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WO2003077349A1 - An rechargeable lithium-ion power battery and manufacture method of the same - Google Patents

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

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Publication number
WO2003077349A1
WO2003077349A1 PCT/CN2003/000171 CN0300171W WO03077349A1 WO 2003077349 A1 WO2003077349 A1 WO 2003077349A1 CN 0300171 W CN0300171 W CN 0300171W WO 03077349 A1 WO03077349 A1 WO 03077349A1
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WO
WIPO (PCT)
Prior art keywords
positive
pole
negative
positive electrode
negative electrode
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Application number
PCT/CN2003/000171
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French (fr)
Chinese (zh)
Inventor
Yongming Ju
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Individual
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Individual
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Priority to AU2003221287A priority Critical patent/AU2003221287A1/en
Publication of WO2003077349A1 publication Critical patent/WO2003077349A1/en
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Ceased legal-status Critical Current

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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
    • H01M50/543Terminals
    • H01M50/552Terminals characterised by their shape
    • H01M50/553Terminals adapted for prismatic, pouch or rectangular cells
    • 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
    • H01M50/50Current 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
    • 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
    • H01M50/534Electrode connections inside a battery casing characterised by the material of the leads or tabs
    • 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
    • H01M50/547Terminals characterised by the disposition of the terminals on the cells
    • H01M50/55Terminals characterised by the disposition of the terminals on the cells on the same side of the cell
    • 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.
  • 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 invention belongs to an environmentally-friendly battery that can be repeatedly charged and discharged.
  • the purpose is to hope that the positive and negative electrode tabs of the large-leaf tab and the separator, which have a unique design, have a multi-layered structure.
  • Negative electrode plates are arranged at regular intervals, and the electrode assembly is more sensitive to internal pressure, so it is more reliable and safer.
  • Safety valve, current collecting performance and heat dissipation performance are better. High-power repeated charge and discharge requirements, so as to achieve the wide application of lithium-ion power batteries.
  • 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 shell is composed of the following features:
  • the positive 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 It is connected to the negative electrode.
  • the positive electrode is made of aluminum foil of a certain thickness, and the positive electrode active material is evenly coated on both sides.
  • the negative electrode is made of copper foil of a certain thickness, and the negative electrode active material is evenly coated on both sides.
  • Unipolar ears or large-leaf multipolar ears with different intervals are shaped as long and narrow rectangular pieces (also known as flattened pieces).
  • Large-leaf monopoles and large-leaf multipolar ears are collectively referred to as large-leaf polar ears.
  • 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 adjustment bolt, the sealing steel ball can slide down vertically in the inner hole of the adjustment bolt, and the outer diameter of the adjustment bolt is machined with a thread that matches the safety valve body; adjustment Bolts are processed with several vertical exhaust grooves, and exhaust holes are opened in the lower part of the exhaust groove; the compression spring is pressed on the upper part of the steel ball, and the lower hole of the sealed steel ball is trapped in the fluorine on the cover injection port. On the rubber ⁇ ; the pressure relief hole at the bottom of the safety valve communicates with the injection hole on the cover.
  • the invention also provides a lithium ion power battery proportion and its manufacturing method that can be repeatedly charged and discharged, 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 into one ⁇ dividing.
  • 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 1-1 is a sectional view of a stacked lithium-ion power battery
  • Figure 1-2 shows a top view of a stacked lithium-ion power battery
  • Figures 1 A, 1 A-1, 1B, IB-1, 1 C, 1 C-1, 1D, 1D-1, 1E, and I E-1 represent the schematic diagrams of the large leaf pole ears on the pole pieces;
  • FIG. 2 is a cross-sectional view of a lithium ion power battery according to the present invention.
  • FIG. 3 and FIG. 4 are stacking methods of pole pieces in the lithium ion power battery of the present invention.
  • Figures 5 and 6 show the structure of a pressure spring type and a plate type safety valve, respectively.
  • each unit battery is composed of a cover plate 1, a negative pole 2, a safety valve 3, and a positive pole.
  • the outer shell 9, the negative pole 2 on the cover plate 1, the safety valve 3, and the positive pole 4 constitute the outer body of the lithium-ion power battery; multiple pairs of positive and negative electrode groups, the diaphragm, and the current collector plye constitute the inner body of the lithium-ion power battery
  • laminated body 7 also known as laminated body.
  • the structure and manufacturing process (method) of the laminated lithium-ion power battery are described below:
  • the laminated inner body 7 of a lithium-ion power battery is composed of one or more pairs of positive and negative electrode sheet groups and a separator.
  • the electrode assembly has a multi-layer structure, and the positive and negative electrode sheets are arranged at regular intervals.
  • the smallest lithium-ion power battery can consist of a pair of positive and negative electrode groups and a separator.
  • the positive electrode 1 3 is composed of an aluminum foil and a positive electrode active material (not shown in the figure).
  • the aluminum foil is a thin metal foil, and the positive electrode active material is evenly coated on both sides (either Lithium cobaltate, or lithium manganate or lithium nickelate, lithium nickel cobaltate).
  • the surface of the aluminum foil is usually smooth, but the aluminum foil with a rougher surface has better adhesion for coating active materials.
  • a suitable aluminum foil thickness ranges from 10 ⁇ m to 80 ⁇ m.
  • the optimal thickness of aluminum foil is 15 ⁇ m ⁇ 2 5 ⁇ m; when charging and discharging requirements are 2 C ⁇ 3 C or greater, other factors are excluded, and aluminum foil is used.
  • the optimal thickness is 20 ⁇ m to 4 5 ⁇ m or more.
  • Negative electrode 1 2 is composed of copper foil and negative electrode active material (not shown in the figure). Copper foil is a thin metal foil, and the negative electrode active material is evenly coated on both sides (either natural graphite, flake graphite, artificial Graphite or petroleum coke). 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 ⁇ m ⁇ 50 ⁇ m.
  • the optimal thickness of copper foil is 8 ⁇ m ⁇ 20 ⁇ m; when charging and discharging requirements are 2 C ⁇ 3 C or greater, other influencing factors are excluded, and copper foil is selected
  • the optimal thickness is 15 ⁇ m ⁇ 3 5 ⁇ ⁇ 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 pole piece.
  • the thickness of the metal foil with a larger capacitance should be slightly larger than that of the metal foil with a small capacitance. thick.
  • 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 active material of the lithium ion power battery according to the present invention The amount has increased greatly regardless of the positive or 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, when the area of the positive electrode piece is less than or equal to 1 0 0 O mmx 5 0 0 mm and greater than or equal to 1 0 0 mm x 5 0 0 m 2, the optimal density of the positive electrode active material per square centimeter is 0.
  • the density of the negative electrode active material per square centimeter is approximately 0. 0 1 ⁇ ⁇ 0. 0 3 8 .
  • the optimal density of the negative electrode active material per square centimeter is 0.04 g ⁇ 0. 0 2 1 g.
  • 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.
  • FIGS. 1A-1 and IB-1 it can be seen that there is a large leaf tab 1 1 on the positive electrode 13, and as shown in FIG. 1A and FIG.
  • large-leaf monopole ear there is only one large leaf tab 1 0 on the negative electrode 12, It is called a large-leaf monopole ear; as shown in Figures 1C and 1C-1, it can be seen that there are multiple large-leaf pole ears on the positive and negative plates, which are called large-leaf multipole ears. Large-leaf monopoles and large-leaf multipoles are collectively referred to as large-leaf poles.
  • Large leaf tabs should use a larger cross-sectional area as far as possible, that is, the tabs should be as wide and thick as possible, and the current collecting (collecting) path should be as short as possible, which is beneficial to the current. Export and cooling.
  • the positive and negative electrodes usually have only one large leaf tab; for a large-capacity lithium-ion power battery, there are several large leaf tabs.
  • large-leaf multipolar ears can better conduct and dissipate heat than large-leaf monopolar ears.
  • the large-leaf monopole ears can also be as shown in Figure ID and Figure ID-1.
  • the large-leaf pole ears of the positive and negative poles can be drawn from the side ends of the pole pieces in different directions.
  • the maximum width of the large leaf tabs from the side ends of the pole pieces in different directions can be the same as the side where the large leaf tabs are located, which is more conducive to the flow and heat dissipation of lithium ion power batteries.
  • the width of the large leaf monopoles must not be greater than the location of the large leaf tabs.
  • the side of the side is half (half) long.
  • the maximum height of the lobe poles is not greater than its own (lobe poles) width, preferably smaller than its width. The smaller the height of the lobe pole, the better.
  • the large-leaf multipole ears can be arbitrarily set at any position on the long or short sides of the positive and negative plates as required.
  • the centerline position should be located at about 1/4 or 3/4 of the side length of the laminated positive and negative plates as much as possible.
  • the inner edge line of the large leaf tab should be as close as possible to the center line of the side where the large leaf tab is located, but it must not obstruct the other tab's tab. Insulation measures must be taken to prevent short-circuiting with the other tab's tab.
  • the positive and negative electrodes of a laminated lithium-ion power battery are usually cut into rectangular pieces.
  • the best aspect ratio for rectangular tablets is 6.2: 3.8 or 6: 4.
  • the positive and negative electrode pieces can also be made into a circle or other desired shapes.
  • the dimensions of the positive and negative electrode sheets are different due to their process requirements. Since the active material of the positive electrode is much more expensive than the active material of the negative electrode, the length and width of the negative electrode sheet are slightly larger than the positive electrode sheet when cutting. This approach not only saves resources, but also gives full play to the material properties of the positive electrode.
  • the positive electrode 1 3 and the negative electrode 1 2 are usually directly cut into rectangular pieces with large leaf monopoles or large leaf multipoles.
  • the method of making large-leaf pole tabs can also be directly processed to form pole pieces by rolling or shearing.
  • 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 Ear; in the case of high power discharge without fast high power charging, the positive electrode
  • the width of the large lobes on the negative electrode 12 may be greater than the width of the large lobes on the negative electrode 12.
  • connection between the 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 1A.
  • the R in the connection of Figure 1A-1 not only has higher mechanical strength, but also helps to prevent the concentration of heat and cause the pole tabs or even the pole pieces to melt.
  • the positive and negative plates of lithium-ion power batteries use corresponding tabs, that is, when the positive electrode 1 3 uses large-leaf monopole ears, and the negative electrode 12 usually uses large-leaf monopole ears; 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 method of the tabs is whether the directly cut tabs 10/1 1 or the welded tabs are raised heads. It can be seen that the tabs are significantly higher than the active material coated on the tabs. The advantage is that it is convenient Scraping powder.
  • the large-leaf tabs shown in Figure ID and Figure 1D-1 are hidden-head style tabs.
  • This hidden-head-style large tabs 17/1 8 can make fuller use of lithium. Space inside the ion battery.
  • the form of the hidden head is exactly the opposite of that of the raised head.
  • the raised and hidden large leaf tabs can be on the long sides of the rectangular positive and negative tabs, or on the short sides of the positive and negative tabs. From the perspective of rationality, the large leaf tabs should be as positive and negative as possible. The long side of the pole piece.
  • the tabs can be fabricated by welding as shown in Figures 1B and 1B-1 (15/16).
  • the 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 welded large leaf poles to make large leaf poles.
  • Welds 1 4 must be firm.
  • Welding The advantage of the tab is that the cut pole piece has less burrs.
  • the positive electrode is made of aluminum, and the negative electrode is made of nickel or copper.
  • the shape of the large leaf tabs can be designed and processed into square, rectangular, semi-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 basic function of the separator is to isolate the positive and negative electrodes, prevent the battery from short circuit, 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 high electrical conductivity. Therefore, porous polyolefin materials are the most suitable. 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 having a microporous structure and a low current cut-off temperature of 15 to 80 ⁇ m.
  • 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 1
