Patent Description:
Secondary batteries are widely used in electric vehicles and consumer electronics because of the advantages of high energy density, high output power, long cycle life, and low environmental pollution. With continuous expansion of the application scope of the secondary batteries, people have imposed increasingly high requirements on the energy density of the secondary batteries. A metal current collector used in the prior art has a relatively large thickness (usually <NUM> to <NUM>) and a relatively high density, resulting in a low energy density of the secondary battery, which cannot meet the increasingly high requirements on the market. Therefore, how to reduce the weight of the current collector to increase the energy density of the secondary battery while ensuring good conductivity and current collection performance for the current collector is a technical issue to be resolved.

<CIT> mentions a current collector, an electrode plate and an electrochemical device.

The current collector includes an insulation layer and at least one conductive layer. The insulation layer is used to support the conductive layer. The at least one conductive layer is used to support an electrode active material layer and is located above at least one surface of the insulation layer. The insulation layer has a density smaller than that of the conductive layer.

On the basis of this, this application is proposed.

<CIT> describes a current collector comprising an insulating layer and a conducting layer. The insulating layer is used to support the conducting layer, the conducting layer is used to support an electrode active material layer, and the conducting layer is located on at least one surface of the insulating layer.

Embodiments of this application provide a negative current collector as specified in any of claims <NUM>-<NUM>, a negative electrode plate as specified in claim <NUM>, an electrochemical apparatus as specified in claim <NUM>, a battery module as specified in claim <NUM>, a battery pack as specified in claim <NUM>, and a device as specified in claims <NUM>-<NUM>, so that the negative current collector has both a small weight and good conductivity and current collection performance, and therefore the electrochemical apparatus has both a higher weight energy density and good electrochemical performance.

A first aspect of the embodiments of this application provides a negative current collector as specified in any of claims <NUM>-<NUM>, where the negative current collector includes a support layer and a metal conductive layer that is disposed on at least one of two opposite surfaces of the support layer in a thickness direction of the support layer. A density of the support layer is less than a density of the metal conductive layer, and the density of the metal conductive layer is <NUM>/cm<NUM> to <NUM>/cm<NUM>. A thickness D<NUM> of the metal conductive layer is <NUM>≤D<NUM>≤<NUM>, preferably <NUM>≤D<NUM>≤<NUM>. When a tensile strain of the negative current collector is <NUM>%, a sheet resistance growth rate T of the metal conductive layer is T≤<NUM>%, preferably T≤<NUM>%, or more preferably T≤<NUM>%.

A second aspect of the embodiments of this application provides a negative electrode plate as specified in claim <NUM>, where the negative electrode plate includes a negative current collector and a negative electrode active material layer disposed on the negative current collector, and the negative current collector is the negative current collector according to the first aspect of the embodiments of this application.

A third aspect of the embodiments of this application provides an electrochemical apparatus as specified in claim <NUM>, where the electrochemical apparatus includes a positive electrode plate, a negative electrode plate, a separator, and an electrolyte, where the negative electrode plate is the negative electrode plate according to the second aspect of the embodiments of this application.

A fourth aspect of this application provides a battery module as specified in claim <NUM>, where the battery module includes the electrochemical apparatus according to the third aspect of this application.

A fifth aspect of this application provides a battery pack, where the battery pack as specified in claim <NUM> includes the battery module according to the fourth aspect of this application.

A sixth aspect of this application provides a device as specified in claims <NUM>-<NUM>, where the device includes the electrochemical apparatus according to the third aspect of this application, and the electrochemical apparatus serves as a power supply of the device.

Preferably, the device includes a mobile device, an electric vehicle, an electric train, a satellite, a ship, and an energy storage system.

According to the negative current collector provided in the embodiments of this application, the metal conductive layer with the smaller thickness is disposed on at least one surface of the support layer, and the density of the support layer is less than the density of the metal conductive layer, greatly reducing the weight of the negative current collector compared to the conventional metal current collector, and therefore significantly improving the weight energy density of the electrochemical apparatus. In addition, when the density of the metal conductive layer is <NUM>/cm<NUM> to <NUM>/cm<NUM> and the tensile strain of the negative current collector is <NUM>%, the sheet resistance growth rate of the metal conductive layer is less than <NUM>%, effectively avoiding a sharp resistance increase caused by tensile deformation for the metal conductive layer with the smaller thickness, ensuring good conductivity and current collection performance for the negative current collector and providing low impedance and small negative-electrode polarization for the electrochemical apparatus. Therefore, the electrochemical apparatus has good electrochemical performance.

The battery module, the battery pack, and the device in this application include the electrochemical apparatus described above, and therefore have at least the same advantages as the electrochemical apparatus.

To describe the technical solutions in the embodiments of this application more clearly, the following briefly introduces the accompanying drawings required for describing the embodiments of this application. Persons of ordinary skill in the art may still derive other drawings from these accompanying drawings without creative efforts.

In order to make the objectives, technical solutions and beneficial technical effects of this application clearer, the following further describes this application in detail with reference to the embodiments. It should be understood that the embodiments described in this specification are merely intended to interpret this application rather than to limit this application.

For simplicity, only some numerical ranges are expressly disclosed in this specification. In addition, although not expressly recorded, each point or individual value between endpoints of a range is included in the range.

In the description of this specification, it should be noted that, unless otherwise stated, "above" and "below" means inclusion of the number itself, and "more" in "one or more" means at least two.

The foregoing invention content of this application is not intended to describe each of the disclosed embodiments or implementations of this application. The following description illustrates exemplary embodiments in more detail by using examples. Throughout this application, guidance is provided by using a series of embodiments and the embodiments may be used in various combinations. In each instance, enumeration is only representative and should not be interpreted as exhaustive.

A first aspect of the embodiments of this application provides a negative current collector <NUM>. Referring to <FIG>, the negative current collector <NUM> includes a support layer <NUM> and a metal conductive layer <NUM> that are laminated. The support layer <NUM> has a first surface 101a and a second surface 101b that are opposite in a thickness direction, and the metal conductive layer <NUM> is disposed on either or both of the first surface 101a and the second surface 101b of the support layer <NUM>.

A density of the support layer <NUM> is less than a density of the metal conductive layer, and the density of the metal conductive layer <NUM> is <NUM>/cm<NUM> to <NUM>/cm<NUM>. A thickness D1 of the metal conductive layer <NUM> is <NUM>≤D<NUM>≤<NUM>, and when a tensile strain of the negative current collector <NUM> is <NUM>%, a sheet resistance growth rate T of the metal conductive layer <NUM> is T≤<NUM>%.

