170 W CN 0300170W WO 03077348 A1 WO03077348 A1 WO 03077348A1
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Prior art keywords
positive electrode
negative electrode
positive
pole
lithium
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PCT/CN2003/000170
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French (fr)
Chinese (zh)
Inventor
Yongming Ju
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Yongming Ju
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Application filed by Yongming Ju filed Critical Yongming Ju
Priority to AU2003221286A priority Critical patent/AU2003221286A1/en
Publication of WO2003077348A1 publication Critical patent/WO2003077348A1/en

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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
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/50Current conducting connections for cells or batteries
    • H01M50/531Electrode connections inside a battery casing
    • H01M50/54Connection of several leads or tabs of plate-like electrode stacks, e.g. electrode pole straps or bridges
    • 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
    • H01M10/058Construction or manufacture
    • H01M10/0585Construction or manufacture of accumulators having only flat construction elements, i.e. flat positive electrodes, flat negative electrodes and flat separators
    • 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
    • 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
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/30Arrangements for facilitating escape of gases
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/50Current conducting connections for cells or batteries
    • H01M50/531Electrode connections inside a battery casing
    • H01M50/536Electrode connections inside a battery casing characterised by the method of fixing the leads to the electrodes, e.g. by welding
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/50Current conducting connections for cells or batteries
    • H01M50/543Terminals
    • 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

Definitions

  • Lithium-ion power battery capable of being repeatedly charged and discharged and manufacturing method thereof
  • the present invention relates to an environmentally friendly battery that can be repeatedly charged and discharged, and more particularly, the present invention relates to a lithium ion power battery that can be repeatedly charged and discharged and a method for manufacturing the same.
  • Cide application 001 01 356.4 discloses "a kind of chrome-fluoride lithium solid power battery that can be repeatedly charged and discharged". Although it is nominally a chrome-fluoride lithium solid power battery that can be repeatedly charged and discharged, its structure and composition are not fully disclosed in practice, so it has little practicality and application value, and it has not fundamentally solved high-power charging and discharging. The problem.
  • the biggest problem of lithium-ion power batteries is the heat generated during the charging and discharging process, and the heat generated during the charging and discharging process has a great adverse effect on the lithium-ion power batteries.
  • an object of the present invention is to provide a lithium ion power battery capable of being repeatedly charged and discharged, which can solve the problem of high power charging and discharging of the lithium ion power battery.
  • the present invention provides a lithium-ion power battery that can be repeatedly charged and discharged.
  • Each single battery consists of a cover plate, a negative pole, a safety valve, a positive pole, a current collector plywood, an inner body, an electrolyte, a cylindrical shape or a square shape.
  • the outer casing is composed of the following features:
  • the positive electrode and negative electrode groups that is, the positive electrode sheet, the negative electrode sheet, and the separator together form an electrode assembly with a disc structure; the positive electrode post is connected to the positive electrode, and the negative electrode post is connected to the negative electrode.
  • the poles are connected; the positive electrode is selected from a certain thickness of aluminum foil, and both sides are coated with a positive electrode active material; the negative electrode is selected from a copper foil of a certain thickness, and both sides are coated with a negative electrode active material having large leaf multipole ears and narrow rectangular pieces (also known as Shown into a piece), large leaf monopoles, large leaf multipoles are collectively called large leaf poles.
  • Large-leaf poles can be either raised or hidden, and the current is exported to the pole through the current collector splint; the positive pole has one or several pole poles, the negative pole has one or several pole poles, The number can be equal or different, and the diameters of the poles can be equal or different.
  • the present invention adopts a structure with large leaf poles that can reduce the current density, which can avoid the extremely harmful heat generated in the lithium ion power battery to the greatest extent.
  • the invention also provides a safety valve for a lithium ion power battery that can be repeatedly charged and discharged.
  • the compression spring is installed in the inner hole of the adjustment bolt, and the inner hole of the adjustment bolt is used to hold the compression spring and seal the steel ball. Stable, the compression spring can slide down vertically in the inner hole of the adjusting bolt, the sealing steel ball can slide down vertically in the inner hole of the adjusting bolt, and the outer diameter of the adjusting bolt is processed with a thread that matches the safety valve body
  • the adjusting bolt is processed with several vertical exhaust grooves, and the lower part of the exhaust groove is provided with exhaust holes; the compression spring is pressed on the upper part of the steel ball, and the lower hole of the sealed steel ball is trapped on the cover injection port.
  • the pressure relief hole at the bottom of the safety valve communicates with the injection hole on the cover.
  • the present invention also provides a lithium-ion power battery that can be repeatedly charged and discharged and a manufacturing method thereof, including the following steps: batching- ⁇ coating (pulling)- ⁇ slicing (if the tabs are directly cut, there is no Welding lugs)- ⁇ rolling- ⁇ making (welding) lugs- ⁇ winding (including casing and sealing), filling- ⁇ forming- ⁇ dividing volume.
  • the invention has a uniquely designed current collecting (current collecting) terminal, that is, an inner body formed by winding positive and negative electrodes of a large leaf tab and a diaphragm at the same time, which is more sensitive to internal pressure, and thus more reliable, safe and secure.
  • the current collecting plywood with better valve, current collecting performance and heat dissipation performance can solve the high-power repeated charging and discharging requirements of the lithium ion power battery, thereby realizing the wide application of the lithium ion power battery.
  • Figure 1A shows a cross-sectional view of a lithium-ion power battery using a cylindrical case
  • FIG. 1B is a top view of a lithium-ion power battery with a cylindrical case
  • Figure 1C shows the winding of the positive and negative pole pieces of a lithium-ion power battery with a cylindrical case
  • FIG. 2A shows a top view of a lithium-ion power battery with a square case
  • Figure 2B shows the winding method of the positive and negative plates of a lithium-ion power battery with a square case
  • Figure 3 is a sectional view of a lithium-ion power battery with a square case
  • Figures 4A, 4 A-1, 4B, 4B-1, 4 C, 4 C-1 4D, and 4D-1 are large-leaf monopoles and large Schematic diagram of leaf multipole;
  • Figures 5 and 6 show the structure of a pressure spring type and a plate type safety valve, respectively.
  • each unit battery consists of a cover plate 1, a negative pole 2, a safety valve 3, a positive pole 4, and an open case.
  • the inner body 7 is composed of: in the inner cavity of the lithium-ion power battery, there is a current collector plywood (also referred to as a pole piece plywood) 6, an electrolyte 8, a negative electrode piece 12, a positive electrode piece 1 3, and a separator 19.
  • the outer casing 9, the cover plate 1, the negative pole 2, the safety valve 3, and the positive pole 4 constitute the outer body of the lithium-ion power battery; the positive and negative pole piece groups, the diaphragm, and the current collector plye constitute the inner body 7 of the lithium-ion power battery.
  • the structure of a wound lithium-ion power battery is described in detail below.
  • the wound inner body 7 of a lithium-ion power battery is composed of a positive electrode, a negative electrode sheet, and a separator.
  • the electrode assembly has a disc-shaped structure as shown in FIG. 1C or FIG. 2B.
  • Figure 4 A-1 is a relatively narrow rectangular piece.
  • the positive electrode 1 3 is composed of an aluminum foil and a positive electrode active material.
  • the aluminum foil is a thin metal foil, and both sides are coated with a positive electrode active material (either lithium cobaltate, lithium manganate or lithium nickelate, or nickel cobalt acid). Lithium).
  • the surface of the aluminum foil is usually smooth, but the aluminum foil with a rougher surface has better adhesion for coating active materials.
  • the suitable aluminum foil thickness ranges from 10 ⁇ m to 80 ⁇ m. When seeking 1 C ⁇ 2 C, exclude other influencing factors.
  • the optimal thickness of aluminum foil is 15 ⁇ m ⁇ 2 5 ⁇ . When charging and discharging requirements are 2 C ⁇ 3 C or greater, exclude other influencing factors and use aluminum foil.
  • the optimal thickness is 20 ⁇ m to 4 5 ⁇ m or more.
  • the negative electrode 1 2 is composed of a copper foil and a negative electrode active material.
  • the copper foil is a thin metal foil, and both sides are uniformly coated with a collection of negative electrode active materials (either natural graphite, flake graphite, artificial graphite, or petroleum coke). Electric body.
  • the surface of the copper foil is usually smooth, but the copper foil with a rougher surface has better adhesion for coating active materials.
  • the suitable thickness of copper foil is 6 ⁇ ⁇ ⁇ 50 ⁇ ⁇ . When the charge and discharge requirements are 1 C ⁇ 2 C, other factors are excluded.
  • the optimal thickness of copper foil is 8 ⁇ ⁇ ⁇ 2 0 ⁇ ⁇ ; charge and discharge When 2 C ⁇ 3 C or more is required, other factors are excluded, and the optimal thickness of copper foil is 15 ⁇ m to 3 5 ⁇ m or more.
  • the thickness of the metal foil is not only related to the area of the current collector, but also to the capacitance of each single-piece pole piece.
  • the thickness of the metal foil should be slightly thicker. Where possible, the metal foil should be as thin as possible, in order to obtain a larger electrode sheet area when applying the same amount of active material, thereby obtaining better electrical properties.
  • the metal foil used for the positive electrode or the negative electrode can also be separately Use wire mesh or flat mesh metal foil.
  • the so-called flat mesh metal foil is formed by punching a number of fine small holes mechanically or chemically or by other methods on a thin aluminum or copper foil, and stretching it in the vertical and horizontal directions.
  • Active materials (excluding conductive agents, binders, and dispersants) of previous lithium-ion batteries accounted for about 90% of the total ingredients, and the remaining about 10% were conductive agents, binders, and dispersants.
  • the amount of active material of the lithium ion power battery involved in the present invention is greatly increased, whether it is the positive electrode or the negative electrode, which is about 93% to 95% or even higher.
  • the density of the positive electrode active material is 0.02 g to 0.06 g per square centimeter, and the optimal density of the positive electrode active material is 0.03 2 g to 0 ⁇ 0 4 2 g per square centimeter; Density per square centimeter is about 0. 0 1 g ⁇ 0. 0 3 g, the optimal density of the negative electrode active material per square centimeter is 0. 0 1 4 g ⁇ 0.
  • the main characteristics of lithium-ion power batteries should be suitable for power applications, and they must meet the requirements of high-power charge and discharge.
  • An important structure in the present invention is to use a large-area collector (current-collection) terminal, that is, a large leaf tab, which is more conducive to current conduction and heat dissipation, and can fully meet the requirements of high-power charge and discharge.
  • the current collecting (collecting) terminal is called a large leaf tab.
  • FIG. 4A and Figure 4A-1 Those with only one pole tab on each pole piece are called large leaf monopoles, as shown in Figure 4A and Figure 4A-1, and those with several pole pieces on each pole piece are called large leaf multipole ears, as shown in Figure 4B, Fig. 4B-1; Fig. 4C, Fig. 4C-1; Fig. 4D, Fig. 4D-1.
  • the positive and negative pole pieces should be cut into elongated pieces that conform to the process size and shape.
  • the size of the positive and negative electrode sheets varies due to their process requirements. Since the price of the active material of the positive electrode is much more expensive than that of the negative electrode, the length and width of the negative electrode sheet are slightly larger than those of the positive electrode when cutting. This method saves resources and gives full play to the material properties of the positive electrode, that is, the area of the positive electrode sheet is slightly smaller than that of the negative electrode sheet, and the area of the negative electrode sheet is slightly larger than that of the positive electrode sheet.
  • the positive electrode 1 3 and the negative electrode 1 2 are usually cut into monopole ears with large leaves (1 1 /
  • large leaf tabs can also be processed by roll cutting or shear stamping to form the pole pieces directly.
  • the positive and negative electrodes usually have only one large leaf tab; for the lithium-ion power battery with larger capacity, there are several large leaf tabs. Therefore, when necessary, the positive and negative electrodes can also be made into large-leaf multipolar ears as shown in Figure B and Figure B-1. Thermal performance will also be better.
  • the width of the tabs of the large leaf tabs 1 1 for the positive electrode and the large leaf tabs 10 for the negative electrode should be as large as possible in cross-section, if possible, that is, the tabs should be as wide as possible and as wide as possible. Thick, the current collecting (collecting) path should be as short as possible, which is conducive to the extraction and heat dissipation of the current. Of course, the larger the width of the large leaf pole ears, the better it is for diversion and heat dissipation.
  • the large leaf tabs on the positive and negative electrodes are pulled out from the same direction, for example, as shown in Figures 4A and 4A-1, whether it is a large leaf monopole or a large leaf multipole, whether it is the last roll
  • the maximum width of the large leaf tabs must be less than half (1/2) of the circumference of the stack where the large leaf tabs are located or formed.
  • the lugs of a larger-capacity power battery and the lugs of a smaller-capacity power battery obviously need to be wider to meet the requirements in terms of the performance of current conduction, heat dissipation, and high-rate charging and discharging.
  • the pitch of the large-leaf multi-pole ears is different. Continue winding, and the pole ears on the pole pieces must be coincident at the same position in order to fit the current collector plate neatly.
  • the distance between the large-leaf multipole ears is related to the diameter (perimeter) of the inner body 7 with a cylindrical shell, and to the circumference of the inner body 7 with a square shell. Because the inner body 7 of the wound lithium-ion power battery is wound, the perimeter of each roll is different. The perimeter of the inner roll is smaller than the perimeter of the outer roll.
  • the pitch of the condyles is smaller than the pitch of the outer condyles.
  • the large-leaf multipole ear Leaf poles also vary in width. If a cylindrical shell is used, the width of the inner condyle is gradually smaller than the width of the outer condyle; if a square housing is used, the width of the inner condyle can be gradually smaller than the width of the outer condyle, or it can be the same width. .
  • the width of the inner condylar ear is very different from the width of the outer conical ear. Therefore, in most cases, the width of the inner condyle is equal to the width of the outer condyle. In other words, the width of the inner ear can be as wide as the width of the outer ear if the requirements are not very strict.
  • the width of the large leaf tabs on the positive electrode 13 is the same as the width of the large leaf tabs on the negative electrode 12.
  • the width of the respective large leaf tabs on the positive and negative electrodes can also be unequal under special requirements.
  • the tab widths on the positive and negative electrodes should be equal.
  • the width of the large leaf tabs on the negative electrode 12 can be larger than the large leaf tabs on the positive electrode 1 3; Case, positive The width of the large leaf tab on 13 may be greater than the width of the large leaf tab on the negative electrode 12.
  • the maximum height of the large leaf tab is usually not greater than its own (large leaf tab) width, preferably smaller than its width.
  • the larger leaf monopole ears of the wound lithium ion power battery should be led out as far as possible from the middle of the pole piece.
  • the large-leaf monopole ears of the wound lithium-ion power battery can be led out from the positions close to the two ends of the pole piece. That is to say, the large-leaf monopole can be drawn from the middle of the pole piece, or from the positions near the two ends of the pole piece.
  • connection between the large lobe pole and the current collector can be a clear angle (that is, the connection is a right angle, an obtuse angle without an arc), or a smooth arc connection (that is, the connection has an R angle), as shown in Figure A.
  • R in the connection of Figure A-1 not only has higher mechanical strength, but also helps to prevent the concentration of heat and cause the pole tabs to be melted or even the pole pieces to be destroyed.
  • the positive and negative plates of lithium-ion power batteries use corresponding tabs, that is, when the positive electrode 1 3 uses large-leaf monopoles, and the negative electrode 12 usually uses large-leaf monopoles; the positive electrode 1 3 uses large-leaf multipoles.
  • the ears and the negative poles 1 2 should also adopt large leaf multipole ears.
  • the tabs on the positive and negative electrodes should be equivalent and the number should be equal.
  • large-leaf multipole ears can be used for the negative electrode, and large-leaf monopoles can be used for the positive pole; in the case of high-power discharge without fast high-power charging, Large-leaf multipole ears can be used for the positive pole, and large-leaf monopole ears can be used for the negative pole.
  • the manufacturing methods of the tabs are directly cut heads 10, 11 or welded tabs.
  • the so-called raised-ear type ears show that the ears are significantly higher than the part coated with the active material on the pole pieces, which has the advantage of being easy to scrape powder.
  • the ears shown in Figures 4D and 4D-1 are hidden-head style ears.
  • the form of the hidden head is exactly the opposite of that of the raised head.
  • Such Vietnamese-headed large leaf pole ears 17 and 18 can more fully utilize the space of the inner cavity of the lithium ion power battery.
  • the tabs 1 5 and 1 6 can be made by welding as shown in Figures 4C and 4C-1. Welding of several metal pieces not only increases the mechanical strength, improves the conductivity, but also improves the heat dissipation performance. Therefore, it is best to use a welded large leaf tab for the large leaf tab. Welds 1 4 must be firm. The advantage of welding the lugs is that there is less burr on the cut pieces.
  • the positive electrode is made of aluminum
  • the negative electrode is made of nickel or copper.
  • the shape of the large leaf tabs can be square, rectangular, half-moon (circular), trapezoidal, or other shapes that facilitate flow and heat dissipation.
  • the best tab shape is a trapezoid with R rounded corners at the connection.
  • the negative electrode 12 is usually placed on the outer layer during winding.
  • the positive electrode 13 can also be placed on the outer layer.
  • the positive and negative electrode sheets must be stacked together and wound to make the inner body.
  • the pole piece When the pole piece is folded inwardly, it may cause powder removal, so it should be considered to process the folding line on the pole piece inwardly folded.
  • the active material at the fold line must be scraped off.
  • Lithium-ion power batteries with cylindrical casings usually do not require folding lines for the positive and negative electrodes. Of course, folding lines can also be processed as needed. If a square shell is used, since the positive electrode 13 is relatively brittle and hard, the first bend has a large degree of deflection, which is easy to cause powder removal and even breakage. In order to prevent the positive electrode 13 from being powdered and broken, the folding line 20 should normally be processed at the first bend of the positive electrode sheet as shown in Fig. 4A, Fig. 4B, Fig. 4C, and Fig. 4D; Simultaneous processing of fold lines at two bends 2 0-
  • the center distance between the folding line 20 and the folding line 20-1 should meet the width of the square needle. Regardless of the width of the folding line 20 or the folding line 20-1, it should be larger than the thickness of the square curling needle.
  • the lithium-ion power battery with a cylindrical casing has a wound inner body 7 that is cylindrical and has a rectangular longitudinal section.
  • the ratio of the diameter of the inner body to its height (aspect ratio), the ideal aspect ratio is 1: 2, that is, the diameter (height) is 1 and the width is
  • the lithium-ion power battery with a square casing has a rectangular inner body 7 after winding, and the ideal aspect ratio is 6. 2: 3. 8 or 6: 4.
  • the basic function of the separator is to separate the positive and negative electrodes, prevent the battery from short-circuiting, and adsorb and maintain the electrolyte.
  • the separator In addition to having good insulation properties, stable chemical and electrochemical properties, the separator must have a certain mechanical strength and a high electrical conductivity. Ratio, it is most suitable to use porous polyolefin materials. In view of the characteristics that lithium-ion power batteries must be charged and discharged with high power, higher safety performance is required.
  • the lithium-ion power battery involved in the present invention mainly uses a polyethylene separator with a thickness of 15 to 80 ⁇ m, which has a microporous structure and a low current cut-off temperature.
  • the selection principle of the separator is as thin as possible, but when the area of the positive or negative electrode piece is less than or equal to 100 Ornm ⁇ 500 mm and greater than or equal to 100 mm ⁇ 50 mm, the charge and discharge requirements are 1 C ⁇ 2 C, Excluding other influencing factors, the optimal thickness of the separator is 25 ⁇ m to 40 ⁇ m; when charging and discharging requirements are 3C or greater, excluding other influencing factors, the optimal thickness of the separator is 4 ⁇ or more. When the battery internal temperature is higher than the limit value
  • Lithium-ion power battery can also be made of polypropylene.
  • the separator of the lithium ion power battery can also be directly coated with a slurry of a polyolefin-based material containing a reasonable amount of a pore-forming agent on the surface of the positive electrode sheet that has been rolled.
  • the separator 19 is generally made in a long shape, and the area of the separator is larger than the positive and negative electrodes no matter the length or width. Except for the ears, the separator 19 must completely shield the positive electrode 13 or negative electrode 1 2 from the periphery, and the edges must not be exposed. In case of short circuit.
  • the material of the lithium ion power battery pole is a metal material with excellent electrical and thermal conductivity. In addition to a certain strength, it must also have good heat dissipation performance.
  • the pole can be cylindrical or sheet-shaped to facilitate faster heat dissipation by lithium ion power.
  • the poles can be installed on any side surface of the lithium-ion power battery; according to different needs, the positive and negative poles can also be installed on different side surfaces of the lithium-ion power battery.
  • one positive pole and one negative pole of a lithium-ion power battery can meet the needs.
  • more poles of a larger-capacity lithium-ion power battery may be installed, for example, two positive poles and two negative poles may be installed at the same time.
  • the number of positive and negative poles may be equal or different.
  • the number of positive and negative poles should be equal; in the case of fast high-power charging without high-power discharge, the number of negative poles can be the same as that of the positive pole
  • the number of poles is equal to or greater than the number of positive poles; in the case of high power discharge without fast high power charging, the number of positive poles may be equal to or greater than the number of negative poles.
  • the diameter of the pole can also be adjusted to meet the above needs.
  • the diameters of the positive and negative poles should be equal; in the case of fast high-power charging without high-power discharge, the negative pole
  • the diameter of the pole can be equal to or larger than the diameter of the positive pole; in the case of high power discharge without fast high power charging, the diameter of the positive pole can be equal to or larger than the diameter of the negative pole The diameter of the pole.
  • Lithium-ion power batteries use multiple electrolytes to accommodate wider temperature changes.
  • Multi-component electrolyte refers to a mixture of two or more solvents and lithium hexafluorophosphate.
  • the lithium-ion power battery uses:
  • LIPF 6 lithium hexafluorophosphate
  • EC ethylene carbonate
  • DEC dimethyl carbonate
  • the solvent ratio is 0.9 5 to 1. 0 5: 0. 9 5 ⁇ 1. 0 5: 0.9 5 ⁇ 1. 0 5; or
  • the lithium-ion power battery case according to the present invention is a part of a lithium-ion power battery, and is also called a battery case.
  • the cell case is also one of the positive and negative electrodes.
  • the cell case is also called the electrode case.
  • the cell case of high-power lithium-ion power batteries should be avoided as much as possible.
  • the cell shell of a high-power lithium-ion power battery cannot be an electrode shell, and the shell must be insulated from the pole.
  • the case can also become an electrode case.
  • the cell case of a wound lithium-ion power battery can be square (including rectangular) or cylindrical.
  • the cylindrical shell consists of a flat surface above and below, and It consists of a cylindrical curved surface and a square shell composed of six planes.
  • the battery cell and the cover plate are complementary.
  • the battery case is square, the cover plate is square, the battery case is cylindrical, and the cover plate is circular.
  • Lithium-ion power battery cell shells have higher airtightness requirements and higher strength, usually metal shells with a certain rigidity, such as stainless steel cell shells.
  • the cell shell of the lithium-ion power battery of the present invention can be either a metal shell, or made of polytetrafluoroethylene or polypropylene or other suitable plastics, and can be bonded or injection-molded. The safety performance is better than that of metal cells. shell.
  • the upper or side of the shell of the lithium-ion power battery is designed and processed with plug-in ports that are convenient for series and parallel connection, so that the batteries can be connected in series or in parallel to form a battery pack.
  • heat sinks can be designed and processed on or inside the housing
  • the cover of the lithium-ion power battery must match the battery case, and the airtightness is high.
  • the cover of the lithium-ion power battery can also be made of PTFE or polypropylene or any other strong acid-resistant plastic with a certain strength and injection molding.
  • the safety valve 3 of the lithium-ion power battery is very important. It is a safety device provided to prevent other accidents such as overcharge and short circuit. It can instantly remove the pressure exceeding the design.
  • the pressure relief hole at the bottom of the safety valve is also the injection port for the lithium-ion power battery.
  • the structure of the pressure spring safety valve is shown in Figures 5-1 and 5- 2.
  • the compression spring (spring) 2 5 is installed in the inner hole of the adjustment bolt 2 3.
  • the inner hole of the adjustment bolt is actually a retainer for the compression spring and the sealed steel ball 2 2.
  • the compression spring can be vertically moved up and down in the inner hole of the adjustment bolt.
  • the sliding steel ball can not swing laterally, and the sealing steel ball can also slide vertically in the inner hole of the adjusting bolt without swinging horizontally.
  • the outer diameter of the adjustment bolt is processed with a thread matching the safety valve body 21, so the adjustment bolt is installed on the safety valve body, and the height can be adjusted at will through the key hole 27, which also serves as an exhaust.
  • the adjusting bolt is processed with a plurality of vertical exhaust grooves 2 4. Through the exhaust groove, the adjusting bolt can be rotated to rotate, and an exhaust hole 2 8 is opened at the lower part of the exhaust groove.
  • the lowest layer is fluoro rubber ⁇ 26 or other corrosion-resistant rubber pads, which are pressed or attached to the liquid injection holes on the lid 1 of the lithium ion battery, and the sealed steel ball is trapped under fluoro rubber ⁇ 26 or other resistant materials. Corroded rubber pad.
  • the pressure relief hole at the bottom of the safety valve communicates with the liquid injection hole on the cover plate 1, so the pressure relief hole is the liquid injection hole when the liquid is injected.
  • the fluorine rubber ring or other corrosion-resistant rubber pads must have some elasticity, so that when the steel ball is pressed against the fluorine rubber pad or other corrosion-resistant rubber pads, the fluorine rubber pads or other corrosion-resistant rubber pads deform
  • the injection hole can be sealed.