  • the optimal thickness of the separator is 20 ⁇ ⁇ ⁇ 4 0 ⁇ ⁇ ;
  • the optimal thickness of the separator is 40 ⁇ m or more.
  • 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 after rolling (the immersion method can also be used to immerse the positive electrode sheet in In the above slurry), the positive electrode sheet is put into a specific solvent to extract a pore-forming agent to form a satisfactory separator integrated with the positive electrode sheet.
  • the shape of the separator is generally consistent with the shape of the positive and negative electrode sheets. Because all positive
  • the area of 1 3 is slightly smaller than that of the negative electrode 12, so the positive electrode 1 3 is wrapped with a separator.
  • the separator is usually made into a bag shape 19 or a book shape 19-1 in order to fit or clamp the positive electrode 13.
  • the bag-shaped diaphragm can heat-seal three sides, or only the adjacent two sides; a diaphragm that only heat-seals adjacent two sides is easier to assemble.
  • the area of the separator is larger than the positive and negative electrodes in both length and width. Except for the ears, the separator 19/1 9-1 must completely surround the positive electrode 1 13 and not expose the edges to prevent short circuit.
  • the material of the lithium ion power battery pole is a metal material with excellent electrical conductivity 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 can be installed, for example, two positive poles and two negative poles can be installed at the same time.
  • the number of positive and negative poles can 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 equal to or greater than the number of positive poles The number of positive poles; in the case of high power discharge without fast high power charging, the number of positive poles can 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 / EC DMC: EMC
  • the solvent ratio is 0.95-1.05: 0.95-1.05: 0.95-1.05; or (4).
  • the solvent ratio is 0.95 to 1.05: 0.95 to 1.05: 0.95 to 1.05: 0.95-1.05.
  • 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 poles.
  • the cell case is also referred to as an electrode case.
  • the cell case of high-power lithium-ion power batteries should be avoided as much as possible.
  • the enclosure must be insulated from the pole. However, in special cases, the case can also become an electrode case.
  • the square case 9 of a lithium-ion power battery consists of several flat surfaces.
  • 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 (thermal bridges) 9-1 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 overcharging and short-circuiting. 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 of the lithium-ion power battery.
  • the reset mechanism is shown in Figure 6-1, 6-2, 6-3, 6-4, 6-5, 6-6. They are as follows:
  • the structure of the pressure spring safety valve is shown in Figure 5 -1, 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 compression spring, a cage of 'sealed steel ball 2 2', and the compression spring can be longitudinal in the inner hole of the adjustment bolt. It can move up and down without being able to swing laterally.
  • the sealing steel ball can also be moved up and down in the inner hole of the adjustment bolt without being able to swing horizontally.
  • the outer diameter of the adjustment bolt is machined with a thread that matches 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 keyhole 27.
  • the keyhole also serves as an exhaust.
  • the adjusting bolt When the rotary 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.
  • the adjusting bolt can be rotated through the exhaust groove to rotate it, 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 aprons. It is pressed or attached to the liquid injection hole 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 on the bottom of the safety valve is in communication with the injection hole on the cover plate 1, so the pressure relief hole is the injection hole when the liquid is injected.
  • 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 with its bottom inner ring just snaps on the upper part of the sealing steel ball, and the lower part of the sealing steel ball is trapped on the fluoro rubber ring 26 or other corrosion-resistant rubber pad on the battery cover, which restrains the sealing 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 Figures 6-1 and 6-2.
  • the reverse bow spring 30 is installed on the lower part of the adjustment bolt 23, and 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 The bottom is pressed tightly on the anti-bow shrapnel. Turn the height adjustment bolt of the keyhole 8 to adjust the tension of the anti-bow spring.
  • the safety valve body is processed with a rectangular exhaust groove 3 1.
  • the anti-bend spring is installed in the rectangular groove and can not be rotated horizontally except that 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 balls 22 can be vertically moved down in the cage.
  • the anti-bow shrapnel is processed with a process assembling hole 3 3, which is crimped on the upper part of the steel ball to fix and seal the steel ball.
  • the lower hole of the sealed steel ball is trapped on the fluorine rubber ring or other corrosion-resistant rubber pad on the cover injection port, which not only fixes the sealed steel ball, but also seals the battery.
  • fluoro rubber ⁇ or other corrosion-resistant rubber pads must have a certain elasticity, so that when the steel ball is pressed against the fluoro rubber ⁇ or other corrosion-resistant rubber pads, the fluoro rubber ⁇ or other corrosion-resistant stock pads will 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 pressure inside the battery is greater than the set value, it will Automatically lift the sealed steel ball to release the pressure, and the gas will be immediately discharged from the pressure release hole 2 9 and escape along the exhaust groove 31 from the exhaust hole 3 2 and the key hole 2 7.
  • the pressure of the anti-bow spring is sufficient to compress the sealing steel ball again to seal the pressure relief hole.
  • the anti-bow shrapnel can be designed and processed into a flat-shaped anti-bow shrapnel.
  • the flat-shaped anti-bow shrapnel works like a half-moon anti-bow shrapnel.
  • the pressure of the tablet-type safety valve can also be adjusted by the screws 3 4 as 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 is the communication hole with the liquid injection hole on the cover plate 1 and also communicates with the pressure relief hole on the bottom of the safety valve, so it is not marked separately.
  • the fluoro rubber ⁇ 26 may be replaced by any other suitable apron.
  • 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-shaped anti-bow shrapnel is the same as that of the half-moon anti-bow shrapnel.
  • the sealed steel ball 2 2 can be designed and processed into a ball 2 2-1 with a horizontal transverse groove, and fluoro rubber 2 6- One is clamped in the horizontal groove on the sealed steel ball 2 2-1.
  • 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 fluoro rubber ⁇ , 6-1 tightly seals the injection hole.
  • the internal pressure is greater than the permissible value and the sealing steel ball 2> 2-1 is jacked up, the fluorine rubber ⁇ 2 6-1 is lifted upward at the same time, and the internal pressure is quickly removed.
  • the sealing steel ball 2 2 can also be designed and processed into a sealing head 2 2-2. Compared with the steel ball 2 2 or 2 2 1 1, the lower part of the sealing frustum protrudes into the injection hole, so the reset is more reliable.
  • the sealing frustum can also be processed with a fixed small handle 3 6, and a compression spring or a reverse 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. The pressure of the fluoro rubber ⁇ 2 6 deforms in the sealing frustum and tightly seals the injection hole. When the internal pressure is greater than the allowable value, the top sealing cone 2 2-2 is quickly released.
  • the sealing frustum can also be designed and processed into 2 2-3 with a horizontal horizontal groove on it, and the fluoro rubber ⁇ 2 6-1 is hooped in the horizontal horizontal groove on the sealing frustum 2 2-3.
  • the fluoro rubber ring 2 6-1 seals the injection hole.
  • the internal pressure is greater than the allowable value and 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 removed.
  • 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 can be installed with thousands of safety valves on the same side surface or on different side surfaces.
  • the medium for preparing the slurry includes NMP (N-fluorenyl-2-pyrrolidone) as the medium or water as the medium; the preparation methods include the wet method and the dry method.
  • NMP N-fluorenyl-2-pyrrolidone
  • the preparation methods include the wet method and the 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.
  • P V D F, graphite (or acetylene black), and carbon black all need to be baked in an oven at about 120 ° C 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.
  • Sequential preparation method After adding CMC to water and stirring for about 3 to 4 hours, add SBR to it and stir for about 0.5 to 1 hour, then add conductive agent graphite (or acetylene black), carbon black and stir for about 0.5 to 1 hour, and finally add cobalt Lithium acid Mix for about 2.5 to 4 hours to form a thicker paste. Sieve out agglomerates and other impurities.
  • the preparation of the positive electrode must be slightly larger than the conductive agent.
  • N M P the medium.
  • P V D F should be baked in an oven at a temperature of about 120 ° C for 2 to 3 hours, while graphite needs to be baked at a temperature of 300 ° C to 500 ° C for 4 to 8 hours.
  • Sequential preparation method Add P V D F to N M P and stir for about 3 to 4 hours, then add the graphite that has been sifted through a 3 2 5 mesh sieve and shake it 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 the graphite after baking and sieving through 300 mesh to stir for about 3 to 4 hours. Pasty.
  • Dry preparation Dry preparation of the positive electrode with N M P as the medium. Materials required: Materials required: P V D F 2.5% to 3.5%, lithium cobaltate 93% to 95%, conductive agent graphite 1.5% to 2 ° /. (Or acetylene black 0.8% ⁇ 1.
  • NM P is restricted by the particle size and particle size distribution of the foregoing substances, especially lithium cobaltate, so it is about the total amount of all the foregoing substances.
  • 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 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 the foregoing method using lithium cobaltate.
  • 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 ⁇ ⁇ ) 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
  • 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% to 50% based on the original solid-liquid ratio, and the solid-liquid ratio of coarser powders above 12 ⁇ m should be based on the original solid-liquid ratio. Up to 10% ⁇ 30%.
  • 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 ° C ⁇ 500 ° C), the rest are dried.
  • the baking material can be placed in a vacuum box for vacuum treatment, without the need for high temperature treatment.
  • the production process of lithium-ion power battery is as follows: ingredients- ⁇ coating- ⁇ production- ⁇ rolling- ⁇ winding and assembly into the inner body (including casing, sealing)- ⁇ injection- ⁇ chemical formation- ⁇ volume .
  • 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, and baked into the oven. After baking, it will become a semi-finished current collecting piece. 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, ⁇ 1 0 ° C, the temperature in the high temperature section is 1 2 0 ° C ⁇ 1 40 ° C, ⁇ 10 ° C.
  • 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 a medium can be higher than that of NMP as a 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 area 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.
  • Most of the current coating processes are single-sided coating, and then the other side is coated; however, double-sided coating can also be applied at the same time.
  • 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.
  • pole pieces of the same polarity negative electrode and negative electrode, positive electrode and positive electrode
  • the back surface metallic surface without active material coating
  • 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 ⁇ 5000mm per minute. The best linear speed is 1200mm ⁇ 35 00mm 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 ⁇ ⁇ to 270 ⁇ m, and the thickness of the positive electrode after rolling is about 110 ⁇ ⁇ to 165 ⁇ ⁇ ; the thickness of the negative electrode before rolling is about 185 ⁇ m to 275 ⁇ m , 110 ⁇ ⁇ ⁇ 165 ⁇ ⁇ after rolling.
  • the optimal thickness of the positive electrode before rolling is 195 ⁇ ⁇ ⁇ 235 ⁇ ⁇ , and 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 ⁇ ⁇ ⁇ 155 ⁇ ⁇ .
  • Battery assembly When assembling, first put the positive electrode sheet into the clip of the bag-shaped separator 19 or the book-shaped separator 19-1, and then arrange the positive electrode tabs in parallel to one end of the inner body 7 and clamp it with a current collector plywood The negative electrode tabs are arranged neatly in parallel to the other end of the inner body, and are also clamped with a current collecting plywood.
  • the positive electrode sheet 1 3 and the negative electrode sheet 12 must be stacked and spaced apart, that is, a negative electrode sheet is stacked, then a positive electrode sheet is stacked, then a negative electrode sheet is stacked, and so on.
  • both sides of the outermost layer of the inner body are usually negative plates.
  • both sides of the outermost layer of the inner body may also be positive electrode sheets.
  • the positive pole 4 is connected to the positive piece 1 3
  • the negative pole 2 is connected to the negative piece 1 2.
  • the assembled inner body must be tightly wrapped with a diaphragm or clamped with a polyethylene or polypropylene frame.
  • the inner body of the assembled state is excluded.
  • the thickness of the separator 19 is excluded.
  • the distance between the positive electrode and the negative electrode must not be greater than 25 ⁇ m (the maximum gap between the positive electrode and the negative electrode-the thickness of the separator + 2 5 ⁇ m).
  • 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.
  • 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 20, and clamps the tabs respectively and fastens them 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 in 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 never 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, and 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.