According to the negative current collector <NUM> provided in this embodiment of this application, the metal conductive layer <NUM> with a smaller thickness is disposed on at least one surface of the support layer <NUM>, and the density of the support layer is less than the density of the metal conductive layer, greatly reducing a weight of the negative current collector <NUM> in comparison to a conventional metal current collector (such as a copper foil), and therefore significantly improving a weight energy density of an electrochemical apparatus.

In addition, the negative current collector <NUM> is sometimes stretched during the processing and use of a negative electrode plate and the electrochemical apparatus, for example, during electrode plate rolling or battery expansion. When the density of the metal conductive layer <NUM> is <NUM>/cm<NUM> to <NUM>/cm<NUM>, and the tensile strain of the negative current collector <NUM> is <NUM>%, the sheet resistance growth rate T of the metal conductive layer <NUM> is T≤<NUM>%. In this way, a sharp resistance increase caused by tensile deformation can be avoided effectively for the metal conductive layer <NUM> with the smaller thickness, ensuring good conductivity and current collection performance for the negative current collector <NUM> and providing low impedance and small negative-electrode polarization for the electrochemical apparatus. Therefore, the electrochemical apparatus has good electrochemical performance, that is, having both higher rate performance and higher cyclic performance.

With the negative current collector <NUM> in this embodiment of this application, the electrochemical apparatus has both the higher weight energy density and good electrochemical performance.

In some optional implementations, the thickness D<NUM> of the metal conductive layer <NUM> may be <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>. The thickness D<NUM> of the metal conductive layer <NUM> may be in a range formed by any two of the foregoing values. Preferably, D<NUM> is <NUM>≤D<NUM>≤<NUM>.

The thickness of the metal conductive layer <NUM> is less than <NUM>, preferably less than <NUM>, which is much less than the thickness of the conventional metal current collector (such as a copper foil). In addition, the density of the support layer <NUM> is less than the density of the metal conductive layer <NUM>, significantly improving the weight energy density of the electrochemical apparatus. The thickness of the metal conductive layer <NUM> is more than <NUM>, preferably more than <NUM>, so that the negative current collector <NUM> has good conductivity and current collection performance, and is also not prone to damages during processing and use of the negative current collector <NUM>. Therefore, the negative current collector <NUM> has good mechanical stability and a longer service life.

In some optional implementations, the density of the metal conductive layer <NUM> may be <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, <NUM>/cm<NUM>, or the like.

In some optional implementations, when the tensile strain of the negative current collector <NUM> is <NUM>%, the sheet resistance growth rate T of the metal conductive layer <NUM> may be <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, <NUM>%, or <NUM>; preferably T≤<NUM>%, or more preferably T≤<NUM>%.

According to the negative current collector <NUM> in this embodiment of this application, a thickness D<NUM> of the support layer <NUM> is preferably <NUM>≤D<NUM>≤<NUM>, for example, may be <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>. The thickness D<NUM> of the support layer <NUM> may be in a range formed by any two of the foregoing values. Preferably D<NUM> is <NUM>≤D2≤<NUM>, or more preferably D<NUM> is <NUM>≤D2≤<NUM>.

The thickness D<NUM> of the support layer <NUM> is preferably more than <NUM>, or more preferably more than <NUM>, so that the support layer <NUM> has a sufficient mechanical strength and is not prone to breakage during the processing and use of the negative current collector <NUM>, to well support and protect the metal conductive layer <NUM>, thereby ensuring good mechanical stability and a longer service life for the negative current collector <NUM>. The thickness D<NUM> of the support layer <NUM> is preferably less than <NUM>, more preferably less than <NUM>, or still more preferably less than <NUM>, so that the electrochemical apparatus have a smaller volume and weight, improving the energy density of the electrochemical apparatus.

In some embodiments, preferably, a volume resistivity of the support layer <NUM> is greater than or equal to <NUM>×<NUM>-<NUM> Ω·m. Because of the relatively large volume resistivity of the support layer <NUM>, a short-circuit resistance can be increased when an internal short circuit occurs in the electrochemical apparatus in case of exceptions such as nail penetration in the electrochemical apparatus, thereby improving safety performance of the electrochemical apparatus.

In some embodiments, preferably, an elongation at break of the support layer <NUM> is greater than or equal to an elongation at break of the metal conductive layer <NUM>, better avoiding breakage of the negative current collector <NUM>.

Optionally, the elongation at break of the support layer <NUM> is greater than or equal to <NUM>%. Further, the elongation at break of the support layer <NUM> is greater than or equal to <NUM>%.

In some embodiments, a Young's modulus E of the support layer <NUM> is preferably E≥<NUM>. The support layer <NUM> has appropriate rigidity to satisfy a support and protection role of the support layer <NUM> for the metal conductive layer <NUM>, ensuring an overall strength of the negative current collector <NUM>. During processing of the negative current collector <NUM>, the support layer <NUM> is not excessively extended or deformed to avoid breakage of the support layer <NUM>, improving bonding firmness between the support layer <NUM> and the metal conductive layer <NUM> to prevent peeling off. In this way, the negative current collector <NUM> has higher mechanical stability and higher operating stability, and the electrochemical apparatus has higher electrochemical performance, such as a longer cycle life.

Further, the Young's modulus E of the support layer <NUM> is more preferably <NUM>. 9GPa≤E≤20GPa, so that the support layer <NUM> has enough rigidity and is also able to withstand deformation to some extent, being flexible to wind during processing and use of the negative current collector <NUM> to better prevent breakage.

In some optional implementations, the Young's modulus E of the support layer <NUM> may be <NUM>. 9GPa, <NUM>. 5GPa, 4GPa, 5GPa, 6GPa, 7GPa, 8GPa, 9GPa, 10GPa, 11GPa, 12GPa, 13GPa, 14GPa, 15GPa, 16GPa, 17GPa, 18GPa, 19GPa, or 20GPa. The Young's modulus E of the support layer <NUM> may be in a range formed by any two of the foregoing values.

In some embodiments, preferably, the support layer <NUM> uses one or more of a polymer material and a polymer-based composite material. Because the density of the polymer material and the polymer-based composite material is obviously smaller than the density of metal, the negative current collector <NUM> is obviously lighter than the conventional metal current collector, so that the weight energy density of the electrochemical apparatus is increased.

The polymer material is, for example, one or more of polyamide (PA), polyimide (PI), polyesters, polyolefins, polyynes, silicone polymers, polyethers, polyols, polysulfones, polysaccharide polymers, amino acid polymers, polysulfur nitride, aromatic polymers, aromatic heterocyclic polymers, epoxy resin, phenol-formaldehyde resin, a derivative thereof, a crosslinked product thereof, and a copolymer thereof.