  • the compression spring is pressed against the upper part of the sealed steel ball with the inner inner part of the bottom part, and the lower part of the sealed steel ball is trapped on the fluorine rubber on the battery cover ⁇ 2 6 or other corrosion-resistant rubber pads to restrain the sealed steel ball from slipping. open.
  • the sealed steel ball automatically closes the injection port due to the pressure of the compression spring to keep the inside of the battery isolated from the external environment.
  • the structure of the tablet safety valve is shown in Figure 6-1 and 6-2.
  • the reverse bow spring piece 30 is installed at the lower part of the adjusting bolt 23, and the adjustment bolt is processed with a thread matching the safety valve body 21. Therefore, the adjustment bolt is installed on the safety valve body, and the bottom is pressed tightly on the reverse bow spring piece. Hole 8 adjusts the height of the bolt and adjusts the tension of the anti-bow spring.
  • the safety valve body is processed with a rectangular exhaust groove 31, and the anti-bend spring is installed in the rectangular groove. It can not be rotated horizontally except it can spring up and down.
  • the inner diameter of the lower part of the safety valve body is small, forming a cage, and the sealing steel ball 22 can be vertically moved down in the cage.
  • the anti-bow spring is processed with a process assembly hole 33, which is crimped on the upper part of the steel ball to fix the sealed steel ball.
  • the lower hole of the sealed steel ball is trapped on the fluoro rubber ⁇ or other corrosion-resistant rubber pad on the cover injection port, which not only fixes the sealed steel ball, but also seals the battery.
  • fluororubber or other corrosion-resistant rubber mats must have some elasticity, so that when the steel ball is pressed against the fluororubber or other corrosion-resistant rubber mats, the fluororubbers or other corrosion-resistant rubber mats will deform.
  • the injection hole can be sealed.
  • the compression spring is snapped on the upper part of the sealing steel ball with the inner ⁇ at the bottom, and the lower part of the sealing steel ball is trapped on the fluoro rubber ⁇ 26 on the battery cover plate, restraining the sealing steel ball from sliding away.
  • the sealed steel ball automatically closes the injection port due to the pressure of the compression spring to keep the inside of the battery isolated from the external environment.
  • the pressure inside the battery is greater than the set value, it will The pressure of the sealed steel ball is automatically lifted to release pressure, and the gas is instantly discharged from the pressure relief hole 29, and escapes from the exhaust hole 32 and the key hole 27 along the exhaust groove 31.
  • the pressure of the anti-bow spring is sufficient to compress the sealing steel ball again to seal the pressure relief hole.
  • the fluorine rubber ring 26 may be replaced by any other suitable rubber.
  • the anti-bow shrapnel can be designed and processed into a flat shape or a half-moon shaped anti-bow shrapnel as shown in Figure 6-1.
  • the working principle of the flat anti-bow shrapnel is the same as that of the half-moon anti-bow shrapnel.
  • the pressure of the tablet-type safety valve can also be adjusted by the screws 3 4 shown in Figure 6-2.
  • the safety valve can also be designed with several vent holes 3 5 in the body.
  • the pressure relief hole 2 9 on the fluorine rubber ⁇ 2 6 and the liquid injection hole on the cover plate 1 are communication holes and also communicate with the pressure relief hole on the bottom of the safety gang, so they are not marked separately.
  • the sealed steel ball 2 2 can be designed and processed into a ball 2 2-1 with horizontal transverse grooves, and the fluorine rubber ⁇ 2 6-1 is hung on the sealed steel ball. 2 2-1 in the horizontal slot.
  • the fluorine rubber ⁇ 2 6-1 seals the injection hole.
  • a fixed small handle 3 5 can also be processed thereon, and a compression spring or an anti-bow spring is sleeved on the fixed small handle.
  • the compression spring or reverse bow spring presses the sealing steel ball 2 2-1 and the fluorine rubber ⁇ 2 6-1 tightly seals the injection hole.
  • the internal pressure is higher than the allowable value, the sealed steel ball 2 2-1 is lifted, and the fluoro rubber ⁇ 2 6-1 is lifted upwards at the same time, and the internal pressure is quickly released.
  • the sealing steel ball 2 2 can also be designed and processed into a sealing frustum 2 2-2. Compared with the steel ball 2 2 or 2 2-1, the lower part of the sealing frustum protrudes into the injection hole, so Bit more reliable.
  • the sealing frustum can also be processed with a fixed small handle 3 6, and a compression spring or an inverse bow spring is sleeved on the fixed small handle. When the internal pressure is less than the allowable value, the compression spring or reverse bow spring presses the sealing frustum 2 2-2, and the pressure of the fluorine rubber ⁇ 26 in the sealing frustum deforms to tightly seal the injection hole. When the internal pressure is greater than the allowable value, lift the sealing cone 2 2-2 and quickly remove the internal pressure.
  • the sealing frustum can also be designed and machined as 2 2-3, which has a horizontal horizontal groove, and the fluoro rubber ⁇ 2 6-1 is hooped in the horizontal horizontal groove on the sealing frustum 2 2-3.
  • the fluorine rubber ⁇ 2 6-1 seals the injection hole.
  • the internal pressure is larger than the permissible value, when the sealing cone 2 2-3 is lifted up, the fluorine rubber ⁇ 2 6-1 is lifted upward at the same time, and the internal pressure is quickly released.
  • the sealing steel ball 2 2 or 2 2-1 or the sealing frustum 2 2-2, 2 2-3 can also be designed as a hollow sleeve, and the compression spring is inserted into a hollow sleeve with better guiding performance. in.
  • the safety valve and the pole should be installed on the same side surface of the lithium-ion battery case, but they can also be installed on different side surfaces as required.
  • safety valves and poles can be installed on any side surface of the lithium-ion power battery.
  • a large-capacity lithium-ion power battery may have several safety valves installed on the same side surface or on different side surfaces.
  • the medium for preparing the slurry includes NM P (N-methyl-2 -pyrrolidone) as the medium or water (deionized water, distilled water, purified water) as the medium; the preparation methods include wet method and dry method.
  • the NMP medium is described first, and then the water medium is described.
  • the wet method is first described (there are also wet methods: sequential preparation method and mixed preparation method), and then the dry method is described. (Positive). It is described below:
  • NM P positive electrode.
  • PVDF, graphite (or acetylene black), and carbon black all need to be about 120. C Bake in an oven for about 2 to 3 hours.
  • Sequential preparation method After adding PVDF to NMP and stirring for about 3 to 4 hours, add conductive agent graphite (or acetylene black), carbon black and stir for about 0.5 to 1 hour, and finally add lithium cobaltate and stir for about 2.5 to 4 hours to become viscous. Pasty.
  • CMC is added to the water and stirred for about 3 to 4 hours, then SBR is added to it and stirred for about 0.5 to 1 hour, and then conductive agent graphite (or acetylene black) and carbon black are added and stirred for about 0.5 to 1 hour, and finally cobalt is added.
  • the lithium acid is stirred for about 2.5 to 4 hours to form a thicker slurry. Sieve out agglomerates and other impurities.
  • the preparation of the positive electrode must be slightly larger than the conductive agent.
  • NMP NMP
  • Materials required: Graphite 93% ⁇ 95% PVDF 5% ⁇ 7%, NMP is about 8% of the total amount of all the aforementioned substances 0% ⁇ 15 0% is the solid-liquid ratio-1: 0 ⁇ 8 ⁇ 1. 5; the optimal solid-liquid ratio 1: 1 ⁇ 1.3.
  • PVDF needs a temperature of about 120. B oven in C oven for 2 ⁇ 3 hours, graphite needs to be baked at 300 ° C ⁇ 500 ° C for 4 ⁇ 8 hours.
  • Sequential preparation method Add P V D F to NM P and stir for about 3 to 4 hours. Then add the graphite that has been sifted through a 3 2 5 mesh screen and stir for about 3 to 4 hours to form a thick slurry.
  • Sequential preparation method Add CMC to water and stir for about 3 to 4 hours, then add SBR to it and stir for about 0.5 to 1 hour. Finally, add graphite after baking and sieving through 300 mesh. Stir for about 3 to 4 hours to become viscous. Pasty.
  • Dry preparation Dry preparation of the positive electrode with N M P as the medium. Materials required: Materials required: PVDF 2.5% to 3.5%, lithium cobaltate 93% to 95%, conductive agent graphite 1.5% to 2% (or acetylene black 0.8% to 1 .
  • N M P is limited by the particle size and particle size distribution of the foregoing materials, especially lithium cobaltate, so it is about the total amount of all the foregoing materials.
  • the particle size of the conductive agent must be equal to or smaller than the positive electrode material (lithium cobaltate, lithium manganate, lithium nickel cobaltate).
  • the medium In order to ensure the quality of the prepared slurry, whether the water (deionized water, distilled water, purified water) or NMP is used as the medium during the preparation of the slurry, it must be based on the particle size, particle size distribution, and conductive agent of the positive electrode material. The amount is carefully calculated, and the medium is added once and cannot be added halfway. The same is true for the negative electrode, whether it is water (deionized water, distilled water, purified water) or NMP as the medium, it must be based on the anode material. And the amount of additives is finely calculated, and the medium should be filled in one time. Do not add it halfway. Otherwise, it is difficult to ensure the quality of the positive electrode slurry or the negative electrode slurry.
  • the active material used for the positive electrode of the lithium-ion power battery can also be lithium manganate, lithium nickelate, or lithium nickel cobaltate.
  • the preparation method is basically the same as that of the foregoing lithium cobaltate preparation method.
  • the particle size of the lithium ion battery positive electrode material can be selected in the range of 2 ⁇ m to 12 ⁇ m, but the optimal particle size should be 5 ⁇ m ⁇ 8 ⁇ m;
  • the particle size distribution of the cathode material must also be as narrow as possible. Taking 5 ⁇ m particle size as an example, too fine (less than 2 ⁇ m) or too thick (more than 12 ⁇ m) powder The total is usually not more than 40%.
  • Cathode material lithium cobaltate, lithium manganate, lithium nickelate, or lithium nickel cobaltate
  • Preparation method of fine powder below 2 ⁇ m, coarser powder above 1 ⁇ m and 2 ⁇ m ⁇ 1 2 ⁇ The preparation method in the range of m is the same except that the solid-liquid ratio is different.
  • the solid-liquid ratio of fine powders below 2 ⁇ m should be increased by 20 from the original solid-liquid ratio. % ⁇ 50%, the solid-liquid ratio of coarser powders above 12 ⁇ m should be reduced by 10% ⁇ 30% based on the original solid-liquid ratio.
  • the anode material graphite is screened by 300 mesh vibration, and the remaining ones on the Internet are usually not suitable for use.
  • the conductive agent involved in the present invention includes graphite, acetylene black, carbon black, etc .; except that graphite is used as a negative electrode material for high-temperature treatment (300 to 500 ° °), the rest is baked. The material can be placed in a vacuum box for vacuum treatment without the need for high temperature treatment.
  • the production process of the lithium-ion power battery is as follows: ingredients- ⁇ coating- ⁇ tableting- ⁇ rolling-winding and assembling into the inner body (including casing and sealing)- ⁇ filling- ⁇ chemical conversion- ⁇ volumetric.
  • Coating also known as drawing pulp.
  • the stirred positive electrode (or negative electrode) slurry is hook-coated on the metal foil current collector, pulled out by a roller knife into the oven and dried. After baking, it will become semi-finished current collector after baking. Care must be taken during coating to avoid scratches, exposed substrates, lightness and weight in the vertical and horizontal directions.
  • the temperature control is very important: the temperature of the preheating section should not be too high, usually the temperature is selected at 90 ° C or below, and the temperature of the intermediate temperature section is between 1 10 ° C ⁇ 1 3 0 ° Between C, ⁇ 10 ° C, the temperature in the high-temperature section is 120. C ⁇ 1 4 0. Between C, ⁇ 10. C. Under the aforementioned temperature conditions, the temperature of the negative electrode slurry can be slightly higher than the temperature of the positive electrode slurry by about 10 to 15 "C during coating and baking, and the temperature of the slurry using water as the medium can be higher than that of NMP as the medium. The temperature of the slurry is slightly higher than about 10 ⁇ 15 ° C.
  • both the positive electrode and the negative electrode must enter the drying tunnel of the coating machine (also known as the puller) from the preheating section, and must not be inverted. If the slurry (especially the negative electrode slurry) first enters the high-temperature section of the coater and bakes suddenly at high temperature, the surface is dried quickly, and it is easy to form a dry shell, which is slightly wrinkled, which will form cracked fine lines. The slurry under the dry shell is sugar-smeared and forms a liquid film invisible to the naked eye between the metal foil.
  • the coating machine also known as the puller
  • the slurry is actually virtually attached to the surface of the metal foil, so it is easy to remove powder and even flakes ( (Ie, large pieces of active material fall off the metal foil), which seriously affects the electrical performance of lithium-ion power batteries.
  • Current coating The cloth process is mostly coated on one side and then coated on the other side; however, it can also be coated on both sides simultaneously.
  • the positive and negative electrode sheets to which the present invention is applied may be coated with active materials on both sides of the metal foil, or may be coated with active materials only on one side of the metal foil.
  • the back surface (metallic surface without active material coating) can be attached to form a current collector with active materials on both sides.
  • the thickness of the metal foil used for single-sided coating must be thinner than the thickness of the aforementioned metal foil, which is about 1/2 to 1/3 of the thickness of the aforementioned metal foil.
  • Line speed control in the coating process is also important. Under the above temperature conditions, the linear speed can be adjusted within the range of 800mm to 500 Omm per minute. The best linear speed is 1200mm ⁇ 3500mm per minute.
  • high-pressure spraying can also be used. Under a certain pressure of the dry protective gas, the slurry is sprayed evenly on the metal foil from the high-speed nozzle, which not only has better adhesion, but also significantly increases the production capacity.
  • the thickness of the positive electrode before rolling is about 170 ⁇ m to 270 ⁇ m
  • the thickness of the positive electrode after rolling is about 110 ⁇ m to 165 ⁇ m
  • the thickness of the negative electrode is about 185 ⁇ m to 275 ⁇ m, 110 ⁇ ⁇ ⁇ 165 ⁇ ⁇ after rolling.
  • the optimal thickness of the positive electrode before rolling is 195 ⁇ m ⁇ 235 ⁇ 01
  • the optimal thickness of the positive electrode after rolling is 135 ⁇ ⁇ 155 ⁇ m
  • the optimal thickness of the negative electrode before rolling is 220 ⁇ ⁇ 250 ⁇ ⁇
  • the optimal thickness after rolling is 135 ⁇ m ⁇ 155 ⁇ ⁇ .
  • the rolling pin of the inner body 7 of the shaped shell is a small cylindrical shaft as shown in FIG. 1A, and the rolling pin of the inner body of the square shell shown in FIG. 2A is a thin sheet with certain rigidity and elasticity.
  • the positive and negative electrodes When winding, the positive and negative electrodes must be staggered, and the distance between the positive electrode 1 3 and the first electrode of the negative electrode 12 must be reasonably calculated, so that the positive electrode tabs 11 on the wound inner body 7 happen to be neat and neat.
  • the parallel arrangement is parallel to one end of the inner body, and the negative electrode tab 10 happens to be neatly arranged parallel to the other end of the inner body.
  • the outermost layer of the inner body 7 may be either a negative electrode sheet or a positive electrode sheet.
  • the positive electrode pole 4 is connected to the positive electrode sheet 1 3, and the negative electrode pole 2 is connected to the negative electrode sheet 12.
  • the surface of the current collecting plywood in contact with the tabs is processed with raised spines. In general, the coverage of the current collector plywood should be larger than the large leaf tab.
  • the method of clamping is also divided into perforated clamps and two-sided clamps.
  • the integrated current collector ply is cut on a solid metal into several wire grooves that can be compressed and can be springed off.
  • the pole ears are inserted into the wire grooves of the current collector ply A or D and fastened with metal bolts 5.
  • the split-type current collecting plywood B or C is connected in series by a plurality of independent metal pieces through a series rod 2 Q, and the tabs are respectively clamped and fastened with metal bolts 5.
  • the integrated current collector plywood can be perforated or double-sided.
  • the split current collector plywood can also be perforated or double-sided. From efficiency As far as the effect is concerned, the efficiency and effect of the perforated clip are better than the two-sided clip.
  • the bolts In order to prevent the bolts connecting the pole ears and poles from loosening, the bolts need to be fixed with curing glue.
  • Inject fluid Before injection, the normal air in the inner cavity of the lithium ion power battery must be drawn out. Except for the moisture in the inner cavity, the inner cavity of the battery must be in a negative pressure state, and then an appropriate amount of electrolyte is injected from the safety valve port.
  • the injection volume of a lithium-ion power battery must be calculated based on its capacity. If the injection volume is too large, it will easily leak and cause the drum shell. If the injection volume is too small, it will easily cause the deterioration of the positive and negative electrode active materials.
  • the injection volume of lithium ion power battery is usually adjusted within the range of 0.1 5 Ah / g ⁇ 0.6 Ah / g; the optimal injection volume is 0.2 Ah / g ⁇ 0.3 5 Ah / g between.
  • the environmental control of the injection is very important, so the injection must be completed in the operation box or other environment that can meet the requirements. Because the pressure relief hole of the safety valve communicates with the liquid injection hole on the cover plate, the injection liquid is usually injected from the pressure relief hole of the safety valve; the liquid injection hole can also be processed on the housing or the cover plate separately.
  • the internal cavity of the lithium-ion power battery must be intentionally filled with solid substances or electrolyte. Depending on the capacity of the lithium-ion power battery, the cavity is about 1% to 10% of the total volume of the internal cavity.
  • the cavity can be filled with a protective gas.
  • Formation is the last key to battery production.
  • the formation principle of high-power lithium-ion batteries must be low current and low voltage. High current must not be formed. Higher voltage formation is required to fully activate the active materials on the positive and negative current collector substrates.
  • the formation process must be completed uninterrupted at one time, and it cannot be stopped or stopped at will.
  • the formation curve should be smoothly connected, and the current should be controlled between 0. 0 1 C / 10 hours- ⁇ 0. 2 C / 5 hours-— 0. 0 5 C / 5 hours- ⁇ 0. 1 C / 4 hours- ⁇ 0.2 C / 1 hour, after the constant current is full, it will be switched to constant pressure to continue charging, so as to ensure sufficient one time.
  • the lithium ion power battery manufactured by this method can not only meet the requirements of high-power charge and discharge, but also avoid the problem of heat accumulation inside the power battery.

Abstract

A rechargeable lithium-ion power battery, each mono-cell is consisted of a cover plate, a negative pole, a safety valve, a positive pole, an electrolyte solution and a case. The positive pole is connected with the positiv- electrode, and the negative pole is connected with the negative electrode. Positive electrode substrate is selected from an aluminum foil with certain thickness, which is coated with positive active material on both sides. Negative electrode substrate is selected from copper foil with certain thickness, which is coated with negative active material on both sides. It is characterized in that an inner body of the battery is an electrode assembly which has plate-shaped structure which is composed of a positive electrode sheet, a negative electrode sheet and separator. Either the positive electrode sheet or the negative electrode sheet is shaped to a long expanded sheet with a big-leaf single tab or big-leaf multiple tabs which have different space , current flows to the poles by means of current-collecting clamp. The positive electrode has one or more electrode poles; the negative electrode has one or more electrode poles.

Description

可反复充放电的锂离子动力电池及其制造方法 技术领域  Lithium-ion power battery capable of being repeatedly charged and discharged and manufacturing method thereof
本发明涉及一种可以反复充放电的环保电池, 更具体而 言, 本发明涉及一种可以反复充放电的锂离子动力电池及其制 造方法。  The present invention relates to an environmentally friendly battery that can be repeatedly charged and discharged, and more particularly, the present invention relates to a lithium ion power battery that can be repeatedly charged and discharged and a method for manufacturing the same.
背景技术  Background technique
由于环保以及节能的要求, 当今世界对能源的需求越来越 迫切, 因此寻求高效率而又洁净的动力源, 是社会发展和科技 进步的必然趋势。  Due to the requirements of environmental protection and energy saving, the world's demand for energy is more and more urgent. Therefore, it is an inevitable trend for social development and technological progress to seek efficient and clean power sources.
已经有 4艮多研究涉足动力电池领域。 当前常见的动力电池 有铅酸电池、 镍镉电池、 镍氢电池、 钠硫电池等。 但由于其能 量密度低, 充电时间长, 而且不能满足大功率充放电的需求, 直接影响这些动力电池的实用性。 近年来, 锌空气电池、 锂离 子电池、 质子交换膜燃料电池等均被认为是作为动力电池发展 的最佳动力电池。 但由于无法满足大功率充放电的要求, 因此 其实用性问题严重阻碍了动力电池的实际应用。  More than 4 studies have been involved in the field of power batteries. Currently common power batteries include lead-acid batteries, nickel-cadmium batteries, nickel-metal hydride batteries, and sodium-sulfur batteries. However, due to its low energy density, long charging time, and inability to meet the needs of high-power charging and discharging, it directly affects the practicability of these power batteries. In recent years, zinc air batteries, lithium ion batteries, and proton exchange membrane fuel cells have been considered as the best power batteries for power battery development. However, because it cannot meet the requirements of high-power charging and discharging, its practical problems have seriously hindered the practical application of power batteries.
中国专利申请 001 01 356. 4 公开了 "一种可反复充放电的 铬氟锂固体动力电池" 。 虽然名义上是可反复充放电的铬氟锂 固体动力电池, 但实际上其结构和组分均未充分公开, 因此基 本不具有实用性和应用价值, 而且也未从根本上解决大功率充 放电的问题。 锂离子动力电池的最大问题是充放电过程中产生 的热量, 而这种在充放电过程中产生的热量对锂离子动力电池 是有很大的不良影响的。  Chinese patent application 001 01 356.4 discloses "a kind of chrome-fluoride lithium solid power battery that can be repeatedly charged and discharged". Although it is nominally a chrome-fluoride lithium solid power battery that can be repeatedly charged and discharged, its structure and composition are not fully disclosed in practice, so it has little practicality and application value, and it has not fundamentally solved high-power charging and discharging. The problem. The biggest problem of lithium-ion power batteries is the heat generated during the charging and discharging process, and the heat generated during the charging and discharging process has a great adverse effect on the lithium-ion power batteries.
因此, 本发明的目的是提供一种能够反复充放电的锂离子 动力电池, 它可以解决锂离子动力电池大功率充放电的问题。  Therefore, an object of the present invention is to provide a lithium ion power battery capable of being repeatedly charged and discharged, which can solve the problem of high power charging and discharging of the lithium ion power battery.
发明内容  Summary of the Invention
本发明提供了一种可反复充放电的锂离子动力电池, 每个 单体电池由盖板、 负极极柱、 安全阀、 正极极柱、 集电夹板、 内本体、 电解液、 圆柱形或方形外壳组成, 其特征在于: 内本 体系由正负极片組即正极片、 负极片与隔膜共同构成具有盘状 结构的电极集合体; 正极极柱与正极相连接, 负极极柱则与负 极相连接; 正极选用一定厚度的铝箔, 两面均勾涂布正极活性 物质, 负极选用一定厚度的铜箔, 两面均匀涂布负极活性物 大叶多极耳的形状狭长的矩形片 (又称为展成片 ) , 大叶单极 耳、 大叶多极耳又统称为大叶极耳。 大叶极耳既可以为扬头式 也可以为藏头式, 并通过集电夹板导出电流至极柱; 正极有一 个或若干个极柱, 负极有一个或若干个极柱, 正负极柱的数量 可以相等也可以不等, 极柱的直径可以相等也可以不等。 The present invention provides a lithium-ion power battery that can be repeatedly charged and discharged. Each single battery consists of a cover plate, a negative pole, a safety valve, a positive pole, a current collector plywood, an inner body, an electrolyte, a cylindrical shape or a square shape. The outer casing is composed of the following features: The positive electrode and negative electrode groups, that is, the positive electrode sheet, the negative electrode sheet, and the separator together form an electrode assembly with a disc structure; the positive electrode post is connected to the positive electrode, and the negative electrode post is connected to the negative electrode. The poles are connected; the positive electrode is selected from a certain thickness of aluminum foil, and both sides are coated with a positive electrode active material; the negative electrode is selected from a copper foil of a certain thickness, and both sides are coated with a negative electrode active material having large leaf multipole ears and narrow rectangular pieces (also known as Shown into a piece), large leaf monopoles, large leaf multipoles are collectively called large leaf poles. Large-leaf poles can be either raised or hidden, and the current is exported to the pole through the current collector splint; the positive pole has one or several pole poles, the negative pole has one or several pole poles, The number can be equal or different, and the diameters of the poles can be equal or different.
本发明采用 了可以减低电流密度的大叶极耳的结构, 它 (们 ) 能够最大限度地避免产生于锂离子动力电池而言非常有 害的热量。  The present invention adopts a structure with large leaf poles that can reduce the current density, which can avoid the extremely harmful heat generated in the lithium ion power battery to the greatest extent.