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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 positive 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 multi-layer laminated structure which is composed of one or more pairs of electrodes, that is positive electrode, negative electrode, and separator, in this electrode assembly, the positive electrode sheet and the negative electrode sheet are separately positioned in sequence. Either the positive electrode sheet or the negative electrode sheet is shaped into rectangle sheet with big-leaf single tab or big-leaf multiple tabs, 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. Amount of the positive pole can be same with that of the negative pole, or different; diameter of the pole can be same, or different.

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 for efficient and clean power sources.

已经有很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。 近些年来, 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。  There have been many studies 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. But because of its low energy density, it takes a long time to charge, and it cannot meet the needs of high-power charge and discharge. It directly affects the practicality 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

本发明属于一种可以反复充放电的环保电池, 目的是希望 以有设计独特的集电 (集流) 端子即大叶极耳的正负极片与隔 膜共同构成具有多重积层结构、 正、 负极片顺序间隔置放整齐 的电极集合体、 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 belongs to an environmentally-friendly battery that can be repeatedly charged and discharged. The purpose is to hope that the positive and negative electrode tabs of the large-leaf tab and the separator, which have a unique design, have a multi-layered structure. Negative electrode plates are arranged at regular intervals, and the electrode assembly is more sensitive to internal pressure, so it is more reliable and safer. Safety valve, current collecting performance and heat dissipation performance are better. High-power repeated charge and discharge requirements, so as to achieve the wide application of lithium-ion power batteries.

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 ( 包括长方形 ) 外壳组成, 其 特征在于: 内本体系由正负极片组即正极片、 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 匀涂布正极活性物质, 负极选用一定厚度的铜箔, 两面均匀涂 布负极活性物质; 正极或负极的极片形式均为带有大叶单极耳 或间距不等的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. (Including rectangle) The shell is composed of the following features: The positive 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 It is connected to the negative electrode. The positive electrode is made of aluminum foil of a certain thickness, and the positive electrode active material is evenly coated on both sides. The negative electrode is made of copper foil of a certain thickness, and the negative electrode active material is evenly coated on both sides. Unipolar ears or large-leaf multipolar ears with different intervals are shaped as long and narrow rectangular pieces (also known as flattened pieces). Large-leaf monopoles and large-leaf multipolar ears are collectively referred to as large-leaf polar ears. 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纹; 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 adjustment bolt, the sealing steel ball can slide down vertically in the inner hole of the adjustment bolt, and the outer diameter of the adjustment bolt is machined with a thread that matches the safety valve body; adjustment Bolts are processed with several vertical exhaust grooves, and exhaust holes are opened in the lower part of the exhaust groove; the compression spring is pressed on the upper part of the steel ball, and the lower hole of the sealed steel ball is trapped in the fluorine on the cover injection port. On the rubber 圏; 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, 包括以下步驟: 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 - → 化成一 →分容。 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 also provides a lithium ion power battery proportion and its manufacturing method that can be repeatedly charged and discharged, 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 into one → dividing. 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, 具体描述本发明, 图中相同的附图标记表 示相同的部件。 其中:  The present invention is described in detail below with reference to the drawings, in which the same reference numerals indicate the same components. among them:

图 1-1为叠层式锂离子动力电池的剖视图;  Figure 1-1 is a sectional view of a stacked lithium-ion power battery;

图 1-2表示叠层式锂离子动力电池的俯视图;  Figure 1-2 shows a top view of a stacked lithium-ion power battery;

图 1 A、 1 A-1、 1B、 IB- 1、 1 C、 1 C-1、 1D、 1D-1、 1E、 I E- 1分别表示大叶极耳在极片上的示意图;  Figures 1 A, 1 A-1, 1B, IB-1, 1 C, 1 C-1, 1D, 1D-1, 1E, and I E-1 represent the schematic diagrams of the large leaf pole ears on the pole pieces;

图 2所示则为本发明的锂离子动力电池的剖视图;  FIG. 2 is a cross-sectional view of a lithium ion power battery according to the present invention;

图 3和图 4 为本发明的锂离子动力电池中的极片的叠放方 式;  FIG. 3 and FIG. 4 are stacking methods of pole pieces in the lithium ion power battery of the present invention;

图 5和图 6分别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 1-1 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 In terms of appearance, the basic structure of a lithium-ion power battery is shown in Figure 1-1. Each unit battery is composed of a cover plate 1, a negative pole 2, a safety valve 3, and a positive pole.

4和敞口外壳 9组成; 而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4 and open case 9; and in the inner cavity of the lithium-ion power battery, there is a current collector plywood (also known as a pole piece plywood) 6, an electrolyte 8, a negative piece 1 2 and a positive piece

1 3 以及隔膜 1 9 (或 1 9 - 1 ) 。 外壳 9 、 盖板 1上的负极 柱 2 、 安全阀 3 、 正极柱 4构成锂离子动力电池的外本体; 多 对正负极片组, 隔膜、 集电夹板构成锂离子动力电池的内本体1 3 and diaphragm 1 9 (or 1 9-1). The outer shell 9, the negative pole 2 on the cover plate 1, the safety valve 3, and the positive pole 4 constitute the outer body of the lithium-ion power battery; multiple pairs of positive and negative electrode groups, the diaphragm, and the current collector plye constitute the inner body of the lithium-ion power battery

7 ( 亦称叠层体) 。 现将叠层式锂离子动力电池的结构、 制作 工艺 (方法) 分述如下: 7 (also known as laminated body). The structure and manufacturing process (method) of the laminated lithium-ion power battery are described below:

叠层式锂离子动力电池的结构  Structure of laminated lithium-ion power battery

锂离子动力电池的叠层式内本体 7 系由一对或多对正负极 片组与隔膜共同构成具有多重积层结构、 正、 负极片顺序间隔 置放整齐的电极集合体。 最小的锂离子动力电池可以由一对正 负极片组与隔膜組成。  The laminated inner body 7 of a lithium-ion power battery is composed of one or more pairs of positive and negative electrode sheet groups and a separator. The electrode assembly has a multi-layer structure, and the positive and negative electrode sheets are arranged at regular intervals. The smallest lithium-ion power battery can consist of a pair of positive and negative electrode groups and a separator.

正极 1 3 系由铝箔、 正极活性物质组成 ( 图中未示出 ) , 铝箔为薄片的金属箔, 两面均匀涂布了正极活性物质 (既可以 是鈷酸锂, 也可以是锰酸锂或镍酸锂、 镍钴酸锂) 。 铝蕩的表 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 m~ 8 0 μ m, 当正极极片的面积小于或等于 1 0 0 001111 5 0 0 mm 而又大于或等于 1 0 O mm x 5 0 mm, 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 m~ 2 5 μ m; 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 ιη~ 4 5 μ ιη或以上。 The positive electrode 1 3 is composed of an aluminum foil and a positive electrode active material (not shown in the figure). The aluminum foil is a thin metal foil, and the positive electrode active material is evenly coated on both sides (either Lithium cobaltate, or lithium manganate or lithium nickelate, lithium nickel cobaltate). The surface of the aluminum foil is usually smooth, but the aluminum foil with a rougher surface has better adhesion for coating active materials. A suitable aluminum foil thickness ranges from 10 μm to 80 μm. When the area of the positive electrode piece is less than or equal to 1 0 0 001 111 5 0 0 mm and greater than or equal to 10 0 mm x 50 mm, charge and discharge When 1 C ~ 2 C is required, exclude other influencing factors, and the optimal thickness of aluminum foil is 15 μm ~ 2 5 μm; when charging and discharging requirements are 2 C ~ 3 C or greater, other factors are excluded, and aluminum foil is used. The optimal thickness is 20 μm to 4 5 μm or more.

负极 1 2 系由铜箔、 负极活性物质组成 ( 图中未示出 ) , 铜箔为薄片的金属箔, 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 m~ 5 0 μ m, 当负极极片的面积小于或等于 1 0 0 O mmx 5 0 0 mm 而又大于或等于 1 0 O mmx 5 0 mm, 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 m~ 2 0 μ m; 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 ηι或以上。  Negative electrode 1 2 is composed of copper foil and negative electrode active material (not shown in the figure). Copper foil is a thin metal foil, and the negative electrode active material is evenly coated on both sides (either natural graphite, flake graphite, artificial Graphite or petroleum coke). 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 μm ~ 50 μm. When the area of the negative electrode piece is less than or equal to 100 mm x 50 mm and greater than or equal to 100 mm x 50 mm, charge and discharge requirements When 1 C-2 C, exclude other influencing factors, the optimal thickness of copper foil is 8 μm ~ 20 μm; when charging and discharging requirements are 2 C ~ 3 C or greater, other influencing factors are excluded, and copper foil is selected The optimal thickness is 15 μm ~ 3 5 μ ηι 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, 较大电容量的金属箔厚度比较小电容量的 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 pole piece. The thickness of the metal foil with a larger capacitance should be slightly larger than that of the metal foil with a small capacitance. thick. 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, 当正极极片的面积小于或等于 1 0 0 O mmx 5 0 0 mm 而又 大于或等于 1 0 0 mmx 5 0 m 时, 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 §~ 0. 0 3 8, 当负极极片的面积小于或 等于 1 0 0 O mmx 5 0 0 mm 而又大于或等于 1 0 O mmx 5 0 mm 时, 负极活性物质的最佳密度每平方厘米为 0. 0 1 4 g~ 0. 0 2 1 g。 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 active material of the lithium ion power battery according to the present invention The amount has increased greatly regardless of the positive or 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, when the area of the positive electrode piece is less than or equal to 1 0 0 O mmx 5 0 0 mm and greater than or equal to 1 0 0 mm x 5 0 0 m 2, the optimal density of the positive electrode active material per square centimeter is 0. 0 2 2 g ~ 0. 0 4 2 g; the density of the negative electrode active material per square centimeter is approximately 0. 0 1 § ~ 0. 0 3 8 , When the area of the negative electrode piece is less than or equal to 100 mm x 500 mm and greater than or equal to 100 mm x 50 mm, the optimal density of the negative electrode active material per square centimeter is 0.04 g ~ 0. 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。 如图 1A - 1 、 图 IB - 1所示, 可 见正极 1 3上有一个大叶极耳 1 1 , 如图 1A、 图 1B所示, 负极 1 2上也只有一个大叶极耳 1 0 , 称为大叶单极耳; 如图 1 C、 图 1 C - 1 所示, 则可见正负极片上有多个大叶极耳, 称为大叶多极耳。 大叶单极耳、 大叶多极耳, 统称为大叶极 耳。  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. As shown in FIGS. 1A-1 and IB-1, it can be seen that there is a large leaf tab 1 1 on the positive electrode 13, and as shown in FIG. 1A and FIG. 1B, there is only one large leaf tab 1 0 on the negative electrode 12, It is called a large-leaf monopole ear; as shown in Figures 1C and 1C-1, it can be seen that there are multiple large-leaf pole ears on the positive and negative plates, which are called large-leaf multipole ears. Large-leaf monopoles and large-leaf multipoles are collectively referred to as large-leaf poles.

