WO2023189217A1 - Method for producing fluorine-containing cyclic olefin composition, and fluorine-containing cyclic olefin composition - Google Patents
Method for producing fluorine-containing cyclic olefin composition, and fluorine-containing cyclic olefin composition Download PDFInfo
- Publication number
- WO2023189217A1 WO2023189217A1 PCT/JP2023/008150 JP2023008150W WO2023189217A1 WO 2023189217 A1 WO2023189217 A1 WO 2023189217A1 JP 2023008150 W JP2023008150 W JP 2023008150W WO 2023189217 A1 WO2023189217 A1 WO 2023189217A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fluorine
- cyclic olefin
- compound
- containing cyclic
- group
- Prior art date
Links
- -1 cyclic olefin Chemical class 0.000 title claims abstract description 353
- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 263
- 239000011737 fluorine Substances 0.000 title claims abstract description 262
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 title claims abstract description 255
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 title claims abstract description 181
- 239000000203 mixture Substances 0.000 title claims abstract description 135
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 44
- 150000001875 compounds Chemical class 0.000 claims abstract description 59
- 238000006243 chemical reaction Methods 0.000 claims abstract description 42
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 34
- 238000002156 mixing Methods 0.000 claims abstract description 21
- 239000003377 acid catalyst Substances 0.000 claims abstract description 20
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 15
- 125000005233 alkylalcohol group Chemical group 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 125000004432 carbon atom Chemical group C* 0.000 claims description 63
- 125000003545 alkoxy group Chemical group 0.000 claims description 24
- 125000000217 alkyl group Chemical group 0.000 claims description 24
- 125000004183 alkoxy alkyl group Chemical group 0.000 claims description 21
- 238000004821 distillation Methods 0.000 claims description 21
- 238000009835 boiling Methods 0.000 claims description 20
- 238000004770 highest occupied molecular orbital Methods 0.000 claims description 16
- 238000000926 separation method Methods 0.000 claims description 14
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims description 11
- 239000001257 hydrogen Substances 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 239000011973 solid acid Substances 0.000 claims description 9
- 150000007522 mineralic acids Chemical class 0.000 claims description 4
- 150000007524 organic acids Chemical class 0.000 claims description 4
- 235000005985 organic acids Nutrition 0.000 claims description 3
- 238000000034 method Methods 0.000 description 15
- 150000001336 alkenes Chemical class 0.000 description 13
- 239000000243 solution Substances 0.000 description 8
- 125000002023 trifluoromethyl group Chemical group FC(F)(F)* 0.000 description 8
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 description 7
- 239000006227 byproduct Substances 0.000 description 7
- 125000001153 fluoro group Chemical group F* 0.000 description 7
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical compound C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 6
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000003729 cation exchange resin Substances 0.000 description 6
- 238000004817 gas chromatography Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical compound FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 6
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 6
- 230000009257 reactivity Effects 0.000 description 6
- 238000005698 Diels-Alder reaction Methods 0.000 description 5
- JFNLZVQOOSMTJK-KNVOCYPGSA-N norbornene Chemical compound C1[C@@H]2CC[C@H]1C=C2 JFNLZVQOOSMTJK-KNVOCYPGSA-N 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- XBFJAVXCNXDMBH-UHFFFAOYSA-N tetracyclo[6.2.1.1(3,6).0(2,7)]dodec-4-ene Chemical compound C1C(C23)C=CC1C3C1CC2CC1 XBFJAVXCNXDMBH-UHFFFAOYSA-N 0.000 description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 4
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 4
