CA2251648A1 - Copolymers of vinylidene fluoride and hexafluoropropylene having reduced extractable content and improved solution clarity - Google Patents
Copolymers of vinylidene fluoride and hexafluoropropylene having reduced extractable content and improved solution clarity Download PDFInfo
- Publication number
- CA2251648A1 CA2251648A1 CA002251648A CA2251648A CA2251648A1 CA 2251648 A1 CA2251648 A1 CA 2251648A1 CA 002251648 A CA002251648 A CA 002251648A CA 2251648 A CA2251648 A CA 2251648A CA 2251648 A1 CA2251648 A1 CA 2251648A1
- Authority
- CA
- Canada
- Prior art keywords
- vinylidene fluoride
- copolymers
- hfp
- vdf
- hexafluoropropylene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- BQCIDUSAKPWEOX-UHFFFAOYSA-N 1,1-Difluoroethene Chemical compound FC(F)=C BQCIDUSAKPWEOX-UHFFFAOYSA-N 0.000 title claims abstract description 158
- 229920001577 copolymer Polymers 0.000 title claims abstract description 150
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 title claims abstract description 124
- 239000012632 extractable Substances 0.000 claims abstract description 50
- 239000000178 monomer Substances 0.000 claims abstract description 40
- 238000009826 distribution Methods 0.000 claims abstract description 16
- 229920001519 homopolymer Polymers 0.000 claims abstract description 16
- 230000002902 bimodal effect Effects 0.000 claims abstract description 6
- 229920000642 polymer Polymers 0.000 claims description 96
- 239000002033 PVDF binder Substances 0.000 claims description 30
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 30
- 238000002844 melting Methods 0.000 claims description 19
- 230000008018 melting Effects 0.000 claims description 19
- 239000003792 electrolyte Substances 0.000 claims description 13
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 claims description 12
- 239000002001 electrolyte material Substances 0.000 claims description 12
- 230000006872 improvement Effects 0.000 claims description 5
- 238000010189 synthetic method Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 abstract description 60
- 238000004519 manufacturing process Methods 0.000 abstract description 19
- 238000003786 synthesis reaction Methods 0.000 abstract description 13
- 238000010276 construction Methods 0.000 abstract description 7
- 229920005609 vinylidenefluoride/hexafluoropropylene copolymer Polymers 0.000 abstract description 7
- 238000000034 method Methods 0.000 description 33
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 32
- 239000002904 solvent Substances 0.000 description 29
- 239000003999 initiator Substances 0.000 description 28
- 238000006116 polymerization reaction Methods 0.000 description 27
- 239000012530 fluid Substances 0.000 description 23
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 description 21
- 238000006243 chemical reaction Methods 0.000 description 19
- 230000008569 process Effects 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 239000000839 emulsion Substances 0.000 description 15
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 14
- 230000015572 biosynthetic process Effects 0.000 description 14
- JMMWKPVZQRWMSS-UHFFFAOYSA-N isopropyl acetate Chemical compound CC(C)OC(C)=O JMMWKPVZQRWMSS-UHFFFAOYSA-N 0.000 description 13
- 239000000463 material Substances 0.000 description 13
- 150000003839 salts Chemical class 0.000 description 13
- 239000007787 solid Substances 0.000 description 13
- 239000008367 deionised water Substances 0.000 description 12
- 229910021641 deionized water Inorganic materials 0.000 description 12
- 235000019439 ethyl acetate Nutrition 0.000 description 12
- 229910052744 lithium Inorganic materials 0.000 description 12
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 12
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 11
- -1 alkali metal salts Chemical class 0.000 description 11
- 238000000113 differential scanning calorimetry Methods 0.000 description 11
- 239000000843 powder Substances 0.000 description 11
- 239000004816 latex Substances 0.000 description 10
- 229920000126 latex Polymers 0.000 description 10
- YKYONYBAUNKHLG-UHFFFAOYSA-N n-Propyl acetate Natural products CCCOC(C)=O YKYONYBAUNKHLG-UHFFFAOYSA-N 0.000 description 10
- 239000007788 liquid Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
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- 239000004094 surface-active agent Substances 0.000 description 7
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 6
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- BGTOWKSIORTVQH-UHFFFAOYSA-N cyclopentanone Chemical compound O=C1CCCC1 BGTOWKSIORTVQH-UHFFFAOYSA-N 0.000 description 6
- XNLICIUVMPYHGG-UHFFFAOYSA-N pentan-2-one Chemical group CCCC(C)=O XNLICIUVMPYHGG-UHFFFAOYSA-N 0.000 description 6
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- XLLIQLLCWZCATF-UHFFFAOYSA-N 2-methoxyethyl acetate Chemical compound COCCOC(C)=O XLLIQLLCWZCATF-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 4
- 229910001290 LiPF6 Inorganic materials 0.000 description 4
- 238000005481 NMR spectroscopy Methods 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
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- YPVDWEHVCUBACK-UHFFFAOYSA-N propoxycarbonyloxy propyl carbonate Chemical compound CCCOC(=O)OOC(=O)OCCC YPVDWEHVCUBACK-UHFFFAOYSA-N 0.000 description 4
- 230000009257 reactivity Effects 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
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- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 3
- 239000004604 Blowing Agent Substances 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 3
- 229910052770 Uranium Inorganic materials 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 3
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- 230000005284 excitation Effects 0.000 description 3
- 230000009477 glass transition Effects 0.000 description 3
- 229940011051 isopropyl acetate Drugs 0.000 description 3
- GWYFCOCPABKNJV-UHFFFAOYSA-N isovaleric acid Chemical compound CC(C)CC(O)=O GWYFCOCPABKNJV-UHFFFAOYSA-N 0.000 description 3
- 229910001416 lithium ion Inorganic materials 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 125000005634 peroxydicarbonate group Chemical group 0.000 description 3
- 239000002006 petroleum coke Substances 0.000 description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000002791 soaking Methods 0.000 description 3
- DHKHKXVYLBGOIT-UHFFFAOYSA-N 1,1-Diethoxyethane Chemical compound CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 description 2
- RFFLAFLAYFXFSW-UHFFFAOYSA-N 1,2-dichlorobenzene Chemical compound ClC1=CC=CC=C1Cl RFFLAFLAYFXFSW-UHFFFAOYSA-N 0.000 description 2
- QURLONWWPWCPIC-UHFFFAOYSA-N 2-(2-aminoethoxy)ethanol;3,6-dichloro-2-methoxybenzoic acid Chemical compound NCCOCCO.COC1=C(Cl)C=CC(Cl)=C1C(O)=O QURLONWWPWCPIC-UHFFFAOYSA-N 0.000 description 2
- VKRSYLVPJNJCNK-UHFFFAOYSA-N C(C=1C(C(=O)OC)=CC=CC1)(=O)OC.C(C)(=O)N(C)C.CC1=CC=CC=C1 Chemical compound C(C=1C(C(=O)OC)=CC=CC1)(=O)OC.C(C)(=O)N(C)C.CC1=CC=CC=C1 VKRSYLVPJNJCNK-UHFFFAOYSA-N 0.000 description 2
- GGVUBHGRFPMLIO-UHFFFAOYSA-N C1=CC=CC=C1.C(CC(C)C)C(=O)CCC(C)C Chemical compound C1=CC=CC=C1.C(CC(C)C)C(=O)CCC(C)C GGVUBHGRFPMLIO-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 229910002097 Lithium manganese(III,IV) oxide Inorganic materials 0.000 description 2
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical group CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 2
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
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- 229910000831 Steel Inorganic materials 0.000 description 2
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 2
- VNDYJBBGRKZCSX-UHFFFAOYSA-L Zinc bromide Inorganic materials Br[Zn]Br VNDYJBBGRKZCSX-UHFFFAOYSA-L 0.000 description 2
- 239000011149 active material Substances 0.000 description 2
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- MDVVHBJPOPLPFR-UHFFFAOYSA-N oxolan-2-one;propan-2-one Chemical compound CC(C)=O.O=C1CCCO1 MDVVHBJPOPLPFR-UHFFFAOYSA-N 0.000 description 2
- JRKICGRDRMAZLK-UHFFFAOYSA-L persulfate group Chemical class S(=O)(=O)([O-])OOS(=O)(=O)[O-] JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 2
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- OHMHBGPWCHTMQE-UHFFFAOYSA-N 2,2-dichloro-1,1,1-trifluoroethane Chemical compound FC(F)(F)C(Cl)Cl OHMHBGPWCHTMQE-UHFFFAOYSA-N 0.000 description 1
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- 230000001419 dependent effect Effects 0.000 description 1
- CSCPPACGZOOCGX-WFGJKAKNSA-N deuterated acetone Substances [2H]C([2H])([2H])C(=O)C([2H])([2H])[2H] CSCPPACGZOOCGX-WFGJKAKNSA-N 0.000 description 1
- SWXVUIWOUIDPGS-UHFFFAOYSA-N diacetone alcohol Natural products CC(=O)CC(C)(C)O SWXVUIWOUIDPGS-UHFFFAOYSA-N 0.000 description 1
- VUPKGFBOKBGHFZ-UHFFFAOYSA-N dipropyl carbonate Chemical compound CCCOC(=O)OCCC VUPKGFBOKBGHFZ-UHFFFAOYSA-N 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000002900 effect on cell Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000011737 fluorine Chemical group 0.000 description 1
- 229910052731 fluorine Chemical group 0.000 description 1
- 229920002313 fluoropolymer Polymers 0.000 description 1
- 239000004811 fluoropolymer Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000013023 gasketing Methods 0.000 description 1
- 239000011245 gel electrolyte Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000000409 membrane extraction Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 125000004123 n-propyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 230000003534 oscillatory effect Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000570 polyether Chemical class 0.000 description 1
- 229920000131 polyvinylidene Polymers 0.000 description 1
- WFRUBUQWJYMMRQ-UHFFFAOYSA-M potassium;1,1,2,2,3,3,4,4,5,5,6,6,7,7,8,8,8-heptadecafluorooctane-1-sulfonate Chemical compound [K+].[O-]S(=O)(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F WFRUBUQWJYMMRQ-UHFFFAOYSA-M 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- XWGJFPHUCFXLBL-UHFFFAOYSA-M rongalite Chemical compound [Na+].OCS([O-])=O XWGJFPHUCFXLBL-UHFFFAOYSA-M 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 229920006126 semicrystalline polymer Polymers 0.000 description 1
- BSWGGJHLVUUXTL-UHFFFAOYSA-N silver zinc Chemical compound [Zn].[Ag] BSWGGJHLVUUXTL-UHFFFAOYSA-N 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000001542 size-exclusion chromatography Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- OPQYOFWUFGEMRZ-UHFFFAOYSA-N tert-butyl 2,2-dimethylpropaneperoxoate Chemical compound CC(C)(C)OOC(=O)C(C)(C)C OPQYOFWUFGEMRZ-UHFFFAOYSA-N 0.000 description 1
- CIHOLLKRGTVIJN-UHFFFAOYSA-N tert‐butyl hydroperoxide Chemical compound CC(C)(C)OO CIHOLLKRGTVIJN-UHFFFAOYSA-N 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
- 229940029284 trichlorofluoromethane Drugs 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229940102001 zinc bromide Drugs 0.000 description 1
Classifications
-
- 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
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/14—Cells with non-aqueous electrolyte
- H01M6/16—Cells with non-aqueous electrolyte with organic electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
- H01M50/426—Fluorocarbon polymers
-
- 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
- H01M10/0565—Polymeric materials, e.g. gel-type or solid-type
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0085—Immobilising or gelification of electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Dispersion Chemistry (AREA)
- General Physics & Mathematics (AREA)
- Inorganic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Cell Separators (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
New and novel copolymers of vinylidene fluoride and hexafluoropropylene containing up to about 24 % by weight hexafluoropropylene having improved solution clarity and fluidity, longer gel times and lower extractables than prior art vinylidine fluoride-hexafluoropropylene copolymers of comparable HFP
content whose syntheses are disclosed in sufficient detail to duplicate, the novel compositions of matter and articles of manufacture containing such copolymers, of the compositions of matter containing such copolymers and of the articles of manufacture containing such copolymers are disclosed. Also disclosed are novel battery constructions based on the novel copolymers of vinylidene fluoride/hexafluoropropylene copolymers of the invention, on vinylidene fluoride homopolymers having a bimodal molecular weight distribution and on vinylidene fluoride/chlorotrifluoroethylene copolymers having a substantially homogeneous monomer distribution.
content whose syntheses are disclosed in sufficient detail to duplicate, the novel compositions of matter and articles of manufacture containing such copolymers, of the compositions of matter containing such copolymers and of the articles of manufacture containing such copolymers are disclosed. Also disclosed are novel battery constructions based on the novel copolymers of vinylidene fluoride/hexafluoropropylene copolymers of the invention, on vinylidene fluoride homopolymers having a bimodal molecular weight distribution and on vinylidene fluoride/chlorotrifluoroethylene copolymers having a substantially homogeneous monomer distribution.
Description
W098/38687 PCT~S98/04071 COPOLYMERS OF VINYLIDENE FLUORIDE AND
HEXAFLUOROPROPYLENE HAVING R~L~
EXTRACTABLE CONTENT AND IMPROVED SOLUTION CLARITY
IR 3490NPl This application claims the benefit of provisional application serial number 60/038,346 filed Feb. 28, 1g97 BACKGROYND OF THE I~Y~NllON
This invention relates to compositions of matter classified in the art of chemistry as fluoropolymers, more specifically as copolymers of vinylidene fluoride (VDF), more specifically as copolymers of vinylidene fluoride and hexafluoropropylene (HFP), still more specifically as copolymers of VDF and HFP having reduced extractable content, longer gel times and improved solution clarity, to novel compositions of matter and articles of manufacture containing such copolymers, as well as to processes for the preparation and use of the copolymers, of compositions of manufacture containing such copolymers and of the , CA 022~1648 1998-10-l~i PCT~S98/04071 articles of manufacture containing such copolymers.
VDF/HFP copolymers are well known and are used for their thermoplastic engineering properties, chemical resistance and inertness toward degradation.
They may be found in applications such as chemically resistant piping, gasketing, plenum cable jacketing, filtration and extraction membranes and in the construction of lithium batteries.
The present invention provides VDF/HFP copolymers containing up to about 24 weight ~ ~12 mole~) HFP
having among other improved properties, substantially improved solution clarity, longer gel times and reduced extractables as these terms are defined hereinafter.
The process used to make the instant copolymers requires one ratio of VDF and HFP for the initial fill of the reactor, and a different ratio of VDF and HFP
during a subsequent continuous feed of the monomers.
Any particular desired average HFP content in the copolymer product has corresponding partlcular initial fill and subsequent feed ratios. The uniformity of compositions prepared this way provide unique and useful properties in comparison to VDF/HFP copolymers described in the prior art.
The present invention also provides lithium batteries fabricated from the VDF/HFP copolymers of the present invention and lithium batteries from other homo and copolymers more specifically described hereinbelow prepared by known processes having analogous structure and which the present inventors CA 022S1648 1998- 10- lS
WO g8/38687 PCT~S98/04071 have recognized as processing properties analogous to ~ those of the VDF/HFP copolymers of the invention which makes them uniquely suitable for lithium battery construction.
nT~rT.oSUp~ OF P~TOR A~T
Rexford in U.S. Pat. No. 3,051,677 described VDF/HFP copolymers of HFP content 30 to 70 wt~ ~15 to 50 mol~) which showed utility as elastomers. To make the copolymers, a batch process with certain initial ratios of VDF and HFP, and a continuous process with fixed ratios of VDF and HFP throughout the process were described. The processes described were such that polymers lacking the improved solution clarity, longer gel times and low extractables of the present invention were made.
Lo in U.S. Pat. No. 3,178,399 described VDF/HFP
copolymers of HFP content of 2 to 26 wt~ (1 to 13 mol~) which showed a numerical value for the product of the tensile strength ~psig) and percent reversible elongation of at least 1,000,000. ~ batch process with certain initial ratios of VDF and HFP, or, alternately, a semicontlnuous process with fixed ratios of V~F and HFP throughout the process were used to make the copolymers. The processes discussed were such that copolymers lacking the improved solution clarity, longer gel times and low extracta~les of the present invention copolymers were made.
Moggi, et al. in Polymer Bulletin 7, 115-122 (1982) analyzed the microstructure and crystal structure of VDF/HFP copolymers by nuclear magnetic W O 98~8687 PCT~S98/04071 - resonance and x-ray diffraction experiments. The copolymers of up to 31 wt~ (up to 16 mol~ HFP were made in a batch emulsion process which was carried only to low conversion. While the low conversion batch process is capable of producing copolymers having solution clarity and low extractables, no such properties are described. It is not a practical process for industrial use because of the low conversions required to make the materials. In addition, no detailed polymerization examples were offered.
Bonardelli et al. in Polymer, vol. 27, 905-gog (June 1986) studied the glass transition temperatures of VDF/HFP copolymers having HFP content up to 62 wt.
(up to 41 mol%). The glass transition temperatures were correlated to the overall HFP content in the copolymers. In making the copolymers for analysis, a semicontinuous emulsion process was used which employed different VDF/HFP ratios for the initial fill of the reactor and for the subsequent continuous feed of monomers. Although reference was made to the use of reactivity ratios to set the VDF/HFP ratio for the initial fill, no detailed polymerization examples were offered, and no mention of copolymers having solution clarity, gel times and low extractables comparable to that of the copolymers of the present invention was made.
Pianca et al. in Polymer, vol. 28, 224-230 (Feb.
1987) examined the microstructure of VDF/HFP
copolymers by nuclear magnetic resonance, and the CA 02251648 1998-10-lS
W098~8~7 PCT~S98/04~71 microstructure determinations were used to explain the trend in glass transition temperatures of the copolymers. The synthesis of the copolymers involved a semicontinuous emulsion process which used different VDF/HFP ratios for the initial fill of the reactor and for the subse~uent continuous feed of monomers. No detailed synthesis examples were provided, and there was no discussion of copolymers having improved solution clarity, longer gel times and low extractables as provided by the copolymers of the present invention.
Abusleme et al. in Eur. Pat. Appl. No. 650,982 Al showed an emulsion process to make polymers and copolymers of fluorinated olefins optionally with one or more non-fluorinated olefins. The process relied on photochemical initiation of polymerization so that lower temperatures and pressures could be used than those used for thermally initiated processes. While there was general mention of the structural regularity of the resulting polymers, the only evidence of regularity concerned poly~vinylidene fluoride) homopolymer, and no claims were made as to regularity of composition. Examples of VDF/HFP copoly~erization were given, but no discussion of the solution extraction properties of the copolymers was given, and there was no relation ~ade between physical properties and the structure of the V~F/HFP copolymers.
Morgan in U.S. Pat. No. 5,543,217 disclosed uniform tetrafluoroethylene/hexafluoropropylene copolymers (TFE/HFP copolymers) made by a PCT~S98/04071 semicontinuous emulsion process. Uniformity was simply defined as there being a low proportion of adjacent ~FP units in the polymer chains; there was no disclosure of the disposition of TFE and HFP units otherwise, and there was no discussion of VDF/HFP
copolymers or the properties to be expected therefrom.
None of these references teaches or suggests a way to obtain VDF/HFP copolymers having solvent solution clarity and fluidity, longer gel times and low extractables comparable to the VDF/HFP copolymers of the instant invention or that such properties are attainable from VDF/HFP copolymers.
U.S. Patent 4,076,929 describes the synthesis of VDF homopolymer having a uniformly distributed relatively high defect structure in its molecular claims.
U.S. Patent 2,752,331 describes the synthesis of VDF-chlorotrifluoroethylene (CTFE) copolymers having a high uniformity of comonomer distribution in its molecular claims.