大叶极耳在条件许可的情况下应当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。 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。 相较于大叶单极 耳而言, 大叶多极耳比大叶单极耳能够更好地导流、 散热。  Large leaf tabs should use a larger cross-sectional area as far as possible, that is, the tabs should be as wide and thick as possible, and the current collecting (collecting) path should be as short as possible, which is beneficial to the current. Export and cooling. For a lithium-ion power battery with a smaller capacity, the positive and negative electrodes usually have only one large leaf tab; for a large-capacity lithium-ion power battery, there are several large leaf tabs. Compared with large-leaf monopolar ears, large-leaf multipolar ears can better conduct and dissipate heat than large-leaf monopolar ears.

大叶单极耳也可如图 ID、 图 ID - 1所示, 正负极的大叶 极耳可以各自从极片的不同方向的侧端引出。 从极片不同方向 的侧端引出的大叶极耳的最大宽度可以与大叶极耳所在的那条 边等长, 更加有利于锂离子动力电池的导流、 散热。  The large-leaf monopole ears can also be as shown in Figure ID and Figure ID-1. The large-leaf pole ears of the positive and negative poles can be drawn from the side ends of the pole pieces in different directions. The maximum width of the large leaf tabs from the side ends of the pole pieces in different directions can be the same as the side where the large leaf tabs are located, which is more conducive to the flow and heat dissipation of lithium ion power batteries.

正负极片上的大叶极耳如果从同一方向或同一侧端引 出例 如向上引出, 如图 1 A、 图 1 A - 1 所示, 大叶单极耳的宽度 不得大于大叶极耳所处的那条边的边长的一半 (二分之一) 。 通常情况下, 大叶极耳的最大高度不大于其自身 (大叶极 耳) 宽度, 最好小于其宽度。 大叶极耳的高度越小越好。 If the large leaf tabs on the positive and negative electrodes are led from the same direction or the same side, for example, upward, as shown in Figures 1A and 1A-1, the width of the large leaf monopoles must not be greater than the location of the large leaf tabs. The side of the side is half (half) long. In general, the maximum height of the lobe poles is not greater than its own (lobe poles) width, preferably smaller than its width. The smaller the height of the lobe pole, the better.

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, 显然要宽大 一些才能满足要求, 故大叶极耳通常或尽量位于正负极片的较 长的边上。 大叶极耳位于正负极片的较长的边上, 姑称为卧式 片, 大叶极耳如果位于正负极片的较短的边上, 则可称为立式 片。 从集流性能而言, 卧式片优于立式片, 故在条件许可的情 况下, 应尽量采用卧式。  The tabs of a large-capacity power battery, and the tabs of a relatively small-capacity power battery, obviously need to be wider to meet the requirements in terms of the performance of flow guidance, heat dissipation, and high-rate charge and discharge. Or try to locate on the longer side of the positive and negative plates. Large lobe tabs are located on the longer sides of the positive and negative tabs, and are tentatively referred to as horizontal tabs. Large lobe tabs are located on the shorter sides of the positive and negative tabs, and can be referred to as vertical tabs. In terms of current collecting performance, the horizontal film is better than the vertical film, so if the conditions permit, the horizontal film should be used as much as possible.

其实, 只要保证不发生短路, 根据需要, 大叶多极耳可以 任意设置于正、 负极片的长边或短边上的任何位置上。  In fact, as long as no short circuit is guaranteed, the large-leaf multipole ears can be arbitrarily set at any position on the long or short sides of the positive and negative plates as required.

正负极片上的大叶单极耳如果从同一方向或同一侧端例如 向上引出, 如图 1 A、 图 1 A - 1 ; 图 1 B、 图 I B - 1所示, 大叶单极耳的中心线位置应尽量位于叠层式正、 负极片的边长 上约 1 / 4处或 3 / 4处。 大叶极耳的内缘线应尽量靠近大叶 极耳所在的那条边的中心线, 但不能妨碍另一极的极耳, 必须 采取绝缘措施防止与另一极的极耳接触短路。  If the large-leaf monopole ears on the positive and negative plates are led out from the same direction or the same side, for example, as shown in Figure 1A, Figure 1 A-1; Figure 1B, Figure IB-1, The centerline position should be located at about 1/4 or 3/4 of the side length of the laminated positive and negative plates as much as possible. The inner edge line of the large leaf tab should be as close as possible to the center line of the side where the large leaf tab is located, but it must not obstruct the other tab's tab. Insulation measures must be taken to prevent short-circuiting with the other tab's tab.

叠层式锂离子动力电池的正负极片, 通常裁切为矩形片。 矩形片最佳的长宽比为 6 . 2 : 3 . 8或 6 : 4 的矩形片。 正负极 片的形状除矩形外, 也可制成圆形或其他需要的形状。  The positive and negative electrodes of a laminated lithium-ion power battery are usually cut into rectangular pieces. The best aspect ratio for rectangular tablets is 6.2: 3.8 or 6: 4. In addition to the rectangular shape, the positive and negative electrode pieces can also be made into a circle or other desired shapes.

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 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, 既节省资源, 又充 分发挥正极的物质性能。  The dimensions of the positive and negative electrode sheets are different due to their process requirements. Since the active material of the positive electrode is much more expensive than the active material of the negative electrode, the length and width of the negative electrode sheet are slightly larger than the positive electrode sheet when cutting. This approach not only saves resources, but also gives full play to the material properties of the positive electrode.

正极 1 3 、 负极 1 2通常直接裁切为带有大叶单极耳或大 叶多极耳的矩形片。 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。  The positive electrode 1 3 and the negative electrode 1 2 are usually directly cut into rectangular pieces with large leaf monopoles or large leaf multipoles. In addition to cutting, the method of making large-leaf pole tabs can also be directly processed to form pole pieces by rolling or shearing.

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 Ear; in the case of high power discharge without fast high power charging, the positive electrode

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。 The width of the large lobes on the negative electrode 12 may be greater than the width of the large lobes on the negative electrode 12.

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 1A、 图 1A - 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 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 1A. The R in the connection of Figure 1A-1 not only has higher mechanical strength, but also helps to prevent the concentration of heat and cause the pole tabs or even the pole pieces to melt.

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 monopole ears, and the negative electrode 12 usually uses large-leaf monopole ears; 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抑或经 过焊接的极耳, 均为扬头式, 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 method of the tabs is whether the directly cut tabs 10/1 1 or the welded tabs are raised heads. It can be seen that the tabs are significantly higher than the active material coated on the tabs. The advantage is that it is convenient Scraping powder.

除扬头式极耳外, 如图 ID、 图 1D - 1所示的大叶极耳 则为藏头式极耳, 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。 藏头式极耳的形式与扬头式 极耳的形式恰巧相反。  In addition to the raised-ear type tabs, the large-leaf tabs shown in Figure ID and Figure 1D-1 are hidden-head style tabs. This hidden-head-style large tabs 17/1 8 can make fuller use of lithium. Space inside the ion battery. The form of the hidden head is exactly the opposite of that of the raised head.

扬头式、 藏头式大叶极耳可以在矩形的正负极片 的长边 上, 也可以在正负极片的短边上, 从合理性考虑, 大叶极耳应 尽量在正负极片的长边上。  The raised and hidden large leaf tabs can be on the long sides of the rectangular positive and negative tabs, or on the short sides of the positive and negative tabs. From the perspective of rationality, the large leaf tabs should be as positive and negative as possible. The long side of the pole piece.

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 1B、 图 1B - 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 order to prevent the high temperature fuse of the lithium ion power battery from melting and thinning the tabs, the tabs can be fabricated by welding as shown in Figures 1B and 1B-1 (15/16). The 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 welded large leaf poles to make large leaf poles. Welds 1 4 must be firm. Welding The advantage of the tab is that the cut pole piece has less burrs. 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 状为连接处带有 R圆角的梯形。  The shape of the large leaf tabs can be designed and processed into square, rectangular, semi-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.

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 isolate the positive and negative electrodes, prevent the battery from short circuit, 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 high electrical conductivity. Therefore, porous polyolefin materials are the most suitable. 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 1 5 ~ 8 0 μ πι 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 1 The lithium ion power battery involved in the present invention mainly uses a polyethylene separator having a microporous structure and a low current cut-off temperature of 15 to 80 μm. 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 1

0 0 0 mm 5 0 0 mm 而又大于或等于 1 0 O mm x 5 O mm、 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 2 0 μ ηι ~ 4 0 μ πι; 充放电要求 3 C或更大时, 排除其他影 响因素, 隔膜的最佳厚度为 4 0 μ m 或以上。 当电池内部温度 高于限定值时 (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。 0 0 0 mm 5 0 0 mm and greater than or equal to 10 O mm x 5 O mm, charge and discharge requirements of 1 C ~ 2 C, excluding other factors, the optimal thickness of the separator is 20 μ ηι ~ 4 0 μ π; When charge and discharge require 3 C or more, excluding other influencing factors, the optimal thickness of the separator is 40 μ m or more. When the internal temperature of the battery is higher than the limit value (whether caused by a short circuit or not), a separator with this feature automatically closes the pores and blocks the passage of lithium ions, and the battery no longer reacts. The separator used in lithium-ion power batteries 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 (也可用沉浸法, 将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。  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 after rolling (the immersion method can also be used to immerse the positive electrode sheet in In the above slurry), the positive electrode sheet is put into a specific solvent to extract a pore-forming agent to form a satisfactory separator integrated with the positive electrode sheet.

