WO2015053302A1 - アミノ置換ホスファゼン化合物の製造方法、非水二次電池用電解液の製造方法および非水二次電池の製造方法 - Google Patents

アミノ置換ホスファゼン化合物の製造方法、非水二次電池用電解液の製造方法および非水二次電池の製造方法 Download PDF

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WO2015053302A1
WO2015053302A1 PCT/JP2014/076904 JP2014076904W WO2015053302A1 WO 2015053302 A1 WO2015053302 A1 WO 2015053302A1 JP 2014076904 W JP2014076904 W JP 2014076904W WO 2015053302 A1 WO2015053302 A1 WO 2015053302A1
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group
compound
production method
carbon atoms
secondary battery
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French (fr)
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吉憲 金澤
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富士フイルム株式会社
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Priority to CN201480055740.3A priority patent/CN105636970B/zh
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
    • C07F9/6564—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms
    • C07F9/6581—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms having phosphorus and nitrogen atoms with or without oxygen or sulfur atoms, as ring hetero atoms
    • C07F9/65812—Cyclic phosphazenes [P=N-]n, n>=3
    • C07F9/65814—Cyclic phosphazenes [P=N-]n, n>=3 n = 3 or 4
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
    • C07F9/6564—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms
    • C07F9/6581—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms having phosphorus and nitrogen atoms with or without oxygen or sulfur atoms, as ring hetero atoms
    • C07F9/65812—Cyclic phosphazenes [P=N-]n, n>=3
    • C07F9/65815—Cyclic phosphazenes [P=N-]n, n>=3 n = 3
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
    • C07F9/6564—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms
    • C07F9/6581—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms having phosphorus and nitrogen atoms with or without oxygen or sulfur atoms, as ring hetero atoms
    • C07F9/65812—Cyclic phosphazenes [P=N-]n, n>=3
    • C07F9/65817—Cyclic phosphazenes [P=N-]n, n>=3 n = 4
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566—Liquid materials
    • H01M10/0567—Liquid materials characterised by the additives
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a method for producing an amino-substituted phosphazene compound, a method for producing an electrolyte for a non-aqueous secondary battery using the same, and a method for producing a non-aqueous secondary battery.
  • Phosphazene compounds are applied in various applications. In recent years, it has attracted attention as a compound that can impart excellent flame retardancy to various materials. For example, in a lithium ion secondary battery, it has been proposed to be used as a compound imparting flame retardancy and to be used as an additive for the electrolytic solution (see Patent Document 1). Therein, a derivative in which a halogenated cyclic phosphazene is substituted with an alcohol compound is used as a flame retardant.
  • the above alkoxy-substituted fluorinated phosphazene includes a compound represented by (PNF 2 ) n and an alcoholate represented by R—OM (wherein R represents an alkyl group and M represents an alkali metal),
  • R—OM an alcoholate represented by R—OM
  • R—OH an alcohol represented by R—OH
  • a basic catalyst such as sodium carbonate or potassium carbonate
  • Non-Patent Document 1 As for the synthesis of a fluorinated phosphazene substituted with an amino group, a method of reacting a compound represented by (PNF 2 ) n with 2 equivalents of an amine (see Non-Patent Document 1) is known. It proposes to carry out amino substitution reaction using dimethylaminotrimethylsilane. On the other hand, as a method for synthesizing a polysubstituted phosphazene compound, a compound represented by (PNCl 2 ) n and a hydroxy compound are reacted in the presence of a catalyst such as zinc oxide or zinc chloride in a short time. It has been proposed to introduce at a high substitution rate (see Patent Documents 7 and 8).
  • the present invention has been made in view of such circumstances, and an object thereof is to provide a new method for synthesizing amino-substituted phosphazene compounds. Furthermore, if necessary, a production method for producing an amino-substituted phosphazene compound at high yield, high selectivity, high purity, and low cost, and an electrolyte for non-aqueous secondary battery and non-aqueous secondary using the same It aims at providing the manufacturing method of a battery.
  • the production method according to [1], wherein the amino-substituted phosphazene compound to be synthesized is a compound represented by the following formula (1).
  • Y 1 represents —NR 1 R 2 .
  • Y 2 represents a fluorine atom or —NR 3 R 4 .
  • R 1 to R 4 each independently represents a monovalent substituent or a hydrogen atom.
  • R 1 and R 2 , R 3 and R 4 may form a ring.
  • n represents 1 or 2.
  • the Lewis acid catalyst is an element selected from the group consisting of aluminum, magnesium, lithium, manganese, iron, copper, zinc, tin, boron, silicon, titanium, zirconium, chromium, cobalt, nickel, molybdenum, and vanadium.
  • M is a metal atom or a metalloid atom
  • Z is a halogen atom.
  • the Lewis acid catalyst is composed of a compound containing an element selected from the group consisting of aluminum, magnesium, lithium, iron, copper (II), boron, and silicon.
  • the Lewis acid catalyst comprises a compound having chlorine or bromine.
  • the Lewis acid catalyst is added in an amount of 0.25 to 1 equivalent to the fluorinated phosphazene compound.
  • the Lewis acid catalyst is selected from the group consisting of AlCl 3 , MgCl 2 , LiCl, LiBr, CuCl 2 , FeCl 3 , ZrCl 4 , ZrOCl 2 , SiCl 4 , Me 2 SiCl 2 , TMS-Cl, and BCl 3.
  • Me represents a methyl group.
  • TMS represents a trimethylsilyl group.
  • Electrolysis for a non-aqueous secondary battery comprising preparing the above-mentioned amino-substituted phosphazene compound-containing electrolyte for a non-aqueous secondary battery through the production method according to any one of [1] to [11] Liquid manufacturing method.
  • a method for producing a nonaqueous secondary battery, comprising a nonaqueous secondary battery comprising the positive electrode, the negative electrode, and the electrolyte for a nonaqueous secondary battery, through the production method according to [12].
  • a new method for synthesizing amino-substituted phosphazene compounds can be provided. Furthermore, if necessary, an amino-substituted phosphazene compound can be produced with high yield, high selectivity, high purity and low cost. Furthermore, the manufacturing method of the electrolyte solution for non-aqueous secondary batteries using the said amino substituted phosphazene compound and a non-aqueous secondary battery can be provided.
  • FIG. 1 is a 19F-NMR spectrum diagram of a product containing a compound (1-1) synthesized in Example 1.
  • FIG. 2 is a 19F-NMR spectrum diagram of a product containing a compound (1-1) synthesized in Comparative Example 1.
  • FIG. 1 is a 1H-NMR spectrum of a compound (1-1).