Baggett and Smith in High Polymers, Vol. XVIII, Ham, John Wiley (1964), Chapter X, Copolymerization, pp 587 et seq., particularly at pages 593 and 610 describe the synthesis of uniform composition distribution copolymers of vinylidene chloride and z5 vinyl chloride and vinyl chloride and vinyl acetate.
U. S. Patent 5,296,318 teaches that only VDF/HFP
copolymers having 8 to 25~ by weight HFP and no other VDF homo- or copolymers are suitable for use in fabrication of lithium battery electrodes and ~ separators.
U.S. Patent 5,348,818 mentions that among other polymers, VDF polymer may be used in forming a solid electrolyte for use in secondary battery ~anufacture.
No particular type of polyvinylidene fluoride is identified and no copolymers thereof of any type are suggested.
European Patent Application 95 120 660.6-1215 published September 4, 1996 teaches use of micro porous (open or closed cell) VDF copolymers of about 7% to about 25~ comonomer content in lithium batteries and the use of VDF homopolymer as a cladding material for such batteries. Use of copolymers used by the instant invention in solid electrolytes and the improved properties provided thereby are not taught or suggested. Similarly the use of the type of VDF
homopolymer used in the present invention in solid electrolytes is not taught of suggested.
None of these references teach or suggest lithium rocking chair batteries of the type contemplated by the present invention and U.S. Patent 5,296,318 expressly teaches away from use of VDF homopolymer of any type, VDF/HFP copolymers of less than 8~ by weight HFP content or other VDF containing copolymers.
U.S. Patent 5,571,634 teaches a lithium ion battery construction employing a VDF-CTFE copolymer where the CTFE content in the copolymer is no less than 8~ by weight.
PCT~S98/04071 ST~Y OF T~ lNV~NLlON
The invention provides in a first composition aspect a copolymer of vinylidene fluoride and hexafluoropropylene containing a maximum of about 24 weight percent hexafluoropropylene, having solutions s of improved clarity and fluidity; for the copolymers having up to about 8 weight percent nominal HFP
content, having wei~ht percent extractables within plus or minus 1.5~ of the percent by weight extractables calculated by an equation selected from the group consisting of:
a) wt.% Extractable = 1.7(HFP mole%) - 3.2, and b) wt.~ Extractable = -1.2 + l.5tHFP mole%) - 8 x 10~6(Mn), and ~or the copolymers having greater than about 8 weight percent nominal HFP content, having a DSC
(differential scanning calorimetry) melting point at least 2.5~C lower than the DSC melting point of copolymers having the same nominal weight percent HFP
prepared by methods for which the prior art provides detail.
The tangible embodiments of this first composition aspect of the invention are straw colored to colorless semi crystalline solids having melting points, as determined by differential scanning calorimetry tDSC), lower than VDF/HFP copolymers having the same nominal HFP percentage content prepared by processes reported in detail in the prior art.
The tangible embodiments of this first composition aspect of the invention also possess - longer gelation times from solution than VDF/HFP
copolymers havin~ the same nominal HFP content prepared by processes reported in detail in the prior art.
The aforementioned physical characteristics taken together with the method of synthesis positively tend to confirm the structure and the novelty of the compositions sought to be patented.
The tangible embodiments of the first composition aspect of the invention have the inherent applied use characteristics of being suitable for paint and powder coating vehicles and as chemically resistant shaped objects and films both supported and unsupported.
Particular mention i5 made of co~olymers of the first composition aspect of the present invention having from about 2 weight% HFP content to about 8 weight%
HFP, still more particularly copolymers having about 3 to 6 weight% HFP which possess the inherent applied use characteristics of being particularly suitable as polymeric separators and polymeric electrode matrices for batteries, particularly lithium batteries.
The prior art, see for example U.S. 5,296,318, has reported lithium batteries made from VDF/HFP
copolymers having from 8% to 25% by weight HFP. It is understood that the copolymers of the present invention having HFP content in that range are also suitable for use in such batteries and would represent an improvement therein. Such improved batteries are g CA 022~1648 1998-10-1 PCT~S98/04071 - also contemplated by the invention as equivalents.
Particular mention is also made of copolymers o~
the first composition aspect of the invention having from about 7 weight percent HFP content to about 15 weight percent ~P content, more particularly copolymers having about 10 weight percent HFP content which possess the inherent applied use characteristic of being suitable as flame resistant insulation for wire and cable.
Still further mention is made of copolymers of the first composition aspect of the invention having greater than about 15 weight percent HFP content, still more particularly of copolymers having about 16 by weight or greater HFP content which have the inherent applied use characteristic as clear, flexible, chemically resistant films.
The invention provides in a second composition of matter aspect, an improved article of manufacture comprising an electrochemical cell having a positive electrode, an absorber separator and a negative electrode wherein at least either one of the electrodes comprises a vinylidene fluoride polymer having an electrolyte material combined therewith and/or said absorber separator comprises a vinylidene fluoride polymer having an electrolyte material combined therewith wherein the improvement comprises the polyvinylidene fluoride polymer consisting essentially of a vinylidene fluoride polymer selected from the group consisting of vinylidene fluoride homopolymer having bimodal molecular weight PCT~US98/04071 - distribution, vinylidene fluoride/chlorotrifluoroethylene copolymer having a substantially homogeneous monomer distribution and a vinylidene fluoride/hexafluoropropylene copolymer as defined in the first composition aspect of the invention.
Special mention is made of embodiments of the second composition of the invention wherein the VDF/HFP copolymer has a hexafluoropropylene content of from about 2 wt % up to about 8 wt ~
hexafluoropropylene, particularly those having from about 3 weight ~ to about 6 weight ~
hexafluoropropylene, still more particularly, those having about 3 weight % hexafluoropropylene.
Vinylidene fluoride homopolymer having bimodal molecular weight distribution means vinylidene fluoride homopolymer prepared as described in U.S.
Patent 4,076,729.
Vinylidene fluoride/chlorotrifluoroethylene copolymer having substantially homogeneous monomer distribution means vinylidene fluoride/chlorotrifluoroethylene copolymer prepared as described in U.S. Patent 2,752,331.
Special mention is made of such VDF/CTFE
copolymers having from about 2 wt.~ up to about 8 wt %
CTFE content, more particularly such VDF/CTFE
copolymers having about 3 to about 6 weight percent CTFE content.
As used herein and in the appended claims, vinylidene fluoride polymers (or VDF polymers) of the CA 022~1648 1998-10-1 PCT~S98/04071 present invention means the polyvinylidene fluoride homopolymer having bimodal molecular weight distribution as defined above, the VDF/CTFE copolymers having substantially uniform monomer distribution as defined above and/or the VDF/HFP copolymers which are the first composition aspect of the invention.
The electrochemical cells of the type of which the second composition of matter aspect of this invention is an improvement are described in PCT
Application WO 95/06332, European Patent Application 95 120 660.6-1215, published as number 730,316 Al on September 4, 1996 and U.S. Patent 5,296,318. The disclosures of the PCT application, the European application and the U.S. Patent are hereby incorporated by reference.
In addition to use of solution casting techniques for preparation of films for use in battery constructions as described in the aforementioned references, use of extrusion techniques to prepare such films and the batteries fabricated therefrom are also contemplated.
It has also been noted that batteries fabricated from the above described VDF polymers, particularly the VDF-HFP copolymers of the present invention, have better adhesion o~ the polymers to metallic portions of electrodes and higher use temperatures than batteries fabricated from VDF-HFP copolymers of the prior art. It has also been observed that VDF-HFP
copolymers of the present invention provide batteries having improved electrical properties including the PCT~S98/04071 capability of higher discharge rates than batteries fabricated from VDF-HFP copolymers of the prior art.
It is expected by the present inventors that in general batteries fabricated according to the present invention will possess such higher temperature use and higher discharge rate capabilities.
The invention provides in a third composition aspect, a solution of a composition of the first composition aspect of the invention having improved solution clarity and fluidity.
Copolymers of vinylidene fluoride and hexafluoropropylene of up to about 24 wt~
hexafluoropropylene are useful semicrystalline thermoplastics. As the HFP content increases in the materials, the crystallinity decreases, and, correspondingly, the flexibility and solvent sensitivity increase. Other properties change as well, such as the final melting point, which decreases with increasing HFP content. In high-purity applications such as membrane filtration or extraction, lithium battery construction, high-transparency film from solution casting, and fluid storage and transport requiring low contaminant levels, it is desirable to have materials with low levels of extractables, little gel formation in the presence of solvent, and good clarity. The VDF/HFP
copolymers provided here show lower extractables, improved solution properties, improved clarity and fluidity, and lower melting points in comparison to the nonuniform VDF/HFP copolymers of otherwise similar CA 022~1648 1998-10-15 PCT~US98/04071 HFP content and manufacture known in the prior art.
D~.~CRIPTION OF T~ DRAWING~
Figure 1 is a comparison of the final differential scanning colorimeter/(DSC) melting point of copolymers of the invention with DSC melting points of prior art compounds whose synthesis is described in detail.
Figure 2 shows the effect on HFP level on polymer extractibles in dimethyl carbonate (DMC) at 40~C for copolymers of the invention and copoly~ers of the prior art whose synthesis is described in detail.
Figure 3 shows the relationship between HFP
content and log of gelation time from solution (20 wt~
in propylene carbonate) of copolymers of the present invention and of copolymers of the prior art having sufficient synthesis detail for reproduction.
Figure 4 is a cross section of an electrochemical cell in accord with the present invention.
DETATT F~n DESC~RTPTIQN
The invention provides copolymers of vinylidene fluoride and hexafluoropropylene having hexafluoro-propylene content o~ up to about 24 wt% and having improved solution clarity and fluidity and reduced extractables. The copolymers are conveniently made by an emulsion polymerization process, but suspension and solution processes may also be used. In an emulsion polymerization process a reactor is charged with deionized water, water-soluble surfactant capable of emulsifying the reaction mass during polymerization, paraffin antifoulant, vinylidene fluoride, PCT~S98/04071 - hexafluoropropylene, chain-transfer agent to control copolymer molecular weight, and initiator to start and maintain the polymerization. To obtain the VDF/HFP
copolymers of the present invention, the initial charge of VDF and HFP monomers is such that the amount of HFP is up to 48% of the combined weight of the monomers initially charged, and then VDF and HFP are fed continuously throughout the reaction such that the amount of the HFP is up to 24% of the combined weight of the monomers fed continuously. The VDF/HFP ratios are different in the initial charge and during the continuous feed, and each final polymer composition has definite and related ratios for the initial charge and continuous feed. The process uses total amounts of VDF and HFP monomers such that the amount of HFP
used is up to about 24% of the combined total weight of the monomers.
The reactor is a pressurized polymerization reactor equipped with a stirrer and heat control means. The temperature of the polymerization can vary depending on the characteristics of the initiator used, but it is typically between 65~ and 105~C, and most conveniently it is between 75~ and 95~C. The temperature is not limited to this range, however, and might be higher or lower if a high-temperature or low-temperature initiator is used. The VDF/~FP ratios used in the polymerization will be dependent on the temperature chosen for reaction. The pressure of the polymerization is typically between 2750 and 6900 kPa, but it can be higher if the equipment permits CA 022~1648 1998-10- lS
PCT~S98/04071 - operation at higher pressure. The pressure is most conveniently between 3790 and 5860 kPa.
Surfactants used in the polymerization are water-soluble, halogenated surfactants, especially fluorinated surfactants such as the ammonium, substituted ammonium, quaternary ammonium, or alkali metal salts of perfluorinated or partially fluorinated alkyl carboxylates, the perfluorinated or partially fluorinated monoalkyl phosphate esters, the perfluorinated or partially fluorinated alkyl ether or polyether carboxylates, the perfluorinated or partially fluorinated alkyl sulfonates, and the perfluorinated or partially fluorinated alkyl sulfates. Some specific, but not limiting examples are the salts of the acids described in U.S. Pat. No.
HEXAFLUOROPROPYLENE HAVING R~L~
EXTRACTABLE CONTENT AND IMPROVED SOLUTION CLARITY
IR 3490NPl This application claims the benefit of provisional application serial number 60/038,346 filed Feb. 28, 1g97 BACKGROYND OF THE I~Y~NllON
This invention relates to compositions of matter classified in the art of chemistry as fluoropolymers, more specifically as copolymers of vinylidene fluoride (VDF), more specifically as copolymers of vinylidene fluoride and hexafluoropropylene (HFP), still more specifically as copolymers of VDF and HFP having reduced extractable content, longer gel times and improved solution clarity, to novel compositions of matter and articles of manufacture containing such copolymers, as well as to processes for the preparation and use of the copolymers, of compositions of manufacture containing such copolymers and of the , CA 022~1648 1998-10-l~i PCT~S98/04071 articles of manufacture containing such copolymers.
VDF/HFP copolymers are well known and are used for their thermoplastic engineering properties, chemical resistance and inertness toward degradation.
They may be found in applications such as chemically resistant piping, gasketing, plenum cable jacketing, filtration and extraction membranes and in the construction of lithium batteries.
The present invention provides VDF/HFP copolymers containing up to about 24 weight ~ ~12 mole~) HFP
having among other improved properties, substantially improved solution clarity, longer gel times and reduced extractables as these terms are defined hereinafter.
The process used to make the instant copolymers requires one ratio of VDF and HFP for the initial fill of the reactor, and a different ratio of VDF and HFP
during a subsequent continuous feed of the monomers.
Any particular desired average HFP content in the copolymer product has corresponding partlcular initial fill and subsequent feed ratios. The uniformity of compositions prepared this way provide unique and useful properties in comparison to VDF/HFP copolymers described in the prior art.
The present invention also provides lithium batteries fabricated from the VDF/HFP copolymers of the present invention and lithium batteries from other homo and copolymers more specifically described hereinbelow prepared by known processes having analogous structure and which the present inventors CA 022S1648 1998- 10- lS
WO g8/38687 PCT~S98/04071 have recognized as processing properties analogous to ~ those of the VDF/HFP copolymers of the invention which makes them uniquely suitable for lithium battery construction.
nT~rT.oSUp~ OF P~TOR A~T
Rexford in U.S. Pat. No. 3,051,677 described VDF/HFP copolymers of HFP content 30 to 70 wt~ ~15 to 50 mol~) which showed utility as elastomers. To make the copolymers, a batch process with certain initial ratios of VDF and HFP, and a continuous process with fixed ratios of VDF and HFP throughout the process were described. The processes described were such that polymers lacking the improved solution clarity, longer gel times and low extractables of the present invention were made.
Lo in U.S. Pat. No. 3,178,399 described VDF/HFP
copolymers of HFP content of 2 to 26 wt~ (1 to 13 mol~) which showed a numerical value for the product of the tensile strength ~psig) and percent reversible elongation of at least 1,000,000. ~ batch process with certain initial ratios of VDF and HFP, or, alternately, a semicontlnuous process with fixed ratios of V~F and HFP throughout the process were used to make the copolymers. The processes discussed were such that copolymers lacking the improved solution clarity, longer gel times and low extracta~les of the present invention copolymers were made.
Moggi, et al. in Polymer Bulletin 7, 115-122 (1982) analyzed the microstructure and crystal structure of VDF/HFP copolymers by nuclear magnetic W O 98~8687 PCT~S98/04071 - resonance and x-ray diffraction experiments. The copolymers of up to 31 wt~ (up to 16 mol~ HFP were made in a batch emulsion process which was carried only to low conversion. While the low conversion batch process is capable of producing copolymers having solution clarity and low extractables, no such properties are described. It is not a practical process for industrial use because of the low conversions required to make the materials. In addition, no detailed polymerization examples were offered.
Bonardelli et al. in Polymer, vol. 27, 905-gog (June 1986) studied the glass transition temperatures of VDF/HFP copolymers having HFP content up to 62 wt.
(up to 41 mol%). The glass transition temperatures were correlated to the overall HFP content in the copolymers. In making the copolymers for analysis, a semicontinuous emulsion process was used which employed different VDF/HFP ratios for the initial fill of the reactor and for the subsequent continuous feed of monomers. Although reference was made to the use of reactivity ratios to set the VDF/HFP ratio for the initial fill, no detailed polymerization examples were offered, and no mention of copolymers having solution clarity, gel times and low extractables comparable to that of the copolymers of the present invention was made.
Pianca et al. in Polymer, vol. 28, 224-230 (Feb.
1987) examined the microstructure of VDF/HFP
copolymers by nuclear magnetic resonance, and the CA 02251648 1998-10-lS
W098~8~7 PCT~S98/04~71 microstructure determinations were used to explain the trend in glass transition temperatures of the copolymers. The synthesis of the copolymers involved a semicontinuous emulsion process which used different VDF/HFP ratios for the initial fill of the reactor and for the subse~uent continuous feed of monomers. No detailed synthesis examples were provided, and there was no discussion of copolymers having improved solution clarity, longer gel times and low extractables as provided by the copolymers of the present invention.
Abusleme et al. in Eur. Pat. Appl. No. 650,982 Al showed an emulsion process to make polymers and copolymers of fluorinated olefins optionally with one or more non-fluorinated olefins. The process relied on photochemical initiation of polymerization so that lower temperatures and pressures could be used than those used for thermally initiated processes. While there was general mention of the structural regularity of the resulting polymers, the only evidence of regularity concerned poly~vinylidene fluoride) homopolymer, and no claims were made as to regularity of composition. Examples of VDF/HFP copoly~erization were given, but no discussion of the solution extraction properties of the copolymers was given, and there was no relation ~ade between physical properties and the structure of the V~F/HFP copolymers.
Morgan in U.S. Pat. No. 5,543,217 disclosed uniform tetrafluoroethylene/hexafluoropropylene copolymers (TFE/HFP copolymers) made by a PCT~S98/04071 semicontinuous emulsion process. Uniformity was simply defined as there being a low proportion of adjacent ~FP units in the polymer chains; there was no disclosure of the disposition of TFE and HFP units otherwise, and there was no discussion of VDF/HFP
copolymers or the properties to be expected therefrom.
None of these references teaches or suggests a way to obtain VDF/HFP copolymers having solvent solution clarity and fluidity, longer gel times and low extractables comparable to the VDF/HFP copolymers of the instant invention or that such properties are attainable from VDF/HFP copolymers.
U.S. Patent 4,076,929 describes the synthesis of VDF homopolymer having a uniformly distributed relatively high defect structure in its molecular claims.
U.S. Patent 2,752,331 describes the synthesis of VDF-chlorotrifluoroethylene (CTFE) copolymers having a high uniformity of comonomer distribution in its molecular claims.
Baggett and Smith in High Polymers, Vol. XVIII, Ham, John Wiley (1964), Chapter X, Copolymerization, pp 587 et seq., particularly at pages 593 and 610 describe the synthesis of uniform composition distribution copolymers of vinylidene chloride and z5 vinyl chloride and vinyl chloride and vinyl acetate.
U. S. Patent 5,296,318 teaches that only VDF/HFP
copolymers having 8 to 25~ by weight HFP and no other VDF homo- or copolymers are suitable for use in fabrication of lithium battery electrodes and ~ separators.
U.S. Patent 5,348,818 mentions that among other polymers, VDF polymer may be used in forming a solid electrolyte for use in secondary battery ~anufacture.
No particular type of polyvinylidene fluoride is identified and no copolymers thereof of any type are suggested.
European Patent Application 95 120 660.6-1215 published September 4, 1996 teaches use of micro porous (open or closed cell) VDF copolymers of about 7% to about 25~ comonomer content in lithium batteries and the use of VDF homopolymer as a cladding material for such batteries. Use of copolymers used by the instant invention in solid electrolytes and the improved properties provided thereby are not taught or suggested. Similarly the use of the type of VDF
homopolymer used in the present invention in solid electrolytes is not taught of suggested.