本发明还提供了一种用于可反复充放电的锂离子动力电池 的安全阀, 其中的压簧装于调节螺栓的内孔中, 调节螺栓的内 孔用于保持压簧、 密封钢球的稳定, 压簧可在调.节螺栓的内孔 中纵向上下滑移, 密封钢球可在调节螺栓的内孔中纵向上下滑 移, 调节螺栓的外径上加工有与安全阀本体相配的螺紋; 调节 螺栓加工有若干竖向的排气槽, 在排气槽的下部则开有排气 孔; 压簧压在钢球的上部, 密封钢球的下部孔则陷压在盖板注 液口上的氟橡胶圏上; 安全阀底部的卸压孔与盖板上的注液孔 相通。  The invention also provides a safety valve for a lithium ion power battery that can be repeatedly charged and discharged. The compression spring is installed in the inner hole of the adjustment bolt, and the inner hole of the adjustment bolt is used to hold the compression spring and seal the steel ball. Stable, the compression spring can slide down vertically in the inner hole of the adjusting bolt, the sealing steel ball can slide down vertically in the inner hole of the adjusting bolt, and the outer diameter of the adjusting bolt is processed with a thread that matches the safety valve body The adjusting bolt is processed with several vertical exhaust grooves, and the lower part of the exhaust groove is provided with exhaust holes; the compression spring is pressed on the upper part of the steel ball, and the lower hole of the sealed steel ball is trapped on the cover injection port. The pressure relief hole at the bottom of the safety valve communicates with the injection hole on the cover.
本发明还提供了一种可反复充放电的锂离子动力电池的配 比及其制造方法, 包括以下步骤: 配料 - →涂布 (拉浆) - → 切片 (如果直接裁切极耳, 则无焊接极耳工序) - →滚压 - → 制作 (焊接) 极耳 - →卷绕 ( 包括装壳、 封口 ) 注液 - → 化成 - →分容。  The present invention also provides a lithium-ion power battery that can be repeatedly charged and discharged and a manufacturing method thereof, including the following steps: batching-→ coating (pulling)-→ slicing (if the tabs are directly cut, there is no Welding lugs)-→ rolling-→ making (welding) lugs-→ winding (including casing and sealing), filling-→ forming-→ dividing volume.
本发明具有设计独特的集电 (集流) 端子即大叶极耳的正 负极片与隔膜同时卷绕在一起而构成的内本体、 对内压更加敏 感、 因而更可靠、 更安全的安全阀、 集流性能、 散热性能更好 的集电夹板解决锂离子动力电池的大功率反复充放电要求, 从 而实现锂离子动力电池的广泛应用。  The invention has a uniquely designed current collecting (current collecting) terminal, that is, an inner body formed by winding positive and negative electrodes of a large leaf tab and a diaphragm at the same time, which is more sensitive to internal pressure, and thus more reliable, safe and secure. The current collecting plywood with better valve, current collecting performance and heat dissipation performance can solve the high-power repeated charging and discharging requirements of the lithium ion power battery, thereby realizing the wide application of the lithium ion power battery.
附图说明  BRIEF DESCRIPTION OF THE DRAWINGS
下面结合附图中的优选实施例, 可以更容易理解本发明的 内容。 在附图中, 相同的附图标记表示相同的部件, 其中: 图 1 A 所示为采用 圆柱形外壳的锂离子动力电池的剖视 图; The content of the present invention can be more easily understood with reference to the preferred embodiments in the accompanying drawings. In the drawings, the same reference numerals denote the same components, wherein: Figure 1A shows a cross-sectional view of a lithium-ion power battery using a cylindrical case;
图 1 B 表示为采用圆柱形外壳的锂离子动力电池的俯视图 形;  FIG. 1B is a top view of a lithium-ion power battery with a cylindrical case;
图 1 C 所示为采用圆柱形外壳的锂离子动力电池的正、 负 极片的卷绕方式;  Figure 1C shows the winding of the positive and negative pole pieces of a lithium-ion power battery with a cylindrical case;
图 2A 所示为采用方形外壳的锂离子动力电池的俯视图 形;  FIG. 2A shows a top view of a lithium-ion power battery with a square case;
图 2 B 所示为采用方形外壳的锂离子动力电池的正、 负极 片的卷绕方式;  Figure 2B shows the winding method of the positive and negative plates of a lithium-ion power battery with a square case;
图 3所示则为采用方形外壳的锂离子动力电池剖视图; 图 4A、 4 A-1、 4B、 4B- 1、 4 C、 4 C-1 4D、 4D-1 为大叶单 极耳和大叶多极耳的示意图;  Figure 3 is a sectional view of a lithium-ion power battery with a square case; Figures 4A, 4 A-1, 4B, 4B-1, 4 C, 4 C-1 4D, and 4D-1 are large-leaf monopoles and large Schematic diagram of leaf multipole;
图 5和图 6分別表示压簧式和压片式安全阀的结构。  Figures 5 and 6 show the structure of a pressure spring type and a plate type safety valve, respectively.
具体实施方式  detailed description
从外观而言, 锂离子动力电池的基本构成如图 1 A、 图 2A 所示, 每个单体电池系由盖板 1 、 负极极柱 2 、 安全阀 3 、 正 极极柱 4和敞口外壳 9 、 内本体 7组成; 在锂离子动力电池的 内腔中, 则有集电夹板 ( 亦称极片夹板) 6 、 电解液 8 、 负极 片 1 2 、 正极片 1 3 以及隔膜 1 9 。 外壳 9 、 盖板 1 、 负极柱 2 、 安全阀 3 、 正极柱 4构成锂离子动力电池的外本体; 正负 极片组, 隔膜、 集电夹板构成锂离子动力电池的内本体 7 。 以 下详细描述卷绕式锂离子动力电池的结构。  From the perspective of appearance, the basic structure of a lithium-ion power battery is shown in Figures 1A and 2A. Each unit battery consists of a cover plate 1, a negative pole 2, a safety valve 3, a positive pole 4, and an open case. 9. The inner body 7 is composed of: in the inner cavity of the lithium-ion power battery, there is a current collector plywood (also referred to as a pole piece plywood) 6, an electrolyte 8, a negative electrode piece 12, a positive electrode piece 1 3, and a separator 19. The outer casing 9, the cover plate 1, the negative pole 2, the safety valve 3, and the positive pole 4 constitute the outer body of the lithium-ion power battery; the positive and negative pole piece groups, the diaphragm, and the current collector plye constitute the inner body 7 of the lithium-ion power battery. The structure of a wound lithium-ion power battery is described in detail below.
卷绕式锂离子动力电池的结构  Structure of wound lithium-ion power battery
锂离子动力电池的卷绕式内本体 7 系由正、 负极片与隔膜 共同构成具有如图 1 C 或如图 2B 所示的盘状结构的电极集合 体, 正负极的展成片均为如图 4 A、 图 4 A - 1 的较为狭长的 矩形片。  The wound inner body 7 of a lithium-ion power battery is composed of a positive electrode, a negative electrode sheet, and a separator. The electrode assembly has a disc-shaped structure as shown in FIG. 1C or FIG. 2B. As shown in Figure 4 A, Figure 4 A-1 is a relatively narrow rectangular piece.
正极 1 3 由铝箔及正极活性物质组成, 铝箔为薄片状之金 属箔, 两面均勾涂布了正极活性物质 (既可以是钴酸锂、 也可 以是锰酸锂或镍酸锂、 镍钴酸锂) 。 铝箔的表面通常比较光 滑, 但表面较为粗糙的铝箔对涂布活性物质而言, 附着力更 好。 较为适宜的铝箔厚度范围为 1 0 μ ιη ~ 8 0 μ m , 充放电要 求 1 C ~ 2 C时, 排除其他影响因素, 选用铝箔的最佳厚度为 1 5 μ ιη~ 2 5 μ ιη; 充放电要求 2 C ~ 3 C或更大时, 排除其 他影响因素, 选用铝箔的最佳厚度为 2 0 μ m~ 4 5 μ m 或以 上。 The positive electrode 1 3 is composed of an aluminum foil and a positive electrode active material. The aluminum foil is a thin metal foil, and both sides are coated with a positive electrode active material (either lithium cobaltate, lithium manganate or lithium nickelate, or nickel cobalt acid). Lithium). The surface of the aluminum foil is usually smooth, but the aluminum foil with a rougher surface has better adhesion for coating active materials. The suitable aluminum foil thickness ranges from 10 μm to 80 μm. When seeking 1 C ~ 2 C, exclude other influencing factors. The optimal thickness of aluminum foil is 15 μm ~ 2 5 μιη. When charging and discharging requirements are 2 C ~ 3 C or greater, exclude other influencing factors and use aluminum foil. The optimal thickness is 20 μm to 4 5 μm or more.
负极 1 2 由铜箔及负极活性物质组成, 铜箔为薄片状之金 属箔, 两面均匀涂布了负极活性物质 (既可以是天然石墨、 也 可以是鳞片石墨、 人造石墨或石油焦炭) 的集电体。 铜箔的表 面通常比较光滑, 但表面较为粗糙的铜箔对涂布活性物质而 言, 附着力更好。 较为适宜的铜箔厚度为 6 μ πι~ 5 0 μ ιη, 充 放电要求 1 C ~ 2 C时, 排除其他影响因素, 选用铜箔的最佳 厚度为 8 μ ιη~ 2 0 μ ιη; 充放电要求 2 C ~ 3 C或更大时, 排 除其他影响因素, 选用铜箔的最佳厚度为 1 5 μ m~ 3 5 μ m 或以上。  The negative electrode 1 2 is composed of a copper foil and a negative electrode active material. The copper foil is a thin metal foil, and both sides are uniformly coated with a collection of negative electrode active materials (either natural graphite, flake graphite, artificial graphite, or petroleum coke). Electric body. The surface of the copper foil is usually smooth, but the copper foil with a rougher surface has better adhesion for coating active materials. The suitable thickness of copper foil is 6 μ π ~ 50 μ ιη. When the charge and discharge requirements are 1 C ~ 2 C, other factors are excluded. The optimal thickness of copper foil is 8 μ ιη ~ 2 0 μ ιη; charge and discharge When 2 C ~ 3 C or more is required, other factors are excluded, and the optimal thickness of copper foil is 15 μm to 3 5 μm or more.
无论正极铝箔抑或负极铜箔, 厚度都不宜太厚。 金属箔 (铝箔 /铜箔) 的厚度既与集流体的面积相关, 更与每一单片 极片的电容量相关, 较大电容量的极片的金属箔厚度比较小电 容量的极片的金属箔的厚度应当稍厚。 在条件许可的情况下金 属箔应当尽可能薄, 以期在涂布同量的活性物质时获得更大的 极片面积, 从而获得更好的电性能。  Neither the positive aluminum foil nor the negative copper foil should be too thick. The thickness of the metal foil (aluminum foil / copper foil) is not only related to the area of the current collector, but also to the capacitance of each single-piece pole piece. The thickness of the metal foil should be slightly thicker. Where possible, the metal foil should be as thin as possible, in order to obtain a larger electrode sheet area when applying the same amount of active material, thereby obtaining better electrical properties.
为了减小金属箔的重量和体积, 也为了增加金属箔的柔韧 性, 以便于将锂离子动力电池制造成能够适应各种不同形态需 要的形状, 无论正极抑或负极所用的金属箔, 还可另行选用丝 网状或平板网状的金属箔。 所谓平板网状的金属箔, 即在薄的 铝箔或铜箔上以机械方法或化学方法或其他方法打出若干细密 的小孔, 经纵横方向上拉伸而成。  In order to reduce the weight and volume of the metal foil, as well as to increase the flexibility of the metal foil, in order to manufacture the lithium-ion power battery into a shape that can meet the needs of various forms, whether the metal foil used for the positive electrode or the negative electrode can also be separately Use wire mesh or flat mesh metal foil. The so-called flat mesh metal foil is formed by punching a number of fine small holes mechanically or chemically or by other methods on a thin aluminum or copper foil, and stretching it in the vertical and horizontal directions.
既往的锂离子电池的活性物质 (不包括导电剂、 粘结剂、 分散剂 ) 在配料总量中约占 9 0 %, 其余约 1 0 %为导电剂、 粘结剂、 分散剂。 本发明涉及的锂离子动力电池的活性物质的 量无论正极抑或负极均有较大增加, 约为 9 3 % ~ 9 5 %甚至 更高。 正极活性物质的密度每平方厘米为 0. 0 2 g~ 0. 0 6 g, 正极活性物质的最佳密度每平方厘米为 0. 0 3 2 g~ 0 · 0 4 2 g; 负极活性物质的密度每平方厘米约为 0. 0 1 g~ 0. 0 3 g, 负极活性物质的最佳密度每平方厘米为 0. 0 1 4 g~ 0.Active materials (excluding conductive agents, binders, and dispersants) of previous lithium-ion batteries accounted for about 90% of the total ingredients, and the remaining about 10% were conductive agents, binders, and dispersants. The amount of active material of the lithium ion power battery involved in the present invention is greatly increased, whether it is the positive electrode or the negative electrode, which is about 93% to 95% or even higher. The density of the positive electrode active material is 0.02 g to 0.06 g per square centimeter, and the optimal density of the positive electrode active material is 0.03 2 g to 0 · 0 4 2 g per square centimeter; Density per square centimeter is about 0. 0 1 g ~ 0. 0 3 g, the optimal density of the negative electrode active material per square centimeter is 0. 0 1 4 g ~ 0.
0 2 1 g。 0 2 1 g.
锂离子动力电池的主要特性应适合动力用途, 就必须适应 大功率充放电要求。 本发明中的重要构成为采用了面积较大的 集电 (集流) 端子即大叶极耳, 大叶极耳更利于导流、 散热, 完全可以适应大功率充放电要求。 为了名称的一致性及尽可能 体现本发明中集电 ( 集流) 端子的特征形象, 故将集电 ( 集 流) 端子称为大叶极耳。 每一极片只有一个极耳的称为大叶单 极耳, 如图 4A、 图 4A - 1所示, 每一极片有若干个极耳的 称为大叶多极耳, 如图 4B、 图 4B - 1 ; 图 4C、 图 4C - 1 ; 图 4D、 图 4D — 1所示。  The main characteristics of lithium-ion power batteries should be suitable for power applications, and they must meet the requirements of high-power charge and discharge. An important structure in the present invention is to use a large-area collector (current-collection) terminal, that is, a large leaf tab, which is more conducive to current conduction and heat dissipation, and can fully meet the requirements of high-power charge and discharge. In order to have the same name and reflect the characteristic image of the current collecting (collecting) terminal in the present invention as much as possible, the current collecting (collecting) terminal is called a large leaf tab. Those with only one pole tab on each pole piece are called large leaf monopoles, as shown in Figure 4A and Figure 4A-1, and those with several pole pieces on each pole piece are called large leaf multipole ears, as shown in Figure 4B, Fig. 4B-1; Fig. 4C, Fig. 4C-1; Fig. 4D, Fig. 4D-1.
裁切极片时, 应将正负极片分别裁切成符合工艺尺寸、 形 状狭长的展成片。  When cutting the pole pieces, the positive and negative pole pieces should be cut into elongated pieces that conform to the process size and shape.
正、 负极片的尺寸因其工艺要求而有所不同, 由于正极的 活性物质的价格远比负极的活性物质昂贵, 故在裁切时采取负 极片的长、 宽均比正极片略大一点的做法, 节省资源, 充分发 挥正极的物质性能, 亦即正极片的面积比负极片的面积略小, 负极片的面积比正极片的面积略大。  The size of the positive and negative electrode sheets varies due to their process requirements. Since the price of the active material of the positive electrode is much more expensive than that of the negative electrode, the length and width of the negative electrode sheet are slightly larger than those of the positive electrode when cutting. This method saves resources and gives full play to the material properties of the positive electrode, that is, the area of the positive electrode sheet is slightly smaller than that of the negative electrode sheet, and the area of the negative electrode sheet is slightly larger than that of the positive electrode sheet.
正极 1 3 、 负极 1 2通常裁切为带有大叶单极耳 ( 1 1 / The positive electrode 1 3 and the negative electrode 1 2 are usually cut into monopole ears with large leaves (1 1 /
1 0 ) 的狭长矩形片并刮去极耳处的浆料; 正极 1 3 、 负极 1 的浆、 。 , 、 ^ 1 0) and scrape the slurry at the pole ears; the positive electrode 1 3 and the negative electrode 1. ,, ^
大叶极耳的制作方法除裁切外, 还可以滚切或剪切冲压的 方式直接加工出成型的极片。  In addition to cutting, large leaf tabs can also be processed by roll cutting or shear stamping to form the pole pieces directly.
较小容量的锂离子动力电池, 正极、 负极通常各只有一个 大叶极耳; 较大容量的锂离子动力电池则有若干个大叶极耳。 故在有需要时, 正负极片也可制作成如图 B、 图 B - 1所示的 大叶多极耳, 大叶多极耳的导流性能显然 较大叶单极耳更 优, 散热性能也会更好。  For the lithium-ion power battery with smaller capacity, the positive and negative electrodes usually have only one large leaf tab; for the lithium-ion power battery with larger capacity, there are several large leaf tabs. Therefore, when necessary, the positive and negative electrodes can also be made into large-leaf multipolar ears as shown in Figure B and Figure B-1. Thermal performance will also be better.
正极的大叶极耳 1 1 、 负极的大叶极耳 1 0的极耳宽度应 当在条件许可的情况下尽可能采用较大的截面积, 也就是说, 极耳应当尽可能宽, 尽可能厚, 集电 (集流) 路径应当尽可能 缩短, 有利于电流的导出和散热。 大叶极耳的宽度当然是越宽越有利于导流、 散热。 但正负 极片上的大叶极耳如果从同一方向例如向上引 出, 如图 4 A 、 图 4 A - 1所示, 无论是大叶单极耳或大叶多极耳, 也无论最 后是卷绕成圆柱形内本体抑或方形内本体, 大叶极耳的最大宽 度须小于大叶极耳所在或所构成的那一圏的周长的一半 ( 1 / 2 ) 。 The width of the tabs of the large leaf tabs 1 1 for the positive electrode and the large leaf tabs 10 for the negative electrode should be as large as possible in cross-section, if possible, that is, the tabs should be as wide as possible and as wide as possible. Thick, the current collecting (collecting) path should be as short as possible, which is conducive to the extraction and heat dissipation of the current. Of course, the larger the width of the large leaf pole ears, the better it is for diversion and heat dissipation. However, if the large leaf tabs on the positive and negative electrodes are pulled out from the same direction, for example, as shown in Figures 4A and 4A-1, whether it is a large leaf monopole or a large leaf multipole, whether it is the last roll The maximum width of the large leaf tabs must be less than half (1/2) of the circumference of the stack where the large leaf tabs are located or formed.
较大容量的动力电池的极耳, 相对较小容量的动力电池的 极耳, 从导流、 散热、 高倍率充放电的性能而言, 显然要更宽 大一些才能满足要求。  The lugs of a larger-capacity power battery and the lugs of a smaller-capacity power battery obviously need to be wider to meet the requirements in terms of the performance of current conduction, heat dissipation, and high-rate charging and discharging.
无论采用圆柱形外壳抑或方形外壳, 大叶多极耳的间距不 等, 继续卷绕, 极片上各个极耳须在相同位置重合, 以便整齐 地装入集电夹板。 大叶多极耳的间距与采用圆柱形外壳的内本 体 7 的直径 (周长) 相关, 与采用方形外壳的内本体 7的周长 相关。 由于卷绕式锂离子动力电池的内本体 7 系经卷绕而成, 每一圏展开的周长是不同的, 内圏展开的周长相对于外圏展开 的周长而言要小, 故内圏极耳的间距小于外圏极耳的间距。  Regardless of the cylindrical case or the square case, the pitch of the large-leaf multi-pole ears is different. Continue winding, and the pole ears on the pole pieces must be coincident at the same position in order to fit the current collector plate neatly. The distance between the large-leaf multipole ears is related to the diameter (perimeter) of the inner body 7 with a cylindrical shell, and to the circumference of the inner body 7 with a square shell. Because the inner body 7 of the wound lithium-ion power battery is wound, the perimeter of each roll is different. The perimeter of the inner roll is smaller than the perimeter of the outer roll. The pitch of the condyles is smaller than the pitch of the outer condyles.
鉴于前述理由 (每一圏展开的周长是不同的, 内圏展开的 周长相对于外圏展开的周长而言要小) , 因此, 大叶多极耳除 间距不等外, 每一大叶极耳的宽度也是不等的。 如果采用圆柱 形外壳, 则内圏极耳的宽度当渐次小于外圏极耳的宽度; 如果 采用方形外壳, 则内圏极耳的宽度既可以渐次小于外圏极耳的 宽度, 也可以等宽。  In view of the foregoing reasons (the perimeter of each palate is different, the perimeter of the inner palate is smaller than the perimeter of the outer palate), therefore, the large-leaf multipole ear Leaf poles also vary in width. If a cylindrical shell is used, the width of the inner condyle is gradually smaller than the width of the outer condyle; if a square housing is used, the width of the inner condyle can be gradually smaller than the width of the outer condyle, or it can be the same width. .
实际上, 内圏极耳的宽度与外圈极耳的宽度差别很小, 故 多数情况下, 内 圏极耳的宽度与外圏极耳的宽度等宽。 换言 之, 内圏极耳的宽度在要求不很严格的情况下也可以与外圏极 耳的宽度等宽。  In fact, the width of the inner condylar ear is very different from the width of the outer conical ear. Therefore, in most cases, the width of the inner condyle is equal to the width of the outer condyle. In other words, the width of the inner ear can be as wide as the width of the outer ear if the requirements are not very strict.
通常情况下, 正极 1 3上的大叶极耳的宽度与负极 1 2上 的大叶极耳的宽度等宽。 当然, 正负极片上各自的大叶极耳的 宽度在特殊要求下也可以不等宽。 较大容量的锂离子动力电池 在需要快速大功率充放电的情况下, 正负极片上的极耳宽度应 当相等。 在需要快速大功率充电而无需大功率放电的情况下, 负极 1 2上的大叶极耳的宽度可以大于正极 1 3 上的大叶极 耳; 在需要大功率放电而无需快速大功率充电的情况下, 正极 1 3上的大叶极耳的宽度可以大于负极 1 2上的大叶极耳的宽 度。 In general, the width of the large leaf tabs on the positive electrode 13 is the same as the width of the large leaf tabs on the negative electrode 12. Of course, the width of the respective large leaf tabs on the positive and negative electrodes can also be unequal under special requirements. For large-capacity lithium-ion power batteries, when fast high-power charging and discharging are required, the tab widths on the positive and negative electrodes should be equal. In the case of fast high-power charging without high-power discharge, the width of the large leaf tabs on the negative electrode 12 can be larger than the large leaf tabs on the positive electrode 1 3; Case, positive The width of the large leaf tab on 13 may be greater than the width of the large leaf tab on the negative electrode 12.
通常情况下, 大叶极耳的最大高度通常不大于其自身 (大 叶极耳) 宽度, 最好小于其宽度。 当然, 大叶极耳的高度越小 越好。 大叶极耳的位置虽然可以随意置放, 但从集流性能而 言, 卷绕式锂离子动力电池的大叶单极耳应尽可能从极片的中 间引出。 而从加工是否方便的角度而言, 卷绕式锂离子动力电 池的大叶单极耳则可以从接近极片两端的位置引 出。 也就是 说, 大叶单极耳既可以从极片的中间引出, 也可以从接近极片 两端的位置引 出。  In general, the maximum height of the large leaf tab is usually not greater than its own (large leaf tab) width, preferably smaller than its width. Of course, the smaller the height of the lobe pole, the better. Although the position of the large leaf pole ears can be placed at will, in terms of current collecting performance, the large leaf monopole ears of the wound lithium ion power battery should be led out as far as possible from the middle of the pole piece. From the perspective of processing convenience, the large-leaf monopole ears of the wound lithium-ion power battery can be led out from the positions close to the two ends of the pole piece. That is to say, the large-leaf monopole can be drawn from the middle of the pole piece, or from the positions near the two ends of the pole piece.
大叶极耳与集流体的连接处既可以是清角 (即连接处是没 有圆弧的直角、 钝角 ) 连接, 也可作光滑圆弧连接 (即连接处 有 R角 ) , 如图 A、 图 A - 1连接处的 R , 不但具有更高的机 械强度, 也有利于防止热量集中而导致熔断极耳甚至熔毁极 片。  The connection between the large lobe pole and the current collector can be a clear angle (that is, the connection is a right angle, an obtuse angle without an arc), or a smooth arc connection (that is, the connection has an R angle), as shown in Figure A. R in the connection of Figure A-1, not only has higher mechanical strength, but also helps to prevent the concentration of heat and cause the pole tabs to be melted or even the pole pieces to be destroyed.
通常情况下, 锂离子动力电池的正负极片采用对应极耳, 即当正极 1 3 采用大叶单极耳, 负极 1 2通常亦采用大叶单极 耳; 正极 1 3 采用大叶多极耳, 负极 1 2 亦当采用大叶多极 耳。 为了因应大功率充放电的需要, 较大容量的锂离子动力电 池在需要快速大功率充放电的情况下, 正负极片上的极耳形式 应当相当、 数量应当相等。 在需要快速大功率充电而无需大功 率放电的情况下, 负极可以采用大叶多极耳, 而正极则可以采 用大叶单极耳; 在需要大功率放电而无需快速大功率充电的情 况下, 正极可以采用大叶多极耳, 负极则可以采用大叶单极 耳。  Under normal circumstances, the positive and negative plates of lithium-ion power batteries use corresponding tabs, that is, when the positive electrode 1 3 uses large-leaf monopoles, and the negative electrode 12 usually uses large-leaf monopoles; the positive electrode 1 3 uses large-leaf multipoles. The ears and the negative poles 1 2 should also adopt large leaf multipole ears. In order to meet the needs of high-power charging and discharging, when the large-capacity lithium-ion power battery needs fast high-power charging and discharging, the tabs on the positive and negative electrodes should be equivalent and the number should be equal. In the case of fast high-power charging without high-power discharge, large-leaf multipole ears can be used for the negative electrode, and large-leaf monopoles can be used for the positive pole; in the case of high-power discharge without fast high-power charging, Large-leaf multipole ears can be used for the positive pole, and large-leaf monopole ears can be used for the negative pole.