Further, the polymer material is, for example, one or more of polycaprolactam (commonly referred to as nylon <NUM>), polyhexamethylene adipamide (commonly referred to as nylon <NUM>), polyterephthalamide (PPTA), polym-phenylene isophthalamide (PMIA), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polyethylene naphthalate (PEN), polycarbonate (PC), polyethylene (PE), polypropylene (PP), poly(p-phenylene ether) (PPE), polyvinyl alcohol (PVA), polystyrene (PS), polyvinyl chloride (PVC), polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTEE), polystyrene sulfonate (PSS), polyacetylene, polypyrrole (PPy), polyaniline (PAN), polythiophene (PT), polypyridine (PPY), silicone rubber (Silicone rubber), polyoxymethylene (POM), polyphenyl, polyphenylene oxide (PPO), polyphenylene sulfide (PPS), polyethylene glycol (PEG), acrylonitrile-butadiene-styrene copolymer (ABS), cellulose, starch, protein, a derivative thereof, a crosslinked product thereof, and a copolymer thereof.

The polymer-based composite material may include, for example, the polymer material and an additive. With the additive, the volume resistivity, elongation at break and Young's modulus of the polymer material can be adjusted. The additive may be one or more of a metal material and an inorganic non-metal material.

The additive of the metal material is, for example, one or more of aluminum, aluminum alloy, copper, copper alloy, nickel, nickel alloy, titanium, titanium alloy, iron, iron alloy, silver, and silver alloy.

The additive of the inorganic non-metallic material is, for example, one or more of a carbon-based material, aluminum oxide, silicon dioxide, silicon nitride, silicon carbide, boron nitride, silicate, and titanium oxide, and for another example, one or more of a glass material, a ceramic material, and a ceramic composite material. The carbon-based material is one or more of graphite, superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotube, graphene, and carbon nanofiber.

In some embodiments, the additive may be one or more of metal-coated carbon-based materials, such as nickel-coated graphite powder and nickel-coated carbon fiber.

Preferably, the support layer <NUM> uses one or more of an insulating polymer material and an insulating polymer-based composite material. The support layer <NUM> has the relatively large volume resistivity, thereby improving the safety performance of the electrochemical apparatus.

Further, preferably, the support layer <NUM> uses one or more of polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polyethylene naphthalate (PEN), polystyrene sulfonate (PSS), and polyimide (PI).

In the negative current collector <NUM> in this embodiment of this application, the support layer <NUM> may be a single-layer structure, or may be a composite-layer structure of two or more layers, such as two layers, three layers, or four layers.

As an example of the composite-layer structure of the support layer <NUM>, referring to <FIG>, the support layer <NUM> is a composite-layer structure formed by laminating a first sublayer <NUM>, a second sublayer <NUM>, and a third sublayer <NUM>. The support layer <NUM> of the composite-layer structure has a first surface 101a and a second surface 101b that are opposite, and the metal conductive layer <NUM> is laminated on the first surface 101a and the second surface 101b of the support layer <NUM>. Certainly, the metal conductive layer <NUM> may be disposed only on the first surface 101a of the support layer <NUM>, or may be disposed only on the second surface 101b of the support layer <NUM>.

When the support layer <NUM> is a composite-layer structure of at least two layers, the material of each sublayer may be the same or different.

In some embodiments, a material of the metal conductive layer <NUM> is one or more of copper, copper alloy, nickel, nickel alloy, titanium, titanium alloy, silver, and silver alloy, preferably one or more of copper, copper alloy, nickel, nickel alloy, titanium, and silver, or more preferably one or more of copper and copper alloy.

The nickel alloy is, for example, a nickel-copper alloy.

A weight percent composition of a copper element in the copper alloy is preferably more than <NUM>%.

In some embodiments, the volume resistivity of the metal conductive layer <NUM> is preferably <NUM>×<NUM>-<NUM> Ω·m to <NUM>×<NUM>-<NUM> Ω·m, so that the negative current collector <NUM> has better conductivity and current collector performance, improving performance of the electrochemical apparatus, that is, improving rate performance and cyclic performance of the electrochemical apparatus. More preferably, a volume resistivity of the metal conductive layer <NUM> is <NUM>×<NUM>-<NUM> Ω·m to <NUM>×<NUM>-<NUM> Ω·m.

In some embodiments, referring to <FIG>, the negative current collector <NUM> further optionally includes a protective layer <NUM>. Specifically, the metal conductive layer <NUM> includes two opposite surfaces in a thickness direction of the metal conductive layer <NUM>, and the protective layer <NUM> is laminated on either or both of the two surfaces of the metal conductive layer <NUM> to protect the metal conductive layer <NUM> from damages such as chemical corrosion or mechanical damages, thereby ensuring operating stability and a service life for the negative current collector <NUM>, and improving electrochemical performance of the electrochemical apparatus. In addition, the protective layer <NUM> can further enhance the mechanical strength of the negative current collector <NUM>.

A material of the protective layer <NUM> may be one or more of metal, metal oxide, and conductive carbon. The protective layer <NUM> made of the metal material is a metal protective layer. The protective layer <NUM> made of the metal oxide material is a metal oxide protective layer.

The metal is, for example, one or more of nickel, chromium, a nickel-based alloy, and a copper-based alloy. The nickel-based alloy is an alloy formed by adding one or more other elements to pure nickel, preferably a nickel-chromium alloy. The nickel-chromium alloy is an alloy formed by metal nickel and metal chromium. Optionally, a weight ratio of nickel to chromium in the nickel-chromium alloy is <NUM>:<NUM> to <NUM>: <NUM>, for example, <NUM>:<NUM>. The copper-based alloy is an alloy formed by adding one or more other elements to pure copper, preferably a nickel-copper alloy. Optionally, a weight ratio of nickel to copper in the nickel-copper alloy is <NUM>:<NUM> to <NUM>: <NUM>, for example, <NUM>:<NUM>.

The metal oxide is, for example, one or more of aluminum oxide, cobalt oxide, chromium oxide, and nickel oxide.

The conductive carbon is, for example, one or more of graphite, superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotube, grapheme, and carbon nanofiber, preferably one or more of carbon black, carbon nanotube, acetylene black, and graphene.

As some examples, referring to <FIG>, the negative current collector <NUM> includes the support layer <NUM>, the metal conductive layer <NUM>, and the protective layer <NUM> that are laminated. The support layer <NUM> has the first surface 101a and the second surface 101b that are opposite in the thickness direction. The metal conductive layer <NUM> is laminated on at least one of the first surface 101a and the second surface 101b of the support layer <NUM>, and the protective layer <NUM> is laminated on a surface of the metal conductive layer <NUM> facing away from the support layer <NUM>.