  • FIG. 6 is a 19F-NMR spectrum diagram of the compound (1-1).
  • 1 is a 1H-NMR spectrum of a compound (1-3).
  • FIG. FIG. 6 is a 19F-NMR spectrum diagram of the compound (1-3).
  • 1 is a 1H-NMR spectrum of a compound (c1).
  • FIG. 10 is a 19F-NMR spectrum diagram of the compound (c1).
  • an amino-substituted phosphazene compound is synthesized by reacting a fluorinated phosphazene compound with an amine compound in the presence of a Lewis acid catalyst.
  • an amino group means a substituted amino group (for example, an alkylamino group or an arylamino group).
  • Preferable examples include an amino group (NR 1 R 2 ) defined in the substituent Y 1 described later.
  • the phosphazene compound is preferably a cyclic phosphazene compound, and preferably a 6-membered or 8-membered cyclic phosphazene compound.
  • the amino-substituted phosphazene compound is preferably a compound represented by the following formula (1).
  • the group other than Y 1 and Y 2 is a fluorine atom among halogen atoms, for example, when applied as an additive (flame retardant) for an electrolyte solution of a lithium ion battery, imparting particularly high flame resistance, or a battery This is preferable because it contributes to maintenance of performance.
  • Y 1 represents —NR 1 R 2 .
  • R 1 and R 2 each represents a monovalent substituent or a hydrogen atom, and is preferably a monovalent substituent.
  • R 1 and R 2 may form a ring with each other, or may have an arbitrary substituent T.
  • the substituent T is not particularly limited, but those exemplified below are preferred. Specifically, a halogen atom (for example, a fluorine atom), a carbonyl group-containing group (for example, 2 to 6 carbon atoms), an alkoxy group (for example, a carbon number) 1-6) and silyl groups (for example, having 1 to 6 carbon atoms).
  • the carbonyl group-containing group includes an acyl group (preferably having 2 to 12 carbon atoms, more preferably 2 to 6 atoms, such as an acetyl group and a propionyl group), an aryloyl group (preferably having 7 to 23 carbon atoms, and having 7 to 15 carbon atoms). More preferred is 7 to 11, particularly preferred is benzoyl group, etc.), acyloxy group (preferably having 2 to 12 carbon atoms, more preferred is 2 to 6), acetyloxy group, propionyloxy group, etc., and aryloyloxy group (carbon number).
  • an acyl group preferably having 2 to 12 carbon atoms, more preferably 2 to 6 atoms, such as an acetyl group and a propionyl group
  • an aryloyl group preferably having 7 to 23 carbon atoms, and having 7 to 15 carbon atoms. More preferred is 7 to 11, particularly preferred is benzoyl group, etc.
  • acyloxy group
  • 7 to 23 is preferable, 7 to 15 is more preferable, and 7 to 11 is particularly preferable, such as benzoyloxy group, (meth) acryloyl group, (meth) acryloyloxy group, carbamoyl group (preferably having 1 to 12 carbon atoms, 1 to 6 are more preferable, and 1 to 3 are particularly preferable, carbamoyl group, N-methylcarbamoyl group, N, N-dimethyl. Carbamoyl, N- phenylcarbamoyl, etc.).
  • R 1 and R 2 are each preferably a hydrogen atom, an alkyl group, or an alkenyl group. Among them, an alkyl group having 1 to 6 carbon atoms is preferable, an alkyl group having 1 to 4 carbon atoms is more preferable, and an alkyl group having 1 to 3 carbon atoms is particularly preferable.
  • R 1 and R 2 may be bonded to each other or condensed to form a ring.
  • a hetero atom such as a nitrogen atom, an oxygen atom, or a sulfur atom may be incorporated.
  • a ring may be formed through the following hetero-linking group.
  • the ring to be formed is preferably a 5-membered ring or a 6-membered ring.
  • a nitrogen-containing five-membered ring is preferable, and examples of the compound forming the ring include pyrrole, imidazole, pyrazole, indazole, indole, benzimidazole, pyrrolidine, imidazolidine, pyrazolidine, indoline, carbazole, or these And the like (both are N-substituted).
  • Examples of the 6-membered ring include piperidine, morpholine, piperazine, and derivatives thereof (all are N-substituted).
  • Y 2 represents a fluorine atom or —NR 3 R 4, and is particularly preferably a fluorine atom.
  • R 3 and R 4 have the same meanings as R 1 and R 2 , and preferred ones are also the same.
  • the substituents may form a ring.
  • the reason why a fluorine atom is preferable among the halogen atoms is the same as described above.
  • R 3 and R 4 may have an arbitrary substituent T. Preferable substituents T have the same meaning as described above.
  • N 1 or 2 and is particularly preferably 1.
  • amino-substituted phosphazene compound Preferred specific examples of the amino-substituted phosphazene compound are shown below. However, the present invention is not limited by the following compounds.
  • the fluorinated phosphazene compound is preferably a compound represented by the following formula (2).
  • n 1 or 2, and is particularly preferably 1.
  • fluorinated phosphazene compounds were selected as reaction raw materials. The reasons for this include application advantages as described above, but reaction advantages in relation to the Lewis acid catalyst employed in the present invention.
  • Halogenated phosphazenes release halogen atoms into the system during the substitution reaction.
  • the fluorine anion is more reactive than the chlorine anion (see, for example, Chem. Ber. 116, 367-374 (1983) “Dar ein und Strukturbetician von Ammoniak-Phosphorpentafluorid (1/1)”). Therefore, the fluorine anion may react with an unreacted substrate to produce a by-product.
  • the Lewis acid catalyst suitably applied in the present invention functions to suppress such side reactions and increase the yield and selectivity. That is, it is understood that the fluorine anion is trapped in the system. From the viewpoint that such an effect appears remarkably, as described above, in the present invention, a substrate having a fluorine atom as a halogen atom and a Lewis acid catalyst are used in combination.
  • mono- and di-substituted amino groups can be selectively synthesized.
  • the Lewis acid catalyst is adapted to the reaction barrier depending on the number of substitutions (each step of the sequential reaction) and selectively generates the compound having the number of substitutions.
  • the above-mentioned Patent Documents 7 and 8 aim at a high substitution rate rather than a reaction selectivity.
  • monosubstituted or disubstituted (particularly monosubstituted) amino groups of fluorinated phosphazenes are particularly useful as flame retardants (International Publication No. 2013/047342 pamphlet).
  • the amine compound means a compound having an amino group in the chemical structure, and the amino group is preferably the NR 1 R 2 (same as NR 3 R 4 ).