隔膜的形状通常与正负极片的形状一致。 因为所有的正极 The shape of the separator is generally consistent with the shape of the positive and negative electrode sheets. Because all positive

1 3 的面积均较负极 1 2 的面积略小, 故以隔膜夹裹正极 1 3 。 隔膜通常制成袋状 1 9或书页状 1 9 - 1 , 以便将正极 1 3装入或夹住。 袋状隔膜可以热封三条边, 也可只热封相邻的 两条边; 只热封相邻两条边的隔膜更易于装配。 The area of 1 3 is slightly smaller than that of the negative electrode 12, so the positive electrode 1 3 is wrapped with a separator. The separator is usually made into a bag shape 19 or a book shape 19-1 in order to fit or clamp the positive electrode 13. The bag-shaped diaphragm can heat-seal three sides, or only the adjacent two sides; a diaphragm that only heat-seals adjacent two sides is easier to assemble.

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 / 1 9 - 1 必须将正极片 1 3 四周完全包住, 不可露出边 缘, 以防短路。 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 area of the separator is larger than the positive and negative electrodes in both length and width. Except for the ears, the separator 19/1 9-1 must completely surround the positive electrode 1 13 and not expose the edges to prevent short circuit. The material of the lithium ion power battery pole is a metal material with excellent electrical conductivity 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。 、 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。  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. 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 can be installed, for example, two positive poles and two negative poles can be installed at the same time. When several poles need to be installed, the number of positive and negative poles can 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 equal to or greater than the number of positive poles The number of positive poles; in the case of high power discharge without fast high power charging, the number of positive poles can 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 0.95 ~ 1.05: 0.95 - 1.05: 0.95 - 1.05; 或  (1), LIPF 6 (lithium hexafluorophosphate) / EC (ethylene carbonate): DMC (dimethyl carbonate): DEC (diethyl carbonate), the solvent ratio is 0.95 ~ 1.05: 0.95-1.05: 0.95-1.05; 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 0.95 ~ 1.05: 0.95 ~ 1.05: 0.95 ~ 1.05; 或  (2), L I P F 6 / E C: E M C (ethyl methyl carbonate): D E C), the solvent ratio is 0.95 ~ 1.05: 0.95 ~ 1.05: 0.95 ~ 1.05; or

( 3 ) 、 L I P F 6 / E C : D M C : E M C, 溶剂比例为 0.95 - 1.05: 0.95 - 1.05: 0.95 - 1.05; 或 ( 4 ) 、 L I P F 6 / E C : D M C : E M C : D E C , 溶 剂 比例为 0· 95 ~ 1· 05: 0.95 ~ 1.05: 0.95 ~ 1· 05: 0.95 - 1.05。 (3), LIPF 6 / EC: DMC: EMC, and the solvent ratio is 0.95-1.05: 0.95-1.05: 0.95-1.05; or (4). LIPF 6 / EC: DMC: EMC: DEC. The solvent ratio is 0.95 to 1.05: 0.95 to 1.05: 0.95 to 1.05: 0.95-1.05.

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 ^ 中的一极, 在此情况下, 电芯壳也称为电极壳。 除非设计上 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。 外壳必须与极柱绝缘。 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 poles. In this case, the cell case is also referred to as an electrode case. Unless necessary by design, the cell case of high-power lithium-ion power batteries should be avoided as much as possible. The enclosure must be insulated from the pole. However, in special cases, the case can also become an electrode case.

锂离子动力电池的方形外壳 9 由若干个平面組成。  The square case 9 of a lithium-ion power battery consists of several flat surfaces.

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 (热桥) 9 - 1 。  In order to dissipate heat as quickly as possible, heat sinks (thermal bridges) 9-1 can be designed and processed on or inside the housing.

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„ 涉及本发明的安全阀有两种, 其一以弹簧 (压簧式) 作复 位机构如图 5-1、 5-2、 5- 3、 5 -4、 5 -5 ; 另一以反弓弹片 (压 片式) 作复位机构如图 6-1、 6 -2、 6 - 3、 6-4、 6-5、 6- 6。 分 述如下: 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 overcharging and short-circuiting. 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 of the lithium-ion power battery. 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 other is an anti-bow spring. (Tablet type) The reset mechanism is shown in Figure 6-1, 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或其他耐腐蚀的胶圈垫, 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 Figure 5 -1, 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 compression spring, a cage of 'sealed steel ball 2 2', and the compression spring can be longitudinal in the inner hole of the adjustment bolt. It can move up and down without being able to swing laterally. The sealing steel ball can also be moved up and down in the inner hole of the adjustment bolt without being able to swing horizontally. The outer diameter of the adjustment bolt is machined with a thread that matches 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 keyhole 27. The keyhole also serves as an exhaust. When the rotary 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. The adjusting bolt can be rotated through the exhaust groove to rotate it, 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 aprons. It is pressed or attached to the liquid injection hole 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 on the bottom of the safety valve is in communication with the injection hole on the cover plate 1, so the pressure relief hole is the injection hole when the liquid is injected.

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 底部内圈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圈 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, 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 with its bottom inner ring just snaps on the upper part of the sealing steel ball, and the lower part of the sealing steel ball is trapped on the fluoro rubber ring 26 or other corrosion-resistant rubber pad on the battery cover, which restrains the sealing 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。 半月形 (反弓弹片 可以根据需要加工为平板形) 反弓弹片 3 0装于调节螺栓 2 3 的下部, 调节螺栓加工有与安全阀本体 2 1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 3 1 , 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 2 2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 3 3 , 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 氟橡胶圈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。 The structure of the tablet safety valve is shown in Figures 6-1 and 6-2. Half-moon-shaped (reverse bow spring can be processed into a flat shape as required) The reverse bow spring 30 is installed on the lower part of the adjustment bolt 23, and 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 The bottom is pressed tightly on the anti-bow shrapnel. Turn the height adjustment bolt of the keyhole 8 to adjust the tension of the anti-bow spring. The safety valve body is processed with a rectangular exhaust groove 3 1. The anti-bend spring is installed in the rectangular groove and can not be rotated horizontally except that 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 balls 22 can be vertically moved down in the cage. The anti-bow shrapnel is processed with a process assembling hole 3 3, which is crimped on the upper part of the steel ball to fix and seal the steel ball. The lower hole of the sealed steel ball is trapped on the fluorine rubber ring or other corrosion-resistant rubber pad on the cover injection port, which not only fixes the sealed steel ball, but also seals the battery.

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 他耐腐蚀的股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, 气体瞬间会从卸压孔 2 9排出, 沿排气槽 3 1从排气孔 3 2 以及钥匙孔 2 7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。  In addition, fluoro rubber 圏 or other corrosion-resistant rubber pads must have a certain elasticity, so that when the steel ball is pressed against the fluoro rubber 圏 or other corrosion-resistant rubber pads, the fluoro rubber 圏 or other corrosion-resistant stock pads will 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 the pressure, and the gas will be immediately discharged from the pressure release hole 2 9 and escape along the exhaust groove 31 from the exhaust hole 3 2 and the key hole 2 7. 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.

反弓弹片可以设计、 加工成平板形反弓弹片。 平板形反弓 弹片的工作原理一如半月形反弓弹片。  The anti-bow shrapnel can be designed and processed into a flat-shaped anti-bow shrapnel. The flat-shaped anti-bow shrapnel works like a 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 as 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, 亦与安全阀底部的卸压孔相通, 故不另行标出。  The pressure relief hole 2 9 on the fluorine rubber 圏 2 6 is the communication hole with the liquid injection hole on the cover plate 1 and also communicates with the pressure relief hole on the bottom of the safety valve, so it is not marked separately.

氟橡胶圏 26可以其他任何合适的胶圈代替。  The fluoro rubber 圏 26 may be replaced by any other suitable apron.

反弓弹片可以设计、 加工成平板形或如图 6 - 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-shaped anti-bow shrapnel is the same as that of the half-moon anti-bow shrapnel.

无论压簧式安全阀抑或压片式安全阀, 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 、 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 plate-type safety valve, the sealed steel ball 2 2 can be designed and processed into a ball 2 2-1 with a horizontal transverse groove, and fluoro rubber 2 6- One is clamped in the horizontal groove on the sealed steel ball 2 2-1. 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 fluoro rubber 圏, 6-1 tightly seals the injection hole. When the internal pressure is greater than the permissible value and the sealing steel ball 2> 2-1 is jacked up, the fluorine rubber 圏 2 6-1 is lifted upward at the same time, and the internal pressure is quickly removed.

密封钢球 2 2也可设计、 加工为密封雒台 2 2 - 2 。 与钢 球 2 2或 2 2 一 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 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, 氟橡胶圈 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 head 2 2-2. Compared with the steel ball 2 2 or 2 2 1 1, the lower part of the sealing frustum protrudes into the injection hole, so the reset is more reliable. The sealing frustum can also be processed with a fixed small handle 3 6, and a compression spring or a reverse 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. The pressure of the fluoro rubber 圏 2 6 deforms in the sealing frustum and tightly seals the injection hole. When the internal pressure is greater than the allowable value, the top sealing cone 2 2-2 is quickly released. The sealing frustum can also be designed and processed into 2 2-3 with a horizontal horizontal groove on it, 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 fluoro rubber ring 2 6-1 seals the injection hole. When the internal pressure is greater than the allowable value and 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 removed.

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千个安全阀。  For safety, a large-capacity lithium-ion power battery can be installed with thousands of safety valves on the same side surface or on different side surfaces.

配比及其配制方法  Mixing ratio and 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。 浆料的配制。 配制浆料的介质有以 NM P ( N -曱基 - 2 -吡咯烷酮) 为介质或以水为介质; 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: In the production process of lithium-ion batteries, the preparation (batch) process and coating process are extremely critical and have the greatest impact on the electrical performance of lithium-ion power batteries. Preparation of slurry. The medium for preparing the slurry includes NMP (N-fluorenyl-2-pyrrolidone) as the medium or water as the medium; the preparation methods include the wet method and the 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 %。 NM P的用量受前述物质特别是受钴酸锂粒径大小、 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 NM P is limited by the aforementioned substances, especially by the particle size and particle size distribution of lithium cobaltate, so it is about 30% ~ 100% of the total amount of all the aforementioned substances, that is, the solid-liquid ratio = 1 (the solid content of the active substance ) : 0. 3 ~ 1 (NM P); Under normal circumstances, the best solid-liquid ratio = 1: 0.3 5 to 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 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 N M P搅拌约 3 ~ 4 小时, 加入导电剂石墨 (或乙炔黑 ) 、 碳黑、 鈷酸锂搅拌约 2. 5 ~ 4 小时成粘稠的浆状。  Mixed formulation method. Add P V D F to N M 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 (羧曱基纤维素 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: C M C (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% ~ 1%, carbon black 1.5% ~ 3% , Lithium cobaltate 93% ~ 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. After adding CMC to water and stirring for about 3 to 4 hours, add SBR to it and stir for about 0.5 to 1 hour, then add conductive agent graphite (or acetylene black), carbon black and stir for about 0.5 to 1 hour, and finally add cobalt Lithium acid Mix for about 2.5 to 4 hours to form a thicker paste. 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, 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, 最后筛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, add conductive agent graphite (or acetylene black), carbon black, lithium cobaltate and stir for about 2.5 ~ 4 hours It becomes a thick viscous slurry, and finally it is sieved to remove agglomerates 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 %、 NM 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 N M P as the medium. Materials required: Graphite 93% ~ 95%, PVDF 5% ~ 7%, NM P is about 80% ~ 150% of the total amount of all the aforementioned substances, that is, the solid-liquid ratio = 1: 0.8 to 1 5; The best solid-liquid ratio = 1: 1 ~ 1.3. P V D F should be baked in an oven at a temperature of about 120 ° C for 2 to 3 hours, while graphite needs to be baked at a temperature of 300 ° C to 500 ° C for 4 to 8 hours.