The protective layer <NUM> (referred to as an upper protective layer) is disposed on the surface of the metal conductive layer <NUM> facing away from the support layer <NUM>, to protect the metal conductive layer <NUM> from chemical corrosion and mechanical damages. This can also optimize an interface between the negative current collector <NUM> and a negative electrode active material layer, and increase the bonding force between the negative current collector <NUM> and the negative electrode active material layer.

In some embodiments, the upper protective layer of the negative current collector <NUM> may be a protective layer of metal oxide, such as alumina oxide, cobalt oxide, nickel oxide, or chromium oxide. The metal oxide protective layer features high hardness and a high mechanical strength, is larger than a surface area, and has better corrosion resistance performance, so as to better protect the metal conductive layer <NUM>.

Further, the upper protective layer of the negative current collector <NUM> is preferably a metal protective layer, where the metal protective layer can improve the conductivity of the negative current collector <NUM>, reduce battery polarization, reduce the risk of lithium precipitation on the negative electrode, and improve cyclic performance and safety performance of the electrochemical apparatus; or more preferably, is a double protective layer, that is, a composite layer formed by a metal protective layer and a metal oxide protective layer, where preferably, the metal protective layer is disposed on a surface of the metal conductive layer <NUM> facing away from the support layer <NUM> and the metal oxide protective layer is disposed on a surface of the metal protective layer facing away from the support layer <NUM>. This can improve both conductivity performance and corrosion resistance performance of the negative current collector <NUM>, and improve an interface between the metal conductive layer <NUM> and the negative electrode active material layer, to obtain the negative current collector <NUM> with better comprehensive performance.

As some other examples, referring to <FIG>, the negative current collector <NUM> includes the support layer <NUM>, the metal conductive layer <NUM>, and the protective layer <NUM> that are laminated. The support layer <NUM> has the first surface 101a and the second surface 101b that are opposite in the thickness direction. The metal conductive layer <NUM> is laminated on at least one of the first surface 101a and the second surface 101b of the support layer <NUM>, and the protective layer <NUM> is laminated on a surface of the metal conductive layer <NUM> facing towards the support layer <NUM>.

The protective layer <NUM> (referred to as a lower protective layer) is provided on the surface of the metal conductive layer <NUM> facing towards the support layer <NUM>. The lower protective layer protects the metal conductive layer <NUM> from chemical corrosion and mechanical damages, and can also increase the bonding force between the metal conductive layer <NUM> and the support layer <NUM>, preventing the metal conductive layer <NUM> from being separated from the support layer <NUM>, and improving a supporting and protection role of the support layer <NUM> for the metal conductive layer <NUM>.

Optionally, the lower protective layer is a metal oxide or metal protective layer. The metal oxide protective layer has relatively high corrosion resistance performance, and is larger than a surface area, further improving the interface bonding force between the metal conductive layer <NUM> and the support layer <NUM>. In this way, the lower protective layer can better protect the metal conductive layer <NUM>, thereby improving performance of the electrochemical apparatus. Moreover, the metal oxide protective layer has higher hardness and a better mechanical strength, further improving the strength of the negative current collector <NUM>. In addition to protecting the metal conductive layer <NUM> from chemical corrosion and mechanical damages, the metal protective layer can improve the conductivity of the negative current collector <NUM>, reduce battery polarization, and reduce the risk of lithium precipitation on the negative electrode, improving the cyclic performance and safety performance of the electrochemical apparatus. Therefore, the lower protective layer of the negative current collector <NUM> is preferably a metal protective layer.

As still some examples, referring to <FIG>, the negative current collector <NUM> includes the support layer <NUM>, the metal conductive layer <NUM>, and the protective layer <NUM> that are laminated. The support layer <NUM> has the first surface 101a and the second surface 101b that are opposite in the thickness direction. The metal conductive layer <NUM> is laminated on at least one of the first surface 101a and the second surface 101b of the support layer <NUM>, and the protective layer <NUM> is laminated on the surface of the metal conductive layer <NUM> facing away from the support layer <NUM> and the surface facing towards the support layer <NUM>.

The protective layer <NUM> is provided on two surfaces of the metal conductive layer <NUM>, that is, an upper protective layer and a lower protective layer are disposed on the metal conductive layer <NUM>, so as to better protect the metal conductive layer <NUM> and make the negative current collector <NUM> have better comprehensive performance.

It can be understood that the protective layer <NUM> on the two surfaces of the metal conductive layer <NUM> may be the same or different in material and thickness.

Preferably, a thickness D<NUM> of the protective layer <NUM> is <NUM>≤D<NUM>≤<NUM> and D<NUM>≤<NUM>. The protective layer <NUM> with the thickness D<NUM> in the foregoing range can effectively protect the metal conductive layer <NUM> and also make the electrochemical apparatus have a higher energy density.

In some embodiments, the thickness D<NUM> of the protective layer <NUM> may be <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or <NUM>, and the thickness D<NUM> of the protective layer <NUM> may be in a range formed by any two of the foregoing values. Preferably, <NUM>≤D<NUM>≤<NUM>, or more preferably, <NUM>≤D<NUM>≤<NUM>.

Further, when the protective layer <NUM> is disposed on the two surfaces of the metal conductive layer <NUM>, that is, the upper protective layer and the lower protective layer are respectively disposed on the two surfaces of the metal conductive layer <NUM>, a thickness Da of the upper protective layer is <NUM>≤Da≤<NUM> and Da≤<NUM>. 1D<NUM>, and a thickness Db of the lower protective layer is <NUM>≤Db≤<NUM> and Db≤<NUM>. Preferably, Da>Db, so that the protective layer <NUM> better protects the metal conductive layer <NUM>, and the electrochemical apparatus has a higher weight energy density. More preferably, <NUM>. 5Da≤Db≤<NUM>.

The metal conductive layer <NUM> may be formed on the support layer <NUM> by means of at least one of mechanical rolling, bonding, vapor deposition (vapor deposition), electroless plating (Electroless plating), and electroplating (electroplating). Preferably, vapor deposition and electroplating are used, that is, the metal conductive layer <NUM> is preferably a vapor deposition layer or an electroplating layer, so as to bond the metal conductive layer <NUM> and the support layer <NUM> tightly, and make the support layer <NUM> effectively play a supporting role for the metal conductive layer <NUM>.

Preferably, the bonding force between the support layer <NUM> and the metal conductive layer <NUM> is F≥100N/m, or more preferably F≥400N/m.