  • the amine compound preferably has 1 to 12 carbon atoms, more preferably 1 to 8 carbon atoms, and particularly preferably 1 to 6 carbon atoms. When the number of carbon atoms is small, it is preferably 1 to 3.
  • the amine compound is preferably a compound represented by H—NR 1 R 2 , and examples thereof include methylamine, ethylamine, dimethylamine, diethylamine, and ethylmethylamine. Of these, dimethylamine and diethylamine are particularly preferable.
  • R 1 and R 2 have the same meaning as defined in the above formula (1).
  • R 1 and R 2 may form a ring as defined above, and preferred examples thereof are the same as those exemplified as the ring formed by R 1 and R 2 of the amino-substituted phosphazene. is there.
  • a basic compound In this reaction, an equivalent amount of hydrogen fluoride is generated after substitution.
  • a basic compound In order to neutralize the generated hydrogen fluoride, a basic compound may be added.
  • the basic compound to be added includes organic and inorganic compounds, and an organic base is particularly preferable. Examples of the organic base include triethylamine and diisopropylethylamine.
  • the amine used for substitution may be used for neutralization.
  • a catalyst having a good trapping property of fluorine anion may be used, and the reaction may be terminated in a form in which the catalyst is incorporated into the catalyst.
  • a Lewis acid catalyst is applied to the synthesis reaction.
  • “Lewis acid” refers to a substance that can accept an electron pair.
  • the metal or metalloid (M) contained in the compound constituting the Lewis acid catalyst aluminum, magnesium, lithium, manganese, iron, copper, zinc, tin, boron, silicon, titanium, zirconium, chromium, cobalt, nickel,
  • metals or metalloids are aluminum, magnesium, lithium, manganese, iron, copper, zinc, tin, boron, silicon, titanium, zirconium, chromium, cobalt, nickel, molybdenum, vanadium.
  • aluminum, magnesium, lithium, iron, copper (II), zinc, boron, silicon are more preferable, aluminum, magnesium, lithium, iron, copper (II), boron, silicon are more preferable, aluminum, magnesium, lithium, Iron and copper are particularly preferable.
  • the Lewis acid catalyst is preferably composed of a compound having at least one MZ bond.
  • M is a metal or metalloid atom, and preferred ones are as defined above.
  • Z is a halogen atom, a sulfonate moiety (such as a trifluoromethanesulfonate moiety), an acylate moiety (acetate moiety), a sulfuric acid moiety, or a nitric acid moiety.
  • Z is preferably a halogen atom, preferably iodine, bromine, or chlorine, more preferably bromine or chlorine, and particularly preferably chlorine.
  • Lewis acids include BF 3 OEt 2 , AlBr 3 , AlCl 3 , ZnI 2 , MgCl 2 , LiCl, LiBr, SnCl 4 , CuCl 2 , FeCl 2 , FeCl 3 , ZnCl 2 , silyl chloride compound, MnCl 2 , CoCl 2 , NiCl 2, ZrOCl 2, ZrCl 4 , SrCl 2, InCl 3, HfOCl 2, GaCl 3, EtAlCl 2, BiCl 3, TiCl 4, GeCl 4, SbCl 3, FeBr 3, VCl 3, MoCl 5, BCl 3, BBr 3 , Cu (OTf) 2 , Ln (OTf) 3 , Fe 2 (SO 4 ) 3 , ZrCl 4 , Zr (SO 4 ) 2 , ZnSO 4 , Fe (NO 3 ) 3 , Ni (NO 3 ) 2 , Mg ( OAc) 2, Fe (
  • AlBr 3 , AlCl 3 , ZnI 2 , MgCl 2 , LiCl, LiBr, SnCl 4 , CuCl 2 , FeCl 3 , ZnCl 2 , silyl chloride compound, MnCl 2 , CoCl 2 , NiCl 2 , ZrOCl 2, ZrCl 4, EtAlCl 2 , TiCl 4, FeBr 3, VCl 3, MoCl 5, BCl 3, BBr 3 are preferred, AlBr 3, AlCl 3, MgCl 2, LiCl, LiBr, CuCl 2, FeCl 3, ZnCl 2 , silyl chloride compounds, ZrCl 4, ZrOCl 2, EtAlCl 2, FeBr 3, more preferably BCl 3, AlCl 3, MgCl 2 , LiCl, LiBr, CuCl 2, FeCl 3, ZrCl 4, ZrOCl 2, silyl chloride of Things, more preferably BCl 3, AlCl 3, M
  • the silyl chloride compound is a general term for compounds having a Si—Cl bond, and is preferably (R S ) ns Si (Cl) 4-ns .
  • R S is an alkyl group (preferably having 1 to 12 carbon atoms, more preferably 1 to 6 carbon atoms, particularly preferably 1 to 3 carbon atoms) or an alkenyl group (preferably having 2 to 12 carbon atoms, more preferably 2 to 6 carbon atoms). ), An aryl group (preferably having 6 to 22 carbon atoms, more preferably 6 to 14 carbon atoms, and particularly preferably 6 to 10 carbon atoms), and particularly preferably an alkyl group.
  • a plurality of R S may be the same or different.
  • ns is an integer of 0 to 3, preferably 2 or 3.
  • SiCl 4 , Me 2 SiCl 2 , TMS-Cl, TES-Cl, PhSiCl 3 , divinyldichlorosilane, and methylvinyldichlorosilane are preferable, and SiCl 4 , Me 2 SiCl 2 , TMS-Cl are preferable.
  • OTf represents a trifluoromethanesulfonate site
  • OAc represents an acetate site.
  • Me represents a methyl group.
  • Et represents an ethyl group.
  • Ph represents a phenyl group.
  • Ac represents an acetyl group.
  • TMS represents a trimethylsilyl group.
  • TES represents a triethylsilyl group.
  • Lewis acid only one Lewis acid may be used, or two or more Lewis acids may be used.
  • the use amount of the Lewis acid catalyst is preferably 0.01 equivalents or more, more preferably 0.05 equivalents or more, and more preferably 0.2 equivalents or more with respect to the fluorinated phosphazene compound as a starting material from the viewpoint of cost. More preferred is 0.25 equivalent or more.
  • the upper limit is preferably 5 equivalents or less, more preferably 3 equivalents or less, still more preferably 2 equivalents or less, and particularly preferably 1 equivalent or less.
  • the amount of the Lewis acid catalyst used is preferably 0.01 to 5 equivalents and 0.05 to 3 equivalents relative to the fluorinated phosphazene compound as the starting material in terms of the upper and lower limits. More preferably, it is 0.2 equivalents to 3 equivalents, still more preferably 0.2 equivalents to 2 equivalents, and particularly preferably 0.25 equivalents to 1 equivalent.