None of these references teach or suggest lithium rocking chair batteries of the type contemplated by the present invention and U.S. Patent 5,296,318 expressly teaches away from use of VDF homopolymer of any type, VDF/HFP copolymers of less than 8~ by weight HFP content or other VDF containing copolymers.
U.S. Patent 5,571,634 teaches a lithium ion battery construction employing a VDF-CTFE copolymer where the CTFE content in the copolymer is no less than 8~ by weight.
PCT~S98/04071 ST~Y OF T~ lNV~NLlON
The invention provides in a first composition aspect a copolymer of vinylidene fluoride and hexafluoropropylene containing a maximum of about 24 weight percent hexafluoropropylene, having solutions s of improved clarity and fluidity; for the copolymers having up to about 8 weight percent nominal HFP
content, having wei~ht percent extractables within plus or minus 1.5~ of the percent by weight extractables calculated by an equation selected from the group consisting of:
a) wt.% Extractable = 1.7(HFP mole%) - 3.2, and b) wt.~ Extractable = -1.2 + l.5tHFP mole%) - 8 x 10~6(Mn), and ~or the copolymers having greater than about 8 weight percent nominal HFP content, having a DSC
(differential scanning calorimetry) melting point at least 2.5~C lower than the DSC melting point of copolymers having the same nominal weight percent HFP
prepared by methods for which the prior art provides detail.
The tangible embodiments of this first composition aspect of the invention are straw colored to colorless semi crystalline solids having melting points, as determined by differential scanning calorimetry tDSC), lower than VDF/HFP copolymers having the same nominal HFP percentage content prepared by processes reported in detail in the prior art.
The tangible embodiments of this first composition aspect of the invention also possess - longer gelation times from solution than VDF/HFP
copolymers havin~ the same nominal HFP content prepared by processes reported in detail in the prior art.
The aforementioned physical characteristics taken together with the method of synthesis positively tend to confirm the structure and the novelty of the compositions sought to be patented.
The tangible embodiments of the first composition aspect of the invention have the inherent applied use characteristics of being suitable for paint and powder coating vehicles and as chemically resistant shaped objects and films both supported and unsupported.
Particular mention i5 made of co~olymers of the first composition aspect of the present invention having from about 2 weight% HFP content to about 8 weight%
HFP, still more particularly copolymers having about 3 to 6 weight% HFP which possess the inherent applied use characteristics of being particularly suitable as polymeric separators and polymeric electrode matrices for batteries, particularly lithium batteries.
The prior art, see for example U.S. 5,296,318, has reported lithium batteries made from VDF/HFP
copolymers having from 8% to 25% by weight HFP. It is understood that the copolymers of the present invention having HFP content in that range are also suitable for use in such batteries and would represent an improvement therein. Such improved batteries are g CA 022~1648 1998-10-1 PCT~S98/04071 - also contemplated by the invention as equivalents.
Particular mention is also made of copolymers o~
the first composition aspect of the invention having from about 7 weight percent HFP content to about 15 weight percent ~P content, more particularly copolymers having about 10 weight percent HFP content which possess the inherent applied use characteristic of being suitable as flame resistant insulation for wire and cable.
Still further mention is made of copolymers of the first composition aspect of the invention having greater than about 15 weight percent HFP content, still more particularly of copolymers having about 16 by weight or greater HFP content which have the inherent applied use characteristic as clear, flexible, chemically resistant films.
The invention provides in a second composition of matter aspect, an improved article of manufacture comprising an electrochemical cell having a positive electrode, an absorber separator and a negative electrode wherein at least either one of the electrodes comprises a vinylidene fluoride polymer having an electrolyte material combined therewith and/or said absorber separator comprises a vinylidene fluoride polymer having an electrolyte material combined therewith wherein the improvement comprises the polyvinylidene fluoride polymer consisting essentially of a vinylidene fluoride polymer selected from the group consisting of vinylidene fluoride homopolymer having bimodal molecular weight PCT~US98/04071 - distribution, vinylidene fluoride/chlorotrifluoroethylene copolymer having a substantially homogeneous monomer distribution and a vinylidene fluoride/hexafluoropropylene copolymer as defined in the first composition aspect of the invention.
Special mention is made of embodiments of the second composition of the invention wherein the VDF/HFP copolymer has a hexafluoropropylene content of from about 2 wt % up to about 8 wt ~
hexafluoropropylene, particularly those having from about 3 weight ~ to about 6 weight ~
hexafluoropropylene, still more particularly, those having about 3 weight % hexafluoropropylene.
Vinylidene fluoride homopolymer having bimodal molecular weight distribution means vinylidene fluoride homopolymer prepared as described in U.S.
Patent 4,076,729.
Vinylidene fluoride/chlorotrifluoroethylene copolymer having substantially homogeneous monomer distribution means vinylidene fluoride/chlorotrifluoroethylene copolymer prepared as described in U.S. Patent 2,752,331.
Special mention is made of such VDF/CTFE
copolymers having from about 2 wt.~ up to about 8 wt %
CTFE content, more particularly such VDF/CTFE
copolymers having about 3 to about 6 weight percent CTFE content.
As used herein and in the appended claims, vinylidene fluoride polymers (or VDF polymers) of the CA 022~1648 1998-10-1 PCT~S98/04071 present invention means the polyvinylidene fluoride homopolymer having bimodal molecular weight distribution as defined above, the VDF/CTFE copolymers having substantially uniform monomer distribution as defined above and/or the VDF/HFP copolymers which are the first composition aspect of the invention.
The electrochemical cells of the type of which the second composition of matter aspect of this invention is an improvement are described in PCT
Application WO 95/06332, European Patent Application 95 120 660.6-1215, published as number 730,316 Al on September 4, 1996 and U.S. Patent 5,296,318. The disclosures of the PCT application, the European application and the U.S. Patent are hereby incorporated by reference.
In addition to use of solution casting techniques for preparation of films for use in battery constructions as described in the aforementioned references, use of extrusion techniques to prepare such films and the batteries fabricated therefrom are also contemplated.
It has also been noted that batteries fabricated from the above described VDF polymers, particularly the VDF-HFP copolymers of the present invention, have better adhesion o~ the polymers to metallic portions of electrodes and higher use temperatures than batteries fabricated from VDF-HFP copolymers of the prior art. It has also been observed that VDF-HFP
copolymers of the present invention provide batteries having improved electrical properties including the PCT~S98/04071 capability of higher discharge rates than batteries fabricated from VDF-HFP copolymers of the prior art.
It is expected by the present inventors that in general batteries fabricated according to the present invention will possess such higher temperature use and higher discharge rate capabilities.
The invention provides in a third composition aspect, a solution of a composition of the first composition aspect of the invention having improved solution clarity and fluidity.
Copolymers of vinylidene fluoride and hexafluoropropylene of up to about 24 wt~
hexafluoropropylene are useful semicrystalline thermoplastics. As the HFP content increases in the materials, the crystallinity decreases, and, correspondingly, the flexibility and solvent sensitivity increase. Other properties change as well, such as the final melting point, which decreases with increasing HFP content. In high-purity applications such as membrane filtration or extraction, lithium battery construction, high-transparency film from solution casting, and fluid storage and transport requiring low contaminant levels, it is desirable to have materials with low levels of extractables, little gel formation in the presence of solvent, and good clarity. The VDF/HFP
copolymers provided here show lower extractables, improved solution properties, improved clarity and fluidity, and lower melting points in comparison to the nonuniform VDF/HFP copolymers of otherwise similar CA 022~1648 1998-10-15 PCT~US98/04071 HFP content and manufacture known in the prior art.
D~.~CRIPTION OF T~ DRAWING~
Figure 1 is a comparison of the final differential scanning colorimeter/(DSC) melting point of copolymers of the invention with DSC melting points of prior art compounds whose synthesis is described in detail.
Figure 2 shows the effect on HFP level on polymer extractibles in dimethyl carbonate (DMC) at 40~C for copolymers of the invention and copoly~ers of the prior art whose synthesis is described in detail.
Figure 3 shows the relationship between HFP
content and log of gelation time from solution (20 wt~
in propylene carbonate) of copolymers of the present invention and of copolymers of the prior art having sufficient synthesis detail for reproduction.
Figure 4 is a cross section of an electrochemical cell in accord with the present invention.
DETATT F~n DESC~RTPTIQN
The invention provides copolymers of vinylidene fluoride and hexafluoropropylene having hexafluoro-propylene content o~ up to about 24 wt% and having improved solution clarity and fluidity and reduced extractables. The copolymers are conveniently made by an emulsion polymerization process, but suspension and solution processes may also be used. In an emulsion polymerization process a reactor is charged with deionized water, water-soluble surfactant capable of emulsifying the reaction mass during polymerization, paraffin antifoulant, vinylidene fluoride, PCT~S98/04071 - hexafluoropropylene, chain-transfer agent to control copolymer molecular weight, and initiator to start and maintain the polymerization. To obtain the VDF/HFP
copolymers of the present invention, the initial charge of VDF and HFP monomers is such that the amount of HFP is up to 48% of the combined weight of the monomers initially charged, and then VDF and HFP are fed continuously throughout the reaction such that the amount of the HFP is up to 24% of the combined weight of the monomers fed continuously. The VDF/HFP ratios are different in the initial charge and during the continuous feed, and each final polymer composition has definite and related ratios for the initial charge and continuous feed. The process uses total amounts of VDF and HFP monomers such that the amount of HFP
used is up to about 24% of the combined total weight of the monomers.
The reactor is a pressurized polymerization reactor equipped with a stirrer and heat control means. The temperature of the polymerization can vary depending on the characteristics of the initiator used, but it is typically between 65~ and 105~C, and most conveniently it is between 75~ and 95~C. The temperature is not limited to this range, however, and might be higher or lower if a high-temperature or low-temperature initiator is used. The VDF/~FP ratios used in the polymerization will be dependent on the temperature chosen for reaction. The pressure of the polymerization is typically between 2750 and 6900 kPa, but it can be higher if the equipment permits CA 022~1648 1998-10- lS
PCT~S98/04071 - operation at higher pressure. The pressure is most conveniently between 3790 and 5860 kPa.
Surfactants used in the polymerization are water-soluble, halogenated surfactants, especially fluorinated surfactants such as the ammonium, substituted ammonium, quaternary ammonium, or alkali metal salts of perfluorinated or partially fluorinated alkyl carboxylates, the perfluorinated or partially fluorinated monoalkyl phosphate esters, the perfluorinated or partially fluorinated alkyl ether or polyether carboxylates, the perfluorinated or partially fluorinated alkyl sulfonates, and the perfluorinated or partially fluorinated alkyl sulfates. Some specific, but not limiting examples are the salts of the acids described in U.S. Pat. No.
2,559,752 of the formula X(CF2)nCOOM, wherein X is hydrogen or fluorine, M is an alkali metal, ammonium, substituted ammonium (e.g., alkylamine of 1 to 4 carbon atoms), or quaternary ammonium ion, and n is an integer from 6 to 20; sulfuric acid esters of polyfluoroalkanols of the formula X(C~2)nCH2OSO3M, where X and M are as above; and salts of the acids of the formula CF3(CF2)n(CX2)mSO3M, where X and M are as above, n is an integer from 3 to 7, and m is an integer from 0 to 2, such as in potassium perfluorooctyl sulfonate. The surfactant charge is from 0.05~ to 2~ by weight on the total monomer weight used, and most preferably the surfactant charge is from 0.1% to 0.2~ by weight.
The paraffin antifoulant is conventional, and any PCT~US98/04071 long-chain, saturated, hydrocarbon wax or oil may be used. Reactor loadings of the paraffin are from 0.01 to 0.3% by weight on the total monomer weight used.
After the reactor has been charged with deionized water, surfactant, and paraffin antifoulant, the reactor is either purged with nitrogen or evacuated to remove oxygen. The reactor is brought to temperature, and chain-transfer agent may optionally be added. The reactor is then pressurized with a mixture of vinylidene fluoride and hexafluoropropylene.
Chain-transfer agents which may be used are well-known in the polymerization of fluorinated monomers.
Alcohols, carbonates, ketones, esters, and ethers are oxygenated compounds which serve as chain-transfer agents. Specific, but not limiting examples, are isopropyl alcohol, such as described in U.S. Pat. No.
4,360,652, acetone, such as described in U.S. Pat. No.
The paraffin antifoulant is conventional, and any PCT~US98/04071 long-chain, saturated, hydrocarbon wax or oil may be used. Reactor loadings of the paraffin are from 0.01 to 0.3% by weight on the total monomer weight used.
After the reactor has been charged with deionized water, surfactant, and paraffin antifoulant, the reactor is either purged with nitrogen or evacuated to remove oxygen. The reactor is brought to temperature, and chain-transfer agent may optionally be added. The reactor is then pressurized with a mixture of vinylidene fluoride and hexafluoropropylene.
Chain-transfer agents which may be used are well-known in the polymerization of fluorinated monomers.
Alcohols, carbonates, ketones, esters, and ethers are oxygenated compounds which serve as chain-transfer agents. Specific, but not limiting examples, are isopropyl alcohol, such as described in U.S. Pat. No.
4,360,652, acetone, such as described in U.S. Pat. No.
3,857,827, and ethyl acetate, as described in the Published Unexamined Application ~Kokai) JP 58065711.
Other classes of compounds which serve as chain-transfer agents in the polymerization of fluorinated monomers are halocarbons and hydrohalocarbons such as chlorocarbons, hydrochlorocarbons, chlorofluorocarbons, and hydrochlorofluoro-carbons;
speci~ic, but not limiting examples are trichlorofluoromethane, such as described in U.S. Pat.
No. 4,569,978, and 1,1-dichloro-2,2,2-trifluoroethane.
Chain-transfer agents may be added all at once at the beginning of the reaction, in portions throughout the reaction, or continuously as the reaction progresses.
_ _ _ _ _ _ _ CA 022~1648 1998-10-15 - The amount of chain-transfer agent and mode of addition which is used depends on the activity of the agent and the desired molecular weight characteristics of the product. The amount of chain-transfer agent used is from 0.05% to 5~ by weight on the total monomer weight used, and preferably it is from 0.1 to 2~ by weight.
The reactor is pressurized by adding vinylidene fluoride and hexafluoropropylene monomers in a definite ratio (first effective ratio) such that the hexafluoropropylene ranges up to 48~ of the combined weight of the monomers initially charged. The first effective ratio used will depend on the relative reactivity of the two monomers at the polymerization temperature chosen. The reactivity of vinylidene fluoride and hexafluoropropylene has been reported in Bonardelli et al., Polymer, vol. 27, 905-909 (June 1986). The relative reactivity is such that to obtain a particular uniform copolymer composition, more hexafluoropropylene has to be charged to the reactor in the initial fill than will be incorporated into the copolymer. At the convenient polymerization temperature range of this invention, about twice as much hexafluoropropylene has to be charged to the reactor in the initial fill as will appear in the polymer.
The reaction can be started and maintained by the addition of any suita~le initiator known for the polymerization of fluorinated monomers including inorganic peroxides, "redox" combinations of oxidizing CA 02251648 1998-10- lS
- and reducing agents, and organic peroxides. ~xamples of typical inorganic peroxides are the ammonium or alkali metal salts of persulfates, which have useful acti~ity in the 65~C to 105~C temperature range.
~Redox" systems can operate at even lower temperatures and examples include combinations of oxidants such as hydrogen peroxide, t-butyl hydroperoxide, cumene hydroperoxide, or persulfate, and reductants such as reduced metal salts, iron (II) salts being a particular example, optionally combined with activators such as sodium formaldehyde sulfoxylate or ascor~ic acid. Among the organic peroxides which can be used for the polymerization are the classes of dialkyl peroxides, peroxyesters, and peroxydi-carbonates. Exemplary of dialkyl peroxides is di-t-lS butyl peroxide, of peroxyesters are t-butyl peroxypivalate and t-amyl peroxypivalate, and of peroxydicarbonates are di(n-propyl) peroxydicarbonate, diisopropyl peroxydicarbonate, di(sec-butyl) peroxydicarbonate, and di(2-ethylhexyl) peroxydi-car~onate. The use of diisopropyl peroxydicarbonate for vinylidene fluoride polymerization and copoly~erization with other fluorinated monomers is taught in U.S. Pat. No. 3,475,396, and its use in making vinylidene fluoride/hexafluoropropylene copolymers is further illustrated in U.S. Pat. No.
Other classes of compounds which serve as chain-transfer agents in the polymerization of fluorinated monomers are halocarbons and hydrohalocarbons such as chlorocarbons, hydrochlorocarbons, chlorofluorocarbons, and hydrochlorofluoro-carbons;
speci~ic, but not limiting examples are trichlorofluoromethane, such as described in U.S. Pat.
No. 4,569,978, and 1,1-dichloro-2,2,2-trifluoroethane.
Chain-transfer agents may be added all at once at the beginning of the reaction, in portions throughout the reaction, or continuously as the reaction progresses.
_ _ _ _ _ _ _ CA 022~1648 1998-10-15 - The amount of chain-transfer agent and mode of addition which is used depends on the activity of the agent and the desired molecular weight characteristics of the product. The amount of chain-transfer agent used is from 0.05% to 5~ by weight on the total monomer weight used, and preferably it is from 0.1 to 2~ by weight.
The reactor is pressurized by adding vinylidene fluoride and hexafluoropropylene monomers in a definite ratio (first effective ratio) such that the hexafluoropropylene ranges up to 48~ of the combined weight of the monomers initially charged. The first effective ratio used will depend on the relative reactivity of the two monomers at the polymerization temperature chosen. The reactivity of vinylidene fluoride and hexafluoropropylene has been reported in Bonardelli et al., Polymer, vol. 27, 905-909 (June 1986). The relative reactivity is such that to obtain a particular uniform copolymer composition, more hexafluoropropylene has to be charged to the reactor in the initial fill than will be incorporated into the copolymer. At the convenient polymerization temperature range of this invention, about twice as much hexafluoropropylene has to be charged to the reactor in the initial fill as will appear in the polymer.
The reaction can be started and maintained by the addition of any suita~le initiator known for the polymerization of fluorinated monomers including inorganic peroxides, "redox" combinations of oxidizing CA 02251648 1998-10- lS
- and reducing agents, and organic peroxides. ~xamples of typical inorganic peroxides are the ammonium or alkali metal salts of persulfates, which have useful acti~ity in the 65~C to 105~C temperature range.
~Redox" systems can operate at even lower temperatures and examples include combinations of oxidants such as hydrogen peroxide, t-butyl hydroperoxide, cumene hydroperoxide, or persulfate, and reductants such as reduced metal salts, iron (II) salts being a particular example, optionally combined with activators such as sodium formaldehyde sulfoxylate or ascor~ic acid. Among the organic peroxides which can be used for the polymerization are the classes of dialkyl peroxides, peroxyesters, and peroxydi-carbonates. Exemplary of dialkyl peroxides is di-t-lS butyl peroxide, of peroxyesters are t-butyl peroxypivalate and t-amyl peroxypivalate, and of peroxydicarbonates are di(n-propyl) peroxydicarbonate, diisopropyl peroxydicarbonate, di(sec-butyl) peroxydicarbonate, and di(2-ethylhexyl) peroxydi-car~onate. The use of diisopropyl peroxydicarbonate for vinylidene fluoride polymerization and copoly~erization with other fluorinated monomers is taught in U.S. Pat. No. 3,475,396, and its use in making vinylidene fluoride/hexafluoropropylene copolymers is further illustrated in U.S. Pat. No.