For example, the metal conductive layer <NUM> is formed on the support layer <NUM> by using the vapor deposition method. Conditions of the vapor deposition process such as a deposition temperature, a deposition rate, and an atmosphere condition of a deposition chamber are properly controlled to make the sheet resistance growth rate of the metal conductive layer <NUM> meet the aforementioned requirement when the negative current collector <NUM> is stretched.

The vapor deposition method is preferably a physical vapor deposition (Physical Vapor Deposition, PVD) method. The physical vapor deposition method is preferably at least one of an evaporation method and a sputtering method. The evaporation method is preferably at least one of a vacuum evaporation method, a thermal evaporation method, and an electron beam evaporation method. The sputtering method is preferably a magnetron sputtering method.

As an example, forming the metal conductive layer <NUM> by using the vacuum evaporation method includes: placing the surface-cleaned support layer <NUM> in a vacuum plating chamber, melting and evaporating a high-purity metal wire in a metal evaporation chamber at a high temperature of <NUM> to <NUM>, and processing the evaporated metal by using a cooling system in the vacuum plating chamber, to finally obtain a deposition on the support layer <NUM> to form the metal conductive layer <NUM>.

A process of forming the metal conductive layer <NUM> by using the mechanical rolling method may include: placing a metal sheet in a mechanical roller, rolling the metal sheet to a predetermined thickness by applying a pressure of 20t to 40t, placing the metal sheet on a surface of the surface-cleaned support layer <NUM>, and then placing the two in the mechanical roller, so as to tightly combine the two by applying a pressure of 30t to 50t.

A process of forming the metal conductive layer <NUM> by means of bonding may include: placing a metal sheet in the mechanical roller, rolling the metal sheet to a predetermined thickness by applying a pressure of 20t to 40t, coating a mixed solution of polyvinylidene fluoride (PVDF) and N-methylpyrrolidone (NMP) on a surface of the surface-cleaned support layer <NUM>, finally bonding the metal conductive layer <NUM> with the predetermined thickness to the surface of the support layer <NUM>, and drying them by heat to make the two tightly combined.

When the negative current collector <NUM> has the protective layer <NUM>, the protective layer <NUM> may be formed on the metal conductive layer <NUM> by using at least one of the vapor deposition method, an in-situ formation method, and a coating method. The vapor deposition method may be the vapor deposition method described above. The in-situ formation method is preferably an in-situ passivation method, that is, a method for forming a metal oxide passivation layer in an original place on the metal surface. The coating method is preferably at least one of roller coating, extrusion coating, blade coating, and gravure coating.

Preferably, the protective layer <NUM> is formed on the metal conductive layer <NUM> by using at least one of the vapor deposition method and the in-situ formation method, so as to provide a higher bonding force between the metal conductive layer <NUM> and the protective layer <NUM>, make the protective layer <NUM> better protect the negative current collector <NUM>, and ensure higher operating performance for the negative current collector <NUM>.

In this embodiment of this application, a density of the metal conductive layer may be determined through measurement by using a method known in the art: in an example, cutting a negative current collector (whose metal conductive layer is metallic copper) with an area of <NUM><NUM>, using a balance accurate to <NUM> to obtain a weigh denoted by m<NUM> in units of g, and measuring the thickness at <NUM> positions by using a micrometer to obtain an average value denoted by d<NUM> in units of µm; immersing the negative current collector in 1mol/L FeCl<NUM> aqueous solution for <NUM>, waiting until the metal conductive layer is fully dissolved, taking out the support layer to rinse with deionized water for <NUM> times, baking the support layer at <NUM> for <NUM>, using the same balance to obtain a weigh denoted by m<NUM> in units of g, measuring the thickness at <NUM> positions by using the same micrometer to obtain an average value denoted by d<NUM> in units of µm, and calculating the density of the metal conductive layer in units of g/cm<NUM> according to the following formula: <MAT>.

Testing is conducted on five same-size negative current collectors to obtain the density of the metal conductive layer, using an average value as the result.

If a tensile strain of the negative current collector is set to ε, and ε=ΔL/L×<NUM>%, where ΔL is an elongation obtained by stretching the negative current collector, and L is an original length of the negative current collector, that is, a length before stretching.

When the tensile strain ε of the negative current collector is <NUM>%, the sheet resistance growth rate T of the metal conductive layer can be determined through measurement by using a method known in the art: in an example, cutting the negative current collector to obtain a <NUM>×<NUM> sample, measuring a sheet resistance in a central region of the sample by using a four-probe method, recording the sheet resistance as R<NUM>, stretching the central region of the sample by using a GOTECH tension tester, configuring initial settings to obtain a sample length of <NUM> between jigs, stretching the sample at a speed of <NUM>/min and at a stretching distance being <NUM>% of the original length of the sample, taking out the stretched sample, testing the sheet resistance of the metal conductive layer between the jigs, recording the sheet resistance as R<NUM>, and calculating, according to a formula T=(R<NUM>-R<NUM>)/R<NUM>×<NUM>%, the sheet resistance growth rate T of the metal conductive layer when the tensile strain of the negative current collector is <NUM>%.

The sheet resistance of the metal conductive layer is tested by using the four-probe method as follows: using the RTS-<NUM> double electric four-probe tester in a test environment with a normal temperature of <NUM>±<NUM>, <NUM>. 1MPa, and relative humidity≤<NUM>%. The test is conducted as follows: cleaning a surface of the sample, placing the sample horizontally on a test bench, placing the four probes to make the probes in good contact with the surface of the metal conductive layer, adjusting an auto-test mode, calibrating a current range of the sample, measuring the sheet resistance in an appropriate current range, and collecting <NUM> to <NUM> data points of the same sample for data measurement accuracy and error analysis; finally, obtaining an average value as the sheet resistance value of the metal conductive layer.

The volume resistivity of the metal conductive layer is set to ρ, and ρ=RS×d, where a unit of ρ is Ω·m, RS is the sheet resistance of the metal conductive layer in units of Q, and d is the thickness of the metal conductive layer in units of m. The sheet resistance RS of the metal conductive layer can be measured by using the four-probe method described above, which is not repeated herein.

The volume resistivity of the support layer is a volume resistivity at <NUM>, and can be determined through measurement by using a method known in the art. In an example, the test is conducted in a room with a constant temperature, a normal pressure, and a low humidity (<NUM>, <NUM>. 1MPa, RH≤<NUM>%). A disk support layer sample with a diameter of <NUM> (the sample size can be adjusted based on an actual size of a test instrument) is prepared. The test is conducted by using a tri-electrode surface resistivity method (GBT1410-<NUM>) with an insulation resistance tester (with a precision of 10Ω). The test method is as follows: placing the disk sample between two electrodes and applying a potential difference between the two electrodes to distribute generated current in the disk sample, and using a picoammeter or electrometer for measuring to avoid measurement errors caused by inclusion of a surface leakage current during measurement. A reading is the volume resistivity in units of Ω·m.