  • the temperature of this reaction is preferably ⁇ 20 ° C. or higher, more preferably ⁇ 15 ° C. or higher, and particularly preferably ⁇ 10 ° C. or higher from the viewpoint of production efficiency.
  • the upper limit is preferably 100 ° C. or lower, more preferably 60 ° C. or lower, and particularly preferably 50 ° C. or lower.
  • the reaction time is preferably within 24 hours, more preferably within 10 hours, further preferably within 5 hours, and particularly preferably within 3 hours. After completion of the reaction, purification such as separation or distillation is performed as necessary.
  • reaction solvent may or may not be used, but it is preferable to use this.
  • solvent to be used those commonly used for this kind of reaction can be appropriately selected and used. For example, acetonitrile etc. are mentioned.
  • the amino-substituted phosphazene compound obtained by the production method of the present invention can be used for various applications. For example, it can be applied as a flame retardant for resins, electrolytes, lubricants, paints and the like applied to various electrical equipment and industrial products. Alternatively, it can also be used as an insecticide (see German Offenlegungsschrift 213991). Recently, the use of non-aqueous secondary batteries is one of the high needs. Below, the outline is demonstrated about preferable embodiment at the time of applying to a non-aqueous secondary battery.
  • alkyl group preferably an alkyl group having 1 to 20 carbon atoms, such as methyl, ethyl, isopropyl, t-butyl, pentyl, heptyl, 1-ethylpentyl, benzyl, 2-ethoxyethyl, 1-carboxymethyl, etc.
  • alkenyl A group preferably an alkenyl group having 2 to 20 carbon atoms such as vinyl, allyl, oleyl and the like
  • an alkynyl group preferably an alkynyl group having 2 to 20 carbon atoms such as ethynyl, butadiynyl, phenylethynyl and the like
  • a cycloalkyl group preferably a cycloalkyl group having 3 to 20 carbon atoms, such as cyclopropyl, cyclopentyl, cyclohexyl, 4-methylcyclohexyl, etc., but the alkyl
  • Aryloxy groups such as phenoxy, 1-naphthylo Si, 3-methylphenoxy, 4-methoxyphenoxy, etc.
  • alkoxycarbonyl groups preferably alkoxycarbonyl groups having 2 to 20 carbon atoms, such as ethoxycarbonyl, 2-ethylhexyloxycarbonyl, etc.
  • aryloxycarbonyl groups preferably Is an aryloxycarbonyl group having 6 to 26 carbon atoms, such as phenoxycarbonyl, 1-naphthyloxycarbonyl, 3-methylphenoxycarbonyl, 4-methoxyphenoxycarbonyl, etc., an amino group (preferably having 0 to 20 carbon atoms)
  • alkylamino group, arylamino group for example, amino, N, N-dimethylamino, N, N-diethylamino, N-ethylamino, anilino, etc.
  • sulfamoyl group preferably having 0 to 20
  • Phosphinyl groups such as —P (R P ) 2 ), (meth) acryloyl groups, (meth) acryloyloxy groups, (meth) acryloylimimino groups ((meth) acrylamido groups), hydroxyl groups, thiol groups, carboxyl groups , Phosphoric acid group, phosphonic acid group, sulfonic acid group, cyano group, halogen atom (eg fluorine atom, chlorine atom, bromine atom, iodine atom) Is mentioned.
  • each of the groups listed as the substituent T may be further substituted with the substituent T described above.
  • the salt may be formed.
  • a compound or a substituent / linking group includes an alkyl group / alkylene group, an alkenyl group / alkenylene group, an alkynyl group / alkynylene group, etc., these may be cyclic or linear, and may be linear or branched These may be substituted as described above or may be unsubstituted.
  • Each substituent defined in the present specification may be substituted through the following linking group L within the scope of the effects of the present invention, or the linking group L may be present in the structure thereof.
  • the alkyl group / alkylene group, alkenyl group / alkenylene group and the like may further have the following hetero-linking group interposed in the structure.
  • the linking group L includes a hydrocarbon linking group [an alkylene group having 1 to 10 carbon atoms (more preferably 1 to 6 carbon atoms, more preferably 1 to 3 carbon atoms), an alkenylene group having 2 to 10 carbon atoms (more preferably carbon atoms).
  • the said hydrocarbon coupling group may form the double bond and the triple bond suitably, and may connect.
  • the ring to be formed is preferably a 5-membered ring or a 6-membered ring.
  • a nitrogen-containing five-membered ring is preferable, and examples of the compound forming the ring include pyrrole, imidazole, pyrazole, indazole, indole, benzimidazole, pyrrolidine, imidazolidine, pyrazolidine, indoline, carbazole, or these And derivatives thereof.
  • 6-membered ring examples include piperidine, morpholine, piperazine, and derivatives thereof. Moreover, when an aryl group, a heterocyclic group, etc. are included, they may be monocyclic or condensed and may be similarly substituted or unsubstituted.
  • RN is a hydrogen atom or a substituent. Examples of the substituent include an alkyl group (preferably having 1 to 24 carbon atoms, more preferably 1 to 12 carbon atoms, further preferably 1 to 6 carbon atoms, and particularly preferably 1 to 3 carbon atoms), and an alkenyl group (preferably having 2 to 24 carbon atoms and 2 carbon atoms).
  • To 12 is more preferable, 2 to 6 is more preferable, and 2 to 3 is particularly preferable, and an alkynyl group (2 to 24 carbon atoms is preferable, 2 to 12 is more preferable, 2 to 6 is more preferable, and 2 to 3 is Particularly preferred), an aralkyl group (preferably 7 to 22 carbon atoms, more preferably 7 to 14 carbon atoms, particularly preferably 7 to 10 carbon atoms), an aryl group (preferably 6 to 22 carbon atoms, more preferably 6 to 14 carbon atoms, 6 to 14 carbon atoms). 10 is particularly preferred).
  • RP is a hydrogen atom, a hydroxyl group, or a substituent.
  • substituents examples include an alkyl group (preferably having 1 to 24 carbon atoms, more preferably 1 to 12 carbon atoms, further preferably 1 to 6 carbon atoms, and particularly preferably 1 to 3 carbon atoms), and an alkenyl group (preferably having 2 to 24 carbon atoms and 2 carbon atoms).
  • To 12 is more preferable, 2 to 6 is more preferable, and 2 to 3 is particularly preferable, and an alkynyl group (2 to 24 carbon atoms is preferable, 2 to 12 is more preferable, 2 to 6 is more preferable, and 2 to 3 is Particularly preferred), an aralkyl group (preferably 7 to 22 carbon atoms, more preferably 7 to 14 carbon atoms, particularly preferably 7 to 10 carbon atoms), an aryl group (preferably 6 to 22 carbon atoms, more preferably 6 to 14 carbon atoms, 6 to 14 carbon atoms).