极耳的制作方法无论是直接裁切的极耳 1 0 , 1 1或经过 焊接的极耳, 均为扬头式。 所谓扬头式极耳, 可见极耳明显高 于极片涂布活性物质的部分, 其优点是便于刮粉。  The manufacturing methods of the tabs are directly cut heads 10, 11 or welded tabs. The so-called raised-ear type ears show that the ears are significantly higher than the part coated with the active material on the pole pieces, which has the advantage of being easy to scrape powder.
除扬头式极耳外, 图 4 D、 图 4 D - 1所示的极耳则为藏 头式极耳。 藏头式极耳的形式与扬头式极耳的形式恰巧相反。 这种藏头式大叶极耳 1 7 , 1 8 能够更充分利用锂离子动力电 池内腔的空间。 为了防止锂离子动力电池在大功率充放电时产生的高温熔 断较薄的极耳, 可以如图 4 C、 图 4 C - 1所示焊接的方法制 作极耳 1 5 , 1 6 , 焊接时可以若干金属片焊接, 既增加了机 械强度、 提高了导流性能, 又改善了散热性能, 因此, 制作大 叶极耳最好采用焊接大叶极耳。 焊接处 1 4必须牢固。 焊接极 耳的优点是裁切的极片毛刺较少。 焊接所用的极耳的材料, 正 极为铝制, 负极为镍制或铜制。 In addition to the raised-ear type ears, the ears shown in Figures 4D and 4D-1 are hidden-head style ears. The form of the hidden head is exactly the opposite of that of the raised head. Such Tibetan-headed large leaf pole ears 17 and 18 can more fully utilize the space of the inner cavity of the lithium ion power battery. In order to prevent the high-temperature fuse of the lithium ion power battery from melting and thinning the tabs, the tabs 1 5 and 1 6 can be made by welding as shown in Figures 4C and 4C-1. Welding of several metal pieces not only increases the mechanical strength, improves the conductivity, but also improves the heat dissipation performance. Therefore, it is best to use a welded large leaf tab for the large leaf tab. Welds 1 4 must be firm. The advantage of welding the lugs is that there is less burr on the cut pieces. The material of the tabs used for welding. The positive electrode is made of aluminum, and the negative electrode is made of nickel or copper.
大叶极耳的形状视需要可以为方形、 长方形、 半月 ( 圆 ) 形、 梯形或其他有利于导流、 散热的形状, 最佳的极耳形状为 连接处带有 R圆角的梯形。  The shape of the large leaf tabs can be square, rectangular, half-moon (circular), trapezoidal, or other shapes that facilitate flow and heat dissipation. The best tab shape is a trapezoid with R rounded corners at the connection.
从经济性考虑, 卷绕时通常将负极 1 2放在外层。 当然, 在有需要的情况下, 也可以将正极 1 3放在外层。  For economic reasons, the negative electrode 12 is usually placed on the outer layer during winding. Of course, if necessary, the positive electrode 13 can also be placed on the outer layer.
由于正负极片必须叠放一起经卷绕方式才能制造成内本体 The positive and negative electrode sheets must be stacked together and wound to make the inner body.
7 , 当极片 内折时, 可能导致脱粉, 故应考虑在极片上的内折 处加工折叠线。 折叠线处的活性物质必须刮去。 采用圆柱形外 壳的锂离子动力电池, 正负极片通常均无须加工折叠线。 当 然, 视实际需要也可以加工有折叠线。 如果采用方形外壳, 则 由于正极 1 3较脆较硬, 第一个折弯处挠曲度很大, 较易发生 脱粉甚至折断。 为了防止正极 1 3脱粉、 折断, 通常应当在正 极片如图 4 A、 图 4 B、 图 4 C、 图 4 D所示的第一个折弯处加 工折叠线 2 0 ; 也可以在第二个折弯处同时加工折叠线 2 0 -7. When the pole piece is folded inwardly, it may cause powder removal, so it should be considered to process the folding line on the pole piece inwardly folded. The active material at the fold line must be scraped off. Lithium-ion power batteries with cylindrical casings usually do not require folding lines for the positive and negative electrodes. Of course, folding lines can also be processed as needed. If a square shell is used, since the positive electrode 13 is relatively brittle and hard, the first bend has a large degree of deflection, which is easy to cause powder removal and even breakage. In order to prevent the positive electrode 13 from being powdered and broken, the folding line 20 should normally be processed at the first bend of the positive electrode sheet as shown in Fig. 4A, Fig. 4B, Fig. 4C, and Fig. 4D; Simultaneous processing of fold lines at two bends 2 0-
1 , 折叠线 2 0与折叠线 2 0 - 1 的中心间距应满足方形卷针 的宽度。 无论折叠线 2 0抑或折叠线 2 0 - 1 的宽度, 均应大 于方形卷针的厚度。 1. The center distance between the folding line 20 and the folding line 20-1 should meet the width of the square needle. Regardless of the width of the folding line 20 or the folding line 20-1, it should be larger than the thickness of the square curling needle.
采用圆柱形外壳的锂离子动力电池, 其卷绕后的内本体 7 为圆柱形, 纵剖面为矩形。 其内本体的直径与其高度比 ( 高宽 比 ) , 较为理想的高宽比为 1 : 2 , 即直径 ( 高 ) 为 1 , 宽为 The lithium-ion power battery with a cylindrical casing has a wound inner body 7 that is cylindrical and has a rectangular longitudinal section. The ratio of the diameter of the inner body to its height (aspect ratio), the ideal aspect ratio is 1: 2, that is, the diameter (height) is 1 and the width is
2 。 2 .
采用方形外壳的锂离子动力电池, 其卷绕后的内本体 7呈 矩形, 较为理想的长宽比为 6. 2: 3. 8或 6 : 4。  The lithium-ion power battery with a square casing has a rectangular inner body 7 after winding, and the ideal aspect ratio is 6. 2: 3. 8 or 6: 4.
隔膜的基本作用乃将正、 负极隔离, 防止电池短路, 吸附 并保持电解液。 隔膜除必须具有良好的绝缘性能、 稳定的化学 及电化学性能而外, 须有一定的机械强度, 亦须有较高的电导 率, 故采用多孔性的聚烯烃类材料最为合适。 鉴于锂离子动力 电池须大功率充放电的特点, 要求有更高的安全性能。 The basic function of the separator is to separate the positive and negative electrodes, prevent the battery from short-circuiting, and adsorb and maintain the electrolyte. In addition to having good insulation properties, stable chemical and electrochemical properties, the separator must have a certain mechanical strength and a high electrical conductivity. Ratio, it is most suitable to use porous polyolefin materials. In view of the characteristics that lithium-ion power batteries must be charged and discharged with high power, higher safety performance is required.
本发明涉及的锂离子动力电池主要采用具有微孔结构且电 流切断温度低的 15 ~ 8 0 μ ιη厚度的聚乙烯隔膜。 隔膜的选用原 则是越薄越-好, 但当正极或 负 极极片 的面积小于或等于 l O O Ornm χ 5 00mm 而又大于或等于 1 00mm χ 5 0mm , 充放电要求 1 C ~ 2 C时, 排除其他影响因素, 隔膜的最佳厚度为 25 μ πι ~ 4 0 μ m; 充放电要求 3C 或更大时, 排除其他影响因素, 隔膜 的最佳厚度为 4 Ο μ ιη 或以上。 当电池内部温度高于限定值时 The lithium-ion power battery involved in the present invention mainly uses a polyethylene separator with a thickness of 15 to 80 μm, which has a microporous structure and a low current cut-off temperature. The selection principle of the separator is as thin as possible, but when the area of the positive or negative electrode piece is less than or equal to 100 Ornm χ 500 mm and greater than or equal to 100 mm χ 50 mm, the charge and discharge requirements are 1 C ~ 2 C, Excluding other influencing factors, the optimal thickness of the separator is 25 μm to 40 μm; when charging and discharging requirements are 3C or greater, excluding other influencing factors, the optimal thickness of the separator is 4 Ομιη or more. When the battery internal temperature is higher than the limit value
(无论是否因短路引起) ., 具有这种特点的隔膜即自行熔闭微 孔, 阻断锂离子的通道, 电池不再发生反应。 锂离子动力电池 选用的隔膜也可采用聚丙烯材料制成的隔膜。 (Whether it is caused by a short circuit or not). A separator with this feature will automatically close the pores, block the passage of lithium ions, and the battery will no longer react. Lithium-ion power battery The separator used can also be made of polypropylene.
锂离子动力电池的隔膜也可采用直接将含有合理量的造孔 剂的聚烯烃类材料的浆料均勾涂覆在已经滚压后的正极片表面 The separator of the lithium ion power battery can also be directly coated with a slurry of a polyolefin-based material containing a reasonable amount of a pore-forming agent on the surface of the positive electrode sheet that has been rolled.
( 也可用沉浸法, 将已经滚压好的正极片沉浸在上述浆料 中 ) , 再将正极片放入特定溶剂中萃取造孔剂而形成与正极片 一体的符合要求的隔膜。 (You can also use the immersion method to immerse the rolled positive electrode sheet in the above slurry), and then place the positive electrode sheet in a specific solvent to extract the pore-forming agent to form a satisfactory separator integrated with the positive electrode sheet.
隔膜 19 通常制成长条状, 隔膜的面积无论长或宽均大于 正负极片, 除极耳外, 隔膜 1 9 必须将正极片 1 3或负极片 1 2 四周完全遮蔽住, 不可露出边缘, 以防短路。  The separator 19 is generally made in a long shape, and the area of the separator is larger than the positive and negative electrodes no matter the length or width. Except for the ears, the separator 19 must completely shield the positive electrode 13 or negative electrode 1 2 from the periphery, and the edges must not be exposed. In case of short circuit.
锂离子动力电池极柱的材质为导电、 导热性能优良的金属 材料, 除应有一定强度外, 还须有良好的散热性能。 极柱可以 为圆柱形外, 亦可采用片状, 以便利锂离子动力更快地散热。  The material of the lithium ion power battery pole is a metal material with excellent electrical and thermal conductivity. In addition to a certain strength, it must also have good heat dissipation performance. The pole can be cylindrical or sheet-shaped to facilitate faster heat dissipation by lithium ion power.
在不同的需要情况下, 极柱可安装于锂离子动力电池的任 何侧表面; 因应不同的需要, 正负极柱也可安装于锂离子动力 电池的不同的侧表面上。  Under different requirements, the poles can be installed on any side surface of the lithium-ion power battery; according to different needs, the positive and negative poles can also be installed on different side surfaces of the lithium-ion power battery.
通常情况下, 锂离子动力电池一个正极柱、 一个负极柱已 可满足需要。 为了因应大功率充放电的需要, 较大容量的锂离 子动力电池的极柱, 可以安装更多的极柱满足, 例如同时安装 两个正极极柱, 两个负极极柱。 当需要安装若干个极柱时, 正 负极柱的数量可以相等, 也可以不等。 在需要快速大功率充放 电的情况下, 正负极柱的数量应当相等; 在需要快速大功率充 电而无需大功率放电的情况下, 负极极柱的数量可以与正极极 柱的数量相等或大于正极极柱的数量; 在需要大功率放电而无 需快速大功率充电的情况下, 正极极柱的数量可以与负极极柱 的数量相等或大于负极极柱的数量。 Generally, one positive pole and one negative pole of a lithium-ion power battery can meet the needs. In order to meet the needs of high-power charging and discharging, more poles of a larger-capacity lithium-ion power battery may be installed, for example, two positive poles and two negative poles may be installed at the same time. When several poles need to be installed, the number of positive and negative poles may be equal or different. In the case of fast high-power charging and discharging, the number of positive and negative poles should be equal; in the case of fast high-power charging without high-power discharge, the number of negative poles can be the same as that of the positive pole The number of poles is equal to or greater than the number of positive poles; in the case of high power discharge without fast high power charging, the number of positive poles may be equal to or greater than the number of negative poles.
也可以调整极柱的直径来满足上述需要, 例如在需要快速 大功率充放电的情况下, 正负极柱的直径应当相等; 在需要快 速大功率充电而无需大功率放电的情况下, 负极极柱的直径可 以与正极极柱的直径相等或大于正极极柱的直径; 在需要大功 率放电而无需快速大功率充电的情况下, 正极极柱的直径可以 与负极极柱的直径相等或大于负极极柱的直径。  The diameter of the pole can also be adjusted to meet the above needs. For example, in the case of fast high-power charging and discharging, the diameters of the positive and negative poles should be equal; in the case of fast high-power charging without high-power discharge, the negative pole The diameter of the pole can be equal to or larger than the diameter of the positive pole; in the case of high power discharge without fast high power charging, the diameter of the positive pole can be equal to or larger than the diameter of the negative pole The diameter of the pole.
锂离子动力电池采用多元电解液, 可适应更宽的温度变 化。 多元电解液指的是两种以上的溶剂混合体与六氟磷酸锂混 合。 锂离子动力电池采用的是:  Lithium-ion power batteries use multiple electrolytes to accommodate wider temperature changes. Multi-component electrolyte refers to a mixture of two or more solvents and lithium hexafluorophosphate. The lithium-ion power battery uses:
( 1 ) 、 L I P F 6 (六氟磷酸锂) / E C ( 乙烯碳酸 酯) : D M C (二甲基碳酸酯) : D E C (二乙基碳酸酯) , 溶剂比例为 0. 9 5 ~ 1. 0 5 : 0. 9 5 ~ 1. 0 5 : 0. 9 5 ~ 1. 0 5; 或  (1), LIPF 6 (lithium hexafluorophosphate) / EC (ethylene carbonate): DMC (dimethyl carbonate): DEC (diethyl carbonate), the solvent ratio is 0.9 5 to 1. 0 5: 0. 9 5 ~ 1. 0 5: 0.9 5 ~ 1. 0 5; or
( 2 ) 、 L I P F 6 / E C: E M C ( 乙基甲基碳酸酯) : D E C ) , 溶剂比例为 0. 9 5 ~ 1. 0 5: 0. 9 5 ~ 1. 0 5: 0. 9 5 - 1. 0 5 ; 或  (2), LIPF 6 / EC: EMC (ethyl methyl carbonate): DEC), the solvent ratio is 0.9 5 to 1. 0 5: 0.9 5 to 1. 0 5: 0.9 5- 1. 0 5; or
( 3 ) 、 L I P F 6 / E C: DM C: EM C, 溶剂比例为 0. 9 5 - 1. 0 5 : 0. 9 5 - 1. 0 5 : 0. 9 5 - 1. 0 5 ; 或 (3), L I P F 6 / E C: DM C: EM C, the solvent ratio is 0.9 5-1. 0 5: 0.9 5-1. 0 5: 0.9 5-1. 0 5; or
( 4 ) 、 L I P F 6 / E C : D M C : E M C: D E C, 溶 剂比例为 0. 9 5 ~ 1. 0 5 : 0. 9 5 - 1. 0 5 : 0. 9 5 ~ 1. 0 5 : 0. 9 5 ~ 1. 0 5 。 (4), LIPF 6 / EC: DMC: EMC: DEC, the solvent ratio is 0.9 5 to 1. 0 5: 0.9 5-1. 0 5: 0.9 5 to 1. 0 5: 0. 9 5 ~ 1. 0 5.
本发明涉及的锂离子动力电池外壳是锂离子动力电池的一 部分, 也称为电芯壳。 在较小的电池中, 电芯壳也是正、 负极 中的一极, 在此情况下, 电芯壳也称为电极壳。 除非设计上的 必需, 大功率锂离子动力电池的电芯壳应尽量避免成为电极 壳。 通常情况下, 大功率锂离子动力电池的电芯壳不能成为电 极壳, 外壳须与极柱绝缘。 但在特殊情况下, 外壳也可成为电 极壳。  The lithium-ion power battery case according to the present invention is a part of a lithium-ion power battery, and is also called a battery case. In smaller batteries, the cell case is also one of the positive and negative electrodes. In this case, the cell case is also called the electrode case. Unless necessary by design, the cell case of high-power lithium-ion power batteries should be avoided as much as possible. Under normal circumstances, the cell shell of a high-power lithium-ion power battery cannot be an electrode shell, and the shell must be insulated from the pole. However, in special cases, the case can also become an electrode case.
卷绕式锂离子动力电池的电芯壳可以是方形 ( 包括长方 形 ) 的也可以是圆柱形的。 圆柱形外壳由上下各一个平面以及 一个圆柱形曲面组成, 方形外壳则由六个平面组成。 电芯亮与 盖板是相辅相成的, 电芯壳是方形的, 盖板自 当为方形, 电芯 壳是圆柱形的, 盖板自 当为圆形。 The cell case of a wound lithium-ion power battery can be square (including rectangular) or cylindrical. The cylindrical shell consists of a flat surface above and below, and It consists of a cylindrical curved surface and a square shell composed of six planes. The battery cell and the cover plate are complementary. The battery case is square, the cover plate is square, the battery case is cylindrical, and the cover plate is circular.
锂离子动力电池电芯壳的气密性要求较高, 且要有较高的 强度, 通常为有一定刚性的金属壳, 例如不锈钢电芯壳。 本发 明的锂离子动力电池的电芯壳既可以是金属壳, 也可以聚四氟 乙烯或聚丙烯或其他合适的塑料制造, 粘接成型, 也可以注塑 成型, 安全性能更优于金属电芯壳。  Lithium-ion power battery cell shells have higher airtightness requirements and higher strength, usually metal shells with a certain rigidity, such as stainless steel cell shells. The cell shell of the lithium-ion power battery of the present invention can be either a metal shell, or made of polytetrafluoroethylene or polypropylene or other suitable plastics, and can be bonded or injection-molded. The safety performance is better than that of metal cells. shell.
锂离子动力电池的外壳除了可以采用刚性包装外 (例如不 锈钢外壳) , 也可以采用软包装。  In addition to the case of lithium-ion power batteries, in addition to rigid packaging (such as stainless steel casing), flexible packaging can also be used.
锂离子动力电池的外壳上方或侧面设计加工有便于串联、 并联的接插端口, 方便电池串联或并联为电池组。  The upper or side of the shell of the lithium-ion power battery is designed and processed with plug-in ports that are convenient for series and parallel connection, so that the batteries can be connected in series or in parallel to form a battery pack.
锂离子动力电池在工作状态下产生的热量如果不能及时散 发, 对电池的安全、 循环寿命均有不良影响。 尤其当众多电池 并联排列时, 产生的热量更大, 散热问题更为明显, 故可在方 形外壳上加工有横向的或纵向的或纵横交错的导风槽, 有利于 尽快散热。  If the heat generated by a lithium-ion power battery under working conditions cannot be dissipated in a timely manner, it will adversely affect the battery's safety and cycle life. Especially when a large number of batteries are arranged in parallel, the heat generated is greater, and the heat dissipation problem is more obvious. Therefore, a horizontal or vertical or crisscross air guide groove can be processed on the rectangular shell, which is beneficial to heat dissipation as soon as possible.
为了尽快散热, 外壳上或其内部可以设计、 加工有散热片 In order to dissipate heat as quickly as possible, heat sinks can be designed and processed on or inside the housing
(热桥) 9 - 1 。 (Thermal bridge) 9-1.
锂离子动力电池的盖板须与电芯壳吻合, 气密性要求较 高。 锂离子动力电池的盖板也可以聚四氟乙烯或聚丙烯或其他 任何耐强酸且有一定强度的塑料制造, 注塑成型。  The cover of the lithium-ion power battery must match the battery case, and the airtightness is high. The cover of the lithium-ion power battery can also be made of PTFE or polypropylene or any other strong acid-resistant plastic with a certain strength and injection molding.
锂离子动力电池的安全阀 3 至关重要, 是为防止过充电、 短路等其他意外事故所设置的安全装置, 可在瞬间卸去超出设 计的压力。 安全阀底部的卸压孔也是锂离子动力电池的注液 口。  The safety valve 3 of the lithium-ion power battery is very important. It is a safety device provided to prevent other accidents such as overcharge and short circuit. It can instantly remove the pressure exceeding the design. The pressure relief hole at the bottom of the safety valve is also the injection port for the lithium-ion power battery.
涉及本发明的安全阀有两种, 一种以弹簧 (压簧式) 作复 位机构, 如图 5-1、 5-2、 5-3、 5 - 4、 5-5 所示; 另一种以反弓 弹片 (压片式) 作复位机构, 如图 6-6、 6-2、 6- 3、 6-4、 6- 5、 6-6所示。 分述如下:  There are two types of safety valves related to the present invention. One is a spring (compression spring type) as a reset mechanism, as shown in Figures 5-1, 5-2, 5-3, 5-4, 5-5. The anti-bow spring (pressing type) is used as the reset mechanism, as shown in Figures 6-6, 6-2, 6-3, 6-4, 6-5, 6-6. They are as follows:
压簧式安全阀的结构如图 5-1、 5- 2 。 压簧 (弹簧) 2 5 装于调节螺栓 2 3 的内孔中, 调节螺栓的内孔实际上是压簧、 密封钢球 2 2 的保持架, 压簧可在调节螺栓的内孔中纵向上下 滑移而不能横向摆动, 密封钢球也可在调节螺栓的内孔中纵向 上下滑移而不能横向摆动。 调节螺栓的外径上加工有与安全阀 本体 2 1相配的螺纹, 故调节螺栓装在安全阀本体上, 可以通 过钥匙孔 2 7 随意调节高低, 钥匙孔兼有排气的作用。 当旋转 调节螺栓施加压力予压簧, 密封钢球即被压簧固定。 调节螺栓 加工有若干竖向的排气槽 2 4 , 通过排气槽可以拧动调节螺栓 使之旋转, 在排气槽的下部则开有排气孔 2 8 。 最下层是氟橡 胶圏 2 6或其他耐腐蚀的胶圏垫, 压在或贴在锂离子电池盖板 1上的注液孔上, 密封钢球则陷压在氟橡胶圏 2 6或其他耐腐 蚀的胶圏垫上。 安全阀底部的卸压孔与盖板 1 上的注液孔相 通, 故卸压孔在注液时即为注液孔。 The structure of the pressure spring safety valve is shown in Figures 5-1 and 5- 2. The compression spring (spring) 2 5 is installed in the inner hole of the adjustment bolt 2 3. The inner hole of the adjustment bolt is actually a retainer for the compression spring and the sealed steel ball 2 2. The compression spring can be vertically moved up and down in the inner hole of the adjustment bolt. The sliding steel ball can not swing laterally, and the sealing steel ball can also slide vertically in the inner hole of the adjusting bolt without swinging horizontally. The outer diameter of the adjustment bolt is processed with a thread matching the safety valve body 21, so the adjustment bolt is installed on the safety valve body, and the height can be adjusted at will through the key hole 27, which also serves as an exhaust. When the rotation adjusting bolt applies pressure to the compression spring, the sealing steel ball is fixed by the compression spring. The adjusting bolt is processed with a plurality of vertical exhaust grooves 2 4. Through the exhaust groove, the adjusting bolt can be rotated to rotate, and an exhaust hole 2 8 is opened at the lower part of the exhaust groove. The lowest layer is fluoro rubber 圏 26 or other corrosion-resistant rubber pads, which are pressed or attached to the liquid injection holes on the lid 1 of the lithium ion battery, and the sealed steel ball is trapped under fluoro rubber 圏 26 or other resistant materials. Corroded rubber pad. The pressure relief hole at the bottom of the safety valve communicates with the liquid injection hole on the cover plate 1, so the pressure relief hole is the liquid injection hole when the liquid is injected.
氟橡胶圈或其他耐腐蚀的胶圏垫除须有一定弹性, 以便密 封钢球压紧氟橡胶圏或其他耐腐蚀的胶圏垫时, 氟橡胶圏或其 他耐腐蚀的胶圏垫产生一定变形而可密封住注液孔。 压簧以其 底部内圏刚好扣压在密封钢球上部, 密封钢球的下部则陷压在 电池盖板上的氟橡胶圏 2 6或其他耐腐蚀的胶圏垫上, 约束密 封钢球不会滑开。 当锂离子动力电池内部的压力小于设定值 时, 密封钢球因压簧的压力 自动将注液口封闭, 保持电池内部 与外部环境隔离, 而当电池内部的压力大于设定值时, 会自动 顶开密封钢球卸压, 气体会在瞬间从卸压孔 2 9排出, 沿排气 孔 2 8顺着排气槽 2 4逸出。 当内压卸去后, 压簧的压力足以 再次压紧密封钢球, 从而将卸压孔密封住。  In addition, the fluorine rubber ring or other corrosion-resistant rubber pads must have some elasticity, so that when the steel ball is pressed against the fluorine rubber pad or other corrosion-resistant rubber pads, the fluorine rubber pads or other corrosion-resistant rubber pads deform The injection hole can be sealed. The compression spring is pressed against the upper part of the sealed steel ball with the inner inner part of the bottom part, and the lower part of the sealed steel ball is trapped on the fluorine rubber on the battery cover 圏 2 6 or other corrosion-resistant rubber pads to restrain the sealed steel ball from slipping. open. When the pressure inside the lithium-ion power battery is less than the set value, the sealed steel ball automatically closes the injection port due to the pressure of the compression spring to keep the inside of the battery isolated from the external environment. When the pressure inside the battery is greater than the set value, it will Automatically lift the sealed steel ball to release pressure, and the gas will be discharged from the pressure release hole 29 in an instant, and escape along the exhaust groove 2 4 along the exhaust hole 28. When the internal pressure is removed, the pressure of the compression spring is sufficient to compress the sealing steel ball again to seal the pressure relief hole.