An elongation at break of the support layer may be determined through measurement by using a method known in the art: in an example, cutting the support layer to obtain a sample of <NUM>×<NUM>, conducting a tension test at a normal temperature and a normal pressure (<NUM>, <NUM>. 1MPa) by using a GOTECH tension tester, configuring initial settings to obtain a sample length of <NUM> between jigs, stretching the sample at a speed of <NUM>/min, and recording a device displacement y (mm) upon breakage out of stretching; finally calculating the elongation at break based on (y/<NUM>)×<NUM>%. The elongation at break of the metal conductive layer can be easily determined through measurement by using the same method.

A Young's modulus E of the support layer can be determined through measurement by a method known in the art: in an example, cutting the support layer to obtain a sample of <NUM>×<NUM>, measuring a sample thickness I (µm) by using a micrometer, conducting a tension test at a normal temperature and a normal pressure (<NUM>, <NUM>. 1MPa) by using a GOTECH tension tester, configuring initial settings to obtain a sample length of <NUM> between jigs, stretching the sample at a speed of <NUM>/min, recording a load Q (N) and a device displacement z (mm) upon breakage out of stretching, where the stress ξ(GPa)=Q/(<NUM>×l) and the strain ξ=z/<NUM>, drawing a stress-strain curve, and obtaining an initial linear curve, where a slope of the curve is the Young's modulus E.

The bonding force F between the support layer and the metal conductive layer may be tested by using a method known in the art: for example, selecting the negative current collector whose metal conductive layer disposed on one surface of the support layer as a to-be-tested sample at a width h of <NUM>, evenly attaching a <NUM> double-sided adhesive to a stainless steel plate at a normal temperature and a normal pressure (<NUM>, <NUM>. 1MPa), evenly attaching the to-be-tested sample to the double-sided adhesive, peeling the metal conductive layer from the support layer of the to-be-tested sample by using the GOTECH tension tester, obtaining a maximum tensile force x (N) based on readings of a tensile force and displacement diagram, and calculating the bonding force F (N/m) between the metal conductive layer and the support layer according to F=x/h.

A second aspect of the embodiments of this application provides a negative electrode plate, including a negative current collector and a negative electrode active material layer that are laminated, where the negative current collector is the negative current collector <NUM> according to the first aspect of the embodiments of this application.

With the negative current collector <NUM> in the first aspect of this embodiment of this application, the negative electrode plate in this embodiment of this application has a high weight energy density and good electrochemical performance than a conventional negative electrode plate.

As an example, the negative electrode plate includes a support layer <NUM>, a metal conductive layer <NUM>, and a negative electrode active material layer that are laminated. The support layer <NUM> includes a first surface 101a and/or a second surface 101b that are opposite, the metal conductive layer <NUM> is laminated on the first surface 101a and/or the second surface 101b of the support layer <NUM>, and the negative electrode active material layer is laminated on a surface of the metal conductive layer <NUM> facing away from the support layer <NUM>.

For the negative electrode plate in this embodiment of this application, the negative electrode active material layer may use a negative electrode active material known in the art. For example, the negative electrode active material for the lithium-ion secondary battery may be one or more of metal lithium, natural graphite, artificial graphite, mesophase carbon microbeads (MCMB for short), hard carbon, soft carbon, silicon, silicon-carbon composite, SiO, Li-Sn alloy, Li-Sn-O alloy, Sn, SnO, SnO<NUM>, spinel-structure lithium titanate, and Li-Al alloy.

Optionally, the negative electrode active material layer may further include a conductive agent. As an example, the conductive agent is one or more of graphite, superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotube, graphene, and carbon nanofiber.

Optionally, the negative electrode active material layer may further include a binder. As an example, the binder is one or more of styrene-butadiene rubber (SBR), water-based acrylic resin (water-based acrylic resin), carboxymethyl cellulose (CMC), polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), ethylene vinyl acetate copolymer (EVA), polyvinyl alcohol (PVA), and polyvinyl butyral (PVB).

The negative electrode plate may be prepared by using a conventional method in the art. Usually, the negative electrode active material and optionally, the conductive agent and the binder are dispersed in a solvent, to obtain a uniform negative electrode paste, where the solvent may be N-methylpyrrolidone (NMP) or deionized water. The negative electrode paste is coated on the negative current collector and undergoes processes such as drying to obtain the negative electrode plate.

A third aspect of the embodiments of this application provides an electrochemical apparatus, where the electrochemical apparatus includes a positive electrode plate, a negative electrode plate, a separator, and an electrolyte, where the negative electrode plate is the negative electrode plate according to the second aspect of the embodiments of this application.

The electrochemical apparatus may be a lithium-ion secondary battery, a lithium primary battery, a sodium-ion battery, or a magnesium-ion battery, which is not limited thereto.

The electrochemical apparatus uses the negative electrode plate according to the second aspect of the embodiments of this application, so that the electrochemical apparatus in this embodiment of this application has a higher weight energy density and good electrochemical performance.

The positive electrode plate may include a positive current collector and a positive electrode active material layer disposed on the positive current collector.

The positive current collector may be a metal foil or a porous metal foil including one or more of aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver, and silver alloy.

The positive electrode active material layer may use a positive electrode active material known in the art. For example, the positive electrode active material for the lithium-ion secondary battery may be a lithium transition metal compound oxide, where the transition metal may be one or more of Mn, Fe, Ni, Co, Cr, Ti, Zn, V, Al, Zr, Ce, and Mg. Elements with high electronegativity, such as one or more of S, F, Cl, and I, may be also added to the lithium transition metal composite oxide, so that the positive electrode active material has higher structural stability and higher electrochemical performance. As an example, the lithium transition metal composite oxide is, for example, one or more of LiMn<NUM>O<NUM>, LiNiO<NUM>, LiCoO<NUM>, LiNi<NUM>-yCoyO<NUM> (<NUM><y<<NUM>), LiNiaCobAl<NUM>-a-bO<NUM> (<NUM><a<<NUM>, <NUM><b<<NUM>, <NUM><a+b<<NUM>), LiMn<NUM>-m-nNimConO<NUM> (<NUM><m<<NUM>, <NUM><n<<NUM>, <NUM><m+n<<NUM>), LiMPO<NUM> (M may be one or more of Fe, Mn, and Co), and Li<NUM>V<NUM> (PO<NUM>)<NUM>.