  • an alkoxy group preferably having 1 to 24 carbon atoms, more preferably 1 to 12, more preferably 1 to 6 and particularly preferably 1 to 3
  • an alkenyloxy group having carbon number
  • More preferably 2 to 12, more preferably 2 to 6, particularly preferably 2 to 3, and an alkynyloxy group preferably having 2 to 24 carbon atoms, more preferably 2 to 12 and more preferably 2 to 6.
  • More preferably, 2 to 3 are particularly preferred
  • an aralkyloxy group preferably 7 to 22 carbon atoms, more preferably 7 to 14 carbon atoms, particularly preferably 7 to 10 carbon atoms
  • an aryloxy group preferably 6 to 22 carbon atoms, 6 to 14 are more preferable, and 6 to 10 are particularly preferable.
  • the number of atoms constituting the linking group L is preferably 1 to 36, more preferably 1 to 24, still more preferably 1 to 12, and particularly preferably 1 to 6.
  • the number of linking atoms in the linking group is preferably 10 or less, and more preferably 8 or less.
  • the lower limit is 1 or more.
  • the number of connected atoms refers to the minimum number of atoms that are located in a path connecting predetermined structural portions and are involved in the connection. For example, in the case of —CH 2 —C ( ⁇ O) —O—, the number of atoms constituting the linking group is 6, but the number of linking atoms is 3. Specific examples of combinations of linking groups include the following.
  • x is an integer of 1 or more, preferably 1 to 500, 1 to 100 is more preferable.
  • Lr is preferably an alkylene group, an alkenylene group or an alkynylene group.
  • the carbon number of Lr is preferably 1 to 12, more preferably 1 to 6, and particularly preferably 1 to 3.
  • a plurality of Lr, R N , R P , x, etc. need not be the same.
  • the direction of the linking group is not limited by the above description, and may be understood as appropriate according to a predetermined chemical formula.
  • substituents or linking groups when there are a plurality of substituents or linking groups indicated by a specific symbol, or when a plurality of substituents etc. (same definition of the number of substituents) are specified simultaneously or alternatively,
  • the substituents and the like may be the same as or different from each other.
  • substituents or linking groups When a plurality of substituents or linking groups are adjacent to each other, they may be bonded to each other or condensed to form a ring.
  • Electrodes An electrolyte solution for a non-aqueous secondary battery is applied to the non-aqueous secondary battery of this embodiment.
  • the electrolyte used for the electrolytic solution is preferably a salt of a metal ion belonging to Group 1 or Group 2 of the periodic table.
  • the material is appropriately selected depending on the intended use of the electrolytic solution. For example, lithium salt, potassium salt, sodium salt, calcium salt, magnesium salt and the like can be mentioned. When used in a secondary battery or the like, lithium salt is preferable from the viewpoint of output.
  • the amino-substituted phosphazene compound produced by the production method of the present invention is used as a non-aqueous electrolyte for a lithium secondary battery, it is preferable to select a lithium salt as the metal ion salt.
  • the lithium salt is preferably a lithium salt usually used for an electrolyte of a non-aqueous electrolyte solution for a lithium secondary battery, and is not particularly limited. For example, those described below are preferable.
  • Inorganic lithium salts inorganic fluoride salts such as LiPF 6 , LiBF 4 , LiAsF 6 , LiSbF 6 ; perhalogenates such as LiClO 4 , LiBrO 4 , LiIO 4 ; inorganic chloride salts such as LiAlCl 4 etc.
  • (L-3) Oxalatoborate salt lithium bis (oxalato) borate, lithium difluorooxalatoborate and the like.
  • Rf 1 and Rf 2 each represent a perfluoroalkyl group.
  • the electrolyte used for electrolyte solution may be used individually by 1 type, or may combine 2 or more types arbitrarily.
  • the electrolyte in the electrolytic solution (preferably a metal ion belonging to Group 1 or Group 2 of the periodic table or a metal salt thereof) is added in an amount so as to obtain a preferable salt concentration described below in the method for preparing the electrolytic solution. It is preferable.
  • the salt concentration is appropriately selected depending on the intended use of the electrolytic solution, but is generally 10% to 50% by mass, more preferably 15% to 30% by mass, based on the total mass of the electrolytic solution.
  • the molar concentration is preferably 0.5M to 1.5M.
  • concentration what is necessary is just to calculate by salt conversion with the metal applied suitably.
  • Non-aqueous solvent As the non-aqueous solvent used in the electrolytic solution of the present embodiment, those commonly used for this type of product can be appropriately selected and applied. Among these, it is preferable to select an aprotic solvent having high ion conductivity.
  • the manufacturing method of the electrolyte solution for non-aqueous secondary batteries of this invention can be implemented by preparing the electrolyte solution for non-aqueous secondary batteries containing this through the manufacturing method of the said amino substituted phosphazene compound. .
  • each component is prepared by a conventional method by dissolving the above components in the non-aqueous electrolyte solvent, including an example in which a lithium salt is used as a metal ion salt.
  • a lithium ion secondary battery according to a preferred embodiment of the present invention includes a nonaqueous secondary battery electrolyte according to the present invention and a positive electrode (positive electrode current collector, positive electrode active material layer) capable of inserting and releasing lithium ions. And a negative electrode (negative electrode current collector, negative electrode active material layer) capable of inserting and releasing lithium ions or dissolving and depositing lithium ions.
  • the separator may be configured to be disposed between the positive electrode and the negative electrode, a current collecting terminal, and an outer case. .
  • a protective element may be attached to at least one of the inside of the battery and the outside of the battery.
  • the active material is a positive electrode active material. It is preferable to use a negative electrode mixture in which the positive electrode mixture and the active material are a negative electrode active material.
  • each component in the dispersion (electrode composition) constituting the electrode mixture will be described.
  • a lithium-containing transition metal oxide for the positive electrode active material.
  • a transition element M a one or more elements selected from Co, Ni, Fe, Mn, Cu, V
  • mixed element M b elements of the first (Ia) group of the metal periodic table other than lithium, elements of the second (IIa) group, Al, Ga, In, Ge, Sn, Pb, Sb, Bi, Si , P, B, etc.
  • elements of the second (IIa) group Al, Ga, In, Ge, Sn, Pb, Sb, Bi, Si , P, B, etc.
  • lithium-containing transition metal oxide examples include specific transition metal oxides including those represented by any of the following formulas (MA) to (MC), or other transition metal oxides such as V 2 O 5 , MnO. 2 etc. are mentioned.