压片式安全阀的结构如图 6 -1、 6-2所示。 反弓弹片 30装 于调节螺栓 2 3 的下部, 调节螺栓加工有与安全阀本体 21相配 的螺紋, 故调节螺栓装在安全阀本体上, 底部紧压在反弓弹片 上, 可以通过拧动钥匙孔 8调节螺栓的高低, 调整反弓弹片的 张力。 安全阀本体内加工有一长方形的排气槽 31 , 反弓弹片 装在长方槽内除可上下弹动外, 不可水平旋转。 安全阀本体的 下部内径较小, 形成保持架, 密封钢球 22 在保持架内可以纵 向上下滑移。 反弓弹片上加工有工艺装配孔 33, 正好扣压在 钢球的上部固定密封钢球。 密封钢球的下部孔则陷压在盖板注 液口上的氟橡胶圏或其他耐腐蚀的胶圏垫上, 既固定住了密封 钢球, 也密封住了电池。 氟橡胶圏或其他耐腐蚀的胶圏垫除须有一定弹性, 以便密 封钢球压紧氟橡胶圏或其他耐腐蚀的胶圏垫时, 氟橡胶圏或其 他耐腐蚀的胶圏垫产生一定变形而可密封住注液孔。 压簧以其 底部内圏刚好扣压在密封钢球上部, 密封钢球的下部则陷压在 电池盖板上的氟橡胶圏 26 上, 约束密封钢球不会滑开。 当锂 离子动力电池内部的压力小于设定值时, 密封钢球因压簧的压 力 自动将注液口封闭, 保持电池内部与外部环境隔离, 而当电 池内部的压力大于设定值时, 会自动顶开密封钢球卸压, 气体 瞬间会从卸压孔 29 排出, 沿排气槽 31 从排气孔 32 以及钥匙 孔 27 逸出。 当内压卸去后, 反弓弹片的压力足以再次压紧密 封钢球, 从而将卸压孔密封住。 The structure of the tablet safety valve is shown in Figure 6-1 and 6-2. The reverse bow spring piece 30 is installed at the lower part of the adjusting bolt 23, and the adjustment bolt is processed with a thread matching the safety valve body 21. Therefore, the adjustment bolt is installed on the safety valve body, and the bottom is pressed tightly on the reverse bow spring piece. Hole 8 adjusts the height of the bolt and adjusts the tension of the anti-bow spring. The safety valve body is processed with a rectangular exhaust groove 31, and the anti-bend spring is installed in the rectangular groove. It can not be rotated horizontally except it can spring up and down. The inner diameter of the lower part of the safety valve body is small, forming a cage, and the sealing steel ball 22 can be vertically moved down in the cage. The anti-bow spring is processed with a process assembly hole 33, which is crimped on the upper part of the steel ball to fix the sealed steel ball. The lower hole of the sealed steel ball is trapped on the fluoro rubber 圏 or other corrosion-resistant rubber pad on the cover injection port, which not only fixes the sealed steel ball, but also seals the battery. In addition, fluororubber or other corrosion-resistant rubber mats must have some elasticity, so that when the steel ball is pressed against the fluororubber or other corrosion-resistant rubber mats, the fluororubbers or other corrosion-resistant rubber mats will deform. The injection hole can be sealed. The compression spring is snapped on the upper part of the sealing steel ball with the inner 圏 at the bottom, and the lower part of the sealing steel ball is trapped on the fluoro rubber 圏 26 on the battery cover plate, restraining the sealing steel ball from sliding away. When the pressure inside the lithium-ion power battery is less than the set value, the sealed steel ball automatically closes the injection port due to the pressure of the compression spring to keep the inside of the battery isolated from the external environment. When the pressure inside the battery is greater than the set value, it will The pressure of the sealed steel ball is automatically lifted to release pressure, and the gas is instantly discharged from the pressure relief hole 29, and escapes from the exhaust hole 32 and the key hole 27 along the exhaust groove 31. When the internal pressure is removed, the pressure of the anti-bow spring is sufficient to compress the sealing steel ball again to seal the pressure relief hole.
氟橡胶圈 26可以其他任何合适的胶圏代替。  The fluorine rubber ring 26 may be replaced by any other suitable rubber.
反弓弹片可以设计、 加工成平板形或如图 6 一 1 的半月形 反弓弹片。 平板形反弓弹片的工作原理同半月形反弓弹片相 同。  The anti-bow shrapnel can be designed and processed into a flat shape or a half-moon shaped anti-bow shrapnel as shown in Figure 6-1. The working principle of the flat anti-bow shrapnel is the same as that of the half-moon anti-bow shrapnel.
压片式安全阀的压力还可以通过如图 6-2 所示的螺钉 3 4 微调反弓弹片的张紧状态。  The pressure of the tablet-type safety valve can also be adjusted by the screws 3 4 shown in Figure 6-2.
为了更为迅速地排气, 安全阀也可以设计为在本体上另行 加工有若干排气小孔 3 5 。  In order to evacuate more quickly, the safety valve can also be designed with several vent holes 3 5 in the body.
氟橡胶圏 2 6上的卸压孔 2 9与盖板 1上的注液孔为相通 孔, 亦与安全岡底部的卸压孔相通, 故不另行标出。  The pressure relief hole 2 9 on the fluorine rubber 圏 2 6 and the liquid injection hole on the cover plate 1 are communication holes and also communicate with the pressure relief hole on the bottom of the safety gang, so they are not marked separately.
无论压簧式安全岡抑或压片式安全阀, 密封钢球 2 2均可 设计、 加工为带有水平横槽的球体 2 2 - 1 , 氟橡胶圏 2 6 - 1 则箍紧在密封钢球 2 2 - 1上的水平横槽中。 压簧或反弓弹 片压下密封钢球 2 2 - 1 时, 氟橡胶圏 2 6 - 1则密封住注液 孔。 为了防止密封钢球 2 2 - 1摆动, 也可在其上加工一固定 小柄 3 5 , 压簧或反弓弹片套在固定小柄上。 当内压小于允许 值时, 压簧或反弓弹片则压住密封钢球 2 2 - 1 , 氟橡胶圏 2 6 - 1 紧密封住注液孔。 当内压大于允许值, 顶起密封钢球 2 2 - 1 时, 氟橡胶圏 2 6 - 1则与其同时向上抬起, 迅速卸去 内压。  Regardless of the pressure spring type safety valve or the pressure plate type safety valve, the sealed steel ball 2 2 can be designed and processed into a ball 2 2-1 with horizontal transverse grooves, and the fluorine rubber 圏 2 6-1 is hung on the sealed steel ball. 2 2-1 in the horizontal slot. When the compression spring or reverse bow spring presses down the sealing steel ball 2 2-1, the fluorine rubber 圏 2 6-1 seals the injection hole. In order to prevent the sealed steel ball 2 2-1 from swinging, a fixed small handle 3 5 can also be processed thereon, and a compression spring or an anti-bow spring is sleeved on the fixed small handle. When the internal pressure is less than the allowable value, the compression spring or reverse bow spring presses the sealing steel ball 2 2-1 and the fluorine rubber 圏 2 6-1 tightly seals the injection hole. When the internal pressure is higher than the allowable value, the sealed steel ball 2 2-1 is lifted, and the fluoro rubber 圏 2 6-1 is lifted upwards at the same time, and the internal pressure is quickly released.
密封钢球 2 2也可设计、 加工为密封锥台 2 2 - 2 。 与钢 球 2 2或 2 2 - 1相比, 密封锥台的下部伸入注液孔, 因而复 位更可靠。 密封锥台上也可加工有固定小柄 3 6 , 压簧或反弓 弹片套在固定小柄上。 当内压小于允许值时, 压簧或反弓弹片 则压住密封锥台 2 2 - 2 , 氟橡胶圏 2 6在密封锥台的压力产 生形变从而紧密封住注液孔。 当内压大于允许值, 顶起密封锥 台 2 2 - 2 时, 迅速卸去内压。 密封锥台也可设计、 加工为 2 2 - 3 , 其上有一水平横槽, 氟橡胶圏 2 6 - 1则箍紧在密封 锥台 2 2 - 3上的水平横槽中。 压簧或反弓弹片压下密封锥台 2 2 - 3 时, 氟橡胶圏 2 6 - 1则密封住注液孔。 当内压大于 允许值, 顶起密封锥台 2 2 - 3 时, 氟橡胶圏 2 6 - 1则与其 同时向上抬起, 迅速卸去内压。 The sealing steel ball 2 2 can also be designed and processed into a sealing frustum 2 2-2. Compared with the steel ball 2 2 or 2 2-1, the lower part of the sealing frustum protrudes into the injection hole, so Bit more reliable. The sealing frustum can also be processed with a fixed small handle 3 6, and a compression spring or an inverse bow spring is sleeved on the fixed small handle. When the internal pressure is less than the allowable value, the compression spring or reverse bow spring presses the sealing frustum 2 2-2, and the pressure of the fluorine rubber 圏 26 in the sealing frustum deforms to tightly seal the injection hole. When the internal pressure is greater than the allowable value, lift the sealing cone 2 2-2 and quickly remove the internal pressure. The sealing frustum can also be designed and machined as 2 2-3, which has a horizontal horizontal groove, and the fluoro rubber 圏 2 6-1 is hooped in the horizontal horizontal groove on the sealing frustum 2 2-3. When the compression spring or reverse bow spring presses down the sealing cone 2 2-3, the fluorine rubber 圏 2 6-1 seals the injection hole. When the internal pressure is larger than the permissible value, when the sealing cone 2 2-3 is lifted up, the fluorine rubber 圏 2 6-1 is lifted upward at the same time, and the internal pressure is quickly released.
密封钢球 2 2或 2 2 - 1或密封锥台 2 2 - 2 、 2 2 - 3 上的固定小柄 3 6也可设计为空心套筒, 将压簧装入导向性能 更好的空心套筒中。  The sealing steel ball 2 2 or 2 2-1 or the sealing frustum 2 2-2, 2 2-3 can also be designed as a hollow sleeve, and the compression spring is inserted into a hollow sleeve with better guiding performance. in.
通常情况下, 安全阀与极柱应安装在锂离子动力电池外壳 的同一个侧表面上, 惟根据需要, 也可以安装在不同的侧表 面。  Generally, the safety valve and the pole should be installed on the same side surface of the lithium-ion battery case, but they can also be installed on different side surfaces as required.
因应不同的需要, 安全阀、 极柱可安装于锂离子动力电池 的任何侧表面。  According to different needs, safety valves and poles can be installed on any side surface of the lithium-ion power battery.
为了安全, 较大容量的锂离子动力电池, 可以在同一个侧 表面或不同的侧表面安装若干个安全阀。  For safety, a large-capacity lithium-ion power battery may have several safety valves installed on the same side surface or on different side surfaces.
活性物质 (浆料) 的配比及其配制方法  Proportion of active substance (slurry) and its preparation method
在锂离子电池的生产工艺中, 配制 (配料) 工序与涂布工 序极为关键, 对锂离子动力电池的电性能影响最大。  In the production process of lithium-ion batteries, the preparation (batching) process and coating process are extremely critical, and have the greatest impact on the electrical performance of lithium-ion power batteries.
桨料的配制。 配制浆料的介质有以 NM P ( N -甲基 - 2 -吡咯烷酮 ) 为介质或以水 (去离子水、 蒸馏水、 纯净水) 为 介质; 配制的方法则有湿法和干法。 本发明的说明书依照介质 区分, 则先说明 NM P介质, 后说明水介质; 依照配制方法区 分, 则先说明湿法 ( 湿法亦有二: 循序配制法、 混合配制 法) , 后说明干法 (正极) 。 兹分述如下:  Preparation of paddle materials. The medium for preparing the slurry includes NM P (N-methyl-2 -pyrrolidone) as the medium or water (deionized water, distilled water, purified water) as the medium; the preparation methods include wet method and dry method. In the description of the present invention, according to the medium, the NMP medium is described first, and then the water medium is described. In accordance with the preparation method, the wet method is first described (there are also wet methods: sequential preparation method and mixed preparation method), and then the dry method is described. (Positive). It is described below:
正极。 以 NM P为介质。 所需材料: P V D F (聚偏二氟 乙烯) 2. 5 % ~ 3. 5 %、 钴酸锂 9 3 % ~ 9 5 %、 导电剂石 墨 1 % ~ 2 % (或乙炔黑 0 . 5 % ~ 1 % ) 、 碳黑 2 % ~ 3 %。 N M P的用量受前述物质特别是受鈷酸锂粒径大小、 粒度 分布的制约, 故约为所有前述物质总量的 3 0 % ~ 1 0 0 %即 固液比 = 1 (活性物质固含量) : 0. 3 ~ 1 ( NM P ) ; 通常 情况下, 最佳的固液比 = 1 : 0. 3 5 ~ 0. 7 。 P V D F、 石 墨 (或乙炔黑 ) 、 碳黑均需在约 1 2 0 。C烘箱内烘烤约 2 ~ 3 小时。 positive electrode. Use NM P as the medium. Materials required: PVDF (polyvinylidene fluoride) 2.5% ~ 3.5%, lithium cobaltate 93% ~ 95%, conductive agent graphite 1% ~ 2% (or acetylene black 0.5% ~ 1%), carbon black 2% ~ 3%. The amount of NMP is affected by the particle size and particle size of the foregoing substances, especially lithium cobaltate. Restriction on distribution, so it is about 30% ~ 100% of the total amount of all the aforementioned substances, that is, the solid-liquid ratio = 1 (active substance solid content): 0.3 ~ 1 (NM P); usually, the best的 solid-liquid ratio = 1: 0.3 5 to 0.7. PVDF, graphite (or acetylene black), and carbon black all need to be about 120. C Bake in an oven for about 2 to 3 hours.
循序配制法。 将 P V D F加入 N M P搅拌约 3 ~ 4 小时 后, 加入导电剂石墨 (或乙炔黑 ) 、 碳黑搅拌约 0. 5 ~ 1 小 时, 最后加入钴酸锂搅拌约 2. 5 ~ 4 小时成粘稠的浆状。  Sequential preparation method. After adding PVDF to NMP and stirring for about 3 to 4 hours, add conductive agent graphite (or acetylene black), carbon black and stir for about 0.5 to 1 hour, and finally add lithium cobaltate and stir for about 2.5 to 4 hours to become viscous. Pasty.
混合配制法。 将 P V D F加入 NM P搅拌约 3 ~ 4 小时, 加入导电剂石墨 (或乙炔黑) 、 碳黑、 钴酸锂搅拌约 2. 5 ~ 4 小时成粘稠的浆状。  Mixed formulation method. Add P V D F to NM P and stir for about 3 to 4 hours. Add conductive agent graphite (or acetylene black), carbon black, and lithium cobaltate and stir for about 2.5 to 4 hours to form a thick paste.
正极。 以水为介质。 所需材料: C M C (羧甲基纤维素 钠) 0. 6 % ~ 0. 9 %、 S B R (丁苯胶乳乳液) 实际固含量 2 % ~ 4 %、 导电剂石墨 1 % ~ 2 %或乙炔黑 0 . 5 % ~ 1 %、 碳黑 1. 5 % ~ 3 %、 钴酸锂 9 3 % ~ 9 5 %。 水 (去离 子水、 蒸馏水、 纯净水) 的用量受前述物质特别是钴酸锂的粒 径的大小、 粒度的分布制约, 故约为所有前述物质总量的 4 0 % ~ 1 30 %即固液比 = 1: 0. 4 ~ 1 · 3; 通常情况下, 最佳 的固液比 = 1 : 0 .6 ~ 1。 S B R可以用 P T F E (聚四氟乙 烯) 代替。  positive electrode. Use water as the medium. Required materials: CMC (sodium carboxymethyl cellulose) 0.6% ~ 0.9%, SBR (styrene-butadiene latex emulsion) actual solid content 2% ~ 4%, conductive agent graphite 1% ~ 2% or acetylene black 0.5% to 1%, carbon black 1.5% to 3%, lithium cobaltate 93% to 95%. The amount of water (deionized water, distilled water, purified water) is limited by the particle size and particle size distribution of the aforementioned substances, especially lithium cobaltate, so it is about 40% ~ 130% of the total amount of all the aforementioned substances. Liquid ratio = 1: 0. 4 ~ 1 · 3; Under normal circumstances, the best solid-liquid ratio = 1: 0.6 ~ 1. S B R can be replaced with P T F E (polytetrafluoroethylene).
循序配制法。 将 C M C加入水中搅拌约 3 ~ 4小时后将 S B R加入其中搅拌约 0. 5 ~ 1 小时, 再将导电剂石墨 (或乙 炔黑 ) 、 碳黑加入搅拌约 0. 5 ~ 1 小时, 最后加入钴酸锂搅 拌约 2. 5 ~ 4 小时成较为粘稠的浆状, 筛去团聚物和其他杂 质。  Sequential preparation method. CMC is added to the water and stirred for about 3 to 4 hours, then SBR is added to it and stirred for about 0.5 to 1 hour, and then conductive agent graphite (or acetylene black) and carbon black are added and stirred for about 0.5 to 1 hour, and finally cobalt is added. The lithium acid is stirred for about 2.5 to 4 hours to form a thicker slurry. Sieve out agglomerates and other impurities.
混合配制法。 首先将 C M C加入水中搅拌 3 ~ 4 小时, 然 后将 S B R加入其中搅拌约 0. 5 ~ 1 小时, 再将导电剂石墨 (或乙炔黑) 、 碳黑、 钴酸锂加入搅拌约 2 . 5 - 4 小时成较 为粘稠的浆状, 最后歸去团聚物和其他杂质。  Mixed formulation method. First add CMC to water and stir for 3 ~ 4 hours, then add SBR and stir for about 0.5 ~ 1 hour, and then add conductive agent graphite (or acetylene black), carbon black, lithium cobaltate and stir for about 2.5-4 It will become a thicker paste when it is small, and finally it will agglomerate and other impurities.
鉴于锂离子动力电池需满足其高倍率充放电特性, 故正极 的配制须略加大导电剂。  In view of the fact that lithium ion power batteries need to meet their high rate charge and discharge characteristics, the preparation of the positive electrode must be slightly larger than the conductive agent.
负极。 以 N M P为介质。 所需材料: 石墨 9 3 % ~ 9 5 % P V D F 5 % ~ 7 % , N M P约为所有前述物质总量的 8 0 % ~ 1 5 0 %即固液比 - 1 : 0■ 8 ~ 1. 5 ; 最佳的固液比 = 1 : 1 ~ 1 . 3 。 P V D F需在温度约 1 2 0 。C的烘箱内烘烤 2 ~ 3 小时, 石墨则需在 3 0 0 °C ~ 5 0 0 °C温度烘烤 4 ~ 8 小时。 negative electrode. Use NMP as the medium. Materials required: Graphite 93% ~ 95% PVDF 5% ~ 7%, NMP is about 8% of the total amount of all the aforementioned substances 0% ~ 15 0% is the solid-liquid ratio-1: 0 ■ 8 ~ 1. 5; the optimal solid-liquid ratio = 1: 1 ~ 1.3. PVDF needs a temperature of about 120. B oven in C oven for 2 ~ 3 hours, graphite needs to be baked at 300 ° C ~ 500 ° C for 4 ~ 8 hours.
循序配制法。 将 P V D F加入 NM P搅拌约 3 ~ 4 小时, 再将经 3 2 5 目 筛网振动筛选备用的石墨加入搅拌约 3 ~ 4 小 时成粘稠的浆状。  Sequential preparation method. Add P V D F to NM P and stir for about 3 to 4 hours. Then add the graphite that has been sifted through a 3 2 5 mesh screen and stir for about 3 to 4 hours to form a thick slurry.
负极。 以水为介质。 所需材料: 石墨 9 3 % ~ 9 5 %、 C M C 0. 9 % ~ 1 . 5 % , S B R固含量 2 % ~ 4 %、 水 (去离 子水、 蒸馏水、 纯净水) 约为所有前述物质总量的 80 % ~ 1 60 %即固液比 = 1: 0. 8 ~ 1 . 6 ; 通常情况下, 最佳的固液 比 = 1: 1 ~ 1. 3 。 C M C需在 1 2 0 。C温度下烘烤 2 ~ 3 小 时, 石墨则需在 3 0 0 °C ~ 5 0 0 °C温度烘烤 4 ~ 8 小时。 S B R可以用 P T F E代替。  negative electrode. Use water as the medium. Materials required: Graphite 93% ~ 95%, CMC 0.9% ~ 1.5%, SBR solid content 2% ~ 4%, water (deionized water, distilled water, purified water) is about the total of all the aforementioned substances The solid-liquid ratio of 80% ~ 160% of the amount = 1: 0.8 ~ 1.6; under normal circumstances, the best solid-liquid ratio = 1: 1 ~ 1.3. C M C needs to be 1 2 0. Baking at 2 ° C to 3 ° C, graphite needs to be baked at 300 ° C ~ 500 ° C for 4 ~ 8 hours. S B R can be replaced by P T F E.
循序配制法。 将 C M C加入水中搅拌约 3 ~ 4 小时后将 S B R加入其中搅拌约 0. 5 ~ 1 小时, 最后将烘烤后并经 3 0 0 目 筛选备用的石墨加入搅拌约 3 ~ 4 小时成粘稠的浆状。  Sequential preparation method. Add CMC to water and stir for about 3 to 4 hours, then add SBR to it and stir for about 0.5 to 1 hour. Finally, add graphite after baking and sieving through 300 mesh. Stir for about 3 to 4 hours to become viscous. Pasty.
干法配制。 以 N M P为介质的正极的干法配制。 所需材 料: 所需材料: P V D F 2. 5 % ~ 3. 5 %、 钴酸锂 9 3 % ~ 9 5 %、 导电剂石墨 1 . 5 % ~ 2 % (或乙炔黑 0. 8 % ~ 1 . Dry preparation. Dry preparation of the positive electrode with N M P as the medium. Materials required: Materials required: PVDF 2.5% to 3.5%, lithium cobaltate 93% to 95%, conductive agent graphite 1.5% to 2% (or acetylene black 0.8% to 1 .
2 % ) 、 碳黑 2 % ~ 3 %。 N M P的用量受前述物质特别是钴 酸锂粒径大小、 粒度分布的制约, 故约为所有前述物庸总量的2%), carbon black 2% ~ 3%. The amount of N M P is limited by the particle size and particle size distribution of the foregoing materials, especially lithium cobaltate, so it is about the total amount of all the foregoing materials.
3 0 % ~ 1 0 0 %即固液比 = 1 ( 固含量) : 0. 3 ~ 1 ( N M P ) , 通常情况下, 最佳的固液比 - 1 : 0. 3 5 ~ 0. 7 。 P V D F、 石墨 (或乙炔黑) 、 碳黑均需在约 1 2 0 °C烘箱内烘 烤 2 ~ 3 小时。 30% ~ 100% means the solid-liquid ratio = 1 (solid content): 0.3 ~ 1 (N M P), under normal circumstances, the best solid-liquid ratio-1: 0.3. 5 ~ 0.7. P V D F, graphite (or acetylene black), and carbon black all need to be baked in an oven at about 120 ° C for 2 to 3 hours.
首先将钴酸锂、 导电剂石墨 (或乙炔黑) 、 碳黑放入混料 机内搅拌 3 小时; 同时将 P V D F与 N M P搅拌约 2 小时, 待 其完全溶解后 (清浆) , 即将混料机搅拌后的混合粉料放入经 过搅拌的 P V D F与 NM P的清浆内继续搅拌约 3 小时成粘稠 的浆状。  First put lithium cobaltate, conductive agent graphite (or acetylene black), carbon black into the mixer and stir for 3 hours; at the same time, stir PVDF and NMP for about 2 hours. After it is completely dissolved (slurry), it will be mixed The mixed powder after the machine is stirred is put into the clear slurry of PVDF and NM P after stirring, and then stirred for about 3 hours to form a thick slurry.
以氷为介质的正极的干法配制。 所需材料: C M C 0. 6 % ~ 0. 9 %、 S B R实际固含量 2 % ~ 4 %、 导电剂石墨 1 % ~ 2 %或乙炔黑 O . 5 % ~ 1 %、 碳黑 1. 5 % ~ 3 %、 钴酸 锂 9 3 % ~ 9 5 %。 水 (去离子水、 蒸馏水、 纯净水) 的用量 受前述物质特别是鈷酸锂的粒径的大小、 粒度的分布制约, 故 约为所有前述物质总量的 4 0 % ~ 1 30 %即固液比 = 1 : 0. 4 - 1.3; 通常情况下, 最佳的固液比 = 1 : 0.6 ~ 1。 S B R 可以用 P T F E (聚四氟乙烯) 代替。 Dry preparation of the positive electrode with ice as the medium. Materials required: CMC 0.6% ~ 0.9%, SBR actual solid content 2% ~ 4%, conductive agent graphite 1 % To 2% or acetylene black O. 5% to 1%, carbon black 1.5% to 3%, lithium cobaltate 93% to 95%. The amount of water (deionized water, distilled water, purified water) is limited by the particle size and particle size distribution of the aforementioned substances, especially lithium cobaltate, so it is about 40% ~ 130% of the total amount of all the aforementioned substances. Liquid-to-liquid ratio = 1: 0.4-1.3; In general, the optimal solid-to-liquid ratio = 1: 0.6 ~ 1. SBR can be replaced with PTFE (polytetrafluoroethylene).