循序配制法。 将 P V D F加入 N M 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 N M P and stir for about 3 to 4 hours, then add the graphite that has been sifted through a 3 2 5 mesh sieve and shake it 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、 蒸镏水、 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 !: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) approximately all of the foregoing 80%-60% of the total amount of material is the solid-liquid ratio-1: 0.8 ~ 1.6; under normal circumstances, the best solid-liquid ratio = 1: 1 ~ 1.3. C M C needs to be baked at 120 ° C for 2 ~ 3 hours, and graphite needs to be baked at 300 ° C ~ 50 0! : Baking for 4 to 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 the graphite after baking and sieving through 300 mesh to stir for about 3 to 4 hours. 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: P V D F 2.5% to 3.5%, lithium cobaltate 93% to 95%, conductive agent graphite 1.5% to 2 ° /. (Or acetylene black 0.8% ~ 1.

2 % ) 、 碳黑 2 % ~ 3 %。 NM 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, 故约为所有前述物质总量的2%), carbon black 2% ~ 3%. The amount of NM P is restricted by the particle size and particle size distribution of the foregoing substances, especially lithium cobaltate, so it is about the total amount of all the foregoing substances.

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。 3 0% ~ 1 0 0% means solid-liquid ratio = 1 (solid content): 0.3-1 (NM P), under normal circumstances, the optimal solid-liquid ratio = 1: 0.3 5 to 0.7. PVDF, graphite (or acetylene black), and carbon black 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 NM 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 NM P for about 2 hours. After it is completely dissolved (slurry), it will be mixed. The mixed powder after being stirred by the feeder is put into the clear slurry of the stirred PVDF and NM P and continued to be stirred for about 3 hours to form a thick slurry.

以水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 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。  Dry preparation of positive electrode with water as medium. Materials required: CMC 0.6% to 0.9%, SBR actual solid content 2% to 4%, conductive agent graphite 1% to 2% or acetylene black 0.5% to 1%, carbon black 1.5% ~ 3%, lithium cobaltate 93-95%. 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 to 1.3; Under normal circumstances, the optimal solid-liquid ratio is 1: 0.6 to 1. S B R can be replaced by P T F E (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质。  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 the machine is stirred is put into the clear slurry of the stirred CMC and water, and the stirring is continued for about 3 hours to form a thick slurry. Finally, the agglomerates and other impurities 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廣, 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, 必须根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。 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 order to ensure the wide range 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 conductivity of the positive electrode material. The dosage of the agent is calculated carefully, and the medium is added once and cannot be added halfway. As for the negative electrode, the same is true, whether water (deionized water, distilled water, purified water) or NMP is used as the medium, the anode material and The amount of additives is carefully 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. In addition to the lithium cobaltate, 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 the foregoing method using lithium cobaltate.

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 πι 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 μ π) 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。  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.

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 %。  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. Up to 10% ~ 30%.

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 °C ~ 5 0 0 °C ) , 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 ° C ~ 500 ° C), the rest are dried. The baking 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 lithium-ion power battery is as follows: ingredients-→ coating-→ production-→ rolling-→ winding and assembly into the inner body (including casing, sealing)-→ injection-→ chemical formation-→ volume .

下面分别描述各个过程。  Each process is described below.

配料过程已经在上面佯细描述, 在此就不再赘述。  The ingredients 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 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 application of the positive electrode and the application 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, and baked into the oven. After baking, it will become a semi-finished current collecting piece. 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, ± 1 0 ° C, the temperature in the high temperature section is 1 2 0 ° C ~ 1 40 ° 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 a medium can be higher than that of NMP as a 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, 即形成龟裂细纹。 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 area 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. Most of the current coating processes are single-sided coating, and then the other side is coated; however, double-sided coating can also be applied at the same time. 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. During assembly, pole pieces of the same polarity (negative electrode and negative electrode, positive electrode and positive electrode) 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 ~ 5 000mm 的范围内调整。 最佳的线 速度为每分钟 1200mm ~ 35 00mm。  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 ~ 5000mm per minute. The best linear speed is 1200mm ~ 35 00mm 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 悍接极耳工序。 裁切极片可以剪板机、 分切机或其他设备完 成  Production. Making (soldering) the tabs, if you cut the tabs directly, there is no process of making the tabs. Cutting pole pieces can be completed by shears, slitters 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 the lithium ion power battery. If the line pressure is too small, it will affect the active material. To metal foil Adhesion, affect electrical performance. The more moderate line pressure of the positive electrode is about 100 ~ 180kg / CM, and the negative electrode is about 80 ~ 160kg / CM.

通常情况下, 正极在滚压前的厚度约为 170 μ ηι~ 270 μ m, 滚压后的厚度约为 110μ ιη~ 165 μ ιη; 负极滚压前的厚度约 为 185 μ m ~ 275 μ m, 滚压后 110μ ιη~ 165 μ ηι。 正极滚压前的 最佳厚度为 195 μ πι~ 235 μ ηι, 滚压后的最佳厚度为 135 μ ιη~ 155 μ m; 负极滚压前的最佳厚度为 220 μ ιη~ 250 μ ιη, 滚压后 的最佳厚度为 135 μ πι~ 155 μ ιη。  Generally, the thickness of the positive electrode before rolling is about 170 μ η to 270 μ m, and the thickness of the positive electrode after rolling is about 110 μ ιη to 165 μ ιη; the thickness of the negative electrode before rolling is about 185 μ m to 275 μ m , 110 μ ιη ~ 165 μ ηι after rolling. The optimal thickness of the positive electrode before rolling is 195 μ π ~ 235 μ ηι, and the optimal thickness of the positive electrode after rolling is 135 μ ιη ~ 155 μ m; the optimal thickness of the negative electrode before rolling is 220 μ ιη ~ 250 μ ιη, The optimal thickness after rolling is 135 μ π ~ 155 μ ιη.

电池的组装。 装配时, 应首先将正极片放入袋状隔膜 1 9 或书页状隔膜 1 9 - 1 的夹片中, 之后须将正极极耳整齐排列 并联于内本体 7 的一端, 并用集电夹板夹住, 负极极耳整齐排 列并联于内本体的另一端, 亦用集电夹板夹住。 正极片 1 3 与 负极片 1 2须间隔层叠置放即叠放一张负极片再叠放一张正极 片, 然后再叠放一张负极片, 依次类推。  Battery assembly. When assembling, first put the positive electrode sheet into the clip of the bag-shaped separator 19 or the book-shaped separator 19-1, and then arrange the positive electrode tabs in parallel to one end of the inner body 7 and clamp it with a current collector plywood The negative electrode tabs are arranged neatly in parallel to the other end of the inner body, and are also clamped with a current collecting plywood. The positive electrode sheet 1 3 and the negative electrode sheet 12 must be stacked and spaced apart, that is, a negative electrode sheet is stacked, then a positive electrode sheet is stacked, then a negative electrode sheet is stacked, and so on.

除非设计必须, 基于经济性考虑, 内本体最外层两侧通常 均为负极片。 换言之, 在特殊需要的情况下, 内本体最外层两 侧也可以是正极片。 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。 装配好的内本体须以隔膜紧密包裹 或以聚乙烯、 聚丙烯框夹紧。  Unless necessary for design, based on economic considerations, both sides of the outermost layer of the inner body are usually negative plates. In other words, in the case of special needs, both sides of the outermost layer of the inner body may also be positive electrode sheets. The positive pole 4 is connected to the positive piece 1 3, and the negative pole 2 is connected to the negative piece 1 2. The assembled inner body must be tightly wrapped with a diaphragm or clamped with a polyethylene or polypropylene frame.

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 m (正极与负极的最大间隙 - 隔膜厚度 + 2 5 μ m) 。  The inner body of the assembled state is excluded. The thickness of the separator 19 is excluded. 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).

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 0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 20, and clamps the tabs respectively and fastens them 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 in 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。 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。  Into. 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 never 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, and 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.