  • the positive electrode active material a particulate positive electrode active material may be used. Specifically, a transition metal oxide capable of reversibly inserting and releasing lithium ions can be used, but the specific transition metal oxide is preferably used.
  • Examples of the lithium-containing transition metal oxides, oxides containing the above transition element M a is preferably exemplified.
  • a mixed element M b (preferably Al) or the like may be mixed.
  • the mixing amount is preferably 0 to 30 mol% with respect to the amount of the transition metal. That the molar ratio of li / M a was synthesized were mixed so that 0.3 to 2.2, more preferably.
  • M 1 is as defined above Ma.
  • a represents 0 to 1.2, preferably 0.1 to 1.15, and more preferably 0.6 to 1.1.
  • b represents 1 to 3 and is preferably 2.
  • a part of M 1 may be substituted with the mixed element M b .
  • the transition metal oxide represented by the above formula (MA) typically has a layered rock salt structure.
  • transition metal compound examples include LiCoO 2 (lithium cobaltate [LCO]), LiNi 2 O 2 (lithium nickelate) LiNi 0.85 Co 0.01 Al 0.05 O 2 (nickel cobalt aluminum acid Lithium [NCA]), LiNi 0.33 Co 0.33 Mn 0.33 O 2 (lithium nickel manganese cobaltate [NMC]), LiNi 0.5 Mn 0.5 O 2 (lithium manganese nickelate).
  • M 2 is as defined above Ma.
  • c represents 0 to 2, preferably 0.1 to 1.15, and more preferably 0.6 to 1.5.
  • d represents 3 to 5 and is preferably 4.
  • Specific examples of the transition metal compound are LiMn 2 O 4 and LiMn 1.5 Ni 0.5 O 4 .
  • Preferred examples of the transition metal oxide represented by the formula (MB) include those represented by the following.
  • an electrode containing Ni is more preferable from the viewpoint of high capacity and high output.
  • Transition metal oxide represented by formula (MC) As the lithium-containing transition metal oxide, it is also preferable to use a lithium-containing transition metal phosphor oxide, and among them, one represented by the following formula (MC) is also preferable. Li e M 3 (PO 4 ) f ... (MC)
  • e 0 to 2, preferably 0.1 to 1.15, and more preferably 0.5 to 1.5.
  • f represents 1 to 5, and preferably 0.5 to 2.
  • the M 3 represents one or more elements selected from V, Ti, Cr, Mn, Fe, Co, Ni, and Cu.
  • the M 3 are, in addition to the mixing element M b above, Ti, Cr, Zn, Zr, may be substituted by other metals such as Nb.
  • Specific examples include, for example, olivine-type iron phosphates such as LiFePO 4 and Li 3 Fe 2 (PO 4 ) 3 , iron pyrophosphates such as LiFeP 2 O 7 , cobalt phosphates such as LiCoPO 4 , and Li 3.
  • Monoclinic Nasicon type vanadium phosphate salts such as V 2 (PO 4 ) 3 (lithium vanadium phosphate) can be mentioned.
  • the a, c, e values representing the composition of Li are values that change due to charge / discharge, and are typically evaluated as values in a stable state when Li is contained.
  • the composition of Li is shown as a specific value, but this also varies depending on the operation of the battery.
  • particularly preferable positive electrode active materials include the following.
  • LiNi 0.33 Co 0.33 Mn 0.33 O 2 LiNi 0.6 Co 0.2 Mn 0.2 O 2 LiNi 0.5 Co 0.3 Mn 0.2 O 2 LiNi 0.5 Mn 0.5 O 2 LiNi 0.5 Mn 1.5 O 4 Since these can be used at a high potential, the battery capacity can be increased, and even when used at a high potential, the capacity retention rate is high, which is particularly preferable.
  • the average particle diameter of the positive electrode active material used is not particularly limited, but is preferably 0.1 ⁇ m to 50 ⁇ m.
  • the specific surface area is not particularly limited, but is preferably 0.01 m 2 / g to 50 m 2 / g by the BET method.
  • the pH of the supernatant when 5 g of the positive electrode active material is dissolved in 100 ml of distilled water is preferably 7 or more and 12 or less.
  • the blending amount of the positive electrode active material is not particularly limited, but is preferably 60 to 98% by mass, and 70 to 95% by mass in 100% by mass of the solid component in the dispersion (mixture) for constituting the active material layer. % Is more preferable.
  • Negative electrode active material As the negative electrode active material, those capable of reversibly inserting and releasing lithium ions are preferable, and there is no particular limitation. Carbonaceous materials, metal oxides such as tin oxide and silicon oxide, metal composite oxides, lithium Examples thereof include a single alloy and a lithium alloy such as a lithium aluminum alloy and a metal capable of forming an alloy with lithium such as Sn or Si.
  • carbonaceous materials or lithium composite oxides are preferably used from the viewpoint of reliability.
  • metal complex oxide what can occlude and discharge
  • the carbonaceous material used as the negative electrode active material is a material substantially made of carbon.
  • Examples thereof include carbonaceous materials obtained by firing artificial graphite such as petroleum pitch, natural graphite, and vapor-grown graphite, and various synthetic resins such as polyacrylonitrile resin and furfuryl alcohol resin.
  • various carbon fibers such as polyacrylonitrile-based carbon fiber, cellulose-based carbon fiber, pitch-based carbon fiber, vapor-grown carbon fiber, dehydrated polyvinyl alcohol-based carbon fiber, lignin carbon fiber, glassy carbon fiber, activated carbon fiber, Examples thereof include mesophase microspheres, graphite whiskers, and flat graphite.
  • amorphous oxide is particularly preferable, and chalcogenite, which is a reaction product of a metal element and an element of Group 16 of the periodic table, is also preferably used.
  • preferable amorphous oxides and chalcogenides include, for example, Ga 2 O 3 , SiO, GeO, SnO, SnO 2 , PbO, PbO 2 , Pb 2 O 3 , Pb 2 O 4 , Pb 3 O 4 , Sb 2 O 3 , Sb 2 O 4 , Sb 2 O 5 , Bi 2 O 3 , Bi 2 O 4 , SnSiO 3 , GeS, SnS, SnS 2 , PbS, PbS 2 , Sb 2 S 3 , Sb 2 S 5 , such as SnSiS 3 may preferably be mentioned.
  • these may be a complex oxide with lithium oxide, for example, Li 2 SnO 2 .
  • the average particle diameter of the negative electrode active material is preferably 0.1 ⁇ m to 60 ⁇ m.