首先将钴酸锂、 导电剂石墨 (或乙炔黑) 、 碳黑放入混料 机内搅拌约 3 小时; 同时将 C M C与水搅拌约 3 小时, 待其完 全溶解后成为清浆, 即将混料机搅拌后的混合粉料放入经过搅 拌的 C M C与水的清浆内继续搅拌约 3 小时成粘稠的浆状, 最 后筛去团聚物和其他杂盾。  First put lithium cobaltate, conductive agent graphite (or acetylene black), carbon black into the mixer and stir for about 3 hours; at the same time, stir the CMC with water for about 3 hours. After it is completely dissolved, it will become a clear slurry. The mixed powder after being stirred by the machine is put into the clear slurry of the stirred CMC and water and stirred for about 3 hours to form a thick slurry. Finally, the agglomerates and other miscellaneous shields are sieved.
在正极的配制中, 选用导电剂须注意, 导电剂的粒径须等 于或小于正极材料 (钴酸锂、 锰酸锂、 镍钴酸锂) 。  In the preparation of the positive electrode, it is necessary to pay attention to the selection of the conductive agent, and the particle size of the conductive agent must be equal to or smaller than the positive electrode material (lithium cobaltate, lithium manganate, lithium nickel cobaltate).
为了保证配制浆料的品质, 在配制浆料过程中, 无论是以 水 (去离子水、 蒸馏水、 纯净水) 为介质抑或以 N M P为介 质, 必须根据正极材料的粒径、 粒度分布以及导电剂的用量精 细计算, 一次性加足介质, 不可中途再添加; 至于负极, 也是 如此, 无论是以水 (去离子水、 蒸馏水、 纯净水) 为介质抑或 以 N M P为介质, 必须才艮据负极材料以及添加剂的用量精细计 算, 一次性加足介质, 不可中途再添加。 否则, 难以保证正极 浆料或负极浆料的品质。  In order to ensure the quality of the prepared slurry, whether the water (deionized water, distilled water, purified water) or NMP is used as the medium during the preparation of the slurry, it must be based on the particle size, particle size distribution, and conductive agent of the positive electrode material. The amount is carefully calculated, and the medium is added once and cannot be added halfway. The same is true for the negative electrode, whether it is water (deionized water, distilled water, purified water) or NMP as the medium, it must be based on the anode material. And the amount of additives is finely calculated, and the medium should be filled in one time. Do not add it halfway. Otherwise, it is difficult to ensure the quality of the positive electrode slurry or the negative electrode slurry.
锂离子动力电池正极选用的活性物质材料除了钴酸锂外, 还可以选用锰酸锂、 镍酸锂或镍钴酸锂, 配制方法与前述的选 用钴酸锂配制的方法基本相同。  In addition to the lithium cobalt oxide, the active material used for the positive electrode of the lithium-ion power battery can also be lithium manganate, lithium nickelate, or lithium nickel cobaltate. The preparation method is basically the same as that of the foregoing lithium cobaltate preparation method.
锂离子动力电池正极材料 (钴酸锂、 锰酸锂、 镍酸锂或镍 鈷酸锂) 的粒径可以在 2 μ m~ 1 2 μ m 范围内选用, 但最佳 的粒径应为 5 μ m ~ 8 μ m; 正极材料的粒度分布亦须尽可能 窄, 以选用粒径 5 μ m 材料为例, 过细 ( 2 μ ιη 以下) 的或过 粗 ( 1 2 μ m以上) 的粉体的总和通常不超过 40 %。  The particle size of the lithium ion battery positive electrode material (lithium cobaltate, lithium manganate, lithium nickelate, or lithium nickel cobaltate) can be selected in the range of 2 μm to 12 μm, but the optimal particle size should be 5 μ m ~ 8 μ m; The particle size distribution of the cathode material must also be as narrow as possible. Taking 5 μm particle size as an example, too fine (less than 2 μm) or too thick (more than 12 μm) powder The total is usually not more than 40%.
正极材料 (钴酸锂、 锰酸锂、 镍酸锂或镍钴酸锂) 2 μ m 以下的微细粉体、 1 2 μ m 以上的较粗粉体的配制方法与 2 μ m~ 1 2 μ m 范围内的配制方法除固液比不同外, 其余相同。 2 μ m 以下的微细粉体的固液比应在原固液比基础上加大 2 0 % ~ 5 0 % , 1 2 μ m 以上的较粗粉体的固液比则应在原固液 比基础上减小 1 0 % ~ 3 0 % 。 Cathode material (lithium cobaltate, lithium manganate, lithium nickelate, or lithium nickel cobaltate) Preparation method of fine powder below 2 μm, coarser powder above 1 μm and 2 μm ~ 1 2 μ The preparation method in the range of m is the same except that the solid-liquid ratio is different. The solid-liquid ratio of fine powders below 2 μm should be increased by 20 from the original solid-liquid ratio. % ~ 50%, the solid-liquid ratio of coarser powders above 12 μm should be reduced by 10% ~ 30% based on the original solid-liquid ratio.
负极材料石墨经 3 0 0 目振动筛选, 网上剩余的通常不宜 使用。 本发明中涉及的导电剂包括了石墨、 乙炔黑、 碳黑等; 上述物质的处理除石墨作为负极材料时需做高温处理外 ( 3 0 0 ~ 5 0 0 °Ο ) , 其余作烘烤处理的材料, 可以放置 在真空箱内作抽真空处理, 无需再作高温处理。  The anode material graphite is screened by 300 mesh vibration, and the remaining ones on the Internet are usually not suitable for use. The conductive agent involved in the present invention includes graphite, acetylene black, carbon black, etc .; except that graphite is used as a negative electrode material for high-temperature treatment (300 to 500 ° °), the rest is baked. The material can be placed in a vacuum box for vacuum treatment without the need for high temperature treatment.
制造方法  Production method
锂离子动力电池的生产工艺流程为: 配料 - →涂布 - →制 片 ― →滚压 - 卷绕并装配成内本体 ( 包括装壳、 封口 ) - → 注液 - →化成 - →分容。  The production process of the lithium-ion power battery is as follows: ingredients-→ coating-→ tableting-→ rolling-winding and assembling into the inner body (including casing and sealing)-→ filling-→ chemical conversion-→ volumetric.
下面分别描述各个过程。  Each process is described below.
配料过程已经在上面详细描述, 在此就不再赘述。  The batching process has been described in detail above, and will not be repeated here.
涂布 ( 亦称拉浆) 。 正极的涂布与负极的涂布并无区别, 故不分别叙述: 将搅拌好的正极 (或负极) 浆料均勾涂覆在金 属箔集流体上, 经辊刀勾速拉出进入烘箱烘烤, 烘烤干后即成 为半成品集流片。 涂布中须注意不可有划痕, 露基体, 纵横方 向上的偏轻偏重等现象。  Coating (also known as drawing pulp). There is no difference between the coating of the positive electrode and the coating of the negative electrode, so they are not described separately: The stirred positive electrode (or negative electrode) slurry is hook-coated on the metal foil current collector, pulled out by a roller knife into the oven and dried. After baking, it will become semi-finished current collector after baking. Care must be taken during coating to avoid scratches, exposed substrates, lightness and weight in the vertical and horizontal directions.
在涂布工艺中, 温度的控制非常重要: 预热区段的温度不 可太高, 通常选择的温度为 9 0 °C或以下, 中温区段的温度在 1 1 0 °C ~ 1 3 0 °C间, ± 1 0 °C、 高温区段的温度在 1 2 0 。C ~ 1 4 0 。C间, ± 1 0 。C。 在前述温度条件下, 涂布烘烤 时, 负极浆料的温度可以较正极浆料的温度稍高约 1 0 ~ 1 5 "C , 以水为介质的浆料的温度可以较 N M P为介质的浆料的温 度稍高约 1 0 ~ 1 5 °C。  In the coating process, the temperature control is very important: the temperature of the preheating section should not be too high, usually the temperature is selected at 90 ° C or below, and the temperature of the intermediate temperature section is between 1 10 ° C ~ 1 3 0 ° Between C, ± 10 ° C, the temperature in the high-temperature section is 120. C ~ 1 4 0. Between C, ± 10. C. Under the aforementioned temperature conditions, the temperature of the negative electrode slurry can be slightly higher than the temperature of the positive electrode slurry by about 10 to 15 "C during coating and baking, and the temperature of the slurry using water as the medium can be higher than that of NMP as the medium. The temperature of the slurry is slightly higher than about 10 ~ 15 ° C.
配制好的浆料涂布于金属箔上后, 无论正极抑或负极均须 从预热区段进入涂布机 (亦称拉浆机) 的烘干巷道, 绝对不可 倒置。 如果浆料 (尤其是负极浆料) 首先进入涂布机的高温区 段骤然高温烘烤, 表面很快烘干, 极易形成一层干壳, 稍一皱 折, 即形成龟裂细紋。 而干壳下的浆料则呈糖稀状, 与金属箔 间形成了一层肉眼看不见的液态膜, 浆料实际上只是虚附在金 属箔的表面, 因此极易脱粉, 甚至脱片 (即大片活性物质从金 属箔上脱落) , 严重影响锂离子动力电池的电性能。 现行的涂 布工艺大多为单面涂布, 然后再涂布另一面; 但也可以双面同 时涂布。 适用本发明的正负极片可以在金属箔的两面涂布活性 物质, 也可以只在金属箔的单面涂布活性物质, 装配时将同极 (负极与负极、 正极与正极) 的极片背面 (没有涂布活性物质 的金属光面 ) 相贴即可成为两面均有活性物质的集电体。 在此 情况下, 单面涂布所选用的金属箔厚度须较前述的金属箔厚度 要薄, 约为前述金属箔厚度的 1 / 2 ~ 1 / 3 间。 After the prepared slurry is coated on the metal foil, both the positive electrode and the negative electrode must enter the drying tunnel of the coating machine (also known as the puller) from the preheating section, and must not be inverted. If the slurry (especially the negative electrode slurry) first enters the high-temperature section of the coater and bakes suddenly at high temperature, the surface is dried quickly, and it is easy to form a dry shell, which is slightly wrinkled, which will form cracked fine lines. The slurry under the dry shell is sugar-smeared and forms a liquid film invisible to the naked eye between the metal foil. The slurry is actually virtually attached to the surface of the metal foil, so it is easy to remove powder and even flakes ( (Ie, large pieces of active material fall off the metal foil), which seriously affects the electrical performance of lithium-ion power batteries. Current coating The cloth process is mostly coated on one side and then coated on the other side; however, it can also be coated on both sides simultaneously. The positive and negative electrode sheets to which the present invention is applied may be coated with active materials on both sides of the metal foil, or may be coated with active materials only on one side of the metal foil. The back surface (metallic surface without active material coating) can be attached to form a current collector with active materials on both sides. In this case, the thickness of the metal foil used for single-sided coating must be thinner than the thickness of the aforementioned metal foil, which is about 1/2 to 1/3 of the thickness of the aforementioned metal foil.
涂布工艺中的线速度控制也很重要。 在上述温度条件下, 线速度可以在每分钟 800mm ~ 500 Omm 的范围内调整。 最佳的线 速度为每分钟 1200mm ~ 3500mm。  Line speed control in the coating process is also important. Under the above temperature conditions, the linear speed can be adjusted within the range of 800mm to 500 Omm per minute. The best linear speed is 1200mm ~ 3500mm per minute.
涂布除可以传统的拉浆方式生产锂离子动力电池的极片 外, 还可以采用高压喷涂的方式。 在干燥的保护气体的一定压 力下, 浆料从高速喷嘴中均匀喷在金属箔上, 不但附着力更 好, 产能也明显提高。  In addition to coating, which can be used to produce pole pieces of lithium-ion power batteries in the traditional drawing method, high-pressure spraying can also be used. Under a certain pressure of the dry protective gas, the slurry is sprayed evenly on the metal foil from the high-speed nozzle, which not only has better adhesion, but also significantly increases the production capacity.
制片。 制作 (焊接) 极耳, 如果直接裁切极耳, 则无制作 焊接极耳工序。 裁切极片可以剪板机、 分切机或其他设备完 成。  Production. Making (welding) the lugs, if the lugs are cut directly, there is no process of making the welding lugs. Cutting the pole pieces can be done with a shears, a slitter or other equipment.
滚压。 滚压在锂离子动力电池生产工艺中的作用不可忽 视。 线压力过大, 不但导致极片变形, 还可能妨碍电解液的渗 透, 影响锂离子的嵌入脱出, 最终势必影响锂离子动力电池的 大功率充放电性能; 线压力过小, 则会影响活性物质对金属箔 的附着力, 影响电性能。 较为适中的线压力正极约为 100 ~ 180kg / C M, 负极约为 80 ~ 160kg / C M。  Roll. The role of rolling in the production process of lithium-ion power batteries cannot be ignored. Excessive line pressure not only causes pole pieces to deform, but also impedes the penetration of the electrolyte and affects the insertion and extraction of lithium ions. It will eventually affect the high-power charge and discharge performance of lithium ion power batteries. If the line pressure is too small, it will affect active materials. Adhesion to metal foil affects electrical performance. The more moderate line pressure of the positive electrode is about 100 ~ 180kg / C M, and the negative electrode is about 80 ~ 160kg / C M.
通常情况下, 正极在滚压前的厚度约为 170 μ πι~ 270 μ m, 滚压后的厚度约为 110 μ m~ 165 μ m; 负极滚压前的厚度约 为 185 μ m~ 275 μ m, 滚压后 110 μ πι~ 165 μ πι。 正极滚压前的 最佳厚度为 195 μ m~ 235 μ 01, 滚压后的最佳厚度为 135 μ πι~ 155 μ m; 负极滚压前的最佳厚度为 220 μ πι~ 250 μ ιη, 滚压后 的最佳厚度为 135 μ m~ 155 μ ηι。  Under normal circumstances, the thickness of the positive electrode before rolling is about 170 μm to 270 μm, the thickness of the positive electrode after rolling is about 110 μm to 165 μm, and the thickness of the negative electrode is about 185 μm to 275 μ m, 110 μ π ~ 165 μ π after rolling. The optimal thickness of the positive electrode before rolling is 195 μm ~ 235 μ01, and the optimal thickness of the positive electrode after rolling is 135 μπι ~ 155 μm; the optimal thickness of the negative electrode before rolling is 220 μπι ~ 250 μ ιη, The optimal thickness after rolling is 135 μ m ~ 155 μ ηι.
卷绕。 装配时, 须将一对正负极片组整齐叠放 ( 中间衬以 隔膜) 以适当而且平均的张紧力卷绕在卷针上, 卷绕好以后用 集电夹板分别夹住正负极的极耳。 卷针有两种, 卷绕配用圆柱 形外壳内本体 7如图 1A 的卷针为一圆柱形小轴, 卷绕配用方 形外壳内本体如图 2A的卷针为有一定刚性及弹性的薄片。 Coiled. When assembling, a pair of positive and negative electrode groups must be neatly stacked (with a separator in the middle) and wound with a suitable and even tension on the winding pin. After winding, clamp the positive and negative electrodes separately Ears. There are two kinds of winding needles. The rolling pin of the inner body 7 of the shaped shell is a small cylindrical shaft as shown in FIG. 1A, and the rolling pin of the inner body of the square shell shown in FIG. 2A is a thin sheet with certain rigidity and elasticity.
也可以将多对正负极片组依照上述方式并联整齐叠放同时 卷绕。 卷绕时, 正负极耳的位置必须错开, 务令在卷绕成内本 体 7后, 正负极耳可以整齐地分列出如图 1 A、 图 2A 所示的相 对的正负两极。  Multiple pairs of positive and negative electrode groups can also be neatly stacked in parallel and wound at the same time. When winding, the positions of the positive and negative ears must be staggered. After winding into the inner body 7, the positive and negative ears can be neatly listed as the positive and negative poles shown in Figures 1A and 2A.
卷绕时还须注意, 正极 1 3上如果加工有折叠线, 应将负 极 1 2 的前端对齐正极 1 3 的折叠线的中心线, 令其不能刺破 隔膜 1 9 。  When winding, please also note that if there is a folding line on the positive electrode 13, the front end of the negative electrode 12 should be aligned with the center line of the folding line of the positive electrode 13 so that it cannot puncture the diaphragm 19.
卷绕后完成装配状态的内本体, 排除隔膜 1 9 的厚度, 正 极与负极的间隙距离, 不得大于 2 5 μ πι (正极与负极的最大 间隙 = 隔膜厚度 + 2 5 μ m ) 。  After winding the inner body in the assembled state, excluding the thickness of the separator 19, the distance between the positive electrode and the negative electrode must not be greater than 25 μm (the maximum gap between the positive electrode and the negative electrode = the thickness of the separator + 2 5 μm).
卷绕时须将正负极耳错开放置, 其正极 1 3 与负极 1 2 的 首个极耳的间距须经合理计算, 使得卷绕好的内本体 7 上的正 极极耳 1 1恰巧整齐地排列并联于内本体的一侧端, 负极极耳 1 0则恰巧整齐地排列并联于内本体的另一侧端。 内本体 7的 最外层既可以为负极片, 也可以是正极片。  When winding, the positive and negative electrodes must be staggered, and the distance between the positive electrode 1 3 and the first electrode of the negative electrode 12 must be reasonably calculated, so that the positive electrode tabs 11 on the wound inner body 7 happen to be neat and neat. The parallel arrangement is parallel to one end of the inner body, and the negative electrode tab 10 happens to be neatly arranged parallel to the other end of the inner body. The outermost layer of the inner body 7 may be either a negative electrode sheet or a positive electrode sheet.
卷绕式锂离子动力电池外壳内的内本体 7通常只有一个。 为了加工上的需要, 可以将若干个内本体并联装入一个卷绕式 锂离子动力电池的外壳 9 内, 组成较大容量的锂离子动力电 池  There is usually only one inner body 7 in the outer shell of a wound lithium-ion battery. In order to meet the processing requirements, several inner bodies can be installed in parallel in a casing 9 of a wound lithium-ion power battery to form a large-capacity lithium-ion power battery.
必须注意的是, 正极极柱 4与正极片 1 3相连接, 负极极 柱 2与负极片 1 2相连接。  It must be noted that the positive electrode pole 4 is connected to the positive electrode sheet 1 3, and the negative electrode pole 2 is connected to the negative electrode sheet 12.
为了夹紧极耳, 无论整体式集电夹板抑或分体式集电夹 板, 集电夹板与极耳接触的表面均加工有凸起的棘刺。 通常而 言, 集电夹板的覆盖面应大于大叶极耳。 夹紧的方法也分为穿 孔夹和两边夹。 整体式集电夹板系在一整体金属上切割若干可 以被压缩而又能弹开的线槽, 将极耳塞入集电夹板 A或 D的线 槽中, 以金属螺栓 5 紧固即可。 分体式集电夹板 B或 C则以若 干相互独立的金属片通过串联杆 2 Q 串联起来, 分别夹住极耳 并以金属螺栓 5 紧固。 整体式集电夹板可以穿孔夹也可以两边 夹, 同样, 分体式集电夹板也可以穿孔夹或者两边夹。 从效率 和效果而言, 穿孔夹的效率和效果比两边夹的方式都要好一 些。 In order to clamp the tabs, whether the integral current collecting splint or the split type current collecting plywood, the surface of the current collecting plywood in contact with the tabs is processed with raised spines. In general, the coverage of the current collector plywood should be larger than the large leaf tab. The method of clamping is also divided into perforated clamps and two-sided clamps. The integrated current collector ply is cut on a solid metal into several wire grooves that can be compressed and can be springed off. The pole ears are inserted into the wire grooves of the current collector ply A or D and fastened with metal bolts 5. The split-type current collecting plywood B or C is connected in series by a plurality of independent metal pieces through a series rod 2 Q, and the tabs are respectively clamped and fastened with metal bolts 5. The integrated current collector plywood can be perforated or double-sided. Similarly, the split current collector plywood can also be perforated or double-sided. From efficiency As far as the effect is concerned, the efficiency and effect of the perforated clip are better than the two-sided clip.
为了防止极耳与极柱连接的螺栓松动, 故需以固化胶将螺 栓固定。  In order to prevent the bolts connecting the pole ears and poles from loosening, the bolts need to be fixed with curing glue.
注液。 注液前必须抽出锂离子动力电池内腔中的常态空 气, 除尽内腔中的水分, 电池内腔须呈负压状态, 然后将适量 的电解液从安全阀口注入。 锂离子动力电池的注液量须根据其 容量计算, 注液量过大不但容易漏液, 且易引起鼓壳; 注液量 过小则易引起正、 负极活性物质的恶化。 锂离子动力电池的注 液量通常在 0. 1 5 Ah/ g~ 0. 6 Ah / g 的范围内调整; 最佳 的注液量在 0. 2 Ah / g ~ 0. 3 5 Ah / g 之间。 注液的环境控 制非常重要, 故须在操作箱中或其他能够达到要求的环境中完 成注液。 因安全阀的卸压孔与盖板上的注液孔相通, 故注液通 常从安全阀的卸压孔注入; 也可以另行在外壳或盖板上加工注 液孔。  Inject fluid. Before injection, the normal air in the inner cavity of the lithium ion power battery must be drawn out. Except for the moisture in the inner cavity, the inner cavity of the battery must be in a negative pressure state, and then an appropriate amount of electrolyte is injected from the safety valve port. The injection volume of a lithium-ion power battery must be calculated based on its capacity. If the injection volume is too large, it will easily leak and cause the drum shell. If the injection volume is too small, it will easily cause the deterioration of the positive and negative electrode active materials. The injection volume of lithium ion power battery is usually adjusted within the range of 0.1 5 Ah / g ~ 0.6 Ah / g; the optimal injection volume is 0.2 Ah / g ~ 0.3 5 Ah / g between. The environmental control of the injection is very important, so the injection must be completed in the operation box or other environment that can meet the requirements. Because the pressure relief hole of the safety valve communicates with the liquid injection hole on the cover plate, the injection liquid is usually injected from the pressure relief hole of the safety valve; the liquid injection hole can also be processed on the housing or the cover plate separately.
锂离子动力电池在装入内本体及注液以后, 仍应保持一定 的空腔, 不可以为了缩小体积或节约外壳材料, 刻意以固体物 质或电解液充满锂离子动力电池的内腔。 视锂离子动力电池的 容量大小不同, 空腔约为内腔总容积的 1 % ~ 1 0 %, 空腔可 以保护气体充填。  After the lithium-ion power battery is installed in the inner body and filled with liquid, a certain cavity should still be maintained. In order to reduce the volume or save the shell material, the internal cavity of the lithium-ion power battery must be intentionally filled with solid substances or electrolyte. Depending on the capacity of the lithium-ion power battery, the cavity is about 1% to 10% of the total volume of the internal cavity. The cavity can be filled with a protective gas.
化成是电池生产的最后关键。 大功率锂离子动电池的化成 原则必须是小电流、 低电压, 绝对不可以大电流, 较高电压化 成, 才能充分激活正、 负集流基体上的活性物质。 化成工序必 须一次性不间断地完成, 中途不可随意中止或停止。 化成曲线 应光滑连接, 电流应控制在 0. 0 1 C / 1 0小时 - → 0. 0 2 C / 5 小时 - — 0. 0 5 C / 5 小时 - → 0. 1 C / 4 小时 -→ 0. 2 C / 1 小时, 恒流充满后转为恒压继续充, 务求一次性 充足。  Formation is the last key to battery production. The formation principle of high-power lithium-ion batteries must be low current and low voltage. High current must not be formed. Higher voltage formation is required to fully activate the active materials on the positive and negative current collector substrates. The formation process must be completed uninterrupted at one time, and it cannot be stopped or stopped at will. The formation curve should be smoothly connected, and the current should be controlled between 0. 0 1 C / 10 hours-→ 0. 2 C / 5 hours-— 0. 0 5 C / 5 hours-→ 0. 1 C / 4 hours-→ 0.2 C / 1 hour, after the constant current is full, it will be switched to constant pressure to continue charging, so as to ensure sufficient one time.
分容。 将电性能各项指标均符合工艺要求的电池与各项电 性能指标未达工艺要求的电池分别置放入库。  Divide. Put batteries with electrical performance indicators that meet the process requirements and batteries with electrical performance indicators that do not meet the process requirements, respectively.
以此方法制造的锂离子动力电池, 不仅可以满足大功率充 放电的要求, 而且可以避免动力电池内部热量聚集的问题。  The lithium ion power battery manufactured by this method can not only meet the requirements of high-power charge and discharge, but also avoid the problem of heat accumulation inside the power battery.

Claims

权利要求 Rights request
1 . 一种可反复充放电的锂离子动力电池, 每个单体电池 由盖板 ( 1 ) 、 负极极柱 ( 2 ) 、 安全阀 ( 3 ) 、 正极极柱 1. A lithium-ion power battery that can be repeatedly charged and discharged. Each single battery is composed of a cover plate (1), a negative pole (2), a safety valve (3), and a positive pole.