Claims

体另片箔乙 2 Body sheet foil 2 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 ( 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 ) 系由一对或多对正负 极片组即正极 ( 1 3 ) 、 负极 ( 1 2 ) 与隔膜 ( 1 9、 1 9 - 1 ) 共同构成具有多重积层结构、 正负极片顺序间隔置放整齐 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 ( 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 ( 1 3 ) 与负极片 ( 1 ) 须间隔层叠置放; 内本体 ( 7 ) 最外层两侧既可以为负极 , 也可以是正极片; 内本体 ( 7 ) 须以隔膜紧密包裹或以聚 烯、 聚丙烯框夹紧; 正极极耳 ( 1 1 ) 整齐排列并联于内本 ( 7 ) 的一端, 负极极耳 ( 1 0 ) 整齐排列并联于内本体的 一端; 正极 ( 1 3 ) 或负极 ( 1 2 ) 可另行选用 网状金属 ; 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 ( 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。  1. A lithium-ion power battery that can be repeatedly charged and discharged. Each single battery consists of a cover plate (1), a negative pole (2), a safety valve (3), a positive pole (4), and an electrolyte (8). ) And casing (9), the positive pole (4) is connected to the positive pole (1 3), the negative pole (2) is connected to the negative pole (1 2); the positive pole (1 3) is selected from a certain thickness of aluminum foil, The positive electrode active material is evenly coated on both sides. The negative electrode (1 2) is made of copper foil of a certain thickness, and the negative electrode active material is evenly coated on both sides. It is characterized in that the inner body (7) is composed of one or more pairs of positive and negative electrode sheets. The positive electrode (1 3), the negative electrode (1 2), and the separator (19, 19-1) together form an electrode assembly having a multi-layered structure, and the positive and negative electrode sheets are arranged in a regular order; The forms are rectangular pieces with large leaf monopoles or large leaf multipoles, and the current is led to the poles through the current collector splint (6); the positive pole has one or several pole poles, and the negative pole has one or several pole poles. The number of positive and negative poles can be Equal or different, the diameter of the poles can be equal or different; in addition to the shape of the poles, the poles can also be sheet-shaped and mounted on the same or different surfaces of the housing (9); The shape of the negative electrode sheet can be made into other shapes besides the rectangular shape. The positive electrode sheet (1 3) and the negative electrode sheet (1) must be stacked and spaced apart. The inner body (7) can be either a negative electrode or both sides of the outermost layer. It can be a positive electrode sheet; the inner body (7) must be tightly wrapped with a diaphragm or clamped with a polyolefine or polypropylene frame; the positive electrode tabs (1 1) are neatly arranged in parallel with one end of the internal electrode (7), and the negative electrode tabs (1) 0) neatly arranged in parallel to one end of the inner body; the positive electrode (1 3) or negative electrode (1 2) can be separately selected as a mesh metal; the active material of the positive electrode (1 3) can be either lithium cobaltate or lithium manganate , Lithium nickelate or lithium nickel cobaltate; the active material of the negative electrode (1 2) can be either natural graphite, flake graphite, artificial graphite or petroleum coke. 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. 0 2 g~ 0. 0 6 g, 最好为 0. 0 3 2 g~ 0. 0 4 2 g; 负极 ( 1 2 ) 活性物质的密度每平方厘米约为 0. 0 1 g~ 0. 0 3 g, 最好为 0. 0 1 4 g~ 0. 0 2 1 g。  2. The rechargeable lithium-ion power battery according to claim 1, characterized in that: the density of the positive electrode (1 3) active material per square centimeter is 0. 0 2 g to 0. 0 6 g, preferably 0 0 3 2 g ~ 0. 0 4 2 g; the density of the negative electrode (1 2) active material per square centimeter is about 0. 0 1 g ~ 0. 0 3 g, preferably 0. 0 1 4 g ~ 0. 0 2 1 g. 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: 正负极片上的大叶极耳如果从同一方向或同 一侧端引 出, 大叶单极耳的最大宽度不得大于大叶极耳所在的 那条边的边长的一半; 正负极片上的大叶极耳如果从同一方向 或同一侧端引出, 大叶单极耳的中心线位置应位于叠层式极片 的边长上约 1 / 4处或 3 / 4处; 正负极的大叶极耳也可以各 自从极片的不同方向的侧端引 出, 从极片不同方向的侧端引 出 的大叶极耳, 其最大宽度可以与大叶极耳所在的那奈边等长。 3. The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: if the large leaf tabs on the positive and negative electrodes are led from the same direction or the same side, the maximum width of the large leaf monopole ears Must not be larger than where the large leaf poles are located The side of that side is half the length; if the large leaf tabs on the positive and negative electrodes are led from the same direction or the same side, the center line position of the large leaf monopoles should be about 1 on the side length of the laminated pole sheet / 4 or 3/4; The large leaf tabs of the positive and negative poles can also be drawn from the side ends of the pole pieces in different directions, and the large leaf tabs drawn from the side ends of the pole pieces in different directions can have a maximum width of It is as long as the side of the large leaf that the pole ears are located on. 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。  4. 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: 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; 大叶极耳除可以直接裁切外, 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 耳既可以为扬头式, 也可以为藏头式; 大叶极耳既可以在正负 极片的长边上, 也可以在正负极片的短边上。  The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: the shape of the large leaf tabs can be square, rectangular, semi-circular, trapezoidal, or other shapes that are favorable for conducting and dissipating heat. The best shape is a trapezoid with an R angle. The connection between the root of the pole ear and the pole piece can be either a clear angle connection or a smooth arc connection. In addition to the large leaf pole ear, it can be cut directly and can be made separately. After the pole piece is rolled and welded to the pole piece, it is best to use the large leaf pole piece; the big leaf pole piece can be either a raised head type or a hidden head type; the big leaf pole piece can be used on the positive and negative pole pieces. On the long side, it can also be on the short side of the positive and negative plates. 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: 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 ply has a plurality of wire grooves which can be compressed and can be opened; the split current collecting ply is 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 . 7.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袋状 ( 1 9 ) 或书页状 ( 1 9 - 1 ) ; 袋状隔膜 ( 1 9 ) 可以从三面热 封, 也可只热封相邻的两边; 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 πι~ 4 Ομ πι; 充放电要求 3 C或更大时, 隔膜的最佳厚 度为 4 Ομ ηι或以上。 The lithium ion power battery capable of being repeatedly charged and discharged according to claim 1, characterized in that: the separator is made of polyethylene or polyimide having a microporous structure and a low current cut-off temperature of 15 μm to 80 μm. Acrylic material is made into bag shape (1 9) or book page shape (1 9-1); bag-shaped diaphragm (1 9) can be heat-sealed from three sides, or only two adjacent sides can be heat-sealed; area of diaphragm (1 9) Both the length and the width are larger than the positive and negative electrodes. Except for the ears, the separator (19) must completely shield the positive electrode (1 3) or negative electrode (1 2) from the periphery, and the edges must not be exposed to prevent short circuit. When the discharge requirement is 1 C to 2 C, the optimal thickness of the separator (19) is 2 Ομπι to 4 Ομπι; when the charge and discharge requirements are 3 C or more, the optimal thickness of the separator is 4 Ομηι or more. 8.—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: 其中的压簧 ( 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 ( 2 5 ) 可在调节螺栓的内孔中纵向上下滑移, 密封 钢球 ( 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 ) 相配的螺纹; 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 ( 2 8 ) ; 压簧 ( 2 5 ) 压在钢球的上部, 密封钢球 ( 28. A safety valve for a lithium ion power battery that can be repeatedly charged and discharged, characterized in that: the compression spring (2 5) is installed in the inner hole of the adjustment bolt (2 3), and the inner hole of the adjustment bolt is used for In order to maintain the stability of the compression spring and the sealing steel ball (2 2), the compression spring (2 5) can slide down vertically in the inner hole of the adjustment bolt, and the sealing steel ball (2 2) can longitudinally move in the inner hole of the adjustment bolt Up and down, the outer diameter of the adjustment bolt is processed with threads that match the safety valve body (2 1); the adjustment bolt is processed with a number of vertical exhaust grooves (2 4). Air holes (2 8); compression springs (2 5) are pressed on the upper part of the steel ball, sealing 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; 压簧The lower hole of 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 is in communication with the injection hole on the cover plate (1); ( 25 ) 也可以反弓弹片 ( 3 0 ) 代替, 反弓弹片 ( 3 0 ) 装于 调节螺栓 ( 2 3 ) 的下部, 调节螺栓加工有与安全阀本体 ( 2(25) The reverse bow spring (30) can also be replaced. The reverse bow spring (30) is installed on the lower part of the adjustment bolt (23), and the adjustment bolt is processed with the safety valve body (2 1 ) 相配的螺紋, 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^ "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; 安全阀本体 ( 2 1 ) 上可以另行加工有排气小孔 ( 31) The matching thread is adjusted by turning the keyhole (2 7) to adjust the tension of the reverse bow spring; a rectangular exhaust groove (3 1) is processed in the safety valve body, and the reverse bow spring (30) can be in the exhaust groove The inner ball springs up and down and cannot be rotated horizontally; the sealed steel ball (2 2) can be moved vertically down in the holder of the safety valve body, and the anti-bow spring (30) is processed with a process assembly hole (3 3), which is buckled in On the upper part of the steel ball, the lower hole of the dense steel ball (2 2) is trapped on the fluoro rubber 圏 (2 6) on the injection port of the cover plate; on the pressure relief hole on the bottom of the safety valve and on the cover plate (1) The injection hole is connected; the safety valve body (2 1) can be separately processed with a vent hole (3 5 ) ; 密封钢球则可以加工为带有水平横槽的球体 ( 2 2 -5); sealed steel balls can be processed into spheres with horizontal grooves (2 2- 1 ) , 氟橡胶圏 ( 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 -1), Viton (2 6-1) is hooped 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 cone (2 2- 2 ) ; 密封锥台 ( 2 2 - 3 ) 可以加工一水平横槽, 氟橡胶圏 ( 2 6 - 2 ) 则箍紧在密封锥台 ( 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); The sealing frustum (2 2-3) can process a horizontal horizontal groove, and the fluoro rubber 圏 (2 6-2) is hooped in the horizontal lateral groove on the sealing frustum (2 2-3); safety valve It can be installed on any surface of the casing (9); 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 It can be installed on the same surface of the housing (9) or on different surfaces. 9.一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:  A method for manufacturing a lithium-ion power battery capable of being repeatedly charged and discharged, comprising the following steps: ( 1 ) 配料, 包括以下各种方法: 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; (1) Ingredients, including the following methods: 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% to 3.5%, lithium cobaltate 93% to 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 0.5; 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 slurry; 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、 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 = 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 a medium is prepared by a sequential preparation method, and 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%, lithium cobaltate 93% ~ 95%; water (deionized water, distilled water, pure The amount of water) is 40% ~ 130% of the total amount of all the aforementioned substances, that is, the solid-liquid ratio-1: 0. 4 ~ 1.3; usually, the best solid-liquid ratio = 1: 0.6 ~ 1; SBR can be replaced by PTFE; CMC is added to 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, 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 N M 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 % , NM 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 °C烘箱内烘烤 2 ~ 3 小时; 将鈷酸锂、 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 NM 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 - 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-3. Dry preparation of positive electrode slurry with NMP 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 NM P is restricted 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 best solid-liquid ratio-1: 0 · 3 5 ~ 0.7; PVDF, graphite (or acetylene black) ), Carbon black should be baked in an oven at about 120 ° C 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 PVDF and NM P are stirred for about 2 hours. After it is completely dissolved (slurry), put the mixed powder after mixing by the mixer into the stirred slurry of PVDF and NM P and continue to stir for about 3 hours to become thick. Pasty A-4. Dry preparation of the positive electrode slurry with water as the medium, the required materials are: CMC 0.6% ~ 0.9%, SBR actual solid content 2% ~ 4%, conductive agent graphite 1% ~ 2 % Or acetylene black 0.5% ~ 1%, carbon black 1. 