  • Examples of the negative electrode active material that can be used in combination with the amorphous oxide negative electrode active material centering on Sn, Si, and Ge include carbon materials that can occlude and release lithium ions or lithium metal, lithium, lithium alloys, lithium A metal that can be alloyed with is preferable.
  • the amount of the negative electrode active material in the dispersion (mixture) forming the electrode mixture is not particularly limited, but it is preferably 60 to 98% by mass, and 70 to 95% by mass in 100% by mass of the solid component. Is more preferable.
  • the conductive material is preferably an electron conductive material that does not cause a chemical change in the configured secondary battery, and a known conductive material can be arbitrarily used.
  • natural graphite scale-like graphite, scale-like graphite, earth-like graphite, etc.
  • artificial graphite carbon black, acetylene black, ketjen black, carbon fiber and metal powder (copper, nickel, aluminum, silver (Japanese Patent Laid-Open No. Sho 63-63)) 148, 554), etc.
  • conductive fibers such as metal fibers or polyphenylene derivatives (described in JP-A-59-20971) can be included as a single kind or a mixture thereof.
  • the addition amount of the conductive material is preferably 1 to 50% by mass, and more preferably 2 to 30% by mass. In the case of carbon or graphite, 2 to 15% by mass is particularly preferable.
  • binders include polysaccharides, thermoplastic resins, and polymers having rubber elasticity. Among them, polyacrylate ester latex, carboxymethylcellulose, polytetrafluoroethylene, and polyvinylidene fluoride are included. More preferable.
  • Binders can be used alone or in combination of two or more.
  • the amount of the binder added is small, the holding power and cohesive force of the electrode mixture are weakened. If the amount is too large, the electrode volume increases and the capacity per electrode unit volume or unit mass decreases. For this reason, the addition amount of the binder is preferably 1 to 30% by mass, and more preferably 2 to 10% by mass.
  • the electrode compound material may contain the filler.
  • the material forming the filler is preferably a fibrous material that does not cause a chemical change in the secondary battery of the present invention.
  • fibrous fillers made of materials such as olefin polymers such as polypropylene and polyethylene, glass, and carbon are used.
  • the addition amount of the filler is not particularly limited, but is preferably 0 to 30% by mass in the dispersion.
  • the positive / negative electrode current collector an electron conductor that does not cause a chemical change in the nonaqueous electrolyte secondary battery of the present invention is used.
  • the current collector for the positive electrode in addition to aluminum, stainless steel, nickel, titanium and the like, those obtained by treating the surface of aluminum or stainless steel with carbon, nickel, titanium or silver are preferable. Those whose surfaces are treated with carbon, nickel, titanium or silver are preferred.
  • the negative electrode current collector aluminum, copper, copper alloy, stainless steel, nickel and titanium are preferable, and aluminum, copper and copper alloy are more preferable.
  • a film sheet shape is usually used, but a net, a punched material, a lath body, a porous body, a foamed body, a molded body of a fiber group, and the like can also be used.
  • the thickness of the current collector is not particularly limited, but is preferably 1 ⁇ m to 500 ⁇ m.
  • the current collector surface is roughened by surface treatment.
  • An electrode mixture of the lithium secondary battery is formed by a member appropriately selected from these materials.
  • the separator used in the non-aqueous secondary battery of the present invention is made of a material that mechanically insulates the positive electrode and the negative electrode, has ion permeability, and has oxidation / reduction resistance at the contact surface between the positive electrode and the negative electrode.
  • a material a porous polymer material, an inorganic material, an organic-inorganic hybrid material, glass fiber, or the like is used.
  • These separators preferably have a shutdown function for ensuring reliability, that is, a function of closing a gap at 80 ° C. or higher to increase resistance and blocking current, and a closing temperature is 90 ° C. or higher and 180 ° C. or lower. It is preferable.
  • the shape of the holes of the separator is usually circular or elliptical, and the size is 0.05 ⁇ m to 30 ⁇ m, preferably 0.1 ⁇ m to 20 ⁇ m. Furthermore, it may be a rod-like or irregular-shaped hole as in the case of making by a stretching method or a phase separation method.
  • the ratio of these gaps, that is, the porosity, is 20% to 90%, preferably 35% to 80%.
  • the polymer material may be a single material such as a cellulose nonwoven fabric, polyethylene, or polypropylene, or may be a material using two or more composite materials. What laminated
  • the inorganic material examples include oxides such as alumina and silicon dioxide, nitrides such as aluminum nitride and silicon nitride, and sulfates such as barium sulfate and calcium sulfate, and those having a particle shape or fiber shape are used.
  • oxides such as alumina and silicon dioxide
  • nitrides such as aluminum nitride and silicon nitride
  • sulfates such as barium sulfate and calcium sulfate
  • those having a particle shape or fiber shape are used.
  • a thin film shape such as a non-woven fabric, a woven fabric, or a microporous film is used.
  • the thin film shape those having a pore diameter of 0.01 ⁇ m to 1 ⁇ m and a thickness of 5 ⁇ m to 50 ⁇ m are preferably used.
  • a separator formed by forming a composite porous layer containing the inorganic particles on the surface layer of the positive electrode and / or the negative electrode using a resin binder can be used.
  • alumina particles having a 90% particle diameter of less than 1 ⁇ m are formed on both surfaces of the positive electrode as a porous layer using a fluororesin binder.
  • the shape of the nonaqueous secondary battery of the present invention can be applied to any shape such as a sheet shape, a square shape, and a cylinder shape.
  • a positive electrode active material or a mixture of negative electrode active materials is mainly used after being applied (coated), dried and compressed on a current collector.
  • the selection and design of each member and the assembly thereof may be performed by a regular method, and general techniques of this type of product can be applied as appropriate.
  • Example 1 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile were charged, and 21.33 g (0.16 mol) of aluminum chloride was cooled while cooling in an ice / methanol bath. Small portions were added. Next, 21.64 g (0.48 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at ⁇ 10 ° C. to 0 ° C.
  • Example 2 Under a nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile are charged into a 500 mL three-necked flask, and 15.23 g (0.16 mol) of magnesium chloride is added little by little while cooling in an ice bath. Added. Next, 21.64 g (0.48 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C. Next, the reaction was carried out for 2 hours while heating to an internal temperature of 45 to 50 ° C.
  • Example 3 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile were charged, and 29.95 g (0) of iron (III) trichloride was cooled in an ice / methanol bath. .16 mol) was added in small portions. At ⁇ 10 ° C. to 0 ° C., 35.11 g (0.48 mol) of diethylamine (Wako Pure Chemical Industries, Ltd.) was added dropwise. Next, the reaction was carried out for 2 hours while heating to an internal temperature of 45 to 50 ° C.