( 4 ) 、 电解液 ( 8 ) 、 外壳 ( 9 ) 组成, 正极极柱 ( 4 ) 与 正极 ( 1 3 ) 相连接, 负极极柱 ( 2 ) 则与负极 ( 1 2 ) 相连 接; 正极 ( 1 3 ) 选用一定厚度的铝箔, 两面均匀涂布正极活 性物质, 负极 ( 1 2 ) 选用一定厚度的铜箔, 两面均匀涂布负 极活性物质; 其特征在于: 内本体 ( 7 ) 是由一对或多对正负 极片组即正极片 ( 1 3 ) 、 负极片 ( 1 2 ) 与隔膜 ( 1 9 ) 共 同构成具有盘状结构的电极集合体; 正极或负极的极片形式均 为带有大叶单极耳或大叶多极耳的矩形片 , 并通过集电夹板(4), electrolyte (8), and casing (9), the positive pole (4) is connected to the positive pole (1 3), and the negative pole (2) is connected to the negative pole (1 2); the positive pole (1) 3) Select a certain thickness of aluminum foil and evenly coat the positive electrode active material on both sides, and the negative electrode (1 2) Select a certain thickness of copper foil and evenly coat the negative electrode active material on both sides; It is characterized by: the inner body (7) is A plurality of pairs of positive and negative electrode groups, that is, a positive electrode sheet (1 3), a negative electrode sheet (1 2), and a separator (1 9) together form an electrode assembly having a disc-like structure; Rectangular slice of leaf monopole or large leaf multipole and pass through current collector splint
( 6 ) 导出电流至极柱; 正极有一个或若干个极柱, 负极有一 个或若干个极柱, 正负极柱的数量可以相等也可以不等、 极柱 的直径可以相等也可以不等; 极柱的形状除可以为圆柱形外, 亦可采用片状, 安装于外壳 ( 9 ) 的同一或不同的任何表面 上; 正负极片 的形状除矩形外, 也可制成其他形状; 正极片(6) exporting the current to the poles; the positive pole has one or several pole poles, and the negative pole has one or several pole poles; the number of the positive pole poles and the negative pole poles can be equal or different, and the diameters of the pole poles can be equal or different; In addition to the shape of the pole, the shape of the pole can also be cylindrical, and it can be mounted on the same or different surface of the casing (9). The shape of the positive and negative electrodes can be made into other shapes besides the rectangular shape. sheet
( 1 3 ) 与负极片 ( 1 2 ) 须间隔层叠置放; 内本体 ( 7 ) 最 外层两侧既可以为负极片, 也可以是正极片; 内本体 ( 7 ) 须 以隔膜紧密包裹或以聚乙烯、 聚丙烯框夹紧; 正极极耳 ( 1(1 3) and the negative electrode sheet (1 2) must be stacked and spaced apart; the inner body (7) can be either the negative electrode sheet or the positive electrode on both sides of the outermost layer; the inner body (7) must be tightly wrapped with a separator or Clamped with polyethylene and polypropylene frames; positive pole tab (1
1 ) 整齐排列并联于内本体 ( 7 ) 的一端, 负极极耳 ( 1 0 ) 整齐排列并联于内本体的另一端; 正极 ( 1 3 ) 或负极 ( 11) neatly arranged in parallel and connected to one end of the inner body (7), negative pole tab (1 0) neatly arranged and connected in parallel to the other end of the inner body; positive electrode (1 3) or negative electrode (1
2 ) 可另行选用网状金属箔; 正极 ( 1 3 ) 的活性物质既可以 是钴酸锂, 也可以是锰酸锂、 镍酸锂或镍钴酸锂; 负极 ( 12) A mesh metal foil may be selected separately; the active material of the positive electrode (1 3) may be lithium cobaltate, or lithium manganate, lithium nickelate, or lithium nickel cobaltate; the negative electrode (1
2 ) 的活性物质既可以是天然石墨, 也可以是鳞片石墨、 人造 石墨或石油焦炭; 外壳 ( 9 ) 既可以是方形的也可以是圆柱形 的; 外壳 ( 9 ) 内通常只装入一个内本体 ( 7 ) , 也可以将若干 个内本体并联装入外壳内, 组成较大容量的动力电池。 2) The active material can be either natural graphite, flake graphite, artificial graphite, or petroleum coke; the shell (9) can be either square or cylindrical; the shell (9) is usually filled with only one The main body (7), or a plurality of inner bodies may be installed in parallel in the casing to form a large-capacity power battery.
2.根据权利要求 1 所述的可反复充放电的锂离子动力电 池, 其特征在于: 正极 ( 1 3 ) 活性物质的密度每平方厘米为 0.02g - 0.06g, 最好为 0.032g - 0.042g; 负极 ( 1 2 ) 活性 物质的密度每平方厘米约为 0. Olg ~ 0.03g, 最好为 0.014g~ 0.021go The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: the density of the positive electrode (1 3) active material is 0.02 g-0.06 g per square centimeter, preferably 0.032 g-0.042 g The density of the negative electrode (1 2) active material per square centimeter is about 0. Olg ~ 0.03g, preferably 0.014g ~ 0.021g o
3.根据权利要求 1 所述的可反复充放电的锂离子动力电 池, 其特征在于: 大叶极耳的最大宽度须小于极耳所在或所构 成的那一圏的周长的一半; 采用圆柱形外壳, 内本体 ( 7 ) 内 圏的大叶极耳的宽度应渐次小于外圏极耳的宽度或等宽; 采用 方形外壳, 内本体内圏的大叶极耳的宽度既可以渐次小于外圏 极耳的宽度, 也可以等宽; 无论采用圆柱形外壳或方形外壳, 大叶多极耳的间距不等; 大叶单极耳可以从极片的中间引出, 也可以从接近极片两端的位置引出; 大叶极耳除可以直接裁切 外, 大叶极耳可以另行制作并于极片滚压后焊接在极片, 最好 采用焊接大叶极耳; 大叶极耳的形状可以为方形、 长方形、 半 圆形、 梯形或其他有利于导流、 散热的形状, 最佳形状为带有 R角的梯形; 极耳根部与极片的连接处既可以为清角连接也可 以为光滑圆弧连接; 正极 ( 13) 、 负极 ( 12) 的大叶极耳位置 须错开卷绕, 正极极耳 ( 11 ) 整齐排列并联于内本体 ( 7 ) 的 一侧, 负极极耳 ( 10) 整齐排列并联于内本体的另一侧; 内本 体 ( 7 ) 最外层既可以为负极片, 也可以是正极片。 The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: the maximum width of the large leaf tabs must be less than half of the circumference of the stack where the tabs are located or formed; Shaped outer shell, the inner body (7) the width of the inner leaflet's large leaf tabs should be gradually smaller than the width of the outer palate poles or the same width; using a square shell, the inner leaflet's large leaf tabs can be gradually smaller than the outer The width of the 圏 pole ears can also be the same width; whether the cylindrical shell or the square shell is used, the spacing of the large leaf multipole ears is different; the large leaf monopole ears can be led out from the middle of the pole piece, or from two close to the pole piece. The end of the large leaf tab can be cut directly, the large leaf tab can be made separately and welded to the pole piece after the pole piece is rolled, it is best to use the large leaf tab; the shape of the large leaf tab can be It is square, rectangular, semi-circular, trapezoidal, or other shapes that are good for flow guidance and heat dissipation. The best shape is a trapezoid with an R angle. The connection between the root of the ear and the pole piece can be either a clear angle connection or Light Sliding arc connection; the positions of the large leaf tabs of the positive electrode (13) and negative electrode (12) must be staggered and wound. Neatly arranged in parallel to the other side of the inner body; the outermost layer of the inner body (7) can be either a negative electrode sheet or a positive electrode sheet.
4.根据权利要求 1 所述的可反复充放电的锂离子动力电 池, 其特征在于: 通常情况下, 大叶极耳的最大高度不大于其 自身宽度, 最好小于其宽度。  The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: in general, the maximum height of the large leaf tab is not larger than its own width, and preferably smaller than its width.
5.根据权利要求 1 所述的可反复充放电的锂离子动力电 池, 其特征在于: 整体式集电夹板上有若干可以被压缩而又能 弹开的线槽; 分体式集电夹板系以若干相互独立的金属片通过 串联杆 ( 2 0 ) 串联; 无论整体式集电夹板抑或分体式集电夹 板, 集电夹板应覆盖极耳, 其与极耳接触的表面上加工有凸起 的棘刺。  The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: the integrated current collecting plate has a plurality of wire grooves which can be compressed and can be opened; the split type current collecting plate is formed by Several independent metal pieces are connected in series through a series rod (20); whether the integrated current collector plywood or the split current collector plywood, the current collector plywood should cover the tabs, and the surface in contact with the tabs has raised thorns .
6.根据权利要求 1 所述的可反复充放电的锂离子动力电 池, 其特征在于: 隔膜 ( 1 9 ) 采用具有微孔结构且电流切断 温度低的 1 5 μ m~ 8 0 μ m 厚度的聚乙烯或聚丙烯材料制成 长条状 ( 1 9 ) ; 隔膜 ( 1 9 ) 的面积无论长或宽均大于正负 极片, 除极耳外, 隔膜 ( 19 ) 必须将正极片 ( 1 3 ) 或负极片 ( 1 2 ) 四周完全遮蔽住, 不可露出边缘, 以防短路; 当充放 电要求 1 C ~ 2 C时, 隔膜 ( 1 9 ) 的最佳厚度为 2 Ομ ιη~ 4 0 μ m; 充放电要求 3 C或更大时, 隔膜的最佳厚度为 4 0 μ m 或以上。 The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: the separator (19) is made of a microporous structure with a low current cut-off temperature of 15 μm to 80 μm. The strip (19) is made of polyethylene or polypropylene material; the area of the separator (19) is larger than the positive and negative electrodes no matter the length or width. Except for the ears, the separator (19) must have the positive electrode (1 3) Or the negative electrode (1 2) is completely shielded around, and the edges must not be exposed to prevent short circuit. When the charge and discharge require 1 C ~ 2 C, the optimal thickness of the separator (1 9) is 2 Ομ ιη ~ 4 0 μm; When charge and discharge require 3 C or more, the optimal thickness of the separator is 40 μm or more.
7.—种用于可反复充放电的锂离子动力电池的安全阀, 其 特征在于: 压簧 ( 2 5 ) 装于调节螺栓 ( 2 3 ) 的内孔中, 调 节螺栓的内孔用于保持压簧、 密封钢球 ( 2 2 ) 的稳定, 压簧 7.—A safety valve for a lithium ion power battery that can be repeatedly charged and discharged, characterized in that: a compression spring (2 5) is installed in an inner hole of an adjustment bolt (2 3), and the inner hole of the adjustment bolt is used for holding Stability of compression springs, sealed steel balls (2 2), compression springs
( 2 5 ) 可在调节螺栓的内孔中纵向上下滑移, 密封钢球 ( 2(2 5) It can slide down vertically in the inner hole of the adjusting bolt to seal the steel ball (2
2 ) 可在调节螺栓的内孔中纵向上下滑移, 调节螺栓的外径上 加工有与安全阀本体 ( 2 1 ) 相配的螺紋; 调节螺栓加工有若 干竖向的排气槽 ( 2 4 ) , 在排气槽的下部则开有排气孔 ( 22) It can be slid up and down in the inner hole of the adjustment bolt. The outer diameter of the adjustment bolt is machined with threads that match the safety valve body (2 1); the adjustment bolt is machined with several vertical exhaust grooves (2 4) There are vent holes (2
8 ) ; 压簧 ( 2 5 ) 压在钢球的上部, 密封钢球 ( 2 2 ) 的下 部孔则陷压在盖板注液口上的氟橡胶圏 ( 2 6 ) 上; 安全阀底 部的卸压孔与盖板 ( 1 ) 上的注液孔相通; 压簧 ( 25 ) 也可以 反弓弹片 ( 3 0 ) 代替, 反弓弹片 ( 3 0 ) 装于调节螺栓 ( 28); the compression spring (2 5) is pressed on the upper part of the steel ball, and the lower hole of the sealed steel ball (2 2) is trapped on the fluorine rubber 圏 (2 6) on the injection port of the cover plate; The pressure hole communicates with the liquid injection hole on the cover plate (1); the pressure spring (25) can also be replaced by a reverse bow spring (30), and the reverse bow spring (30) is installed on the adjusting bolt (2)
3 ) 的下部, 调节螺栓加工有与安全阀本体 ( 2 1 ) 相配的螺 纹, 通过拧动钥匙孔 ( 2 7 ) 调整反弓弹片的张力; 安全阀本 体内加工有一长方形的排气槽 ( 3 1 ) , 反弓弹片 ( 3 0 ) 可 以在排气槽内上下弹动而不可水平转动; 密封钢球 ( 2 2 ) 在 安全阀本体的保持架内可以纵向上下滑移, 反弓弹片 ( 3 0 ) 上加工有工艺装配孔 ( 3 3 ) , 扣压在钢球的上部, 密封钢球3) The lower part of the adjusting bolt is processed with a thread matching the safety valve body (2 1), and the tension of the reverse bow spring is adjusted by turning the key hole (2 7); a rectangular exhaust groove (3 1), the anti-bow spring (3 0) can be bounced up and down in the exhaust slot and cannot be rotated horizontally; the sealed steel ball (2 2) can be vertically lowered in the holder of the safety valve body, and the anti-bow spring (3) 0) Process assembly holes (3 3) are machined on the top of the steel ball to seal the steel ball
( 2 2 ) 的下部孔则陷压在盖板注液口上的氟橡胶圏 ( 2 6 ) 上; 安全阀底部的卸压孔与盖板 ( 1 ) 上的注液孔相通; 安全 阀本体 ( 2 1 ) 上可以另行加工有排气小孔 ( 3 5 ) ; 密封钢 球则可以加工为带有水平横槽的球体 ( 2 2 - 1 ) , 氟橡胶圏The lower hole of (2 2) is trapped on the fluorine rubber 圏 (2 6) on the injection port of the cover plate; the pressure relief hole at the bottom of the safety valve communicates with the injection hole on the cover plate (1); the safety valve body ( 2 1) can be separately processed with exhaust holes (3 5); sealed steel balls can be processed into spheres with horizontal horizontal grooves (2 2-1), fluoro rubber 圏
( 2 6 - 1 ) 箍紧在密封钢球 ( 2 2 - 1 ) 上的水平横槽中; 密封钢球 ( 2 2 ) 可加工为密封锥台 ( 2 2 - 2 ) ; 密封锥台(2 6-1) hoop tightly in the horizontal horizontal groove on the sealing steel ball (2 2-1); the sealing steel ball (2 2) can be processed into a sealing frustum (2 2-2); sealing frustum
( 2 2 - 3 ) 可以加工一水平横槽, 氟橡胶圏 ( 2 6 - 2 ) 则 箍紧在密封雉台 ( 2 2 - 3 ) 上的水平横槽中; 安全阀可安装 于外壳 ( 9 ) 的任何表面上; 较大容量的锂离子动力电池, 可 以在同一个侧表面或不同的侧表面安装若干个安全阀; 通常情 况下, 安全阀 ( 3 ) 与极柱既可以安装在外壳 ( 9 ) 的同一个 表面上, 也可以安装在不同的表面上。 (2 2-3) can process a horizontal horizontal groove, fluoro rubber 圏 (2 6-2) is hooped in the horizontal horizontal groove on the sealing pedestal (2 2-3); the safety valve can be installed in the housing (9 ) On any surface; a large-capacity lithium-ion power battery can install several safety valves on the same side surface or different side surfaces; usually, the safety valve (3) and the pole can be installed in the housing ( 9) can be installed on different surfaces on the same surface.
8.—种可反复充放电的锂离子动力电池的制造方法, 其特 征在于, 包括以下步骤 ( 1 ) 配料, 包括以下各种方法: 8. A method for manufacturing a lithium ion power battery that can be repeatedly charged and discharged, characterized in that it includes the following steps (1) Ingredients, including the following methods:
A、 以循序配制法配制以 NM P为介质的正极浆料, 所需材料为: P V D F (聚偏二氟乙烯) 2 · 5 % ~ 3 · 5 %、 钴酸锂 9 3 % - 9 5 %、 导电剂石墨 1 % ~ 2 %或乙炔黑 0. 5 % ~ 1 %、 碳黑 2 % ~ 3 %; N M P的用量受钴酸锂粒径大 小、 粒度分布的制约, 通常情况下的固液比 = 1 ( 固含量) : 0. 3 - 1 ( NM P ) ; 最佳的固液比 - 1 : 0. 3 5 ~ 0. 7 ; P V D F、 石墨 (或乙炔黑) 、 碳黑均需在约 1 2 0 °C烘箱内 烘烤约 2 ~ 3 小时; 将 P V D F加入 N M P搅拌约 3 ~ 4 小时 后, 加入导电剂石墨 (或乙炔黑 ) 、 碳黑搅拌约 0. 5 ~ 1 小 时, 最后加入钴酸锂搅拌约 2. 5 ~ 4 小时成粘稠的浆状;  A. The sequential preparation method is used to prepare the positive electrode slurry with NM P as the medium. The required materials are: PVDF (polyvinylidene fluoride) 2 · 5% ~ 3 · 5%, lithium cobaltate 9 3%-95% 1, graphite conductive agent 1% ~ 2% or acetylene black 0.5% ~ 1%, carbon black 2% ~ 3%; the amount of NMP is limited by the particle size and particle size distribution of lithium cobaltate, usually solid-liquid Ratio = 1 (solid content): 0.3-1 (NM P); optimal solid-liquid ratio-1: 0.3 to 5; 0.7; PVDF, graphite (or acetylene black), and carbon black all need to be in Bake in an oven at about 120 ° C for about 2 to 3 hours; add PVDF to NMP and stir for about 3 to 4 hours, then add conductive agent graphite (or acetylene black), carbon black and stir for about 0.5 to 1 hour, and finally Add lithium cobaltate and stir for about 2.5 to 4 hours to form a thick paste;
A - 2 、 以循序配制法配制以水为介质的正极浆料, 所需材料为: C M C 0 · 6 % ~ 0 · 9 %、 S B R实际固含量 2 % ~ 4 %、 导电剂石墨 1 % ~ 2 %或乙炔黑 0. 5 % ~ 1 %、 碳黑 1 . 5 % ~ 3 %、 钴酸锂 9 3 % ~ 9 5 %; 水 (去离子 水、 蒸馏水、 純净水) 的用量为所有前述物质总量的 4 0 % ~ 1 3 0 %即固液比 = 1 : 0. 4 ~ 1 · 3 ; 通常情况下, 最佳的 固液比 = 1 : 0. 6 ~ 1 ; S B R可以用 P T F E代替; 将 C M C加入水中搅拌约 3 ~ 4 小时后将 S B R加入其中搅拌约 0. 5 ~ 1 小时, 再将导电剂石墨 (或乙炔黑) 、 碳黑加入搅拌约 0. 5 ~ 1 小时, 最后加入钴酸锂搅拌约 2. 5 ~ 4 小时成较为 粘稠的浆状, 筛去团聚物和其他杂质;  A-2. The positive electrode slurry with water as the medium is prepared by the sequential preparation method. The required materials are: CMC 0 · 6% ~ 0 · 9%, SBR actual solid content 2% ~ 4%, conductive agent graphite 1% ~ 2% or 0.5% ~ 1% of acetylene black, 1.5% ~ 3% of carbon black, 93% ~ 95% of lithium cobaltate; the amount of water (deionized water, distilled water, purified water) is all 40% ~ 130% of the total amount of the aforementioned substances, that is, the solid-liquid ratio = 1: 0.4 to 1.3; under normal circumstances, the best solid-liquid ratio = 1: 0.6 to 1; SBR can be used 5 ~ 1 hour, add CMC to water and stir for about 3 to 4 hours, then add SBR to it and stir for about 0.5 to 1 hour, and then add conductive agent graphite (or acetylene black) and carbon black for about 0.5 to 1 hour, Finally, add lithium cobaltate and stir for about 2.5 to 4 hours to form a thicker slurry. Sieve out agglomerates and other impurities;
A - 3、 以干法配制以 NM P为介质的正极浆料, 所 需材料为: P V D F 2. 5 % ~ 3 . 5 %、 钴酸锂 9 3 % ~ 9 5 %、 导电剂石墨 1 . 5 % ~ 2 % (或乙炔黑 0 . 8 % ~ 1 . 2 % ) 、 碳黑 2 % ~ 3 % , N M P的用量受钴酸锂粒径大小、 粒 度分布的制约, 为所有前述物质总量的 3 5 % ~ 9 0 %即固液 比 = 1 ( 固含量) : 0. 3 ~ 1 , 最佳的固液比 = 1 : 0. 3 5 ~ 0. 7 ; P V D F、 石墨 (或乙炔黑) 、 碳黑均需在约 1 2 0 。(:烘箱内烘烤 2 ~ 3 小时; 将钴酸锂、 导电剂石墨 (或乙炔 黑) 、 碳黑放入混料机内搅拌 3 小时; 同时将 P V D F与 N M P搅拌约 2 小时, 待其完全溶解后 (清浆) , 即将混料机搅拌 后的混合粉料放入经过搅拌的 P V D F与 NM P的清浆内继续 搅拌约 3 小时成粘稠的浆状; A-3. Dry preparation of positive electrode slurry with NM P as the medium, the required materials are: PVDF 2.5% ~ 3.5%, lithium cobaltate 93% ~ 95%, conductive agent graphite 1. 5% ~ 2% (or acetylene black 0.8% ~ 1.2%), carbon black 2% ~ 3%, the amount of NMP is limited by the particle size and particle size distribution of lithium cobaltate, which is the total amount of all the aforementioned substances 35% ~ 90% of the solid-liquid ratio = 1 (solid content): 0.3 ~ 1, the optimal solid-liquid ratio = 1: 0.3 5 ~ 0.7; PVDF, graphite (or acetylene black) ), Carbon black are required to be about 120. (: Baking in an oven for 2 to 3 hours; Put lithium cobaltate, conductive agent graphite (or acetylene black), carbon black into the mixer and stir for 3 hours; at the same time, stir PVDF and NMP for about 2 hours, wait for them to completely After dissolving (clearing), stir the mixer The mixed powder is put into the clear slurry of PVDF and NM P after stirring, and then stirred for about 3 hours to form a thick slurry;
A - 4、 以干法配制以水为介质的正极浆料, 所需材 料为: C M C 0. 6 °/。 ~ 0. 9 %、 S B R实际固含量 2 % ~ 4 %、 导电剂石墨 1 % ~ 2 %或乙炔黑 0. 5 % ~ 1 %、 碳黑 1. A-4. Dry preparation of the positive electrode slurry with water as the medium, the required materials are: C M C 0.6 °. ~ 0.9%, S B R actual solid content 2% ~ 4%, conductive agent graphite 1% ~ 2% or acetylene black 0.5% ~ 1%, carbon black 1.
5 % ~ 3 %、 鈷酸锂 ' 9 3 % ~ 9 5 %; 水 (去离子水、 蒸馏 水、 纯净水) 的用量为所有前述物质总量的 4 0 % ~ 1 3 0 % 即固液比 = 1 : 0 · 4 ~ 1 · 3 ; 通常情况下, 最佳的固液比 -5% ~ 3%, lithium cobaltate '93% ~ 95%; the amount of water (deionized water, distilled water, purified water) is 40% ~ 130% of the total amount of all the aforementioned substances, that is, the solid-liquid ratio = 1: 0 · 4 ~ 1 · 3; Under normal circumstances, the best solid-liquid ratio-
1 : 0. 6 - 0. 1 ; 将钴酸锂、 导电剂石墨 (或乙炔黑) 、 碳 黑放入混料机内搅拌约 3 小时; 同时将 CM C与水搅拌约 3 小 时, 待其完全溶解后成为清浆, 即将混料机搅拌后的混合粉料 放入经过搅拌的 C M C与水的清浆内继续搅拌约 3 小时成粘稠 的浆状, 最后歸去团聚物和其他杂质; 1: 0.6-0.1; Put lithium cobaltate, conductive agent graphite (or acetylene black), carbon black into the mixer and stir for about 3 hours; at the same time, stir CMC with water for about 3 hours, wait for it After it is completely dissolved, it will become a clear slurry. That is, the mixed powder mixed by the mixer is put into the clear slurry of the stirred CMC and water and continued to be stirred for about 3 hours to form a thick slurry. Finally, aggregates and other impurities are removed;
B、 配制以 NM P为介质的负极浆料, 所需材料为: 石墨 9 3 % ~ 9 5 %、 P V D F 5 % ~ 7 %、 N M P为所有前 述物质总量的 8 0 % - 1 5 0 %即固液比 - 1 : 0 . 8 ~ 1 . B. Preparation of negative electrode slurry with NM P as the medium, the required materials are: graphite 93% ~ 95%, PVDF 5% ~ 7%, NMP is 80%-150% of the total amount of all the foregoing substances That is, the solid-liquid ratio-1: 0.8 ~ 1.
5 ; 最佳的固液比 = 1 : 1 ~ 1 · 3 ; P V D F、 需在温度约 15; The best solid-liquid ratio = 1: 1 ~ 1 · 3; P V D F, need to be at about 1
2 0 。C的烘箱内烘烤 2 ~ 3 小时, 石墨则需在 3 0 0 °C ~ 5 0 0 °C温度烘烤 4 ~ 8 小时; 负极材料经 3 2 5 目振动筛选, 网 上剩余的通常不宜使用; 将 P V D F加入 NM P搅拌约 3 ~ 4 小时, 再将经 3 2 5 目 筛网振动筛选备用的石墨加入搅拌约2 0. B oven in C for 2 ~ 3 hours, graphite needs to be baked at 300 ° C ~ 500 ° C for 4 ~ 8 hours; the anode material is screened by 3 2 5 mesh vibration, and the remaining ones on the Internet are usually not suitable for use. ; Add PVDF to NM P and stir for about 3 to 4 hours, and then add the spare graphite that has been sifted through a 3 2 5 mesh screen to stir for about 3 to 4 hours.
