The present disclosure relates to electrode binders, cathode electrode materials, and lithium ion batteries.
Binder is an important component of a cathode electrode and an anode electrode of a lithium ion battery. The binder is a high molecular weight compound for adhering an electrode active material to a current collector. A main role of the binder is to adhere and maintain the electrode active material, stabilize the electrode structure, and buffer an expansion and contraction of the electrode during a charge and discharge process.
A commonly used binder in lithium ion batteries is organic fluorine-containing polymers, such as polyvinylidene fluoride (PVDF).
Implementations are described by way of example only with reference to the attached figures.
Comparative Example 2 of the lithium ion battery being overcharged.
A detailed description with the above drawings is made to further illustrate the present disclosure.
In one embodiment, an electrode binder of a lithium ion battery is provided. The electrode binder is a polymer obtained by polymerizing a dianhydride monomer with a diamine monomer.
The dianhydride monomer can be represented by the formulas I, II, or III below.
In the formula III, R is a bivalent organic substituent, which can be bisphenol
A unit, —O—, —S—, or —CH2—. The dianhydride monomer can comprise, but is not limited to, one or more of 4,4′-(4,4′-isopropylidenediphenoxy)bis(phthalic anhydride), 2,3,3′,4′-diphenyl ether tetracarboxylic acid dianhydride, 1,2,4,5-benzenetetracarboxylic anhydride, and 3,3′,4,4′-biphenyltetracarboxylic dianhydride.
The diamine monomer can at least comprise a monomer represented by formula IV.
In one embodiment, the diamine monomer can further comprise a monomer represented by formula V.
In the formula V, R4 is a bivalent organic substituent, which can be —(CH2)n-, —O—, —S—, —CH2—O—CH2—, —CH(NH)—(CH2)n—,
A molar ratio of the monomer of formula IV to the monomer of formula V can be 1:2 to 10:1, and in some embodiments can be 1:1 to 3:1.
A molar ratio of all the dianhydride monomer to all the diamine monomer can be 1:10 to 10:1, and in some embodiments can be 1:2 to 4:1.
A molecular weight of the electrode binder can range from about 1000 to about 50000.
One embodiment of a method for making the electrode binder comprises a step of polymerizing the dianhydride monomer with the diamine monomer, which specifically can comprise:
mixing the dianhydride monomer and the diamine monomer in an organic solvent to form a mixture, and heating and stirring the mixture to fully carry the reaction thereby obtaining the electrode binder.
The diamine monomer can be dissolved in an organic solvent to form a diamine solution. A mass ratio of the diamine monomer to the organic solvent in the diamine solution can be 1:100 to 1:1, and can be 1:10 to 1:2 in some embodiments.
The dianhydride monomer can be dissolved in an organic solvent to form a dianhydride solution. A mass ratio of the dianhydride monomer to the organic solvent in the dianhydride solution, can be 1:100 to 1:1, and can be 1:10 to 1:2 in some embodiments.
The organic solvent can dissolve the diamine monomer and the dianhydride monomer, such as N,N-dimethylformamide, N,N-dimethylacetamide, propylene carbonate, and N-methyl-2-pyrrolidone.
A pump can be used to transfer the dianhydride solution to the diamine solution or vice versa. After the mixing, the stirring can continue for a period of time to form a complete reaction. The stirring can last for about 2 hours to about 72 hours, and about 12 hours to about 24 hours in some embodiments. The temperature of the polymerizing can be at about 160° C. to about 200° C.
During the polymerizing, a catalyst can be added. The catalyst can be at least one of benzoic acid, benzenesulfonic acid, phenylacetic acid, pyridine, quinoline, pyrrole, and imidazole. A mass percentage of the catalyst to a sum of the dianhydride monomer and the diamine monomer can be about 0.5% to about 5%.
First, the dianhydride monomer and the diamine monomer can be completely dissolved in the organic solvent, and then heated to a temperature of about 30° C. to about 60° C. at which the mixture is stirred for about 1 hour to about 10 hours, and 2 hours to 4 hours in some embodiments. The catalyst is then added to the mixture followed by heating the mixture to a temperature of about 160° C. to about 200° C. at which the mixture is stirred for about 6 hours to about 48 hours, and 12 hours to 24 hours in some embodiments, to obtain the polymer.