4,360,652. The use of di(n-propyl~ peroxydicarbonate in ~inylidene fluoride polymerizations is described in the Published Unexamined Application (Kokai) JP
58065711. The quantity of an initiator required for a ,, CA 022~1648 lsss-lo-PCT~S98/04071 - polymerization is related to its activity and the temperature used for the polymerization. The total amount of initiator used is generally between 0.05% to 2.5% by weight on the total monomer weight used.
Typically, sufficient initiator is added at the beginning to start the reaction and then additional initiator may be optionally added to maintain the polymerization at a convenient rate. The initiator may be added in pure form, in solution, in suspension, or in emulsion, depending upon the initiator chosen.
As a particular example, peroxydicarbonates are conveniently added in the form of an aqueous emulsion.
As the reaction progresses, a mixture of vinylidene fluoride and hexafluoropropylene monomers is fed in a definite ratio ( second effective ratio) so as to maintain reaction pressure. The second effective ratio used corresponds to the monomer unit ratio desired in the final composition of the copolymer, and it can range up to 24% of the com~ined weight of the monomers being fed continuously throughout the reaction. The feed of vinylidene fluoride, hexafluoropropylene, and optionally initiator and chain-transfer agent is continued until the desired reactor fill is obtained.
Upon reaching the desired reactor fill, the monomer feeds are terminated. To achieve the copolymer havin~ optimum solution clarity and minimal extractables, all other feeds are stopped at the same time as the monomer feeds, and the reactor is vented as soon as is practicable. Alternatively, to achieve - CA 022~1648 1998-10-1 PCT~S98/04071 - highest yield at the expense of solution clarity and extractables, a react-out period to consume residual monomer is used with optional continuation of initiator feed. For react-out, the reaction temperature and agitation are maintained for a period S of 20 to 30 minutes, but a longer period can be used if required in order to consume monomer to the point where the reactor pressure is no longer falling to any significant degree. A settling period of typically 10 to 40 minutes may be used following the react-out period. During the settling period, temperature is maintained but no initiator feed is used. The reactor is then cooled and vented.
The product is recovered as a latex. To obtain dry resin, the latex is coagulated, the coagulum is separated and the separated coagulum may be washed.
To provide powder, the coagulum is dried.
For the coagulation step, several well-known methods can be used including freezing, the addition of acids or salts, or mechanical shear with optional heating. The powder, if desired, can be further processed into pellets or other convenient resin forms.
The electrochemical cells of the present invention are based on a positive electrode, an absorber-separator sometimes referred as a solid electrolyte and negative electrode operatively associated with one another wherein at least one of the electrodes or the absorber-separator, and preferably both electrodes and the absorber-separator CA 022~1648 1998-10-1 P~T~S98/04071 comprise a vinylidene fluoride polymer of the present invention and wherein the vinylidene fluoride polymer of the present invention electrodes have an electrode material combined therewith and the vinylidene fluoride polymer of the present invention absorber-separator has an electrolyte ~aterial combined therewith. A plurality of electrodes and absorber-separator elements can be used in the cell structure in order to increase the voltage, and/or amperage of the combined elements in a manner well known to the art.
Vinylidene fluoride polymer of the present invention is not required to have an open or closed porous structure for operability. It provides enhanced electrolyte mobility in combination with the intrinsic ionic conductivity effects of the polymer regardless of its initial porous or non porous state.
Vinylidene fluoride electrode or separator-absorber combined with electrode or electrolyte materials at the surface of the pores of the porous polymer was previously believed to make the utilization of the active material, whether electrode material or electrolyte material more efficient and provide a method for the easy manufacture of the efficient electrodes and separator-absorber structures. There are, however, other advantages to use of porous polymer structures even for the polyvinylidene fluoride polymers of the present invention.
It is also believed that the segregation of the active materials on the surface of active pores will CA 022~1648 1998-10-1 PCT~S98/04071 - allow for varying the amount of binder in the electrode of the separator-absorber to enhance strength with minimum effect on cell performance. The electrochemical cells formed in this way therefore will have improved mechanical properties and can be made to be self-supporting i.e., secondary reinforcing structures do not have to be employed such as a metal or other conventional battery casing material.
This also leads to ease of fabrication where the electrochemical cell is enveloped or enclosed in a vinylidene fluoride homopolymer which will adhere to the porous electrodes and/or the absorber-separator structures. Adhesion can be obtained by simple heat bonding or radio frequency (rf) welding or other similar processes well known in the art. Adhesives are not required, but importantly, the exterior part of the electrochemical cell (i.e., the envelope) is of the same type or a substantially similar type of material as the electrodes and absorber-separa~or and is more compatible therewith and adherent thereto, thereby simplifying and reducing the cost of manufacture in that only one type of material is used for the structural components of the cell as compared to either conventional dry cell or secondary cell construction.
Polyvinylidene fluoride in general absorbs rf frequency and may also ~e heated by dielectric techniques. Heat guns may also be used for sealing polyvinylidene fluoride surfaces under pressure.
Welding rods may also be employed to heat seal two CA 022~1648 1998-10-1 - pieces easily as is done in the fabrication of larger polyvinylidene fluoride structures. The joints obtained are usually as strong as the basic resins employed. Because polyvinylidene fluoride polymers are abrasion resistant and tough as well as chemical resistant, they are useful in the internal and external element of the battery and, as noted previously, can be assembled by non-adhesive means by heat bonding.
By selecting vinylidene fluoride polymers of the present invention for electrodes and such polymers or conventional VDF polymer for cladding that are either extremely flexible or somewhat rigid, structures can be fabricated that are in turn either flexible or somewhat rigid. Further in this regard, enhanced rigidity can be obtained by cross-linking the vinylidene fluoride homo- or copolymers in general either chemically, but preferably by employing high energy radiation such as high energy (about 10 to about 20 Mrad) electron beam radiation, with some attendant dehydrofluorination. One potential benefit is the further stabilization of the amorphous regions in the vinylidene fluoride polymers, i.e., inhibitions of crystallization over time which is important since ionic conductivity of the electrolyte is believed to occur primarily in the amorphous or open regions.
As noted previously, vinylidene fluoride polymers in general affect ionic conductivity in a manner that makes them suitable for the fabrication of electrochemical cells.
Since mobility of charged species is required in PCT~US98/04071 - electrochemical cells, it is believed that the migration of charged species in polyvinylidene fluoride polymers will be through the amorphous phase.
The vinylidene fluoride polymers of the present invention have been recognized by the invention as having enhanced amorphous phases which are more stable and particularly for the HFP and CTFE copolymers provide this benefit to conductivity and the like at lower comonomer levels, thus, providing solubility and temperature advantages approaching that of homopolymers.
In the triboelectric series, most polymers stabilize electrons. Vinylidene fluoride polymers, however, are unique in stabilizing positive holes and are one of the most effective media in this regard, presumably due to the highly negative gem-difluorocar~on group.
In the special case of lithium ion batteries such as the rocking-chair batteries described herein, the high specific charge and small ionic size of the lithium ion may lead to specific interactions in the host vinylidene fluoride poly~er environment, considering the extent of the non-polarizable, negative gem-difluorocarbon groups available.
Since conductivity is inversely related to crystallinity of the polyvinylidene fluoride polymer, it has been determined that conventional copolymers of vinylidene fluoride with about 7 to about 25 hexafluoropropylene sufficiently reduce the crystalline structure of the polymer without PCT~S98/04071 sacrificing mechanical properties so that acceptable ionic conductivity effects of the polymer can be obtained. The inventors have discovered that the vinylidene fluoride polymers of the present invention provide benefits equal to or better than the above conventional VDF/HFP copolymers at comonomer levels below 8% by weight, preferably below 6~ by weight.
When employing vinylidene fluoride polymers of the present invention in the manu~acture of electrodes or absorber-separators, plasticizers such as organic carbonates (e.g., ethylene carbonate, propylene carbonate, dimethylcarbonate and the like) are utilized in order to minimize the effect of the crystalline structure and promote ionic conductivity.
Other solvents or plasticizers may also be employed including diethoxyethane, diethylcarbonate, dimethoxyethane, dipropyl carbonate and mixtures ~ thereof especially the two or three component mixtures.
Similarly, and in accord with the present invention, the various porous or non-porous structures, depending on the their tensile strength, can be mechanically oriented by stretching or the application of tensile forces in order to enhance the amount of beta conformation within the polymer structure and thereby possibly promote ionic conductivity depending upon the electrolyte and polyvinylidene fluoride composition.
Using solvent and non-solvent combinations, polyvinylidene fluoride polymers of the present CA 022S1648 1998-10-lS
PCT~S~8/01~71 invention are cast in thin membranes. This method ls described by Benzinger et al. in U.S. Patent No.
4,384,047 which is incorporated herein by re~erence.
The electrode materials or the electrolyte materials as described herein can be incorporated into polyvinylidene fluoride solution prior to casting it into a film or sheet, after which the solution may, if desired, be converted to a porous polyvinylidene fluoride membrane combined with the electrode of electrolyte materials. These films or sheets, either with or without the electrode or electrolyte materials can be any where from about 0.25 to about 100, particularly from about 0.5 to about 10, and especially from about 1 to about 8 mils thick, and are especially suitable for further treatment by stretching or the application of tensile forces in order to promote the beta conformation necessary to achieve ferroelectric properties in polyvinylidene fluoride.
There are three classes of organic liquids, that may be used to make solutions or dispersions of vinylidene fluoride polymers. Active solvents are those organic li~uids that dissolve or swell vinylidene fluoride polymers at room temperature and typically consist of lower alkyl ketones, esters and amides. Latent solvents are those organic liquids that do not dissolve vinylidene fluoride homo- or copolymers at room temperature; however, will dissolve polyvinylidene fluoride at elevated temperatures and typically are medium chain length alkyl ketones, CA 022~1648 1998-10- lS
PCT~S98/04071 - esters, glycol ethers and organic carbonates. Non-solvents are organic liquids that do not dissolve or swell vinylidene fluoride polymers up to the boiling point of the liquid or the crystalline melting point of the vinylidene fluoride polymer, whichever condition is met first. These liquids typically are aromatic hydrocarbons, aliphatic hydro-carbons and chlorinated hydrocarbons or other chlorinated organic liquids. The solvents and latent solvents are used in the manufacture of the polyvinylidene fluoride films or sheets of the present invention.
Examples of these organic liquids are given in Table A which follows.
CA 022S1648 1998-10-lS
PCT~S98/04071 - TABLE A
LIQUIDS TO PREPARE SOLUTIONS OR DISPERSIONS OF PVDF
ACTIVE SOLVENTS LATENT SOLVENTS NON SOLVENTS
(APPROX.) DISSOLUTION
TEMPERATURE IN ~C
Acetone Butyrolactone (65) Hexane TetrahydrofuranIsophorone (75) Pentane 5Methyl Ethyl KetoneMethyl Isoamyl Ketone Benzene (102) Dimethyl FormamideCycloh~n~ (70) Toluene Dimethyl Acetamide Dimethyl Phthalate (110) Methanol Tetramethyl Urea Propylene Glycol Methyl Ethanol Ether (115) Dimethyl Sulfcxide Propylene Carbonate (80) Car~on Tetrachloride Trimethyl Phosphate Diacetone Alcohol (100) o-Dichlorobenzene N-Methyl Glycerol Tricetate (100) Trichloroethylene Pyrrolidone The suitability of any given liquid depends upon the exact PVDF resin type and grade.
Other methods have been developed for the manufacture, when desired, of open cell foam porous polyvlnylidene fluoride polymers which are formulated to contain chemical or physical blowing agents such as absorbed carbon dioxide. It is preferred to use physical blowing agents in the manufacture of electrochemical cells since trace amounts of the chemical ~lowing agents in the foam structure could adversely affect the functioning of the cell. Where carbon dioxide or comparable physical blowing agents are employed, they are incorporated into the polyvinylidene fluoride at super critical pressures CA 022~l648 l998- lO- l~
PCT/US3~i~1C 1'71 followed by heat treatment to expand the article thus produced. Open cell film5 of varying thickness have been made in this manner with excellent mechanical integrity and which have specific gravities about one as compared to solid polyvinylidene fluoride which has a specific gravity of from about 1.76 about 1.78.
Similarly, polyvinylidene fluoride powders can be sintered to form a porous structure by heating the powders in a non-solvent slurry, or under pressure between opposed platens, until the individual particles sufficiently melt flow into one another to form the desired open cell structure. Other art known methods for sintering powder polymers such as PT~E for forming open cell porous structures as described by Menassen et al . "A Polymer Chemist ' s View on Fuel Cell Electrodes,~' Procee~ing of the 34th Internation~l Power Source SymDosium, June 25-28, 1990, pp. 408-10 can also be used.
A porous film made by casting polyvinylidene provide polymers of the present invention from a mixture of solvents and non-solvents as described by Benzinger et al. in U.S. Patent 4,383,047, which is about 10 mils thick after formation from the casting solution, may be utilized for the manufacture of an electrochemical cell. The polymer comprises a copolymer of Example 1 herein below. This film is used in fabricating an absorber-separator of solid electrolyte by making a solution of LiPF6 in 1:1 mixture by weight of ethylene carbonate:propylene carbonate which is heated to about 125~C and the CA 022~l648 lsss-lo-PCT~S98/04071 - porous copolymer film immersed in the solution until it is com~ined with the film.
Similarly, a positive electrode is made from the same porous copolymer. A dispersion of LiMn2O4, SS
carbon black and LiPF6 in a 1:1 mixture of ethylene carbonate and propylene carbonate along with tetrahydrofuran (THF) was combined with the porous film by soaking the film in the suspension which is agitated in a vibrating beaker in order to keep solid material in suspension until adequately combined with the film. The film is then placed on an aluminum foil.
A negative electrode is prepared by making a dispersion or suspension of petroleum coke, SS carbon black and LiPF6 in a 1:1 ethylene carbonate propylene carbonate solution in the same manner as was done for the preparation of the positive electrode and after combining the suspension with the porous film, a copper foil was placed on the film.
The proportions of the various components of the electrode and the absorber-separator or solid electrolyte are substantially the same as those set forth in Examples 1 and 8 of Gozdz et al., U.S. Patent No. 5,296,318.
The electrodes and electrolyte can also be made from sintered polyvinylidene fluoride by forming a dry blend of the electrode or electrolyte materials with powdered polyvinylidene fluoride. Dry mixing techniques, known in the art may be employed, such as tumbler type mixing. For example, the mixture of _ . .
CA 022~1648 1998-10-1 PCT~S~0l~71 polyvinylidene fluoride powder and the electrode or electrolyte materials can be subjected to tumbling or ball milling for a time to sufficiently ensure that a good mixture is obtained. A steel or other metal vessel, or ceramic vessel is employed, especially where either is lined with a polyvinylidene fluoride or PTFE layer. In the case of ball milling, steel or other metal, or ceramic grinding balls, also coated with a polyvinylidene fluoride or PTFE layer are used.
The polyvinylidene fluoride or PTFE coating is employed to substantially minimize or substantially eliminate the introduction of impurities into the system. The milled mixtures are formed into electrodes and electrolytes by the application of heat and pressure as noted herein.
One of skill in the art will recognize that non-porous VDF/HFP copolymer of the 1st composition aspect of the invention or other vinylidene fluoride polymers of the invention, porous or non-porous may be substituted for the described VDF/HFP of Example 1 to make analogous batteries.
Solvents such as ethylene carbonate and propylene carbonate, and their equivalents, especially as noted herein, including mixtures thereof, which are employed in the electrode or electrolyte can be added afterwards by soaking the electrodes and electrolyte structures in such solvents. The soaking can be carried out at room temperature or above to maximize the solvating effect of these materials and to produce optimum ionic conductivity n the electrodes or electrolyte.
CA 02251648 1998-10-lS
PCT~S98/0~~71 ~ The positive electrode and the negative electrode thus prepared, are then placed on opposite sides of the absorber-separator prepared as described above with the copper and aluminum surfaces facing outwardly to form a cell as illustrated in Fig. 4 in which copper film 14 is shown as extending along one surface of negative electrode 16 which is operatively associated with absorber-separator 18 combined with the electrolyte. aluminum film 22 is in contact with positive electrode 20 which is in turn in contact with the other face of absorber-separator 18, all of the elements being operatively associated with one another. An envelope 12 of polyvinylidene fluoride homopolymer extends completely around the cell.
Envelope 12 may be a single film or a plurality of films e.g., two or three films and extends around all sides and completely envelops cell 10. Copper and aluminum leads (not shown) are passed through envelope 10 to make electrical contact with films 14 and 22, respectively and are connected to a load (not shown) to for~ an electric circuit.
The other electrolytes described herein for the rocking-chair cells may also be employed in lieu of the LiPF6 salt and LiNiO2 or LiCoO2 materials substituted for the LiMn2O4 materials in the forgoing example. Additionally, graphite rather than petroleum coke may be employed in the manuf acture of the negative electrode although, petroleum coke is especially preferred.
The vinylidene fluoride polymers of the present invention may also be employed in cells having a CA 022~1648 1998-10-1 PCT/US~)81'~ 71 - lithium organic electrolyte where the polymer is used either as a binder for particular electrode active materials, as a solid electrolyte for polymeric cells, a porous mesh supporting a quasi-solid state gel electrolyte and as the cell base material.
The vinylidene fluoride polymers of the present invention as described herein can also be used in lithium/oxyhalide cells as a bottom insulator. They may also be used in zinc bromide cells as a binder for bipolar electrodes or in nickel-metal hydride cells as a binder for the hydride electrode or for the nickel electrode.
The vinylidene fluoride polymers of the present invention are also suitable for use in a silver-zinc cell where the vinylidene fluoride polymers are used as a binder for the zinc electrode or in a lead-acid cell as a spacer between the electrodes and as a separator. The vinylidene fluoride polymers may also be used in thermal batteries for cathode active materials. In addition to nickel-metal hydride cells, the vinylidene fluoride polymers may also be used in other alkaline cells such as nickel-cadmium cells, and zinc-air cells, especially where a buffered electrolyte is employed to counteract the dehydrohalogenation effect of the alkali medium of these cells.
The following Examples further illustrate the best mode contemplated by the inventors for carrying out their invention and are to be construed as illustrative and not as in limitation thereof.
Melt viscosity measurements are by ASTM D3835 at CA 022S1648 1998-10-lS
PCT~US98/04071 ~ 232~C and 100 s-1.
Thermal properties are measured with a Differential Scanning Calorimeter (DSC) according to ASTM ~3418.
HFP content was determined by 19F NMR according to the signal assignments and method described in Pianca et al., Polymer, vol. 28, 224-230 (Feb. 1987).
A Unity 400 spectrometer at 376.3 MHz was used.
Spectra were obtained either in deuterated dimethyl formamide at 50~ C with an excitation pulse width of 8.0 microseconds and a recycle delay of 10 seconds, in deuterated dimethyl sulfoxide at 80~ C with an excitation pulse width of 6.0 microseconds and recycle delay of 5 seconds, or in deuterated acetone at 50~ C
with an excitation pulse width of 8.0 microseconds and a recycle delay of 20 seconds.
Molecular weights were measured by size exclusion chromatography ~SEC). A Waters 150 C chromatographic device with a set of PL gel 2 mixed B columns with bead size of 10 microns was used at an operating temperature of 105 degrees C. HPLC grade dimethyl sulfoxide (DMS0) was used as the eluant at flow rate of 1.0 mL/min. The samp}es were prepared by dissolution in DMS0 for 5 hours at 100 degrees C, followed by filtration.
.
CA 022~l648 l998- lO- l~
PCT/US~lU,'~ 1' 71 MPT.F! 1 Into a 7.5 liter, stainless steel reactor were charged 4.799 kg of deionized water, 0.230 kg of a 1 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.004 kg of paraffin wax. The mixture was purged with nitrogen and agitated for 30 minutes. The reactor was sealed and heated to 80 degrees Celsius.