3 ~ 4小时成粘稠的浆状; 3 to 4 hours into a thick paste;
B - 1 、 配制以水为介质的负极浆料, 所需材料为: 石墨 9 3 % ~ 9 5 %、 C M C 0. 8 % ~ 1. 5 %、 S B R固含 量 2 % ~ 4 %、 水 (去离子水、 蒸馏水、 纯净水) 为所有前述 物质总量的 8 0 % - 1 6 0 %即固液比 - 1 : 0. 8 ~ 1 . 6 ; 最佳的固液比 - 1 : 1 ~ 1. 3 ; C M C需在 1 2 0 °C温度下烘 烤 2 ~ 3 小时, 石墨则需在 3 0 0 °C ~ 5 0 0 °( 温度烘烤 4 ~ B-1. To prepare the negative electrode slurry with water as the medium, the required materials are: graphite 93% ~ 95%, CMC 0.8% ~ 1.5%, SBR solid content 2% ~ 4%, water ( Deionized water, distilled water, purified water) is 80%-160% of the total amount of all the aforementioned substances, that is, the solid-liquid ratio-1: 0. 8 ~ 1. 6; the optimal solid-liquid ratio-1: 1 ~ 1.3; CMC should be baked at 120 ° C for 2 ~ 3 hours, graphite should be baked at 300 ° C ~ 500 ° (temperature baking 4 ~
8 小时; S B R可以用 P T F E代替; 负极材料经 3 0 0 目振 动筛选, 网上剩佘的通常不宜使用; 将 C M C加入水中搅拌约8 hours; S B R can be replaced by P T F E; the anode material is screened by 300 mesh vibration, the leftovers on the Internet are generally not suitable for use; add C M C to water and stir for about
3 ~ 4 小时后将 S B R (或 P T F E ) 加入其中搅拌约 0 .After 3 ~ 4 hours, add S B R (or P T F E) to it and stir for about 0.
5 ~ 1 小时, 最后将烘烤后并经 3 2 5 目 筛选备用的石墨加入 搅拌约 3 ~ 4 小时成粘稠的浆状; 正极材料的粒径可以在 2 μ m~ 1 2 μ m 范围内选用 佳的粒径应为 5 μ m~ 8 μ m; 正极材料的粒度分布过细或过粗 的粉体的总和通常不超过 40% ; 2 μ m以下的微细粉体的固液 比应在原固液比基础上加大 20% ~ 50% , 1 2 μ m 以上的较粗 粉体的固液比则应在原固液比基础上减小 10% ~ 30%; 在正 极的配制中, 选用的导电剂材料的粒径须等于或小于正极材料 的粒径; 5 to 1 hour. Finally, add graphite after baking and sieve through 3 2 5 mesh and stir for about 3 to 4 hours to form a thick paste; The particle size of the positive electrode material can be selected within the range of 2 μm to 12 μm. The optimal particle size should be 5 μm to 8 μm; the total particle size distribution of the positive electrode material is usually not more than 40 %; The solid-liquid ratio of fine powders below 2 μm should be increased by 20% to 50% based on the original solid-liquid ratio, and the solid-liquid ratio of coarser powders above 12 μm should be based on the original solid-liquid ratio 10% ~ 30%; In the preparation of the positive electrode, the particle size of the conductive material selected must be equal to or smaller than the particle size of the positive electrode material;
( 2 ) 涂布: 将搅拌好的正极或负极浆料均勾涂覆在金属 箔集流体上, 经辊刀勾速拉出进入烘箱烘烤, 烘烤干后即成为 半成品集流片; 涂布中须注意不可有划痕, 露基体, 纵横方向 上的偏轻偏重等现象; 无论正极抑或负极, 配制好的浆料涂布 于金属箔上后均须从预热区段进入涂布机的烘干巷道, 绝对不 可倒置; 预热区段的温度通常为 9 0 °C或以下, 中温区段的温 度在 1 1 0 。C ~ 1 3 0 °C间, ± 1 0 ° (:、 高温区段的温度在 1 (2) Coating: Coat the stirred positive or negative electrode slurry onto the metal foil current collector, pull it out through a roller knife into the oven and bake, and it will become a semi-finished current collector after the baking is dried; The cloth must be careful not to have scratches, exposed substrates, lightness and weight in the vertical and horizontal directions; whether it is the positive or negative electrode, the prepared slurry must enter the coating machine from the preheating section after coating on the metal foil. The drying tunnel must not be inverted; the temperature of the preheating zone is usually 90 ° C or below, and the temperature of the medium temperature zone is 1 1 0. C ~ 1 3 0 ° C, ± 1 0 ° (:, the temperature of the high temperature section is 1
2 0 °C ~ 1 4 0 。C间, ± 1 0 °C; 在前述温度条件下, 涂布烘 烤时, 负极浆料的温度可以较正极浆料的温度稍高 1 0 °C ~ 12 0 ° C ~ 1 4 0. Between C, ± 10 ° C; under the aforementioned temperature conditions, the temperature of the negative electrode slurry can be slightly higher than the temperature of the positive electrode slurry during coating and baking 10 ° C ~ 1
5 。C , 以水为介质的浆料温度可以较 NM P为介质的浆料温度 稍高 1 0 °C ~ 1 5 。C; 涂布的线速度可以在每分钟 8 0 0 mm ~5. C, the temperature of the slurry with water as the medium can be slightly higher than that of the slurry with NM P as the medium by 10 ° C ~ 15 ° C. C; The linear speed of coating can be 800 mm ~
5 0 0 0 mm 的范围内调整; 最佳的线速度为每分钟 1 2 0 0 mm- 3 5 0 0 mm; 涂布后的正极 ( 1 3 ) 的活性物质的密度每 平方厘米为 0. 0 28~ 0. 0 68, 最佳密度每平方厘米则为 0 ·Adjust within the range of 5 0 0 0 mm; the best linear speed is 12 0 mm-3 5 0 0 mm per minute; the density of the active material of the coated positive electrode (1 3) is 0 per square centimeter. 0 2 8 ~ 0. 0 6 8 , the optimal density is 0 per square centimeter
0 3 2 g ~ 0. 0 4 2 g; 涂布后负极 ( 1 2 ) 的活性物质的密 度每平方厘米约为 0. 0 1 g~ 0. 0 3 g, 最佳密度每平方厘米 为 0. 0 1 4 g~ 0. 0 2 1 g; 既可以单面涂布, 可以双面同时 涂布; 单面涂布活性物质, 装配时须将同极的极片背面相贴成 为两面均有活性物质的集电体; 单面涂布所选用的金属箔厚度 须较前述的金属箔厚度要薄; 0 3 2 g ~ 0. 0 4 2 g; The density of the active material of the negative electrode (1 2) after coating is about 0.0 1 g per square centimeter, and the optimal density is 0 per square centimeter. 0 1 4 g ~ 0. 0 2 1 g; both single-sided coating and simultaneous double-sided coating; single-sided coating of active materials, the back of the pole pieces of the same polarity must be attached to each other during assembly Active material current collector; The thickness of the metal foil used for single-sided coating must be thinner than the thickness of the aforementioned metal foil;
( 3 ) 制片: 正极 ( 1 3 ) 裁切为带有大叶单极耳或大叶 多极耳的矩形片并刮去极耳 ( 1 1 ) 处的浆料; 负极 ( 1 2 )
Figure imgf000029_0001
(3) Production: the positive electrode (1 3) is cut into a rectangular sheet with a large leaf monopole or a large leaf multipole and scrapes off the slurry at the pole (1 1); the negative electrode (1 2)
Figure imgf000029_0001
0 ) 处的浆料; 制作极耳的方法除裁切外, 可以滚切或剪切冲 压的方式直接加工出成型的极片; 大叶极耳还可以另行制作并 于正负极片滚压后焊接在正负极片上; 大叶极耳的最大宽度小 于周长的 1 / 2 , 大叶极耳的最大高度不大于其自身宽度, 最 好小于其宽度; 特殊需要时, 大叶极耳的最小宽度可以小于其 高度; 采用圆柱形外壳, 内圏的大叶极耳的宽度渐次小于外圏 极耳的宽度; 采用方形外壳, 内圈的大叶极耳的宽度既可以渐 次小于外圏极耳的宽度, 也可以等宽; 通常情况下, 正负极片 上的大叶极耳的宽度等宽; 但在特殊要求下, 正负极片上大叶 极耳的宽度也可以不等宽; 在需要快速大功率充电而无需大功 率放电的情况下, 负极的大叶极耳的宽度可以大于正极的大叶 极耳的宽度; 在需要大功率放电而无需快速大功率充电的情况 下, 正极的大叶极耳的宽度可以大于负极的大叶极耳的宽度; 正极采用大叶单极耳, 负极亦采用大叶单极耳; 正极采用大叶 多极耳, 负极亦当采用大叶多极耳; 在需要快速大功率充电而 无需大功率放电的情况下, 负极可以采用大叶多极耳, 而正极 则可以采用大叶单极耳; 在需要大功率放电而无需快速大功率 充电的情况下, 正极可以采用大叶多极耳, 负极则可以采用大 叶单极耳; 采用大叶多极耳, 则极耳的间距不等; 大叶极耳的 形状可以设计、 加工为方形、 长方形、 半圆形、 梯形或其他有 利于导流、 散热的形状, 最佳的极耳形状为带有 R圆角的梯形 极耳; 大叶极耳的根部与极片的连接处可以为清角连接, 也可 以为光滑圆弧连接; 大叶极耳可以加工为扬头式 ( 1 0 / 1 1 ) , 也可以为藏头式 ( 1 7 / 1 8 ) ; In addition to cutting, the method of making the tabs can be directly processed into rolled pole pieces by cutting or cutting; the large-leaf tabs can also be made separately and rolled on the positive and negative electrode pieces. After welding on the positive and negative plates; the maximum width of the large leaf tab is small At 1/2 of the perimeter, the maximum height of the large leaf tabs is not greater than its own width, preferably smaller than its width; when special needs are required, the minimum width of the large leaf tabs can be smaller than its height; a cylindrical shell is used, and the inner ridge The width of the large leaf tab is gradually smaller than the width of the outer palate. With a square shell, the width of the large leaf tab of the inner ring can be gradually smaller than the width of the outer palate and equal width. Generally, the positive The width of the large leaf tabs on the negative electrode sheet is the same width; but under special requirements, the width of the large leaf tabs on the positive and negative electrode sheet can also be unequal. In the case of fast high-power charging without high-power discharge, The width of the large leaf tab of the negative electrode can be larger than the width of the large leaf tab of the positive electrode. In the case of high power discharge without fast high power charging, the width of the large leaf tab of the positive electrode can be larger than that of the negative electrode Wide leaf monopole ears for the positive electrode and large leaf monopole ears for the negative electrode; large leaf multipole ears for the positive electrode and large leaf multipole ears for the negative electrode; In the case of rate discharge, large-leaf multipole ears can be used for the negative electrode, and large-leaf monopole ears can be used for the positive electrode. In the case of high-power discharge without fast high-power charging, large-leaf multipole ears can be used for the positive electrode. For the negative electrode, large-leaf monopoles can be used; for large-leaf multi-poles, the spacing of the poles can be different; the shape of the large-leaf poles can be designed and processed into square, rectangular, semi-circular, trapezoidal, or other conductive The shape of the flow and heat dissipation, the best shape of the tab is a trapezoidal tab with R rounded corners; the connection between the root of the large leaf tab and the pole piece can be a clear angle connection or a smooth arc connection; large Leaf pole ears can be processed into a raised head type (1 0/1 1) or a hidden head type (1 7/1 8);
隔膜 ( 1 9 ) 采用具有微孔结构且电流切断温度低的 1 5 μ m~ 8 0 μ m 厚度的聚乙烯材料或聚丙烯材料制成的长条状 ( 1 9 ) ; 充放电要求 1 C ~ 2 C时, 隔膜 ( 1 9或 1 9 - 1 ) 的最佳厚度为 2 0 μ m~ 4 0 μ m; 充放电要求 3 C或更大 时, 隔膜的最佳厚度为 4 Ο μ πι 或以上; 除极耳外, 隔膜 ( 1 9 ) 必须将正极 ( 1 3 ) 或负极 ( 1 2 ) 四周完全遮蔽住, 不 可露出边缘, 以防短路; 可用沉浸法将已经滚压后的正极 ( 1 3 ) 沉浸在含有合理量的造孔剂的聚烯烃类材料的浆料中, 再 将正极 ( 1 3 ) 放入特定溶剂中萃取造孔剂而形成与正极片一 体的隔膜; 也可将含有合理量的造孔剂的聚烯烃类材料的浆料 直接涂覆在已经滚压后的正极 ( 1 3 ) 的表面, 再将正极 ( 1 3 ) 放入特定溶剂中萃取造孔剂而形成与正极片一体的隔膜 ( 1 9 ) ; The diaphragm (19) is made of a polyethylene or polypropylene material with a microporous structure and a low current cut-off temperature of 15 μm to 80 μm (19); a charge and discharge requirement of 1 C At ~ 2 C, the optimal thickness of the separator (19 or 19-1) is 20 μm to 40 μm; when the charge and discharge requirements are 3 C or greater, the optimal thickness of the separator is 4 Ο μ πι Or above; except for the ears, the diaphragm (1 9) must completely shield the positive electrode (1 3) or negative electrode (12) from the surroundings, and the edges must not be exposed to prevent short circuits; the immersed positive electrode ( 1 3) Immerse in a slurry of a polyolefin-based material containing a reasonable amount of a pore-forming agent, and then place the positive electrode (1 3) in a specific solvent to extract the pore-forming agent to form a separator integral with the positive electrode sheet; A slurry of a polyolefin-based material containing a reasonable amount of a pore former is directly coated on the surface of the positive electrode (1 3) that has been rolled, and the positive electrode (1 3) Put the pore-forming agent into a specific solvent to form a separator integrated with the positive electrode sheet (19);
( 4 ) 滚压: 滚压工艺中, 正极的线压力为 1 0 0 ~ 1 8 O kg / C M, 负极的线压力为 8 0 ~ 1 6 0 kg / C M; 正极 ( 1 3 ) 在滚压前的厚度约为 1 7 0 μ m~ 2 7 0 μ m, 滚压后 的厚度约为 1 1 0 μ πι~ 1 6 5 μ m, 正极滚压前的最佳厚度为 1 5 μ m~ 2 3 5 μ m, 滚压后的最佳厚度为 1 3 5 μ m~ 1 5 5 μ m; 负极 ( 1 2 ) 滚压前的厚度约为 1 8 5 μ m ~ 2 7 5 μ m, 滚压后 1 1 0 μ ιη~ 1 6 5 μ m, 负极滚压前的最佳厚度 为 2 2 0 μ ιη~ 2 5 0 μ ιη, 滚压后的最佳厚度为 1 3 5 μ m~ 1 5 5 μ m;  (4) Rolling: In the rolling process, the linear pressure of the positive electrode is 100 to 18 kg / cm, and the linear pressure of the negative electrode is 80 to 160 kg / cm; the positive electrode (1 3) is rolling The thickness before rolling is about 170 μm to 27.0 μm, and the thickness after rolling is about 110 μm to 165 μm.The optimal thickness before rolling is 15 μm ~ 2 3 5 μ m, the optimal thickness after rolling is 1 3 5 μ m ~ 1 5 5 μ m; the thickness of the negative electrode (1 2) before rolling is about 1 8 5 μ m ~ 2 7 5 μ m, After rolling 1 1 0 μ ιη ~ 1 6 5 μ m, the optimal thickness of the negative electrode before rolling is 2 2 0 μ ιη ~ 2 5 0 μ ιη, and the optimal thickness after rolling is 1 3 5 μ m ~ 1 5 5 μ m;
( 5 ) 卷绕: 卷绕配用 圆柱形外壳内本体的卷针为圆轴 形, 卷绕配用方形外壳内本体的卷针为有一定刚性及弹性的薄 片; 当极片 内折时, 通常应在极片上的内折处加工折叠线并刮 去折叠线处的活性物质; 正极 ( 1 3 ) 上如果加工有折叠线, 应将负极 ( 1 2 ) 前端对齐正极 ( 1 3 ) 的折叠线的中心线, 令其不能刺破隔膜 ( 1 9 ) ; 卷绕时, 须将一对正负极片组整 齐叠放, 中间衬以隔膜 ( 1 9 ) 紧密卷绕成内本体 ( 7 ) ; 也 可以将多对正负极片并联整齐叠放, 同时紧密卷绕成一个内本 体; 动力电池通常只装入一个内本体 ( 7 ) ; 也可以将若干个 内本体并联装入外壳 ( 9 ) 内, 组成较大容量的动力电池; 卷 绕时, 正负极片上的大叶极耳必须错开位置, 极耳可以整齐相 对分列正负两极; 采用圆柱形外壳的卷绕后的内本体 ( 7 ) 的 纵剖面为矩形; 采用方形外壳的卷绕后的内本体 ( 7 ) 呈矩 形, ; 卷绕成型后的内本体 ( 7 ) , 排除隔膜 ( 1 9 ) 厚度, 正极 ( 1 3 ) 与负极 ( 1 2 ) 的间隙距离, 不得大于 2 5 μ m;  (5) Winding: The rolling pin of the inner body of the cylindrical shell used for winding is a round shaft, and the rolling pin of the inner body of the rectangular shell used for winding is a thin sheet with certain rigidity and elasticity; when the pole piece is folded inward, Generally, the folding line should be processed at the inner fold on the pole piece and the active material at the folding line should be scraped off; if the folding line is processed on the positive electrode (1 3), the front end of the negative electrode (1 2) should be aligned with the folding of the positive electrode (1 3) The center line of the wire so that it cannot pierce the diaphragm (19); when winding, a pair of positive and negative electrode groups must be neatly stacked, and the middle lined with the diaphragm (19) is tightly wound into the inner body (7) It is also possible to stack multiple pairs of positive and negative electrodes in parallel neatly at the same time, and tightly wind them into an inner body; power batteries are usually only installed in one inner body (7); several inner bodies can also be installed in parallel to the casing (9 ), A large-capacity power battery is formed; when winding, the large leaf tabs on the positive and negative electrodes must be staggered, and the tabs can be neatly aligned with the positive and negative poles; the wound inner body with a cylindrical shell (7) The longitudinal section is moment The rolled inner body (7) with a square shell is rectangular, and the rolled inner body (7) excludes the thickness of the separator (1 9) and the gap between the positive electrode (1 3) and the negative electrode (1 2) Distance, not more than 2 5 μ m;
( 6 ) 注液: 注液前必须抽出锂离子动力电池内腔中的常 态空气, 然后将适量的电解液从安全阀 ( 3 ) 内的注液孔注 入; 注液量通常在 0 . 1 5 Ah/ g ~ 0 . 6 Ah / g 的范围内调 整; 最佳的注液量在 0. 2 Ah/ g~ 0. 3 5 Ah/ g; 采用可适应 更宽的温度变化的多元电解液: L I P F 6 / E C : D M C : D E C , 溶剂比例为 0. 9 5 ~ 1 . 0 5 : 0. 9 5 ~ 1 . 0 5 : 0. 9 5 - 1. 0 5 ; 或 L I P F 6 / E C: E M C: D E C, 溶剂 比例为 0. 9 5 ~ 1. 0 5 : 0. 9 5 ~ 1. 0 5 : 0. 9 5 ~ 1. 0 5 ; 或 1^ 1 ? ? 6 / £ 0; : 01^ (: : £ € , 溶剂比例为 0. 9 5 - 1. 0 5 : 0. 9 5 - 1. 0 5 : 0. 9 5 - 1. 0 5 ; 或 L I P F 6 / E C: DM C: EM C: D E C , 溶剂比例为 0. 9 5 ~ 1. 0 5 : 0. 9 5 - 1. 0 5 : 0. 9 5 - 1. 0 5: 0. 9 5 - 1 0 5; (6) Liquid injection: Before the liquid injection, the normal air in the inner cavity of the lithium ion power battery must be extracted, and then an appropriate amount of electrolyte is injected from the liquid injection hole in the safety valve (3); the liquid injection amount is usually 0.1. 5 Ah / g ~ 0.6 Ah / g adjustment; the optimal injection volume is 0.2 Ah / g ~ 0.3 5 Ah / g; using a multi-electrolyte that can adapt to wider temperature changes: LIPF 6 / EC: DMC: DEC, the solvent ratio is 0.9 5 to 1. 0 5: 0.9 5 to 1. 0 5: 0. 9 5-1. 0 5; or LIPF 6 / EC: EMC: DEC, the solvent ratio is 0.9 5 to 1. 0 5: 0.9 5 to 1. 0 5: 0.9 5 to 1. 0 5 ; Or 1 ^ 1?? 6 / £ 0;: 01 ^ (:: £ €, solvent ratio is 0.9 5-1. 0 5: 0.9 5-1. 0 5: 0.9 5-1 0 5; OR LIPF 6 / EC: DM C: EM C: DEC with a solvent ratio of 0.9 5 to 1. 0 5: 0.9 5-1. 0 5: 0.9 5-1. 0 5 : 0. 9 5-1 0 5;
( 7) 化成: 化成原则必须是小电流、 低电压, 绝对不可 以大电流, 较高电压化成, 才能充分激活正、 负集流基体上的 活性物质, 化成工序必须一次性不间断地完成, 中途不可随意 中止或停止, 化成曲线应光滑连接, 电流应控制在 0. 0 1 C / 1 0小时→→ 0. 0 2 C / 5小时→→ 0. 0 5 C / 5小时→ → 0. 1 C / 4小时→→ 0. 2 C / 1小时, 恒流充满后转为恒 压继续充, 务求一次性充足。  (7) Formation: The formation principle must be low current and low voltage, and no large current can be formed. Higher voltage formation can fully activate the active materials on the positive and negative current collector substrates. The formation process must be completed uninterrupted at one time. Do not stop or stop arbitrarily in the middle, the formation curve should be smoothly connected, and the current should be controlled at 0. 0 1 C / 10 hours → → 0. 0 2 C / 5 hours → → 0. 0 5 C / 5 hours → → 0. 1 C / 4 hours → → 0.2 C / 1 hour, after the constant current is full, it will be converted to constant pressure to continue charging, so as to be sufficient at one time.
( 8 ) 分容: 分容。 将电性能各项指标均符合工艺要求的 电池与各项电性能指标未达工艺要求的电池分别置放入库。  (8) Capacity division: Capacity division. Put batteries with electrical performance indicators that meet process requirements and batteries with electrical performance indicators that do not meet process requirements, respectively.
PCT/CN2003/000170 2002-03-08 2003-03-07 A rechargeable lithium-ion power battery and manufacture method of the same WO2003077348A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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CN100418251C (en) * 2005-01-14 2008-09-10 比亚迪股份有限公司 Preparation method of electrode plates of lithium cell
JP4519685B2 (en) 2005-03-14 2010-08-04 株式会社東芝 Non-aqueous electrolyte battery
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CN109755472A (en) * 2019-01-18 2019-05-14 梅州市量能新能源科技有限公司 Novel high-energy metric density lithium battery
CN111654094A (en) * 2019-11-06 2020-09-11 洛阳北光新能源科技有限公司 Non-rechargeable lithium battery
CN111403671B (en) * 2020-03-20 2022-11-11 广东顺德工业设计研究院(广东顺德创新设计研究院) Method for manufacturing lithium ion battery
CN112103455A (en) * 2020-08-28 2020-12-18 中天储能科技有限公司 Tab structure, application of tab structure, preparation method and preparation device
CN114678521B (en) * 2022-04-24 2023-03-24 江苏金锋源新能源有限公司 Method for improving specific surface area of lithium ion battery anode material precursor

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11154500A (en) * 1997-11-21 1999-06-08 Japan Storage Battery Co Ltd Nonaqueous electrolyte secondary battery
JPH11162446A (en) * 1997-11-26 1999-06-18 Yuasa Corp Unit cell and battery device with it
JPH11250884A (en) * 1998-02-27 1999-09-17 Hitachi Ltd Battery
US6007944A (en) * 1997-04-10 1999-12-28 Varta Batterie Aktiengesellschaft Rechargeable lithium-ion cell
EP1102342A2 (en) * 1999-11-17 2001-05-23 Shin-Kobe Electric Machinery Co. Ltd Cylindrical lithium-ion battery
JP2001143666A (en) * 1999-11-17 2001-05-25 Shin Kobe Electric Mach Co Ltd Cylindrical lithium ion cell

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1214480C (en) * 1997-12-22 2005-08-10 三菱电机株式会社 Lithium ion secondary battery and its manufacture

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6007944A (en) * 1997-04-10 1999-12-28 Varta Batterie Aktiengesellschaft Rechargeable lithium-ion cell
JPH11154500A (en) * 1997-11-21 1999-06-08 Japan Storage Battery Co Ltd Nonaqueous electrolyte secondary battery
JPH11162446A (en) * 1997-11-26 1999-06-18 Yuasa Corp Unit cell and battery device with it
JPH11250884A (en) * 1998-02-27 1999-09-17 Hitachi Ltd Battery
EP1102342A2 (en) * 1999-11-17 2001-05-23 Shin-Kobe Electric Machinery Co. Ltd Cylindrical lithium-ion battery
JP2001143666A (en) * 1999-11-17 2001-05-25 Shin Kobe Electric Mach Co Ltd Cylindrical lithium ion cell

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104600250A (en) * 2014-11-21 2015-05-06 天津力神电池股份有限公司 Preparation method of lithium ion battery multi-pole-ear pole piece, preparation method of pole group and battery
EP3996182A1 (en) * 2020-11-10 2022-05-11 Prime Planet Energy & Solutions, Inc. Battery
CN113206286A (en) * 2021-04-26 2021-08-03 佰凡电池(江苏)有限公司 Lithium ion battery configuration system
CN113206286B (en) * 2021-04-26 2023-11-14 佰凡电池(江苏)有限公司 Lithium ion battery assembly system

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