After the reaction, the electrode binder can be purified by washing the obtained polymer with a cleaning solvent, and dried. The catalyst and the organic solvent are soluble to the cleaning solvent, and the electrode binder is insoluble to the cleaning solvent. The cleaning solvent can be water, methanol, ethanol, a mixture of methanol and water, or a mixture of ethanol and water (a concentration of the methanol or the ethanol can be 5 wt % to 99 wt %).
One embodiment of a cathode electrode material comprises a cathode active material, a conducting agent, and the above-described electrode binder, which are uniformly mixed with each other. A mass percentage of the electrode binder in the cathode electrode material can be in a range from about 0.01% to about 50%, such as from about 1% to about 20%.
The cathode active material can be at least one of layer type lithium transition metal oxides, spinel type lithium transition metal oxides, and olivine type lithium transition metal oxides, such as olivine type lithium iron phosphate, layer type lithium cobalt oxide, layer type lithium manganese oxide, spinel type lithium manganese oxide, lithium nickel manganese oxide, and lithium cobalt nickel manganese oxide.
The conducting agent can be carbonaceous materials, such as at least one of carbon black, conducting polymers, acetylene black, carbon fibers, carbon nanotubes, and graphite.
One embodiment of an anode electrode material comprises an anode active material, a conducting agent, and the above-described electrode binder, which are uniformly mixed with each other. A mass percentage of the electrode binder in the anode electrode material can be in a range from about 0.01% to about 50%, such as from about 1% to about 20%.
The anode active material can be at least one of lithium titanate, graphite, mesophase carbon micro beads (MCMB), acetylene black, carbon fibers, carbon nanotubes, and cracked carbon. The conducting agent can be carbonaceous materials, such as at least one of carbon black, conducting polymers, acetylene black, carbon fibers, carbon nanotubes, and graphite.
One embodiment of a lithium ion battery comprises a cathode electrode, an anode electrode, a separator, and an electrolyte liquid. The cathode electrode and the anode electrode are spaced from each other by the separator. At least one of the cathode electrode and the anode electrode can comprise the above-described electrode binder. The cathode electrode can further comprise a cathode current collector and the cathode electrode material located on a surface of the cathode current collector. The anode can further comprise an anode current collector and an anode electrode material located on a surface of the anode current collector. The anode electrode material and the cathode electrode material are opposite to each other and spaced by the separator.
If one of the cathode electrode material and the anode electrode material comprises the above-described polymer as the binder, the other one can comprises a conventional material as the binder. The conventional material as the binder can be at least one of polyvinylidene fluoride (PVDF), polyvinylidene fluoride, polytetrafluoroethylene (PTFE), fluoro rubber, ethylene propylene diene monomer, and styrene-butadiene rubber (SBR). In one embodiment, both the cathode electrode material and the anode electrode material comprise the above-described polymer as the binder.
The separator can be polyolefin microporous membrane, modified polypropylene fabric, polyethylene fabric, glass fiber fabric, superfine glass fiber paper, vinylon fabric, or composite membrane of nylon fabric, and wettable polyolefin microporous membrane composited by welding or bonding.
The electrolyte liquid comprises a lithium salt and a non-aqueous solvent. The non-aqueous solvent can comprise at least one of cyclic carbonates, chain carbonates, cyclic ethers, chain ethers, nitriles, amides and combinations thereof, such as ethylene carbonate (EC), diethyl carbonate (DEC), propylene carbonate (PC), dimethyl carbonate (DMC), ethyl methyl carbonate (EMC), butylene carbonate, gamma-butyrolactone, gamma-valerolactone, dipropyl carbonate, N-methyl pyrrolidone (NMP), N-methylformamide, N-methylacetamide, N,N-dimethylformamide, N,N-diethylformamide, diethyl ether, acetonitrile, propionitrile, anisole, succinonitrile, adiponitrile, glutaronitrile, dimethyl sulfoxide, dimethyl sulfite, vinylene carbonate, ethyl methyl carbonate, dimethyl carbonate, diethyl carbonate, fluoroethylene carbonate, chloropropylene carbonate, acetonitrile, succinonitrile, methoxymethylsulfone, tetrahydrofuran, 2-methyltetrahydrofuran, epoxy propane, methyl acetate, ethyl acetate, propyl acetate, methyl butyrate, ethyl propionate, methyl propionate, 1,3-dioxolane, 1,2-diethoxyethane, 1,2-dimethoxyethane, and 1,2-dibutoxy.