Optionally, the positive electrode active material layer may further include a conductive agent. As an example, the conductive agent is one or more of graphite, superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotube, graphene, and carbon nanofiber.

Optionally, the positive electrode active material layer may further include a binder. As an example, the binder is one or more of styrene-butadiene rubber (SBR), water-based acrylic resin (water-based acrylic resin), carboxymethyl cellulose (CMC), polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), ethylene vinyl acetate copolymer (EVA), polyvinyl alcohol (PVA), and polyvinyl butyral (PVB).

The positive electrode plate may be prepared by using a conventional method in the art. Usually, the positive electrode active material and optionally, the conductive agent and the binder are dispersed in a solvent (such as NMP) to obtain a uniform positive electrode paste. The positive electrode paste is coated on the positive current collector and undergoes processes such as drying to obtain the positive electrode plate.

There is no particular limitation on the aforementioned separator, and any known porous separators with electrochemical and chemical stability can be selected, for example, mono-layer or multi-layer membranes made of one or more of glass fiber, nonwoven fabric, polyethylene, polypropylene, and polyvinylidene fluoride may be used.

The electrolyte includes an organic solvent and electrolyte salt. The organic solvent, as a medium for transferring ions in electrochemical reactions, may use an organic solvent for the electrolyte of the electrochemical apparatus known in the art. The electrolyte salt, as a source of ions, may be electrolyte salt for the electrolyte of the electrochemical apparatus known in the art.

For example, the organic solvent used in the lithium-ion secondary batteries may be one or more of ethylene carbonate (EC), propylene carbonate (PC), ethyl methyl carbonate (EMC), diethyl carbonate (DEC), dimethyl carbonate (DMC), dipropyl carbonate (DPC), methyl propyl carbonate (MPC), ethyl propyl carbonate (EPC), butylene carbonate (BC), fluoroethylene carbonate (FEC), methyl formate (MF), methyl acetate (MA), ethyl acetate (EA), propyl acetate (PA), methyl propionate (MP), ethyl propionate (EP), propyl propionate (PP), methyl butyrate (MB), ethyl butyrate (EB), <NUM>,<NUM>-butyrolactone (GBL), sulfolane (SF), methyl sulfonyl methane (MSM), methyl ethyl sulfone (EMS), and diethyl sulfone (ESE).

For example, the electrolytic salt used in the lithium-ion secondary batteries may be one or more of LiPF<NUM> (lithium hexafluorophosphate), LiBF<NUM> (lithium tetrafluoroborate), LiClO<NUM> (lithium perchlorate), LiAsF<NUM> (lithium hexafluoroborate), LiFSI (lithium bisfluorosulfonyl imide), LiTFSI (lithium bis-trifluoromethanesulfon imide), LiTFS (lithium trifluoromethanesulfonat), LiDFOB (lithium difluorooxalatoborate), LiBOB (lithium bisoxalatoborate), LiPO<NUM>F<NUM> (lithium difluorophosphate), LiDFOP (lithium difluorophosphate), and LiTFOP (lithium tetrafluoro oxalate phosphate).

The positive electrode plate, the separator, and the negative electrode plate are stacked in sequence, so that the separator is isolated between the positive electrode plate and the negative electrode plate to obtain a battery core, or are wound to obtain the battery core. To prepare the electrochemical apparatus, the battery core is placed in a packing housing and the electrolyte was injected and sealed.

A fourth aspect of the embodiments of this application provides a battery module, where the battery module includes any one or more of the electrochemical apparatuses according to the third aspect of this application.

Further, a quantity of electrochemical apparatuses included in the battery module may be adjusted based on application and a capacity of the battery module.

In some embodiments, referring to <FIG> and <FIG>, in a battery module <NUM>, a plurality of electrochemical apparatuses <NUM> may be arranged in sequence along a length direction of the battery module <NUM>, or certainly, may be arranged in any other manners. Further, the plurality of electrochemical apparatuses <NUM> may be secured by using fasteners.

Optionally, the battery module <NUM> may further include a housing having an accommodating space, and the plurality of electrochemical apparatuses <NUM> are accommodated in the accommodating space.

A fifth aspect of the embodiments of this application provides a battery pack, where the battery pack includes any one or more of the battery modules according to the fourth aspect of this application. That is, the battery pack includes any one or more of electrochemical apparatuses according to the third aspect of this application.

A quantity of battery modules in the battery pack may be adjusted based on application and a capacity of the battery pack.

In some embodiments, referring to <FIG> and <FIG>, the battery pack <NUM> may include a battery box and a plurality of battery modules <NUM> disposed in the battery box. The battery box includes an upper case <NUM> and a lower case <NUM>. The upper case <NUM> may cover the lower case <NUM> to form a closed space for accommodating the battery modules <NUM>. The plurality of battery modules <NUM> may be arranged in the battery box in any manner.

A sixth aspect of the embodiments of this application provides a device, where the device includes any one or more of the electrochemical apparatuses according to the third aspect of this application. The electrochemical apparatus may be used as a power supply for the device.

Preferably, the device may be, but is not limited to, a mobile device (for example, a mobile phone or a notebook computer), an electric vehicle (for example, a full electric vehicle, a hybrid electric vehicle, a plug-in hybrid electric vehicle, an electric bicycle, an electric scooter, an electric golf vehicle, or an electric truck), an electric train, a ship, a satellite, an energy storage system, and the like.

For example, <FIG> illustrates a device including the electrochemical apparatus of this application. The device is a full electric vehicle, a hybrid electric vehicle, a plug-in hybrid electric vehicle, and the like, and the electrochemical apparatus of this application supplies power to the device.

The battery module, the battery pack, and the device in this application include the electrochemical apparatus provided in this application, and therefore have at least the same advantages as the electrochemical apparatus.

Content disclosed in this application is described in more detail in the following embodiments. Unless otherwise stated, all parts, percentages, and ratios reported in the following embodiments are based on weights, all reagents used in the embodiments are commercially available or synthesized in a conventional manner, and can be used directly without further processing, and all instruments used in the embodiments are commercially available.

Select a support layer with a predetermined thickness, perform surface cleaning treatment, place the surface-cleaned support layer in a vacuum plating chamber, melt and evaporate a high-purity copper wire in a metal evaporating chamber at a high temperature of <NUM> to <NUM>, and process the evaporated metal by using a cooling system in the vacuum plating chamber, to finally obtain a deposition on two surfaces of the support layer to form a conductive layer.