The reactor was charged with 0.355 kg of vinylidene fluoride, 0.049 kg of hexafluoropropylene (a ratio of 88 vinylidene fluoride/12 hexafluoropropylene), and 0.120 kg of a 5 wt~ solution of ethyl acetate in deionized water. The reaction conditions were stabilized at 80 degrees Celsius and 4480 kPa, and then the polymerization was begun by introducing 0.026 kg of an initiator emulsion consisting of 2 wt~ di-n-propyl peroxydicarbonate and 0.15 wt~ mixed perfluoroalkanoate salts dispersed in deionized water.
The pressure rose to 4550 kPa with the addition of the initiator emulsion. The polymerization was maintained by the addition of the initiator emulsion at the rate of 0.112 kg per hour, and by the addition of a mixture of vinylidene fluoride/hexafluoropropylene in the ratio 95 vinylidene fluoride/5 hexafluoropropylene so as to maintain pressure. After 4.2 hours, totals of 1.890 kg of vinylidene fluoride and 0.140 kg of hexafluoropropylene had been charged to the reactor.
All feeds were stopped, and the reactor was cooled.
After 5 minutes of cooling, agitation speed was reduced by 78~ and surplus gases were vented.
Agitation was stopped, the reactor was further cooled, CA 022~1648 1998-10- lS
PCT~S98/04071 - and then it was emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with boiling water, and drying the solids at 110 degrees Celsius to yield fine powder.
The resin so made had a melt viscosity of 2770 Pa.s, had a DSC melting point of 152 degrees Celsius, and had a hexafluoropropylene content as measured by NM~
of 5.4 wt~.
MP~F! 2 Into a 7.5 liter, stainless steel reactor were charged 4.913 kg of deionized water, 0.230 kg of a 1 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.004 k~ of paraffin wax. The mixture was purged with nitrogen and agitated for 30 minutes. The reactor was sealed and heated to 80 degrees Celsius.
The reactor was charged with 0.415 kg of vinylidene fluoride, 0.215 kg of hexafluoropropylene (a ratio of 66 vinylidene fluoride/34 hexafluoropropylene), and o.olO kg of ethyl acetate. The pressure was at 4895 kPa. The reaction conditions were stabilized at 80 degrees Celsius, and then the polymerization was begun by introducing 0.040 kg of an initiator emulsion consisting of 2 wt~ di-n-propyl peroxydicarbonate and 0.15 wt% mixed perfluoroalkanoate salts dispersed in deionized water. The pressure dropped upon initiation and it was then maintained at 4825 kPa. The polymerization was maintained by the addition of the initiator emulsion at the rate of 0.176 kg per hour, and by the addition of a mixture of ~inylidene fluoride/hexafluoropropylene in the ratio 84 vinylidene fluoride/16 hexafluoropropylene so as to CA 022~1648 1998-10-1 PCT~S98/04071 - maintain pressure. After 2.2 hours, totals of 1.585 kg of vinylidene fluoride and 0.445 kg of hexafluoropropylene had been charged to the reactor.
Monomer feeds were stopped, and residual monomer was consumed by maintaining the initiator emulsion feed and 80 degrees Celsius for 20 minutes. The initiator feed and agitation were stopped and the reactor was allowed to settle 10 minutes. The reactor was cooled to 45 degrees Celsius, vented, and then it was emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with boiling water, and drying the solids at 80 degrees Celsius to yield fine powder. The resin so made had a melt viscosity of 1220 Pa.s, had a DSC melting point of 114 degrees Celsius, and had a hexafluoropropylene content as measured by NMR of 17.2 wt.~.
~X~MPT.~ 3 (Comparative Example to Example 1) Into a 7.5 liter, stainless steel reactor were charged 4.799 kg of deionized water, 0.230 kg of a 1 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.004 kg of paraffin wax. The mixture was purged with nitrogen and agitated for 30 minutes. The reactor was sealed and heated to 80 degrees Celsius.
The reactor was charged with 0.400 kg of vinylidene fluoride, 0.030 kg of hexafluoropropylene (a ratio of 93 vinylidene fluoride/7 hexafluoropropylene), and 0.120 kg of a 5 wt.~ solution of ethyl acetate in deionized water. The reaction conditions were stabilized at 80 degrees Celsius and 4480 kPa, and then the polymerization was begun by introducing 0.026 kg of an initiator emulsion consisting of 2 wt~ di-n-CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 - propyl peroxydicarbonate and 0.15 wt~ mixed perfluoroalkanoate salts dispersed in deionized water.
The polymerization was maintained by the addition of the initiator emulsion at the rate of 0.112 kg per hour, and by the addition of a mixture of vinylidene fluoride/hexafluoropropy~ene in the ratio 93 vinylidene fluoride/7 hexafluoropropylene so as to maintain pressure. After 3.1 hours, totals of 1.890 kg of vinylidene fluoride and 0.140 kg of hexafluoropropylene had been charged to the reactor.
Monomer feeds were stopped, and residual monomer was consumed by maintaining the initiator emulsion feed and 80 degrees Celsius for 20 minutes. The initiator feed and agitation were stopped, and the reactor was allowed to settle for 10 minutes. The reactor was cooled to 45 degrees Celsius, vented, and then it was emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with boiling water, and drying the solids at 110 degrees Celsius to yield fine powder. The resin so made had a melt viscosity of 2550 Pa.s, had a DSC
melting point of 154 degrees Celsius, and had a hexafluoropropylene content as measured by NMR of 6.0 wt.~.
~!lrl~MPT.~;! 4 Into a 293 liter stainless steel reactor were charged 200.0 kg of deionized water, 1.00 kg of a 10 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.015 kg of paraffin oil. The reactor was evacuated and heated to a temperature of 91 degrees Celsius during the charging, and agitation was used.
CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 To the reactor were added 12.6 kg of vinylidene fluoride, 0.8 kg of hexafluoropropylene (a ratio of 94 vinylidene fluoride/6 hexafluoropropylene), and 0.5 kg of ethyl acetate, which brought the reactor pressure to 4480 kPa. During the pressurization, when the pressure reached 3445 kPa, a feed of initiator emulsion consisting of 2 wt~ di-n-propyl peroxydicarbonate and 0.15 wt~ mixed perfluoroalkanoate salts dispersed in deionized water was begun and was maintained at 9.0 kg/h until 4.6 kg of initiator emulsion had been added. The rate of further initiator emulsion addition was adjusted so as to maintain a total monomer feed rate of 27.0 kg/h. A
monomer mixture in the ratio 94 vinylidene fluoride/6 hexafluoropropylene was fed to the reactor so as to maintain pressure at 4480 kPa until the totals of 85.3 kg of vinylidene fluoride and 5.4 kg of hexafluoropropylene had been charged to the reactor.
All feeds were stopped, and residual monomer was consumed by maintaining 91~ Celsius and agitation for 20 minutes and then by maintaining 91~ C for 35 minutes. The reactor was cooled, vented, and emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with water, and drying the solids to yield fine powder. The resin so made had a melt viscosity of 1740 Pa.s, had a DSC
melting point of 155 degrees Celsius, and had a hexafluoropropylene content as measured by NMR of 4.7 wt.~.
~MPT.~.~ 5 to 12 Copolymers of examples 5 to 8 are made similarly to W098/38687 PCT~,8~'71 copolymers of Examples 1 or 2, and copolymers of examples 9 to 12 are made similarly to copolymers of Examples 3 or 4 and are shown in Table I.
o ~ u~ ~ ~ .~r ~ u~ ~
0 ~ ~ r-~ N I O 111 ~ U'l O ~o 3 _1 0 ~ ~P O O O O ~ O 0 0 r1 ~-~ N
O o ~ r r-~ ~~ ~ r ~i ~ O r~r "~ 0 o a ~
0 u~ O O r~
,t) ~D VJ ~~ ,~, o r~ N .r '~ 'I
r~ 0 ~r ~ O O o o ,~ o o ~ ~ _~
~ o r o~D m o ~ ~ ~ o o,o ~ o ~ ~r ~ c~ "
0 ~r .r O O O O ~ O O ~ r~ ~r o ~ ~ o o ~ o ~ o ~ ~ 0 ~ ul ~
O~ O O O ~D O O U- C
~ r .~~ O ~, 0 0 'r ~ 0 ~-~ ~ ' 0"~ "~ o o o o ~1 0 0 N ~ 0 X
3 o ~ o o o ~ ~ ~ ~ o H X 0 ~ O ~, . ~ ~.In ~r ~ m ~ ~
~ ~ ~ ~ D o ,~
O ~ r ~ I o ~4 0 ~r~r o o o o ,~ o o 0 ~ o r-U~ Ul N
0 r ,~, O ~ m ~ o u~
~3 m ~ ~r o o o o ,~ o o ,~
C r m o o ~o ul O 0 ~D ~o OmI rO~ ~ O ~ N
0 ~ ~r O O O O _I O O ~ ~1 ~.~
0 Ul Ul O o 0 Ul ~D o N
m ~ o oo o o ~n 0 ~r N N 0~ r O O . ~, ~n r ~ o ~ I o 0 ~ ~n r ~ .r 0 .r~r O o o o _~ o o N ~ ~I r L
,; ~n ~ ~ 1~ s _Y ~ o L~ L~
L~ 0 ' ' >~ ) 3 L v S _ " i" y ~ o~ y, ~ ~, , ~ :~ , - S ' ~ ~ U U I ~ C Y I j ~ ~ E
~rl ~ L L~ 0 0 O~ 0 1~ L~ .
._ g L L 2 0 g ~ 2 C) 111 S
U') O U'l O
CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 The term "solution(s) having improved clarity and fluidity" as used in the specification and claims of this application means that the solution(s) of any particular copolymer of this invention having a particular nominal HFP content will provide solution(s) having descriptive properties analogous to those shown by Example 2 in Table II when dissolved in any of the solvents listed at the same concentration levels at which a copolymer having about the same particular nominal HFP content made by a typical process described in detail in the prior art provides solution descriptive properties analogous to those shown in Table II for Example 12.
T~'VAT-UATION OF T~ SOT~UTION PROP~TT~ OF T}
1 5 F~MPT,P~.~
The solution properties of examples 2 and 12 are shown in Table II. Mixtures of the indicated weight percent were prepared, using heat when necessary to dissolve the polymer completely and form a clear solution. Solutions were then allowed to cool and observed daily over a period of two weeks. The copolymer 2 showed a reduced tendency to gel and to be clearer than the copolymer 12. The retention of fluidity and clarity by the copolymer 2 is advantageous in applications which rely on polymer solutions, such as in the production of cast films and membranes.
The reduction in tendency toward gelation by the copolymers of the present invention is further CA 022~l648 lggs-lo-l~
W098/38687 PCT~S98/04071 shown in Table II A. The gelation times of propylene carbonate solutions of some of the examples are shown in the table. A Rheometrics dynamic stress rheometer DSR-200 was used to measure the gelation times of 20 wt~ solutions of the polymers in propylene carbonate (the propylene carbonate was of nominal 99.7~ purity). The rheometer was fitted with a Peltier fixture and solvent trap. A 40 mm parallel plate geometry was used with a gap of 1 mm. Solid copolymer was mixed with propylene carbonate at room temperature on the day of measurement, the container was sealed, and the solution was formed by heating and stirring the mixture in the sealed container for l.0 hour in a Pierce Reacti-Therm Heating/Stirring Module set at 120~C. The solutions were quickly loaded at the end of the dissolution period into the test fixture, which was preset at 100~C. A temperature cooling ramp in dynamic oscillatory mode at 1 Hz was begun as soon as the fixture temperature re-equilibrated at 100~C; re-equilibration typically required a minute or less. The cooling ramp was from 100~C to 15~C at a rate of 30~C/m. When 15~C was reached, a l minute equilibration time was used, and then a time sweep measurement was begun. The sample was held at 15~C during the time sweep measurement performed at l radian/s. The time sweep was continued until the gel point was reached. The gel point was taken as the point at which the solution storage modulus, G', and the loss modulus, Gn, became equal. The gel CA 022~1648 1998-10-1~
W098/38687 PCTtUS98tO4071 time was taken as the time duration in the time sweep to reach the gel point.
The relation between HFP content and the logarithm of the gel time of the 20 wt~ propylene carbonate solutions is shown in Figure 3. It can be seen that the copolymers prepared according to the present invention have longer gelation times than the copolymers prepared according to the prior art synthesis over the whole range of HFP content. The reduced tendency toward gelation by the copolymers of the present invention is advantageous in processing such solutions for film casting and other solution applications.
CA 022~l648 l998-l0-l~
TABLE II
SOLUTION PRO~l~:K~ S
Polymer ~pp~rPnre concentration and solvent [a] Example 2 Example 12 10% in MEK fluid, clear fluid clear 20~ in MER fluid, clear by day 2, loose gel, clear 30% in MEKby day 14,some gel,clear by day l, loose qel, 10 cloudy; by day 4, gel, cloudy 10% in MPK fluid, clear fluid, clear 20% in MPR fluid, clear by hour 2, some gel, clear; by day l, gel, slightly cloudy 10% in MiBK fluid, clear by day 4, gel, clear 10~ in CPO fluid, clear fluid, clear 10% in CHO fluid, clear fluid, clear 20% in CHOby day 2,some gel,clear by day 1, some gel, clear;
20 by day 2, some gel, cloudy 10~ in EtoAC fluid, clear by day 7, some gel, clear 20% in EtoAC fluid, clear by day l, fluid, cloudy;
by day 3, some gel, cloudy 10% in n-PrOAc fluid, clear fluid, clear 10% in i-PrOAc fluid, clear by day 6, some gel, clear 10% in EGMEA fluid, clear by day 6, gel, clear 10~ in DMC fluid, clear by day 7, some gel, clear 20~ in DMC fluid, clear by day l, some gel, cloudy; by day 2, mostly gel, cloudy 20% in Blend 2 fluid, clear by day 14, fluid, cloudy [a] Polymer concentrations are Wt~ unless stated otherwise. MEK is methyl ethyl ketone, MPR is methyl propyl ketone, MiBK is methyl isobutyl ketone, CPO is cyclopentanone, CHO is cycloh~Y~none, EtOAc is ethyl acetate, N-PrOAc is n-propyl acetate, i-PrOAc is isopropyl acetate, EGMEA is ethylene glycol monomethyl ether acetate, DMC is dimethyl carbonate, Blend 2 is composed of 35.4 parts MiBK, 29.8 parts CHO, and 30 parts DMC by weight.
- CA 022~1648 1998-10-1~
Tli3LE II A
SOLlrrION GEI~TION TI~nE ta]
Fxam~1e N~mher Gel~tion T~me 6 4,913 6 8,322 6 12,924 1,553 3,191 2 77,000 2 52,400 12 14,100 12 47,500 [a] 20 wt~ solutions at 15~C in propylene carbonate. Gelation time is in seconds.
E~AT.UATTON OF FTTM GLOSS ANn ~T.AT~TTy Some of the non-gelled solutions from the solution property tests were used to make films which were tested for gloss and clarity. The films were cast on a Leneta Form 2A opacity chart using a 0.127 meter draw down applicator having a 250 micrometer gap. The cast films were dried for three days at room temperature. Film gloss was determined using a HunterLab Progloss PG-2 gloss meter, and the results are shown in Table III. Film haze was measured by determining the whiteness index (CIEL~3 L* value) of the film on the black portion of the opacity chart using a HunterLab Labscan 2 colorimeter, and the results are shown in Table IV.
CA 022~1648 1998-10-1~
W098t38687 PCT~S98/04071 Films from copolymer 2 showed higher gloss from a wider range of solvents than films from copolymer 12. The haze in films from 2 and 12 was generally similar, but noticeably less haze was observed in films from 2 in several instances. The results, taken together, show that VDF/HFP copolymer of the present invention demonstrates an increased utility for high-gloss, high-transparency film applications.
CA 022~1648 1998-10-1~
- TABLE III
GLOSS OF CAST FILMS
Polymer Gloss, 20 degree / 60 degree concentration and solvent [a]Example 2 Example 12 20~ in MEK33.6 / 69.0 31.3 / 68.7 10% in MPK31.4 / 68.9 1.3 / 18.7 10~ in CPO0.7 / 16.9 2.0 / 27.7 10~ in EtOAc29.4 / 66.6 29.4 / 68.0 10% in n-PrOAc31.9 / 70.1 16.0 / 57.0 10% in i-PrOAc31.6 / 69.4 15.4 / 56.2 10% in DMC35.4 / 70.6 30.1 / 68.6 20% in Blend 234.6 / 71.2 0.1 / 2.4 [a] Polymer concentration and solvent indicates the wt% and solvent the films were cast from. MEK is methyl ethyl ketone, MPK is methyl propyl ketone, CPO is cyclopentanone, EtOAc is ethyl acetate, n-PrOAc is n-propyl acetate, i-PrOAc is isopropyl acetate, DMC is dimethyl carbonate, Blend 2 is composed of 35.4 parts methyl isob~tyl ketone, 29.8 parts cycloh~none, and 30 parts DMC by weight.
WO 98/38687 PCT/US33/0 1' 71 'rABLE IV
CLARITY OF CAST FILMS
Polymer Clarity, CIELA~3 L* [b]
concentration and solvent [a] Example 2 Exampie 12 20'~ in MEK 6.59 6.22 10% in MPK 6.19 14.48 10% in CPO 15.18 15.56 10% in EtOAc 7.38 5.84 1010% in n-PrOAc 5.64 7.34 10'~ in i-PrOAc 5.61 7.79 10% in DMC 6.21 5.73 20~ in Blend 2 5.36 17.85 [a] Polymer concentration and solvent indicates the wt'~ and solvent the films were cast from. MEK is methyl ethyl ketone, MPK is methyl propyl ketone, CPO is cyclopentanone, EtOAc is ethyl acetate, n-PrOAc is n-propyl acetate, i-PrOAc is isopropyl acetate, DMC is dimethyl carbonate, Blend 2 is composed of 35.4 parts methyl isobutyl ketone, 29.8 parts cycloh~n~ne, and 30 parts DMC by weight.
[b] Guide to haze:
L* ~ 7 no haze 257 ~ L* c 9 very slight haze 9 ~ L~ < 11 slight haze 11 ~ L* ~ 15 moderate haze 15 < L* severe haze CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 EVALUATION QF T~T~' T~T~'T~M~T PROPT~'T~TI~ OF THE T~'~MPLES
The final melting point is an important parameter ln the use and processing of semicrystalline polymers. It is known that the final melting point of VDF/HFP copolymers is related to the HFP content in the copolymers. The relation between HFP content and final melting point of the VDF/HFP copolymer examples is shown in Figure l.
The copolymers of the present invention and the copolymers prepared according to the prior art synthesis which details are available can be seen to fall on different melting point curves, indicating that they are different materials, with the prior art copolymers having a higher melting point at a given HFP content. The lower melting point property of the copolymers of the present invention can allow lower processing temperatures than for the prior art synthesis copolymers.
T~VALUATION OF E~TRACT~RT~FS IN Dl~ ~Y I ~ CARBON~TE
Gener~l Procedllre lg of polymer and 9g of dimethyl carbonate were placed in a closed 25 ml container. The contents of the container were continually agitated by appropriate means while maintaining the desired temperature by appropriate means for 24 hours. The entire contents of the container were then transferred to a centrifuge tube and centrifuged to separate undissolved polymer. The liquid phase was transferred to a suitable tared container and the solvent evaporated. The residue in the container W098/38687 PCT~S98/04071 was weighed and reported as percent by weight extractables.
The amount of polymer extracted into dimethyl carbonate at 40~C was measured. The data is shown in Table V. Copolymers prepared according to synthetic methods in the prior art for which details are available are labeled "N". Copolymers prepared according to the methods described for the present invention are labeled "U".