The lithium salt can comprise at least one of lithium chloride (LiCl), lithium hexafluorophosphate (LiPF6), lithium tetrafluoroborate (LiBF4), lithium methanesulfonate (LiCH3SO3), lithium trifluoromethanesulfonate (LiCF3SO3), lithium hexafluoroarsenate (LiAsF6), lithium hexafluoroantimonate (LiSbF6), lithium perchlorate (LiClO4), Li[BF2(C2O4)], Li[PF2(C2O4)2], Li[N(CF3SO2)2], Li[C(CF3SO2)3], and lithium bisoxalatoborate (LiBOB).
In molar ratio, 0.4 parts of 2,2′-bis(4-aminophenoxyphenyl)propane (BAPP), 0.6 parts of 4,4′-oxydianiline (ODA), and m-cresol as the organic solvent are added in a triple-neck flask (a solid content of the solution is about 10%), stirred at room temperature to dissolve completely. 1 part of 2,3,3′,4′-diphenyl ether tetracarboxylic acid dianhydride is then added and dissolved completely. The solution is heated to about 50° C. and reacted for about 4 hours followed by adding 1.5 mL of benzoic acid as the catalyst. Then the solution is heated to about 180° C. and reacted for about 24 hours. Finally, the reaction is terminated and the solution is precipitated in methanol to obtain the cathode electrode binder, which is a fiber shaped polymer represented by formula VI.
85% of LiNi1/3Co1/3Mn1/3O2, 5% of the electrode binder obtained in Example 1, and 10% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode. The counter electrode is lithium metal. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v). The counter electrode, the cathode electrode, the electrolyte liquid are assembled to form a lithium ion battery.
87% of LiNi1/3Co1/3Mn1/3O2, 3% of the electrode binder obtained in Example 1, and 10% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode. The counter electrode is lithium metal. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v). The counter electrode, the cathode electrode, the electrolyte liquid are assembled to form a lithium ion battery.
88% of LiNi1/3Co1/3Mn1/3O2, 2% of the electrode binder obtained in Example 1, and 10% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode. The counter electrode is lithium metal. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v). The counter electrode, the cathode electrode, the electrolyte liquid are assembled to form a lithium ion battery.
88.5% of LiNi1/3Co1/3Mn1/3O2, 1.5% of the electrode binder obtained in Example 1, and 10% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode. The counter electrode is lithium metal. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v). The counter electrode, the cathode electrode, the electrolyte liquid are assembled to form a lithium ion battery.
94% of LiNi1/3Co1/3Mn1/3O)2, 3% of the electrode binder obtained in Example 1, and 3% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode.
94% of anode graphite, 3.5% of PVDF, and 2.5% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on a copper foil and vacuum dried at about 100° C. to obtain the anode electrode.
The cathode electrode and the anode electrode are assembled and rolled up to form a 63.5 mm×51.5 mm×4.0 mm sized soft packaged battery. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v).
85% of LiNi1/3Co1/3Mn1/3O2, 5% of PVDF as the binder, and 10% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode. The counter electrode is lithium metal. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v). The counter electrode, the cathode electrode, the electrolyte liquid are assembled to form a lithium ion battery.
94% of LiNi1/3Co1/3Mn1/3O2, 3% of PVDF as the binder, and 3% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on an aluminum foil and vacuum dried at about 120° C. for about 12 hours to obtain the cathode electrode.
94% of anode graphite, 3.5% of PVDF, and 2.5% of the conducting graphite by mass percent are mixed and dispersed by the NMP to form a slurry. The slurry is coated on a copper foil and vacuum dried at about 100° C. to obtain the anode electrode.