A material, thickness, and density of the metal conductive layer and preparation processing conditions (such as vacuum, atmosphere, humidity, and temperature) can be adjusted, and a material and thickness of the support layer can be adjusted, so as to obtain different T values for the negative current collector.

Fully stir and mix a negative electrode active material graphite, conductive carbon black, a thickener sodium carboxymethyl cellulose (CMC), and a binder styrene-butadiene rubber emulsion (SBR) in an appropriate amount of deionized water at a weight ratio of <NUM>:<NUM>:<NUM>:<NUM> to obtain a uniform negative electrode paste, coat the negative electrode paste on the negative current collector, and conduct processes such as drying to obtain the negative electrode plate.

A copper foil with a thickness of <NUM>.

Different from the negative electrode plate in the foregoing embodiments of this application, a conventional negative current collector is used.

An aluminum foil with a thickness of <NUM>.

Fully stir and mix a positive electrode active material LiNi<NUM>/<NUM>Co<NUM>/<NUM>Mn<NUM>/<NUM>O<NUM> (NCM333), conductive carbon black, and polyvinylidene fluoride (PVDF) in an appropriate amount of N-methylpyrrolidone (NMP) solvent at a weight ratio of <NUM>:<NUM>:<NUM> to obtain a uniform positive electrode paste, coat the positive electrode paste on the positive current collector, and conduct processes such as drying to obtain the positive electrode plate.

Evenly mix ethylene carbonate (EC) and ethyl methyl carbonate (EMC) at a volume ratio of <NUM>:<NUM> to obtain an organic solvent, and then evenly dissolve 1mol/L LiPF<NUM> in the organic solvent.

Laminate the positive electrode plate, the separator (PP/PE/PP composite film), and the negative electrode plate in sequence, wind them into a battery core, pack the battery core into a packing housing, inject the electrolyte into the battery core, and conduct processes such as sealing, waiting, hot pressing, cold pressing, and formation, to obtain the lithium-ion secondary battery.

At <NUM>, charge the lithium-ion secondary battery to <NUM>. 2V at a constant current rate of 1C, charge the battery to a current less than or equal to <NUM>. 05C at a constant voltage, and then discharge the battery to <NUM>. 8V at a constant current rate of 1C. This is a charge and discharge cycle, and a discharge capacity this time is a discharge capacity of the first cycle. The battery is charged and discharged for <NUM> cycles by using the foregoing method, and a discharge capacity of the 1000th cycles is recorded.

At <NUM>, charge the lithium-ion secondary battery to <NUM>. 2V at a constant current rate of 1C, charge the battery to a current less than or equal to <NUM>. 05C at a constant voltage, and then discharge the battery to <NUM>. 0V at a constant current rate of 1C, to obtain a 1C-rate discharge capacity of the lithium-ion secondary battery.

At <NUM>, charge the lithium-ion secondary battery to <NUM>. 2V at a constant current rate of 1C, charge the battery to a current less than or equal to <NUM>. 05C at a constant voltage, and then discharge the battery to <NUM>. 0V at a constant current rate of 4C, to obtain a 4C-rate discharge capacity of the lithium-ion secondary battery.

Role of the negative current collector of this application in improving the weight energy density of the electrochemical apparatus.

In Table <NUM>, the weight percent composition of the negative current collector refers to a percentage obtained by dividing the weight of the negative current collector per unit area by the weight of the conventional negative current collector per unit area.

Compared with the conventional copper-foil negative current collector, the weights of the negative current collectors in the embodiments of this application are all reduced at different degrees, thereby improving the weight energy density of the battery.

Electrical performance of the negative current collector of this application.

In Table <NUM>, the copper alloy is composed of <NUM> wt% copper and <NUM> wt% nickel.

The volume resistivity of the support layer is <NUM>×<NUM><NUM> Ω·m, and the thickness D<NUM> of the support layer is <NUM>.

When the metal conductive layer and the support layer are the same in material and thickness, negative current collectors with different T values can be obtained by adjusting preparation conditions of the metal conductive layer.

An overcurrent test is conducted on the positive current collectors in Table <NUM>. The overcurrent test method includes: cutting the negative current collector to a width of <NUM>, coating a negative electrode active material layer <NUM> wide in the middle of the width direction and perform rolling to form a negative electrode plate, and cutting the electrode plate obtained by rolling into strips of <NUM>×<NUM> in the width direction, with <NUM> pieces for each electrode plate. During testing, non-coated conductive areas on both sides of the electrode plate sample are connected to positive and negative terminals of a charge and discharge machine, and then the charge and discharge machine is set to allow a 5A current to pass through the electrode plate for <NUM>. The test is successful if the electrode plate does not blow; otherwise, the test fails. <NUM> samples in each sample set were tested, and the test results are shown in Table <NUM> below.

It can be seen from Table <NUM> and Table <NUM> that when the tensile strain of the negative current collector is <NUM>%, the sheet resistance growth rate T of the metal conductive layer is not greater than <NUM>%. In this case, the negative current collector has better electrical performance. The negative electrode plate using the negative current collector has better overcurrent performance after undergoing rolling. Otherwise, the negative current collector has poor conductivity performance, with little practical value for battery products. Preferably, when the tensile strain of the negative current collector is <NUM>%, the sheet resistance growth rate T of the metal conductive layer satisfies T≤<NUM>%. More preferably, T≤<NUM>%.

Impact of the protective layer on electrochemical performance of the electrochemical apparatus.

For the negative current collectors in Table <NUM>, a protective layer is disposed on a basis of the negative current collector <NUM> in Table <NUM>.

The nickel-based alloy contains 90wt% nickel and 10wt% chromium.

The dual-layer protective layer includes a nickel protective layer with a thickness of <NUM> disposed on a surface of the metal conductive layer facing away from the support layer, and a nickel oxide protective layer with a thickness of <NUM> disposed on a surface of the nickel protective layer facing away from the support layer.

Claim 1:
A negative current collector, wherein the negative current collector comprises a support layer and a metal conductive layer that is disposed on at least one of two opposite surfaces of the support layer in a thickness direction of the support layer;
a density of the support layer is less than a density of the metal conductive layer;
the density of the metal conductive layer is <NUM>/cm<NUM> to <NUM>/cm<NUM>;
a thickness D<NUM> of the metal conductive layer is <NUM>≤D<NUM>≤<NUM>; and
when a tensile strain of the negative current collector is <NUM>%, a sheet resistance growth rate T of the metal conductive layer is T≤<NUM>%
wherein the methods for measuring the density of the metal conductive layer, the tensile strain of the negative current collector and the sheet resistance growth rate T of the metal conductive layer is defined in the description.