W098/38687 PCT~S98~IC71 TABLE V
~ffect of HFP Content, Molecular Number and Uniformity of Compositional Distribution on Polymer Dissolution in DMC
Sample }IFP ~w MnExtracta~leComposition Lot # (mole%) (40~C) DMC
K2801 4.5 460000 145000 12.0% N
K2801 4.5 495000 157000 10.5~ N
9521 2.1 427000 167000 3.11% N
9527 3.6 473000 150000 14.30~ N
9529 2.8 417000 148000 9.29% N
88 3.6 375000 138000 4.04% U
2.3 483000 188000 0.23% U
94 2.4 676000 240000 0.41~ U
96 (Exl) 2.4 409000 159000 0.28~ U
98 2.4 351000 14~000 1.11% U
100 (Ex5) 1.5 523000 194000 0.41% U
104 3.1 433000 157000 1.61~ U
A cursory ex~mi~tion shows that all N samples have higher levels of polymer extracted into dimethyl carbonate. Figure 2 shows a plot of the extractables as a function of HFP content (mole%).
Two distinct curves are outlined for the two classes of materials. The upper curve (N samples) shows significantly higher levels of extractables for a given level of HFP compared to the U curve.
Measured slopes for these curves are 3%
extractables/mole % HFP for the N polymers and l.7%
extractables/mole % HFP for the U polymers.
CA 022~l648 lsss-lo-l~
:W098/38687 PCT~S98/04071 The observed and calculated % extractables under both the single and dual functional model are shown for the N polymers in Table VI and for the U
polymers in Table VII.
Table VI
Comparison of Wt. % Extractables of N polymer as a function of HFP content or HFP content and Mn % Extractable % Extractable % Extractable (mea~) (calc model 1) (calc model 2) 12.0% 12.6% 13.4%
10.5% 12.6% 10.1%
3.11% 5.7% 3.2~
14.30% 10.0% 10.5%
9.29% 7.7% 9.7%
(Model 1) ~ Extractable = 2.9~HFP mole~) -0.4 (Model 2) ~ Extractable = 46.4 + 1.7(HFP mole~) - 0.00020(Mn) CA 022~l648 lsss-lo-l~
W098/38687 PCT~S98/04071 Table VII
Comparison of Wt.% Extractables of U polymer as a function of HFP content of HFP content of Mn % Extractable % Extractable ~ Extractable (meas) (calc model 1) (calc model 2) 4.04~ 2.9% 3.1%
0.23~ 0.71% 0.
0.41~ 0.88% 0.48 0.28% 0.88% 1.1 1.11~ 0.88~ 1.2 0.41~ -0.65~ -0.50 1.61% 2.1% 2.2 (Model 1) ~ Extractable 5 1.7(HFP mole~) -3.2 (Model 2) ~ Extractable = -1.2 + 1.5(HFP mole~) - 8 x 10~6(Mn) In the specification and the attached claims, the expression "having weight percent extractables within 1.5~ of the percent by weight extractables calculated by an equation selected from the group consisting of:
a) wt~ Extractable = 1.7(HFP mole~) - 3.2, and b) wt~ Extractable = -1.2 + 1.5(HFP mole~ x 10~6(Mn) means that the measured value of percent extractables in dimethylcarbonate at 40~C must be within 1.5 absolute percentage points from the extractable value calculated for the particular polymer by either equation.
That is, if the calculated value of ~
extractables by either equation 1 or 2 is 3.0 and the observed value is between 1.5 and 4.5% it falls ~ . ~
W098/38687 PCT~S98/04071 - within the intended coverage value. Similarly if the observed value is 8.0~ it will be within the intended coverage if the calculated value from either equation ranges from 6.5~ to 9.5~.
~Y~ple 13 - Poly~inylidene Fluoride/ Chlorotri-fluorethylene Copolymer Ha~ing Substantially Homogeneous Monomer Distribution Following a procedure analogous to that of Example l provide an initial charge containing 0.40 kg of vinylidene fluoride and 0.0124 kg of chlorotrifluorethylene (97 VDF/3 CTFE) and ~aintain the reaction by a continuous feed of 96 VDF to 4 CTFE together with initiator emulsion for a total feed convenient for the reactor size of about l.9525 kg of VDF and 0.0775 kg CTFE to obtain the title copolymer having about 4.0~ CTFE content.
In the abo~e described proceedure for determining extractables in dimethyl carbonate, centrifugation for thirty minutes at 1500 rpm at ambient temperature was employed to separate the solution from the insoluble matter and drying at 50 deg. C for 70 hours under mechanical pump vacuum was used to determine the weight of solids in the separated solution.
58065711. The quantity of an initiator required for a ,, CA 022~1648 lsss-lo-PCT~S98/04071 - polymerization is related to its activity and the temperature used for the polymerization. The total amount of initiator used is generally between 0.05% to 2.5% by weight on the total monomer weight used.
Typically, sufficient initiator is added at the beginning to start the reaction and then additional initiator may be optionally added to maintain the polymerization at a convenient rate. The initiator may be added in pure form, in solution, in suspension, or in emulsion, depending upon the initiator chosen.
As a particular example, peroxydicarbonates are conveniently added in the form of an aqueous emulsion.
As the reaction progresses, a mixture of vinylidene fluoride and hexafluoropropylene monomers is fed in a definite ratio ( second effective ratio) so as to maintain reaction pressure. The second effective ratio used corresponds to the monomer unit ratio desired in the final composition of the copolymer, and it can range up to 24% of the com~ined weight of the monomers being fed continuously throughout the reaction. The feed of vinylidene fluoride, hexafluoropropylene, and optionally initiator and chain-transfer agent is continued until the desired reactor fill is obtained.
Upon reaching the desired reactor fill, the monomer feeds are terminated. To achieve the copolymer havin~ optimum solution clarity and minimal extractables, all other feeds are stopped at the same time as the monomer feeds, and the reactor is vented as soon as is practicable. Alternatively, to achieve - CA 022~1648 1998-10-1 PCT~S98/04071 - highest yield at the expense of solution clarity and extractables, a react-out period to consume residual monomer is used with optional continuation of initiator feed. For react-out, the reaction temperature and agitation are maintained for a period S of 20 to 30 minutes, but a longer period can be used if required in order to consume monomer to the point where the reactor pressure is no longer falling to any significant degree. A settling period of typically 10 to 40 minutes may be used following the react-out period. During the settling period, temperature is maintained but no initiator feed is used. The reactor is then cooled and vented.
The product is recovered as a latex. To obtain dry resin, the latex is coagulated, the coagulum is separated and the separated coagulum may be washed.
To provide powder, the coagulum is dried.
For the coagulation step, several well-known methods can be used including freezing, the addition of acids or salts, or mechanical shear with optional heating. The powder, if desired, can be further processed into pellets or other convenient resin forms.
The electrochemical cells of the present invention are based on a positive electrode, an absorber-separator sometimes referred as a solid electrolyte and negative electrode operatively associated with one another wherein at least one of the electrodes or the absorber-separator, and preferably both electrodes and the absorber-separator CA 022~1648 1998-10-1 P~T~S98/04071 comprise a vinylidene fluoride polymer of the present invention and wherein the vinylidene fluoride polymer of the present invention electrodes have an electrode material combined therewith and the vinylidene fluoride polymer of the present invention absorber-separator has an electrolyte ~aterial combined therewith. A plurality of electrodes and absorber-separator elements can be used in the cell structure in order to increase the voltage, and/or amperage of the combined elements in a manner well known to the art.
Vinylidene fluoride polymer of the present invention is not required to have an open or closed porous structure for operability. It provides enhanced electrolyte mobility in combination with the intrinsic ionic conductivity effects of the polymer regardless of its initial porous or non porous state.
Vinylidene fluoride electrode or separator-absorber combined with electrode or electrolyte materials at the surface of the pores of the porous polymer was previously believed to make the utilization of the active material, whether electrode material or electrolyte material more efficient and provide a method for the easy manufacture of the efficient electrodes and separator-absorber structures. There are, however, other advantages to use of porous polymer structures even for the polyvinylidene fluoride polymers of the present invention.
It is also believed that the segregation of the active materials on the surface of active pores will CA 022~1648 1998-10-1 PCT~S98/04071 - allow for varying the amount of binder in the electrode of the separator-absorber to enhance strength with minimum effect on cell performance. The electrochemical cells formed in this way therefore will have improved mechanical properties and can be made to be self-supporting i.e., secondary reinforcing structures do not have to be employed such as a metal or other conventional battery casing material.
This also leads to ease of fabrication where the electrochemical cell is enveloped or enclosed in a vinylidene fluoride homopolymer which will adhere to the porous electrodes and/or the absorber-separator structures. Adhesion can be obtained by simple heat bonding or radio frequency (rf) welding or other similar processes well known in the art. Adhesives are not required, but importantly, the exterior part of the electrochemical cell (i.e., the envelope) is of the same type or a substantially similar type of material as the electrodes and absorber-separa~or and is more compatible therewith and adherent thereto, thereby simplifying and reducing the cost of manufacture in that only one type of material is used for the structural components of the cell as compared to either conventional dry cell or secondary cell construction.
Polyvinylidene fluoride in general absorbs rf frequency and may also ~e heated by dielectric techniques. Heat guns may also be used for sealing polyvinylidene fluoride surfaces under pressure.
Welding rods may also be employed to heat seal two CA 022~1648 1998-10-1 - pieces easily as is done in the fabrication of larger polyvinylidene fluoride structures. The joints obtained are usually as strong as the basic resins employed. Because polyvinylidene fluoride polymers are abrasion resistant and tough as well as chemical resistant, they are useful in the internal and external element of the battery and, as noted previously, can be assembled by non-adhesive means by heat bonding.
By selecting vinylidene fluoride polymers of the present invention for electrodes and such polymers or conventional VDF polymer for cladding that are either extremely flexible or somewhat rigid, structures can be fabricated that are in turn either flexible or somewhat rigid. Further in this regard, enhanced rigidity can be obtained by cross-linking the vinylidene fluoride homo- or copolymers in general either chemically, but preferably by employing high energy radiation such as high energy (about 10 to about 20 Mrad) electron beam radiation, with some attendant dehydrofluorination. One potential benefit is the further stabilization of the amorphous regions in the vinylidene fluoride polymers, i.e., inhibitions of crystallization over time which is important since ionic conductivity of the electrolyte is believed to occur primarily in the amorphous or open regions.
As noted previously, vinylidene fluoride polymers in general affect ionic conductivity in a manner that makes them suitable for the fabrication of electrochemical cells.
Since mobility of charged species is required in PCT~US98/04071 - electrochemical cells, it is believed that the migration of charged species in polyvinylidene fluoride polymers will be through the amorphous phase.
The vinylidene fluoride polymers of the present invention have been recognized by the invention as having enhanced amorphous phases which are more stable and particularly for the HFP and CTFE copolymers provide this benefit to conductivity and the like at lower comonomer levels, thus, providing solubility and temperature advantages approaching that of homopolymers.
In the triboelectric series, most polymers stabilize electrons. Vinylidene fluoride polymers, however, are unique in stabilizing positive holes and are one of the most effective media in this regard, presumably due to the highly negative gem-difluorocar~on group.
In the special case of lithium ion batteries such as the rocking-chair batteries described herein, the high specific charge and small ionic size of the lithium ion may lead to specific interactions in the host vinylidene fluoride poly~er environment, considering the extent of the non-polarizable, negative gem-difluorocarbon groups available.
Since conductivity is inversely related to crystallinity of the polyvinylidene fluoride polymer, it has been determined that conventional copolymers of vinylidene fluoride with about 7 to about 25 hexafluoropropylene sufficiently reduce the crystalline structure of the polymer without PCT~S98/04071 sacrificing mechanical properties so that acceptable ionic conductivity effects of the polymer can be obtained. The inventors have discovered that the vinylidene fluoride polymers of the present invention provide benefits equal to or better than the above conventional VDF/HFP copolymers at comonomer levels below 8% by weight, preferably below 6~ by weight.
When employing vinylidene fluoride polymers of the present invention in the manu~acture of electrodes or absorber-separators, plasticizers such as organic carbonates (e.g., ethylene carbonate, propylene carbonate, dimethylcarbonate and the like) are utilized in order to minimize the effect of the crystalline structure and promote ionic conductivity.
Other solvents or plasticizers may also be employed including diethoxyethane, diethylcarbonate, dimethoxyethane, dipropyl carbonate and mixtures ~ thereof especially the two or three component mixtures.
Similarly, and in accord with the present invention, the various porous or non-porous structures, depending on the their tensile strength, can be mechanically oriented by stretching or the application of tensile forces in order to enhance the amount of beta conformation within the polymer structure and thereby possibly promote ionic conductivity depending upon the electrolyte and polyvinylidene fluoride composition.
Using solvent and non-solvent combinations, polyvinylidene fluoride polymers of the present CA 022S1648 1998-10-lS
PCT~S~8/01~71 invention are cast in thin membranes. This method ls described by Benzinger et al. in U.S. Patent No.
4,384,047 which is incorporated herein by re~erence.
The electrode materials or the electrolyte materials as described herein can be incorporated into polyvinylidene fluoride solution prior to casting it into a film or sheet, after which the solution may, if desired, be converted to a porous polyvinylidene fluoride membrane combined with the electrode of electrolyte materials. These films or sheets, either with or without the electrode or electrolyte materials can be any where from about 0.25 to about 100, particularly from about 0.5 to about 10, and especially from about 1 to about 8 mils thick, and are especially suitable for further treatment by stretching or the application of tensile forces in order to promote the beta conformation necessary to achieve ferroelectric properties in polyvinylidene fluoride.
There are three classes of organic liquids, that may be used to make solutions or dispersions of vinylidene fluoride polymers. Active solvents are those organic li~uids that dissolve or swell vinylidene fluoride polymers at room temperature and typically consist of lower alkyl ketones, esters and amides. Latent solvents are those organic liquids that do not dissolve vinylidene fluoride homo- or copolymers at room temperature; however, will dissolve polyvinylidene fluoride at elevated temperatures and typically are medium chain length alkyl ketones, CA 022~1648 1998-10- lS
PCT~S98/04071 - esters, glycol ethers and organic carbonates. Non-solvents are organic liquids that do not dissolve or swell vinylidene fluoride polymers up to the boiling point of the liquid or the crystalline melting point of the vinylidene fluoride polymer, whichever condition is met first. These liquids typically are aromatic hydrocarbons, aliphatic hydro-carbons and chlorinated hydrocarbons or other chlorinated organic liquids. The solvents and latent solvents are used in the manufacture of the polyvinylidene fluoride films or sheets of the present invention.
Examples of these organic liquids are given in Table A which follows.
CA 022S1648 1998-10-lS
PCT~S98/04071 - TABLE A
LIQUIDS TO PREPARE SOLUTIONS OR DISPERSIONS OF PVDF
ACTIVE SOLVENTS LATENT SOLVENTS NON SOLVENTS
(APPROX.) DISSOLUTION
TEMPERATURE IN ~C
Acetone Butyrolactone (65) Hexane TetrahydrofuranIsophorone (75) Pentane 5Methyl Ethyl KetoneMethyl Isoamyl Ketone Benzene (102) Dimethyl FormamideCycloh~n~ (70) Toluene Dimethyl Acetamide Dimethyl Phthalate (110) Methanol Tetramethyl Urea Propylene Glycol Methyl Ethanol Ether (115) Dimethyl Sulfcxide Propylene Carbonate (80) Car~on Tetrachloride Trimethyl Phosphate Diacetone Alcohol (100) o-Dichlorobenzene N-Methyl Glycerol Tricetate (100) Trichloroethylene Pyrrolidone The suitability of any given liquid depends upon the exact PVDF resin type and grade.
Other methods have been developed for the manufacture, when desired, of open cell foam porous polyvlnylidene fluoride polymers which are formulated to contain chemical or physical blowing agents such as absorbed carbon dioxide. It is preferred to use physical blowing agents in the manufacture of electrochemical cells since trace amounts of the chemical ~lowing agents in the foam structure could adversely affect the functioning of the cell. Where carbon dioxide or comparable physical blowing agents are employed, they are incorporated into the polyvinylidene fluoride at super critical pressures CA 022~l648 l998- lO- l~
PCT/US3~i~1C 1'71 followed by heat treatment to expand the article thus produced. Open cell film5 of varying thickness have been made in this manner with excellent mechanical integrity and which have specific gravities about one as compared to solid polyvinylidene fluoride which has a specific gravity of from about 1.76 about 1.78.
Similarly, polyvinylidene fluoride powders can be sintered to form a porous structure by heating the powders in a non-solvent slurry, or under pressure between opposed platens, until the individual particles sufficiently melt flow into one another to form the desired open cell structure. Other art known methods for sintering powder polymers such as PT~E for forming open cell porous structures as described by Menassen et al . "A Polymer Chemist ' s View on Fuel Cell Electrodes,~' Procee~ing of the 34th Internation~l Power Source SymDosium, June 25-28, 1990, pp. 408-10 can also be used.
A porous film made by casting polyvinylidene provide polymers of the present invention from a mixture of solvents and non-solvents as described by Benzinger et al. in U.S. Patent 4,383,047, which is about 10 mils thick after formation from the casting solution, may be utilized for the manufacture of an electrochemical cell. The polymer comprises a copolymer of Example 1 herein below. This film is used in fabricating an absorber-separator of solid electrolyte by making a solution of LiPF6 in 1:1 mixture by weight of ethylene carbonate:propylene carbonate which is heated to about 125~C and the CA 022~l648 lsss-lo-PCT~S98/04071 - porous copolymer film immersed in the solution until it is com~ined with the film.
Similarly, a positive electrode is made from the same porous copolymer. A dispersion of LiMn2O4, SS
carbon black and LiPF6 in a 1:1 mixture of ethylene carbonate and propylene carbonate along with tetrahydrofuran (THF) was combined with the porous film by soaking the film in the suspension which is agitated in a vibrating beaker in order to keep solid material in suspension until adequately combined with the film. The film is then placed on an aluminum foil.
A negative electrode is prepared by making a dispersion or suspension of petroleum coke, SS carbon black and LiPF6 in a 1:1 ethylene carbonate propylene carbonate solution in the same manner as was done for the preparation of the positive electrode and after combining the suspension with the porous film, a copper foil was placed on the film.
The proportions of the various components of the electrode and the absorber-separator or solid electrolyte are substantially the same as those set forth in Examples 1 and 8 of Gozdz et al., U.S. Patent No. 5,296,318.
The electrodes and electrolyte can also be made from sintered polyvinylidene fluoride by forming a dry blend of the electrode or electrolyte materials with powdered polyvinylidene fluoride. Dry mixing techniques, known in the art may be employed, such as tumbler type mixing. For example, the mixture of _ . .
CA 022~1648 1998-10-1 PCT~S~0l~71 polyvinylidene fluoride powder and the electrode or electrolyte materials can be subjected to tumbling or ball milling for a time to sufficiently ensure that a good mixture is obtained. A steel or other metal vessel, or ceramic vessel is employed, especially where either is lined with a polyvinylidene fluoride or PTFE layer. In the case of ball milling, steel or other metal, or ceramic grinding balls, also coated with a polyvinylidene fluoride or PTFE layer are used.
The polyvinylidene fluoride or PTFE coating is employed to substantially minimize or substantially eliminate the introduction of impurities into the system. The milled mixtures are formed into electrodes and electrolytes by the application of heat and pressure as noted herein.
One of skill in the art will recognize that non-porous VDF/HFP copolymer of the 1st composition aspect of the invention or other vinylidene fluoride polymers of the invention, porous or non-porous may be substituted for the described VDF/HFP of Example 1 to make analogous batteries.