5 % ~ 3 % 、 钴酸锂 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 ; 将鈷酸锂、 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 to be completely After dissolving, it becomes a clear slurry. That is, the mixed powder mixed by the mixer is placed in 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 impurities are sieved out; 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 the 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 to 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Bake in an oven at 20 ° C for 2 to 3 hours. Graphite needs to be baked at 300 ° C to 500 ° C for 4 to 8 hours. The anode material is screened by 3 2 5 mesh vibration. It is generally not suitable to use; add PVDF to NM P and stir for about 3 to 4 hours, and then add spare graphite that has been screened through a 3 2 5 mesh screen and stir for about 3 - 小时成粘稠的浆状; 3-hour 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 Ό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 ~ 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 to 1.6; the optimal solid-liquid ratio = 1 to 1 to 1.3; CMC should be baked at 120 ° C for 2 ~ 3 hours, graphite should be baked at 300 ° C ~ 500 ° C for 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, 网上剩余的通常不宜使用; 将 CM 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 remaining ones on the Internet are generally not suitable for use; add CM 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; 5 to 1 hour. Finally, add graphite after baking and sieve through 3 2 5 mesh. Stir for about 3-4 hours to form a thick paste. 正极材料的粒径可以在 2 μ m~ 1 2 μ m 范围内选用, 最 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^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; The particle size of the positive electrode material can be selected in the range of 2 μm to 12 μm, and the optimal particle size should be 5 μm to 8 μm; the particle size distribution of the positive electrode material is too fine or too coarse The sum of the powders usually does not exceed 40%; for fine powders below 2 μm, the solid-liquid ratio should be increased by 20 ° / based on the original solid-liquid ratio. ~ 50%, the solid-liquid ratio of coarser powders larger than 12 μm should be reduced by 10% to 30% based on the original solid-liquid ratio; in the preparation of the positive electrode, the particle size of the conductive material used 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 °C、 高温区段的温度在 1 1 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 ~ 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 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 , 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; (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 it. After baking, it becomes a semi-finished current collector sheet; 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, ± 10 ° C, the temperature in the high-temperature section is 1 1 0 ° C ~ 1 40. 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 10 ° C ~ 15 ° C during coating and baking, using water as a medium The temperature of the slurry can be slightly higher than the temperature of the slurry with NM P as the medium. The temperature of the coating can be adjusted within the range of 8 0 mm to 5 0 0 mm per minute. The best linear speed is 1 200 mm-3 5 0 mm per minute; the density of the active material of the coated positive electrode (1 3) per square centimeter is 0.0 2 8 ~ 0.06 8 , most The best density per square centimeter is 0, 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 ~ 0. 0 3 g , Optimum density per square centimeter is 0. 0 1 4 g to 0. 0 2 1 g; both can be coated on one side, can be coated on both sides at the same time; the active material is coated on one side. The back of the pole pieces are pasted 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; ( 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 )  (3) Production: the positive electrode (1 3) is cut into a rectangular piece with large leaf monopole or large leaf multipole and scrapes off the slurry at the pole (1 1); the negative electrode (1 2) 0 ) 处的浆料; 正负极片最佳的长宽比为 6 . 2 : 3 . 8或 6 : 4 ; 正负极片的形状除矩形外, 也可制成圆形或其他需要的形 状; 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极耳所在 的那条边长的一半 ( 1 / 2 ) , 从极片两端或不同方向引 出的 大叶极耳, 其最大宽度可以与极耳所在的那条边等长; 大叶极 耳的最大高度不大于其自身宽度, 最好小于其宽度; 最小宽度 不应小于其高度; 特殊需要时, 大叶极耳的最小宽度可以小于 其高度; 正负极片上的极耳如果从同一方向引 出, 大叶单极耳 的中心线位置应位于叠层式极片的边长上约 1 / 4处或 3 / 4 处; 大叶单极耳的内缘线应靠近极片的中心线; 大叶极耳既可 以为扬头式, 也可以为藏头式; 扬头式或藏头式大叶极耳既可 以在矩形片的长边上, 也可以在矩形片的短边上; 在条件许可 的情况下, 应尽量采用卧式; 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, 负极亦当釆用大叶多极耳; 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; 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 ) ; 0); the best aspect ratio of the positive and negative electrode sheet is 6.2: 3.8 or 6: 4; the shape of the positive and negative electrode sheet can be made into a circle or other shapes besides rectangular shape. Shape; in addition to cutting, the pole pieces can be directly processed by rolling or shear punching; large leaf ears can also be made separately and welded to the positive and negative poles after being rolled On the pole piece; the maximum width of the large leaf pole ear is smaller than the pole ear The half of the long side (1/2) of the large leaf pole ears drawn from the two ends of the pole piece or in different directions can have a maximum width equal to the side of the pole ear; the maximum height of the large leaf pole ears Not more than its own width, preferably less than its width; The minimum width should not be less than its height; In special needs, the minimum width of the large leaf tabs can be less than its height; If the tabs on the positive and negative electrodes are drawn from the same direction, the The centerline position of the leaf monopole should be about 1/4 or 3/4 on the side length of the laminated pole piece; the inner edge line of the large leaf monopole should be close to the center line of the pole piece; The ears can be either raised or hidden heads. The raised or hidden large leaf pole ears can be on either the long side or the short side of the rectangular plate. Under normal circumstances, the horizontal type should be used as much as possible. Generally, the width of the large leaf tabs on the positive and negative plates is the same width; but under special requirements, the width of the large leaf tabs on the positive and negative plates can also be unequal. In the case of fast high-power charging without high-power discharge, the negative The width of the large leaf tab of the pole can be greater than the width of the large leaf tab of the positive pole. In the case of high power discharge without fast high power charging, the width of the large leaf tab of the positive pole can be larger than that of the negative pole. Wide leaf monopole ears for the positive electrode and large leaf monopole ears for the negative electrode; large leaf multipole ears for the negative electrode; large leaf multipole ears for the negative electrode; when high-speed charging is required, high-power charging is not required. In the case of a large-leaf multipole ear for the negative electrode, and a large-leaf monopole ear for the positive electrode; in the case of high-power discharge without fast high-power charging, the large-leaf multipole ear can be used for the positive electrode, and the negative electrode can be Large-leaf monopole ears can be used; the shape of the large-leaf pole ears can be square, rectangular, semi-circular, trapezoidal, or other shapes that facilitate flow and heat dissipation. The best shape of the ear ears is a trapezoid with R rounded corners. Tabs; 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; the large leaf tab can be processed into a raised head (1 0/1 1), or Hidetou (17/18); ( ) 滚压: 滚压工艺中, 正极的线压力为 1 0 0 ~ 1 8 0 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 οι~ 1 6 5 μ m, 正极滚压前的最佳厚度为 1 9 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 m ~ 1 6 5 μ m, 负极滚压前的最佳厚度 为 2 2 0 μ m ~ 2 5 0 μ m, 滚压后的最佳厚度为 1 3 5 μ m~() Rolling: In the rolling process, the linear pressure of the positive electrode is 100 ~ 180 kg / CM, the linear pressure of the negative electrode is 80 ~ 160 kg / CM; the positive electrode (1 3) before rolling The thickness is about 170 μ m to 2 70 μ m, and the thickness after rolling is about 110 μ μm to 1 6 5 μ m. The optimal thickness before the positive electrode rolling is 195 μ m ~ 2 3 5 μ m, the optimal thickness after rolling is 1 3 5 μ m to 1 5 5 μ m; the thickness of the negative electrode (1 2) before rolling is about 1 8 5 μ m to 2 7 5 μ m, After rolling 1 110 μm ~ 16 5 μm, Optimum thickness before negative electrode rolling 2 2 0 μ m ~ 2 5 0 μ m, the optimal thickness after rolling is 1 3 5 μ m ~ 1 5 5 μ m; 1 5 5 μ m; ( 5 ) 装配: 外壳 ( 9 ) 上通常只装配一个正极柱、 一个负 极柱; 较大容量的锂离子动力电池则可以安装若干个极柱, 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; 也可以调整极柱的直径来 满足上述需要, 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;  (5) Assembly: Usually only one positive pole and one negative pole are assembled on the casing (9); a large-capacity lithium ion power battery can be installed with several pole posts, and 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 equal to the number of positive poles 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 can be equal to or greater than the number of negative poles; the diameter of the poles can also be adjusted To meet the above requirements, the diameter of the positive and negative poles should be equal when fast high-power charging and discharging are required. In the case of fast high-power charging without high-power discharging, the diameter of the negative pole can be the same as that of the positive pole The diameter is equal to or greater than the diameter of the positive pole; when high power discharge is required without fast high power charging , The diameter of the positive pole may be equal to or greater than the diameter of the negative pole and the negative pole diameter; 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袋状 ( 1 9 ) 或书页状 ( 1 9 - 1 ) , 以便将正极 ( 1 3 ) 装入或 夹住, 袋状隔膜 ( 1 9 ) 可以从三面热封, 也可只热封相邻的 两边, 以便将正极片 1 3装入或夹住。 ; 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~ 40 μ m; 充放电要求 3 C或更大时, 隔膜的最佳厚度为 40 μ ιη或以 上; 除极耳外, 隔膜 ( 1 9 ) 必须将正极 ( 1 3 ) 或负极 ( 1 The diaphragm (1 9) is made of a polyethylene or polypropylene material with a microporous structure and a low current cut-off temperature of 15 μ m to 80 μ m. The bag shape (1 9) or book shape (1 9- 1), so that the positive electrode (1 3) can be installed or clamped, and the bag-shaped separator (1 9) can be heat-sealed from three sides, or only the adjacent two sides can be heat-sealed, so as to load or clamp the positive electrode sheet 13 . When the charge and discharge requirements are 1 C to 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 more, the optimal thickness of the separator 40 μ ιη or more; except for the ears, the separator (1 9) must have the positive electrode (1 3) or the negative electrode (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 ) 沉浸在舍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 ( 12) completely shield the surroundings, and do not expose the edges to prevent short circuits; the immersed positive electrode (1 3) can be immersed in a slurry of a polyolefin-based material containing a reasonable amount of pore-forming agent, and then The positive electrode (1 3) is put into a specific solvent to extract a pore-forming agent to form a separator integrated with the positive electrode sheet; a slurry of a polyolefin-based material containing a reasonable amount of a pore-forming agent may also be directly coated after the rolling Positive (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 ) ; 3) on the surface, and then put the positive electrode (1 3) into a specific solvent to extract the pore-forming agent to form a separator (1 9) integrated with the positive electrode sheet; 装配时, 应首先将正极片放入袋状隔膜 ( 1 9 ) 或书页状 隔膜 ( 1 9 - 1 ) 的夹片 中, 正极片 ( 1 3 ) 与负极片 ( 1 2 ) 须间隔层叠置放即叠放一张负极片再叠放一张正极片, 然 后再叠放一张负极片, 依次类推; 之后须将正极极耳整齐排列 并联于内本体 7 的一端, 并用集电夹板夹住, 负极极耳整齐排 列并联于内本体的另一端, 亦用集电夹板夹住; 内本体 ( 7 ) 须以隔膜紧密包裹或以聚乙烯、 聚丙烯框夹紧; 装配好的内本 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; When assembling, the positive electrode sheet should first be put into the clip of a bag-shaped separator (1 9) or a book-shaped separator (1 9-1), and the positive electrode sheet (1 3) and the negative electrode sheet (1 2) It must be stacked at intervals, that is, a negative electrode sheet and a positive electrode sheet, and then a negative electrode sheet, and so on; and then the positive electrode tabs must be arranged in parallel to one end of the inner body 7, It is clamped with a current collector plywood, and the negative electrode tabs are neatly arranged in parallel to the other end of the inner body. It is also clamped with a current collector plywood; the inner body (7) must be tightly wrapped with a diaphragm or clamped with a polyethylene or polypropylene frame; assembly A good inner body (7), excluding the thickness of the separator (1 9), and the gap distance between the positive electrode (1 3) and the negative electrode (1 2) should not be greater than 2 5 μm; ( 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 L I P F 6 / E C : D M C : E M 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 : 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 ;  (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 best 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, with a solvent ratio of 0.9 5 to 1. 0 5: 0.9 5 to 1. 0 5: 0.9 5-1. 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 LIPF 6 / EC: DMC: EMC, the 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: DMC: EMC: DEC with a solvent ratio of 0.9 5-1. 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 小时一 → 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 material on the positive and negative current collector substrates. The formation process must be completed without interruption 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 a → 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 ensure sufficient one time; ( 8 ) 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: Put batteries with electrical performance indicators that meet process requirements and batteries with electrical performance indicators that do not meet process requirements, respectively.
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CN112290169A (en) * 2020-03-31 2021-01-29 蜂巢能源科技有限公司 Lithium ion battery liquid injection device and method
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CN109449322A (en) * 2018-12-21 2019-03-08 河南鼎能电子科技有限公司 A kind of novel lithium battery with super thin metal shell
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