The cathode electrode and the anode electrode are assembled and rolled up to form a 63.5 mm×51.5 mm×4.0 mm sized soft packaged battery. The electrolyte liquid is 1 M of LiPF6 dissolved in a solvent mixture of EC/DEC/EMC=1/1/1(v/v/v).
Cycling Performance Test of Batteries
The test conditions are as follows: in the voltage range of 2.8V to 4.3V, the batteries are charged and discharged at a constant current rate (C-rate) of 0.2 C. The cycling performance of the lithium ion battery in Example 2 for the first 50 cycles is shown in
Impedance Test
The lithium ion batteries in Example 2 and Comparative Example 1 are charged to 4.3 V to be full state. The batteries are subjected to an AC impedance test with a frequency range of 100 mHz to 100 kHz and an amplitude of 5 mV. Referring to
Liquid Absorption Rate Test
The pristine cathode electrodes of Example 2 and Comparative Example 1 are first weighed, and then immersed in an electrolyte liquid for about 48 hours. The cathode electrodes are taken out from the electrolyte liquid, and the residual electrolyte liquid are wiped off from the surface, and then the cathode electrodes are weighed again. Liquid absorption rate (R) is calculated by R=(Mafter−Mbefore)/Mbefore×100%, wherein Mbefore is the mass of the cathode electrode before being immersed in the electrolyte liquid, and Mafter is the mass of the cathode electrode after being immersed in the electrolyte liquid. The R value for Example 2 is 12.1%, and the R value for Comparative Example 1 is 15.2%, which reveal that although the cathode electrode using the conventional PVDF (Comparative Example 1) has a higher liquid absorption rate, the cathode electrode of Example 2 also has a sufficient liquid absorption rate to meet the requirement for a cathode electrode in the lithium ion battery.
Binding Force Test
The binding force tests are carried out for the cathode electrodes of Example 2 and Comparative Example 1, respectively. Adhesive tape having a width of 20 mm±1 mm is used. First, 3 to 5 outer layers of the adhesive tape are peeled off, and then more than 150 mm long of the adhesive tape is taken. The adhesive tape does not contact a hand or any other object. One end of the adhesive tape is adhered to the cathode electrode, and the other end of the adhesive tape is connected to a holder. A roller under its own weight is rolled on the cathode electrode at a speed of about 300 mm/min back and forth over the entire length of the cathode electrode three times. The test is carried out after resting the cathode electrode in the test environment for about 20 minutes to about 40 minutes. The adhesive tape is peeled from the cathode electrode by a testing machine at a speed of about 300 mm/min±10 mm/min. The test results are shown in Table 2, revealing that the electrode binder of Example 2 has a stronger binding force than the PVDF of Comparative Example 1.
Overcharge Test
The batteries of Example 6 and Comparative Example 2 are both overcharged to 10V at a current rate of 1 C to observe the phenomenon. Referring to
In the present disclosure, the polymer obtained by polymerizing the dianhydride monomer with diamine monomer can be used as an electrode binder in the lithium ion battery. The polymer has a small effect on the charge and discharge cycling performance of the lithium ion battery, and can improve the thermal stability of lithium ion battery as an overcharge protection to the electrode.
Finally, it is to be understood that the above-described embodiments are intended to illustrate rather than limit the present disclosure. Variations may be made to the embodiments without departing from the spirit of the present disclosure as claimed. Elements associated with any of the above embodiments are envisioned to be associated with any other embodiments. The above-described embodiments illustrate the scope of the present disclosure but do not restrict the scope of the present disclosure.
Number | Date | Country | Kind |
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201410591508.3 | Oct 2014 | CN | national |
This application claims all benefits accruing under 35 U.S.C. §119 from China Patent Application No. 201410591508.3, filed on Oct. 29, 2014 in the State Intellectual Property Office of China, the content of which is hereby incorporated by reference. This application is a continuation under 35 U.S.C. §120 of international patent application PCT/CN2015/091984 filed on Oct. 15, 2015, the content of which is also hereby incorporated by reference.
Number | Date | Country | |
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Parent | PCT/CN2015/091984 | Oct 2015 | US |
Child | 15498810 | US |