  • Example 4 Under a nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile are charged into a 500 mL three-necked flask, and a small amount of 13.90 g (0.16 mol) of lithium bromide is cooled in an ice bath. Added in increments. Next, 14.43 g (0.32 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C.
  • reaction was carried out for 2 hours while heating to an internal temperature of 45 to 50 ° C.
  • the progress of the reaction was confirmed by 19F-NMR using monofluorinated benzene as an internal standard.
  • the reaction conversion rate was 96%, and no disubstituted product was confirmed.
  • 38.49 g of a colorless and transparent compound (1-1) was obtained with a yield of 88% by liquid separation or vacuum distillation purification. Further, when the purity was confirmed by gas chromatography, the purity was 99.99% or more.
  • Example 5 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile are charged, and 10.4 g (0.08 mol) of dichlorodimethylsilane is cooled in an ice bath. Added in increments. Next, 14.43 g (0.32 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C. Next, the reaction was carried out for 0.5 hours while maintaining the internal temperature at 5 ° C.
  • Example 6 Under a nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (manufactured by Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile were charged into a 500 mL three-necked flask and cooled with an ice / methanol bath, 21.51 g of copper chloride (II). 16 mol) was added in small portions. Next, 21.64 g (0.48 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at ⁇ 10 ° C. to 0 ° C.
  • reaction was carried out for 2 hours while heating to an internal temperature of 45 to 50 ° C.
  • the reaction conversion rate was 94%, and no disubstituted product was confirmed.
  • 39.00 g of colorless and transparent compound (1-1) was obtained with a yield of 89% by liquid separation or vacuum distillation purification. Further, when the purity was confirmed by gas chromatography, the purity was 99.99% or more.
  • Example 7 When the reaction was carried out by replacing the copper (II) chloride of Example 6 with boron trichloride, the compound (1-1) was similarly obtained with a high reaction conversion rate.
  • Example 8 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile are charged, and 17.38 g (0.08 mol) of trimethylchlorosilane is added little by little while cooling in an ice bath. Added. Next, 14.43 g (0.32 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C. Next, the reaction was carried out for 0.5 hours while maintaining the internal temperature at 5 ° C.
  • Example 9 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 42 mL of acetonitrile were charged, and 7.11 g (0.053 mol) of aluminum chloride was cooled while cooling in an ice / methanol bath. Small portions were added. Next, 14.43 g (0.32 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at ⁇ 10 ° C. to 0 ° C. at a rate of 0.3 g / min.
  • reaction was carried out for 2 hours while heating to an internal temperature of 45 to 50 ° C.
  • the reaction conversion rate was 98%, and no disubstituted product was confirmed.
  • 38.23 g of a colorless and transparent compound (1-1) was obtained with a yield of 87% by liquid separation or vacuum distillation purification. Further, when the purity was confirmed by gas chromatography, the purity was 99.99% or more.
  • Example 10 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 42 mL of acetonitrile were charged, and 7.65 g (0.08 mol) of magnesium chloride was added in small portions while cooling in an ice bath. Added. Next, 14.43 g (0.32 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C. Next, the reaction was carried out for 1 hour while maintaining the internal temperature at 0 ° C.
  • Example 11 Under a nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 42 mL of acetonitrile are charged into a 500 mL three-necked flask and cooled in an ice / methanol bath, 13.90 g (0.16 mol) of lithium bromide. Was added in small portions. Next, 14.43 g (0.32 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at ⁇ 10 ° C. to 0 ° C. at a rate of 0.3 g / min.
  • dimethylamine gas manufactured by Aldrich
  • reaction was carried out for 1 hour while maintaining the internal temperature at ⁇ 10 ° C.
  • the progress of the reaction was confirmed by 19F-NMR using monofluorinated benzene as an internal standard.
  • the reaction conversion rate was 95%, and no disubstituted product was confirmed.
  • 38.93 g of a colorless and transparent compound (1-1) was obtained with a yield of 89% by liquid separation or vacuum distillation purification. Further, when the purity was confirmed by gas chromatography, the purity was 99.99% or more.
  • Example 12 In a 500 mL three-necked flask under nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 42 mL of acetonitrile were charged, and 7.65 g (0.08 mol) of magnesium chloride was added in small portions while cooling in an ice bath. Added. Next, 9.93 g (0.32 mol) of monomethylamine gas was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C. Next, the reaction was carried out for 1 hour while maintaining the internal temperature at 0 ° C.
  • Example 13 Under a nitrogen flow, 40.0 g (0.16 mol) of hexafluorophosphazene (product of Tokyo Chemical Industry Co., Ltd.) and 200 mL of acetonitrile are charged into a 500 mL three-necked flask, and 15.3 g (0.16 mol) of magnesium chloride is added little by little while cooling in an ice bath. Added. Next, 19.86 g (0.64 mol) of dimethylamine gas (manufactured by Aldrich) was bubbled at a rate of 0.3 g / min at 0 ° C. to 5 ° C. Next, the reaction was carried out for 2 hours while maintaining the internal temperature at 30 ° C.
  • the progress of the reaction was confirmed by 19F-NMR using monofluorinated benzene as the internal standard. As a result, the reaction conversion rate to the target product was 50%, and 6% of the disubstituted product was produced. In addition, the generation of unidentified by-products could be confirmed.
  • the NMR spectrum is shown in FIG. After completion of the reaction, 18.35 g of a colorless and transparent compound (1-1) was obtained with a yield of 42% by liquid separation or vacuum distillation purification. Further, when the purity was confirmed by gas chromatography, the purity was 99.11%.
  • reaction conversion rate to the target product was 35%, and 9% of the disubstituted product was produced. In addition, the generation of unidentified by-products could be confirmed.
  • 11.4 g of a colorless and transparent compound (c1) was obtained in a yield of 26% by liquid separation or vacuum distillation purification (FIGS. 5-1 and 5-2). Further, when the purity was confirmed by gas chromatography, the purity was 99.35%.
  • the selectivity in Table 1 represents the production rate of the target substitution product in the reaction system.
  • Selectivity (%) [Target substitution product conversion rate / (Target substitution product conversion rate + Other substitution product conversion rate]]
  • Example Compounds 1-7, 1-8, and 1-12 were synthesized using a predetermined amine compound instead of dimethylamine of Example 1. It was confirmed that the target compound was obtained with good yield and selectivity.

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PCT/JP2014/076904 2013-10-11 2014-10-08 アミノ置換ホスファゼン化合物の製造方法、非水二次電池用電解液の製造方法および非水二次電池の製造方法 WO2015053302A1 (ja)

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