Solvents such as ethylene carbonate and propylene carbonate, and their equivalents, especially as noted herein, including mixtures thereof, which are employed in the electrode or electrolyte can be added afterwards by soaking the electrodes and electrolyte structures in such solvents. The soaking can be carried out at room temperature or above to maximize the solvating effect of these materials and to produce optimum ionic conductivity n the electrodes or electrolyte.
CA 02251648 1998-10-lS
PCT~S98/0~~71 ~ The positive electrode and the negative electrode thus prepared, are then placed on opposite sides of the absorber-separator prepared as described above with the copper and aluminum surfaces facing outwardly to form a cell as illustrated in Fig. 4 in which copper film 14 is shown as extending along one surface of negative electrode 16 which is operatively associated with absorber-separator 18 combined with the electrolyte. aluminum film 22 is in contact with positive electrode 20 which is in turn in contact with the other face of absorber-separator 18, all of the elements being operatively associated with one another. An envelope 12 of polyvinylidene fluoride homopolymer extends completely around the cell.
Envelope 12 may be a single film or a plurality of films e.g., two or three films and extends around all sides and completely envelops cell 10. Copper and aluminum leads (not shown) are passed through envelope 10 to make electrical contact with films 14 and 22, respectively and are connected to a load (not shown) to for~ an electric circuit.
The other electrolytes described herein for the rocking-chair cells may also be employed in lieu of the LiPF6 salt and LiNiO2 or LiCoO2 materials substituted for the LiMn2O4 materials in the forgoing example. Additionally, graphite rather than petroleum coke may be employed in the manuf acture of the negative electrode although, petroleum coke is especially preferred.
The vinylidene fluoride polymers of the present invention may also be employed in cells having a CA 022~1648 1998-10-1 PCT/US~)81'~ 71 - lithium organic electrolyte where the polymer is used either as a binder for particular electrode active materials, as a solid electrolyte for polymeric cells, a porous mesh supporting a quasi-solid state gel electrolyte and as the cell base material.
The vinylidene fluoride polymers of the present invention as described herein can also be used in lithium/oxyhalide cells as a bottom insulator. They may also be used in zinc bromide cells as a binder for bipolar electrodes or in nickel-metal hydride cells as a binder for the hydride electrode or for the nickel electrode.
The vinylidene fluoride polymers of the present invention are also suitable for use in a silver-zinc cell where the vinylidene fluoride polymers are used as a binder for the zinc electrode or in a lead-acid cell as a spacer between the electrodes and as a separator. The vinylidene fluoride polymers may also be used in thermal batteries for cathode active materials. In addition to nickel-metal hydride cells, the vinylidene fluoride polymers may also be used in other alkaline cells such as nickel-cadmium cells, and zinc-air cells, especially where a buffered electrolyte is employed to counteract the dehydrohalogenation effect of the alkali medium of these cells.
The following Examples further illustrate the best mode contemplated by the inventors for carrying out their invention and are to be construed as illustrative and not as in limitation thereof.
Melt viscosity measurements are by ASTM D3835 at CA 022S1648 1998-10-lS
PCT~US98/04071 ~ 232~C and 100 s-1.
Thermal properties are measured with a Differential Scanning Calorimeter (DSC) according to ASTM ~3418.
HFP content was determined by 19F NMR according to the signal assignments and method described in Pianca et al., Polymer, vol. 28, 224-230 (Feb. 1987).
A Unity 400 spectrometer at 376.3 MHz was used.
Spectra were obtained either in deuterated dimethyl formamide at 50~ C with an excitation pulse width of 8.0 microseconds and a recycle delay of 10 seconds, in deuterated dimethyl sulfoxide at 80~ C with an excitation pulse width of 6.0 microseconds and recycle delay of 5 seconds, or in deuterated acetone at 50~ C
with an excitation pulse width of 8.0 microseconds and a recycle delay of 20 seconds.
Molecular weights were measured by size exclusion chromatography ~SEC). A Waters 150 C chromatographic device with a set of PL gel 2 mixed B columns with bead size of 10 microns was used at an operating temperature of 105 degrees C. HPLC grade dimethyl sulfoxide (DMS0) was used as the eluant at flow rate of 1.0 mL/min. The samp}es were prepared by dissolution in DMS0 for 5 hours at 100 degrees C, followed by filtration.
.
CA 022~l648 l998- lO- l~
PCT/US~lU,'~ 1' 71 MPT.F! 1 Into a 7.5 liter, stainless steel reactor were charged 4.799 kg of deionized water, 0.230 kg of a 1 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.004 kg of paraffin wax. The mixture was purged with nitrogen and agitated for 30 minutes. The reactor was sealed and heated to 80 degrees Celsius.
The reactor was charged with 0.355 kg of vinylidene fluoride, 0.049 kg of hexafluoropropylene (a ratio of 88 vinylidene fluoride/12 hexafluoropropylene), and 0.120 kg of a 5 wt~ solution of ethyl acetate in deionized water. The reaction conditions were stabilized at 80 degrees Celsius and 4480 kPa, and then the polymerization was begun by introducing 0.026 kg of an initiator emulsion consisting of 2 wt~ di-n-propyl peroxydicarbonate and 0.15 wt~ mixed perfluoroalkanoate salts dispersed in deionized water.
The pressure rose to 4550 kPa with the addition of the initiator emulsion. The polymerization was maintained by the addition of the initiator emulsion at the rate of 0.112 kg per hour, and by the addition of a mixture of vinylidene fluoride/hexafluoropropylene in the ratio 95 vinylidene fluoride/5 hexafluoropropylene so as to maintain pressure. After 4.2 hours, totals of 1.890 kg of vinylidene fluoride and 0.140 kg of hexafluoropropylene had been charged to the reactor.
All feeds were stopped, and the reactor was cooled.
After 5 minutes of cooling, agitation speed was reduced by 78~ and surplus gases were vented.
Agitation was stopped, the reactor was further cooled, CA 022~1648 1998-10- lS
PCT~S98/04071 - and then it was emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with boiling water, and drying the solids at 110 degrees Celsius to yield fine powder.
The resin so made had a melt viscosity of 2770 Pa.s, had a DSC melting point of 152 degrees Celsius, and had a hexafluoropropylene content as measured by NM~
of 5.4 wt~.
MP~F! 2 Into a 7.5 liter, stainless steel reactor were charged 4.913 kg of deionized water, 0.230 kg of a 1 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.004 k~ of paraffin wax. The mixture was purged with nitrogen and agitated for 30 minutes. The reactor was sealed and heated to 80 degrees Celsius.
The reactor was charged with 0.415 kg of vinylidene fluoride, 0.215 kg of hexafluoropropylene (a ratio of 66 vinylidene fluoride/34 hexafluoropropylene), and o.olO kg of ethyl acetate. The pressure was at 4895 kPa. The reaction conditions were stabilized at 80 degrees Celsius, and then the polymerization was begun by introducing 0.040 kg of an initiator emulsion consisting of 2 wt~ di-n-propyl peroxydicarbonate and 0.15 wt% mixed perfluoroalkanoate salts dispersed in deionized water. The pressure dropped upon initiation and it was then maintained at 4825 kPa. The polymerization was maintained by the addition of the initiator emulsion at the rate of 0.176 kg per hour, and by the addition of a mixture of ~inylidene fluoride/hexafluoropropylene in the ratio 84 vinylidene fluoride/16 hexafluoropropylene so as to CA 022~1648 1998-10-1 PCT~S98/04071 - maintain pressure. After 2.2 hours, totals of 1.585 kg of vinylidene fluoride and 0.445 kg of hexafluoropropylene had been charged to the reactor.
Monomer feeds were stopped, and residual monomer was consumed by maintaining the initiator emulsion feed and 80 degrees Celsius for 20 minutes. The initiator feed and agitation were stopped and the reactor was allowed to settle 10 minutes. The reactor was cooled to 45 degrees Celsius, vented, and then it was emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with boiling water, and drying the solids at 80 degrees Celsius to yield fine powder. The resin so made had a melt viscosity of 1220 Pa.s, had a DSC melting point of 114 degrees Celsius, and had a hexafluoropropylene content as measured by NMR of 17.2 wt.~.
~X~MPT.~ 3 (Comparative Example to Example 1) Into a 7.5 liter, stainless steel reactor were charged 4.799 kg of deionized water, 0.230 kg of a 1 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.004 kg of paraffin wax. The mixture was purged with nitrogen and agitated for 30 minutes. The reactor was sealed and heated to 80 degrees Celsius.
The reactor was charged with 0.400 kg of vinylidene fluoride, 0.030 kg of hexafluoropropylene (a ratio of 93 vinylidene fluoride/7 hexafluoropropylene), and 0.120 kg of a 5 wt.~ solution of ethyl acetate in deionized water. The reaction conditions were stabilized at 80 degrees Celsius and 4480 kPa, and then the polymerization was begun by introducing 0.026 kg of an initiator emulsion consisting of 2 wt~ di-n-CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 - propyl peroxydicarbonate and 0.15 wt~ mixed perfluoroalkanoate salts dispersed in deionized water.
The polymerization was maintained by the addition of the initiator emulsion at the rate of 0.112 kg per hour, and by the addition of a mixture of vinylidene fluoride/hexafluoropropy~ene in the ratio 93 vinylidene fluoride/7 hexafluoropropylene so as to maintain pressure. After 3.1 hours, totals of 1.890 kg of vinylidene fluoride and 0.140 kg of hexafluoropropylene had been charged to the reactor.
Monomer feeds were stopped, and residual monomer was consumed by maintaining the initiator emulsion feed and 80 degrees Celsius for 20 minutes. The initiator feed and agitation were stopped, and the reactor was allowed to settle for 10 minutes. The reactor was cooled to 45 degrees Celsius, vented, and then it was emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with boiling water, and drying the solids at 110 degrees Celsius to yield fine powder. The resin so made had a melt viscosity of 2550 Pa.s, had a DSC
melting point of 154 degrees Celsius, and had a hexafluoropropylene content as measured by NMR of 6.0 wt.~.
~!lrl~MPT.~;! 4 Into a 293 liter stainless steel reactor were charged 200.0 kg of deionized water, 1.00 kg of a 10 wt~ solution of a mixture of perfluoroalkanoate salts, and 0.015 kg of paraffin oil. The reactor was evacuated and heated to a temperature of 91 degrees Celsius during the charging, and agitation was used.
CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 To the reactor were added 12.6 kg of vinylidene fluoride, 0.8 kg of hexafluoropropylene (a ratio of 94 vinylidene fluoride/6 hexafluoropropylene), and 0.5 kg of ethyl acetate, which brought the reactor pressure to 4480 kPa. During the pressurization, when the pressure reached 3445 kPa, a feed of initiator emulsion consisting of 2 wt~ di-n-propyl peroxydicarbonate and 0.15 wt~ mixed perfluoroalkanoate salts dispersed in deionized water was begun and was maintained at 9.0 kg/h until 4.6 kg of initiator emulsion had been added. The rate of further initiator emulsion addition was adjusted so as to maintain a total monomer feed rate of 27.0 kg/h. A
monomer mixture in the ratio 94 vinylidene fluoride/6 hexafluoropropylene was fed to the reactor so as to maintain pressure at 4480 kPa until the totals of 85.3 kg of vinylidene fluoride and 5.4 kg of hexafluoropropylene had been charged to the reactor.
All feeds were stopped, and residual monomer was consumed by maintaining 91~ Celsius and agitation for 20 minutes and then by maintaining 91~ C for 35 minutes. The reactor was cooled, vented, and emptied of latex. Polymer resin was isolated by coagulating the latex, washing the resulting solids with water, and drying the solids to yield fine powder. The resin so made had a melt viscosity of 1740 Pa.s, had a DSC
melting point of 155 degrees Celsius, and had a hexafluoropropylene content as measured by NMR of 4.7 wt.~.
~MPT.~.~ 5 to 12 Copolymers of examples 5 to 8 are made similarly to W098/38687 PCT~,8~'71 copolymers of Examples 1 or 2, and copolymers of examples 9 to 12 are made similarly to copolymers of Examples 3 or 4 and are shown in Table I.
o ~ u~ ~ ~ .~r ~ u~ ~
0 ~ ~ r-~ N I O 111 ~ U'l O ~o 3 _1 0 ~ ~P O O O O ~ O 0 0 r1 ~-~ N
O o ~ r r-~ ~~ ~ r ~i ~ O r~r "~ 0 o a ~
0 u~ O O r~
,t) ~D VJ ~~ ,~, o r~ N .r '~ 'I
r~ 0 ~r ~ O O o o ,~ o o ~ ~ _~
~ o r o~D m o ~ ~ ~ o o,o ~ o ~ ~r ~ c~ "
0 ~r .r O O O O ~ O O ~ r~ ~r o ~ ~ o o ~ o ~ o ~ ~ 0 ~ ul ~
O~ O O O ~D O O U- C
~ r .~~ O ~, 0 0 'r ~ 0 ~-~ ~ ' 0"~ "~ o o o o ~1 0 0 N ~ 0 X
3 o ~ o o o ~ ~ ~ ~ o H X 0 ~ O ~, . ~ ~.In ~r ~ m ~ ~
~ ~ ~ ~ D o ,~
O ~ r ~ I o ~4 0 ~r~r o o o o ,~ o o 0 ~ o r-U~ Ul N
0 r ,~, O ~ m ~ o u~
~3 m ~ ~r o o o o ,~ o o ,~
C r m o o ~o ul O 0 ~D ~o OmI rO~ ~ O ~ N
0 ~ ~r O O O O _I O O ~ ~1 ~.~
0 Ul Ul O o 0 Ul ~D o N
m ~ o oo o o ~n 0 ~r N N 0~ r O O . ~, ~n r ~ o ~ I o 0 ~ ~n r ~ .r 0 .r~r O o o o _~ o o N ~ ~I r L
,; ~n ~ ~ 1~ s _Y ~ o L~ L~
L~ 0 ' ' >~ ) 3 L v S _ " i" y ~ o~ y, ~ ~, , ~ :~ , - S ' ~ ~ U U I ~ C Y I j ~ ~ E
~rl ~ L L~ 0 0 O~ 0 1~ L~ .
._ g L L 2 0 g ~ 2 C) 111 S
U') O U'l O
CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 The term "solution(s) having improved clarity and fluidity" as used in the specification and claims of this application means that the solution(s) of any particular copolymer of this invention having a particular nominal HFP content will provide solution(s) having descriptive properties analogous to those shown by Example 2 in Table II when dissolved in any of the solvents listed at the same concentration levels at which a copolymer having about the same particular nominal HFP content made by a typical process described in detail in the prior art provides solution descriptive properties analogous to those shown in Table II for Example 12.
T~'VAT-UATION OF T~ SOT~UTION PROP~TT~ OF T}
1 5 F~MPT,P~.~
The solution properties of examples 2 and 12 are shown in Table II. Mixtures of the indicated weight percent were prepared, using heat when necessary to dissolve the polymer completely and form a clear solution. Solutions were then allowed to cool and observed daily over a period of two weeks. The copolymer 2 showed a reduced tendency to gel and to be clearer than the copolymer 12. The retention of fluidity and clarity by the copolymer 2 is advantageous in applications which rely on polymer solutions, such as in the production of cast films and membranes.
The reduction in tendency toward gelation by the copolymers of the present invention is further CA 022~l648 lggs-lo-l~
W098/38687 PCT~S98/04071 shown in Table II A. The gelation times of propylene carbonate solutions of some of the examples are shown in the table. A Rheometrics dynamic stress rheometer DSR-200 was used to measure the gelation times of 20 wt~ solutions of the polymers in propylene carbonate (the propylene carbonate was of nominal 99.7~ purity). The rheometer was fitted with a Peltier fixture and solvent trap. A 40 mm parallel plate geometry was used with a gap of 1 mm. Solid copolymer was mixed with propylene carbonate at room temperature on the day of measurement, the container was sealed, and the solution was formed by heating and stirring the mixture in the sealed container for l.0 hour in a Pierce Reacti-Therm Heating/Stirring Module set at 120~C. The solutions were quickly loaded at the end of the dissolution period into the test fixture, which was preset at 100~C. A temperature cooling ramp in dynamic oscillatory mode at 1 Hz was begun as soon as the fixture temperature re-equilibrated at 100~C; re-equilibration typically required a minute or less. The cooling ramp was from 100~C to 15~C at a rate of 30~C/m. When 15~C was reached, a l minute equilibration time was used, and then a time sweep measurement was begun. The sample was held at 15~C during the time sweep measurement performed at l radian/s. The time sweep was continued until the gel point was reached. The gel point was taken as the point at which the solution storage modulus, G', and the loss modulus, Gn, became equal. The gel CA 022~1648 1998-10-1~
W098/38687 PCTtUS98tO4071 time was taken as the time duration in the time sweep to reach the gel point.
The relation between HFP content and the logarithm of the gel time of the 20 wt~ propylene carbonate solutions is shown in Figure 3. It can be seen that the copolymers prepared according to the present invention have longer gelation times than the copolymers prepared according to the prior art synthesis over the whole range of HFP content. The reduced tendency toward gelation by the copolymers of the present invention is advantageous in processing such solutions for film casting and other solution applications.
CA 022~l648 l998-l0-l~
TABLE II
SOLUTION PRO~l~:K~ S
Polymer ~pp~rPnre concentration and solvent [a] Example 2 Example 12 10% in MEK fluid, clear fluid clear 20~ in MER fluid, clear by day 2, loose gel, clear 30% in MEKby day 14,some gel,clear by day l, loose qel, 10 cloudy; by day 4, gel, cloudy 10% in MPK fluid, clear fluid, clear 20% in MPR fluid, clear by hour 2, some gel, clear; by day l, gel, slightly cloudy 10% in MiBK fluid, clear by day 4, gel, clear 10~ in CPO fluid, clear fluid, clear 10% in CHO fluid, clear fluid, clear 20% in CHOby day 2,some gel,clear by day 1, some gel, clear;
20 by day 2, some gel, cloudy 10~ in EtoAC fluid, clear by day 7, some gel, clear 20% in EtoAC fluid, clear by day l, fluid, cloudy;
by day 3, some gel, cloudy 10% in n-PrOAc fluid, clear fluid, clear 10% in i-PrOAc fluid, clear by day 6, some gel, clear 10% in EGMEA fluid, clear by day 6, gel, clear 10~ in DMC fluid, clear by day 7, some gel, clear 20~ in DMC fluid, clear by day l, some gel, cloudy; by day 2, mostly gel, cloudy 20% in Blend 2 fluid, clear by day 14, fluid, cloudy [a] Polymer concentrations are Wt~ unless stated otherwise. MEK is methyl ethyl ketone, MPR is methyl propyl ketone, MiBK is methyl isobutyl ketone, CPO is cyclopentanone, CHO is cycloh~Y~none, EtOAc is ethyl acetate, N-PrOAc is n-propyl acetate, i-PrOAc is isopropyl acetate, EGMEA is ethylene glycol monomethyl ether acetate, DMC is dimethyl carbonate, Blend 2 is composed of 35.4 parts MiBK, 29.8 parts CHO, and 30 parts DMC by weight.
- CA 022~1648 1998-10-1~
Tli3LE II A
SOLlrrION GEI~TION TI~nE ta]
Fxam~1e N~mher Gel~tion T~me 6 4,913 6 8,322 6 12,924 1,553 3,191 2 77,000 2 52,400 12 14,100 12 47,500 [a] 20 wt~ solutions at 15~C in propylene carbonate. Gelation time is in seconds.
E~AT.UATTON OF FTTM GLOSS ANn ~T.AT~TTy Some of the non-gelled solutions from the solution property tests were used to make films which were tested for gloss and clarity. The films were cast on a Leneta Form 2A opacity chart using a 0.127 meter draw down applicator having a 250 micrometer gap. The cast films were dried for three days at room temperature. Film gloss was determined using a HunterLab Progloss PG-2 gloss meter, and the results are shown in Table III. Film haze was measured by determining the whiteness index (CIEL~3 L* value) of the film on the black portion of the opacity chart using a HunterLab Labscan 2 colorimeter, and the results are shown in Table IV.
CA 022~1648 1998-10-1~
W098t38687 PCT~S98/04071 Films from copolymer 2 showed higher gloss from a wider range of solvents than films from copolymer 12. The haze in films from 2 and 12 was generally similar, but noticeably less haze was observed in films from 2 in several instances. The results, taken together, show that VDF/HFP copolymer of the present invention demonstrates an increased utility for high-gloss, high-transparency film applications.
CA 022~1648 1998-10-1~
- TABLE III
GLOSS OF CAST FILMS
Polymer Gloss, 20 degree / 60 degree concentration and solvent [a]Example 2 Example 12 20~ in MEK33.6 / 69.0 31.3 / 68.7 10% in MPK31.4 / 68.9 1.3 / 18.7 10~ in CPO0.7 / 16.9 2.0 / 27.7 10~ in EtOAc29.4 / 66.6 29.4 / 68.0 10% in n-PrOAc31.9 / 70.1 16.0 / 57.0 10% in i-PrOAc31.6 / 69.4 15.4 / 56.2 10% in DMC35.4 / 70.6 30.1 / 68.6 20% in Blend 234.6 / 71.2 0.1 / 2.4 [a] Polymer concentration and solvent indicates the wt% and solvent the films were cast from. MEK is methyl ethyl ketone, MPK is methyl propyl ketone, CPO is cyclopentanone, EtOAc is ethyl acetate, n-PrOAc is n-propyl acetate, i-PrOAc is isopropyl acetate, DMC is dimethyl carbonate, Blend 2 is composed of 35.4 parts methyl isob~tyl ketone, 29.8 parts cycloh~none, and 30 parts DMC by weight.
WO 98/38687 PCT/US33/0 1' 71 'rABLE IV
CLARITY OF CAST FILMS
Polymer Clarity, CIELA~3 L* [b]
concentration and solvent [a] Example 2 Exampie 12 20'~ in MEK 6.59 6.22 10% in MPK 6.19 14.48 10% in CPO 15.18 15.56 10% in EtOAc 7.38 5.84 1010% in n-PrOAc 5.64 7.34 10'~ in i-PrOAc 5.61 7.79 10% in DMC 6.21 5.73 20~ in Blend 2 5.36 17.85 [a] Polymer concentration and solvent indicates the wt'~ and solvent the films were cast from. MEK is methyl ethyl ketone, MPK is methyl propyl ketone, CPO is cyclopentanone, EtOAc is ethyl acetate, n-PrOAc is n-propyl acetate, i-PrOAc is isopropyl acetate, DMC is dimethyl carbonate, Blend 2 is composed of 35.4 parts methyl isobutyl ketone, 29.8 parts cycloh~n~ne, and 30 parts DMC by weight.
[b] Guide to haze:
L* ~ 7 no haze 257 ~ L* c 9 very slight haze 9 ~ L~ < 11 slight haze 11 ~ L* ~ 15 moderate haze 15 < L* severe haze CA 022~1648 1998-10-1~
W098/38687 PCT~S98/04071 EVALUATION QF T~T~' T~T~'T~M~T PROPT~'T~TI~ OF THE T~'~MPLES
The final melting point is an important parameter ln the use and processing of semicrystalline polymers. It is known that the final melting point of VDF/HFP copolymers is related to the HFP content in the copolymers. The relation between HFP content and final melting point of the VDF/HFP copolymer examples is shown in Figure l.
The copolymers of the present invention and the copolymers prepared according to the prior art synthesis which details are available can be seen to fall on different melting point curves, indicating that they are different materials, with the prior art copolymers having a higher melting point at a given HFP content. The lower melting point property of the copolymers of the present invention can allow lower processing temperatures than for the prior art synthesis copolymers.
T~VALUATION OF E~TRACT~RT~FS IN Dl~ ~Y I ~ CARBON~TE
Gener~l Procedllre lg of polymer and 9g of dimethyl carbonate were placed in a closed 25 ml container. The contents of the container were continually agitated by appropriate means while maintaining the desired temperature by appropriate means for 24 hours. The entire contents of the container were then transferred to a centrifuge tube and centrifuged to separate undissolved polymer. The liquid phase was transferred to a suitable tared container and the solvent evaporated. The residue in the container W098/38687 PCT~S98/04071 was weighed and reported as percent by weight extractables.
The amount of polymer extracted into dimethyl carbonate at 40~C was measured. The data is shown in Table V. Copolymers prepared according to synthetic methods in the prior art for which details are available are labeled "N". Copolymers prepared according to the methods described for the present invention are labeled "U".
W098/38687 PCT~S98~IC71 TABLE V
~ffect of HFP Content, Molecular Number and Uniformity of Compositional Distribution on Polymer Dissolution in DMC
Sample }IFP ~w MnExtracta~leComposition Lot # (mole%) (40~C) DMC
K2801 4.5 460000 145000 12.0% N
K2801 4.5 495000 157000 10.5~ N
9521 2.1 427000 167000 3.11% N
9527 3.6 473000 150000 14.30~ N
9529 2.8 417000 148000 9.29% N
88 3.6 375000 138000 4.04% U
2.3 483000 188000 0.23% U
94 2.4 676000 240000 0.41~ U
96 (Exl) 2.4 409000 159000 0.28~ U
98 2.4 351000 14~000 1.11% U
100 (Ex5) 1.5 523000 194000 0.41% U
104 3.1 433000 157000 1.61~ U
A cursory ex~mi~tion shows that all N samples have higher levels of polymer extracted into dimethyl carbonate. Figure 2 shows a plot of the extractables as a function of HFP content (mole%).
Two distinct curves are outlined for the two classes of materials. The upper curve (N samples) shows significantly higher levels of extractables for a given level of HFP compared to the U curve.
Measured slopes for these curves are 3%
extractables/mole % HFP for the N polymers and l.7%
extractables/mole % HFP for the U polymers.
CA 022~l648 lsss-lo-l~
:W098/38687 PCT~S98/04071 The observed and calculated % extractables under both the single and dual functional model are shown for the N polymers in Table VI and for the U
polymers in Table VII.
Table VI
Comparison of Wt. % Extractables of N polymer as a function of HFP content or HFP content and Mn % Extractable % Extractable % Extractable (mea~) (calc model 1) (calc model 2) 12.0% 12.6% 13.4%
10.5% 12.6% 10.1%
3.11% 5.7% 3.2~
14.30% 10.0% 10.5%
9.29% 7.7% 9.7%
(Model 1) ~ Extractable = 2.9~HFP mole~) -0.4 (Model 2) ~ Extractable = 46.4 + 1.7(HFP mole~) - 0.00020(Mn) CA 022~l648 lsss-lo-l~
W098/38687 PCT~S98/04071 Table VII
Comparison of Wt.% Extractables of U polymer as a function of HFP content of HFP content of Mn % Extractable % Extractable ~ Extractable (meas) (calc model 1) (calc model 2) 4.04~ 2.9% 3.1%
0.23~ 0.71% 0.
0.41~ 0.88% 0.48 0.28% 0.88% 1.1 1.11~ 0.88~ 1.2 0.41~ -0.65~ -0.50 1.61% 2.1% 2.2 (Model 1) ~ Extractable 5 1.7(HFP mole~) -3.2 (Model 2) ~ Extractable = -1.2 + 1.5(HFP mole~) - 8 x 10~6(Mn) In the specification and the attached claims, the expression "having weight percent extractables within 1.5~ of the percent by weight extractables calculated by an equation selected from the group consisting of:
a) wt~ Extractable = 1.7(HFP mole~) - 3.2, and b) wt~ Extractable = -1.2 + 1.5(HFP mole~ x 10~6(Mn) means that the measured value of percent extractables in dimethylcarbonate at 40~C must be within 1.5 absolute percentage points from the extractable value calculated for the particular polymer by either equation.
That is, if the calculated value of ~
extractables by either equation 1 or 2 is 3.0 and the observed value is between 1.5 and 4.5% it falls ~ . ~
W098/38687 PCT~S98/04071 - within the intended coverage value. Similarly if the observed value is 8.0~ it will be within the intended coverage if the calculated value from either equation ranges from 6.5~ to 9.5~.
~Y~ple 13 - Poly~inylidene Fluoride/ Chlorotri-fluorethylene Copolymer Ha~ing Substantially Homogeneous Monomer Distribution Following a procedure analogous to that of Example l provide an initial charge containing 0.40 kg of vinylidene fluoride and 0.0124 kg of chlorotrifluorethylene (97 VDF/3 CTFE) and ~aintain the reaction by a continuous feed of 96 VDF to 4 CTFE together with initiator emulsion for a total feed convenient for the reactor size of about l.9525 kg of VDF and 0.0775 kg CTFE to obtain the title copolymer having about 4.0~ CTFE content.
In the abo~e described proceedure for determining extractables in dimethyl carbonate, centrifugation for thirty minutes at 1500 rpm at ambient temperature was employed to separate the solution from the insoluble matter and drying at 50 deg. C for 70 hours under mechanical pump vacuum was used to determine the weight of solids in the separated solution.
Claims (10)
We Claim:
1. An improved electrochemical cell having a positive electrode, an absorber-separator and a negative electrode wherein at least either one of the electrodes comprises a vinylidene fluoride polymer having an electrolyte material combined therewith and/or said absorber-separator comprises a vinylidene fluoride polymer having an electrolyte material combined therewith wherein the improvement comprises the vinylidene fluoride polymer consisting essentially of a vinylidene fluoride polymer selected from the group consisting of vinylidene fluoride homopolymer having a bimodal molecular weight distribution, vinylidene fluoride/
chlorotrifluoroethylene copolymer having substantially homogeneous monomer distribution and a copolymer of vinylidene fluoride and hexafluoropropylene containing a maximum of about 24 weight percent hexafluoropropylene, having solutions of improved clarity and fluidity; for the copolymers having up to about 8 weight percent nominal HFP
content, having weight percent extractables within plus or minus 1.5% of the percent by weight extractables calculated by an equation selected from the group consisting of:
a) Wt% Extractables = 1.7(HFP mole%) - 3.2, and b) Wt% Extractables = -1.2 + 1.5(HFP mole%) - 8 x 10 -6(Mn), and for the copolymers having greater than about 8 weight percent nominal HFP content, having a DSC melting point at least 2.5°C lower than copolymers of the same nominal weight percent HFP
content prepared by synthetic methods for which the prior art provides details.
chlorotrifluoroethylene copolymer having substantially homogeneous monomer distribution and a copolymer of vinylidene fluoride and hexafluoropropylene containing a maximum of about 24 weight percent hexafluoropropylene, having solutions of improved clarity and fluidity; for the copolymers having up to about 8 weight percent nominal HFP
content, having weight percent extractables within plus or minus 1.5% of the percent by weight extractables calculated by an equation selected from the group consisting of:
a) Wt% Extractables = 1.7(HFP mole%) - 3.2, and b) Wt% Extractables = -1.2 + 1.5(HFP mole%) - 8 x 10 -6(Mn), and for the copolymers having greater than about 8 weight percent nominal HFP content, having a DSC melting point at least 2.5°C lower than copolymers of the same nominal weight percent HFP
content prepared by synthetic methods for which the prior art provides details.
2. A battery as defined in claim 1 wherein the vinylidene fluoride polymer is a vinylidene fluoride homopolymer having a bimodal molecular weight distribution.
3. A battery as defined in claim 1 wherein the vinylidene fluoride polymer is a vinylidene fluoride/chlorotrifluoroethylene copolymer having up to about 20% by weight chlorotrifluoroethylene and having a substantially homogeneous monomer distribution.
4. A battery as defined in claim 3 wherein the VDF/CTFE copolymer has up to about 8% by weight CTFE
content.
content.
5. A battery as defined in claim 4 wherein the VDF/CTFE copolymer has from about 2% to about 6%
CTFE content.
CTFE content.
6. A battery as defined in claim 1 wherein the polyvinylidene fluoride polymer is a VDF/HFP
copolymer.
copolymer.
7. A battery as defined in claim 6 wherein the VDF/HFP copolymer has up to about 8% by weight HFP
content.
content.
8. A battery as defined in claim 7 wherein the VDF/HFP copolymer has from about 2% to about 6% by weight HFP content.
9. An improved electrochemical cell having a positive electrode, an absorber-separator and a negative electrode wherein at least either one of the electrodes comprises a vinylidene fluoride polymer having an electrolyte material combined therewith and/or said absorber-separator comprises a vinylidene fluoride polymer having an electrolyte combined therewith wherein the improvement comprises the vinylidene fluoride polymer consisting essentially of a VDF/HFP copolymer having up to about 8 Wt.% hexafluoropropylene and having weight percent extractables with plus or minus 1.5% of the weight percent extractables calculated by either equation a) or b) defined in claim 1.
10. A battery as defined in claim 9 wherein the hexafluoropropylene content of the VDF/HFP copolymer is from about 2% to about 6% by weight.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US3834697P | 1997-02-28 | 1997-02-28 | |
US60/038,346 | 1997-02-28 | ||
US3101598A | 1998-02-26 | 1998-02-26 | |
US09/031,015 | 1998-02-26 |
Publications (1)
Publication Number | Publication Date |
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CA2251648A1 true CA2251648A1 (en) | 1998-09-03 |
Family
ID=26706722
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002251648A Abandoned CA2251648A1 (en) | 1997-02-28 | 1998-02-27 | Copolymers of vinylidene fluoride and hexafluoropropylene having reduced extractable content and improved solution clarity |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0907976A4 (en) |
JP (1) | JP2002513506A (en) |
KR (1) | KR100537303B1 (en) |
CN (1) | CN1311577C (en) |
CA (1) | CA2251648A1 (en) |
HU (1) | HUP9903748A3 (en) |
ID (1) | ID20294A (en) |
WO (1) | WO1998038687A1 (en) |
Families Citing this family (21)
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DE69836150T2 (en) | 1997-12-26 | 2007-08-30 | Kureha Corp. | Polymer electrolyte and non-aqueous battery containing the same |
JP4092669B2 (en) * | 1998-04-27 | 2008-05-28 | ソニー株式会社 | Solid electrolyte secondary battery |
IT1307756B1 (en) * | 1999-02-05 | 2001-11-19 | Ausimont Spa | ELECTROLYTE POLYMERS FOR LITHIUM RECHARGEABLE BATTERIES. |
GB2346729B (en) * | 1999-02-10 | 2003-01-15 | Aea Technology Plc | Polymer electrolyte |
GB0018635D0 (en) * | 2000-07-31 | 2000-09-13 | Aea Technology Plc | Polymer electrolyte |
JP5100951B2 (en) | 2000-09-29 | 2012-12-19 | コーディス・コーポレイション | Coated medical device |
DE10104988A1 (en) * | 2001-02-03 | 2002-08-08 | Varta Geraetebatterie Gmbh | Process for the production of electrode foils |
JP4684651B2 (en) * | 2002-08-26 | 2011-05-18 | Jx日鉱日石エネルギー株式会社 | Method for producing ion conductive film |
US7279174B2 (en) | 2003-05-08 | 2007-10-09 | Advanced Cardiovascular Systems, Inc. | Stent coatings comprising hydrophilic additives |
US7066970B2 (en) | 2003-05-09 | 2006-06-27 | The Gillette Company | Electrochemical cells |
US20050118344A1 (en) | 2003-12-01 | 2005-06-02 | Pacetti Stephen D. | Temperature controlled crimping |
US9114198B2 (en) | 2003-11-19 | 2015-08-25 | Advanced Cardiovascular Systems, Inc. | Biologically beneficial coatings for implantable devices containing fluorinated polymers and methods for fabricating the same |
EP1756892A1 (en) * | 2004-06-09 | 2007-02-28 | The Gillette Company | Electrochemical cells |
JP4815795B2 (en) * | 2004-12-01 | 2011-11-16 | ソニー株式会社 | Lithium ion secondary battery |
CN101046503B (en) * | 2006-03-29 | 2011-02-16 | 深圳市比克电池有限公司 | Method for testing explosion cause of lithium ion cell explosion |
CN104151754B (en) * | 2014-08-15 | 2016-05-25 | 上海三爱富新材料股份有限公司 | High fluidity ethylene-tetrafluoroethylene copolymer composition and method of making the same |
CN106898825B (en) * | 2017-05-03 | 2019-02-05 | 江苏强劲新能源科技有限公司 | A kind of preparation method of bipolarity Zinc ion battery |
CN109692497B (en) * | 2017-10-20 | 2021-03-16 | 中国石油化工股份有限公司 | Microwave extraction agent composition, method for measuring fluorine in aqueous fluororesin base material and application thereof |
US11657984B2 (en) | 2018-06-20 | 2023-05-23 | Lg Chem, Ltd. | Separator for electrochemical device, method for manufacturing same, and electrochemical device comprising same |
CN112585795B (en) * | 2018-09-14 | 2022-03-29 | 株式会社吴羽 | Resin-dispersed electrolyte solution, polymer gel electrolyte and method for producing same, and secondary battery and method for producing same |
US20220102756A1 (en) * | 2020-09-30 | 2022-03-31 | GM Global Technology Operations LLC | Methods for forming solid gel electrolyte membranes and batteries incorporating the same |
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US5093427A (en) * | 1990-05-10 | 1992-03-03 | Atochem North America, Inc. | Copolymers of vinylidene fluoride and hexafluoropropylene and process for preparing the same |
US5429891A (en) * | 1993-03-05 | 1995-07-04 | Bell Communications Research, Inc. | Crosslinked hybrid electrolyte film and methods of making and using the same |
US5460904A (en) * | 1993-08-23 | 1995-10-24 | Bell Communications Research, Inc. | Electrolyte activatable lithium-ion rechargeable battery cell |
US5296318A (en) * | 1993-03-05 | 1994-03-22 | Bell Communications Research, Inc. | Rechargeable lithium intercalation battery with hybrid polymeric electrolyte |
TW342537B (en) * | 1995-03-03 | 1998-10-11 | Atochem North America Elf | Polymeric electrode, electrolyte, article of manufacture and composition |
-
1998
- 1998-02-27 KR KR1019980708803A patent/KR100537303B1/en not_active IP Right Cessation
- 1998-02-27 JP JP53795098A patent/JP2002513506A/en not_active Abandoned
- 1998-02-27 ID IDW980106D patent/ID20294A/en unknown
- 1998-02-27 HU HU9903748A patent/HUP9903748A3/en unknown
- 1998-02-27 EP EP98908864A patent/EP0907976A4/en not_active Withdrawn
- 1998-02-27 CN CNB988002078A patent/CN1311577C/en not_active Expired - Fee Related
- 1998-02-27 WO PCT/US1998/004071 patent/WO1998038687A1/en active IP Right Grant
- 1998-02-27 CA CA002251648A patent/CA2251648A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
EP0907976A1 (en) | 1999-04-14 |
CN1217824A (en) | 1999-05-26 |
KR20000065176A (en) | 2000-11-06 |
WO1998038687A1 (en) | 1998-09-03 |
CN1311577C (en) | 2007-04-18 |
HUP9903748A3 (en) | 2000-06-28 |
JP2002513506A (en) | 2002-05-08 |
ID20294A (en) | 1998-11-26 |
EP0907976A4 (en) | 2005-11-02 |
KR100537303B1 (en) | 2006-07-14 |
HUP9903748A2 (en) | 2000-03-28 |
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