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 239000012299 nitrogen atmosphere Substances 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010494 dissociation reaction Methods 0.000 description 3
- 230000005593 dissociations Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000003760 magnetic stirring Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 125000000542 sulfonic acid group Chemical group 0.000 description 3
- 239000013076 target substance Substances 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- BBMCTIGTTCKYKF-UHFFFAOYSA-N 1-heptanol Chemical compound CCCCCCCO BBMCTIGTTCKYKF-UHFFFAOYSA-N 0.000 description 2
- CETWDUZRCINIHU-UHFFFAOYSA-N 2-heptanol Chemical compound CCCCCC(C)O CETWDUZRCINIHU-UHFFFAOYSA-N 0.000 description 2
- 238000003775 Density Functional Theory Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 125000004106 butoxy group Chemical group [*]OC([H])([H])C([H])([H])C(C([H])([H])[H])([H])[H] 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 229940023913 cation exchange resins Drugs 0.000 description 2
- 229920001429 chelating resin Polymers 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- MGNZXYYWBUKAII-UHFFFAOYSA-N cyclohexa-1,3-diene Chemical compound C1CC=CC=C1 MGNZXYYWBUKAII-UHFFFAOYSA-N 0.000 description 2
- 125000001511 cyclopentyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C1([H])[H] 0.000 description 2
- 125000001887 cyclopentyloxy group Chemical group C1(CCCC1)O* 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- 125000004786 difluoromethoxy group Chemical group [H]C(F)(F)O* 0.000 description 2
- 125000001028 difluoromethyl group Chemical group [H]C(F)(F)* 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 description 2
- 125000005745 ethoxymethyl group Chemical group [H]C([H])([H])C([H])([H])OC([H])([H])* 0.000 description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 2
- 125000004785 fluoromethoxy group Chemical group [H]C([H])(F)O* 0.000 description 2
- 125000004216 fluoromethyl group Chemical group [H]C([H])(F)* 0.000 description 2
- 125000006343 heptafluoro propyl group Chemical group 0.000 description 2
- QNVRIHYSUZMSGM-UHFFFAOYSA-N hexan-2-ol Chemical compound CCCCC(C)O QNVRIHYSUZMSGM-UHFFFAOYSA-N 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005649 metathesis reaction Methods 0.000 description 2
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 2
- 125000004184 methoxymethyl group Chemical group [H]C([H])([H])OC([H])([H])* 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 2
- 125000000740 n-pentyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 2
- ZWRUINPWMLAQRD-UHFFFAOYSA-N nonan-1-ol Chemical compound CCCCCCCCCO ZWRUINPWMLAQRD-UHFFFAOYSA-N 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 125000006340 pentafluoro ethyl group Chemical group FC(F)(F)C(F)(F)* 0.000 description 2
- JYVLIDXNZAXMDK-UHFFFAOYSA-N pentan-2-ol Chemical compound CCCC(C)O JYVLIDXNZAXMDK-UHFFFAOYSA-N 0.000 description 2
- 125000004115 pentoxy group Chemical group [*]OC([H])([H])C([H])([H])C([H])([H])C(C([H])([H])[H])([H])[H] 0.000 description 2
- 125000005815 pentoxymethyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])OC([H])([H])* 0.000 description 2
- 125000005460 perfluorocycloalkyl group Chemical group 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 125000002572 propoxy group Chemical group [*]OC([H])([H])C(C([H])([H])[H])([H])[H] 0.000 description 2
- 125000005767 propoxymethyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])[#8]C([H])([H])* 0.000 description 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 2
- 125000003652 trifluoroethoxy group Chemical group FC(CO*)(F)F 0.000 description 2
- 125000004205 trifluoroethyl group Chemical group [H]C([H])(*)C(F)(F)F 0.000 description 2
- 125000000876 trifluoromethoxy group Chemical group FC(F)(F)O* 0.000 description 2
- OJOWICOBYCXEKR-KRXBUXKQSA-N (5e)-5-ethylidenebicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(=C/C)/CC1C=C2 OJOWICOBYCXEKR-KRXBUXKQSA-N 0.000 description 1
- MIOPJNTWMNEORI-GMSGAONNSA-N (S)-camphorsulfonic acid Chemical compound C1C[C@@]2(CS(O)(=O)=O)C(=O)C[C@@H]1C2(C)C MIOPJNTWMNEORI-GMSGAONNSA-N 0.000 description 1
- GWYPDXLJACEENP-UHFFFAOYSA-N 1,3-cycloheptadiene Chemical compound C1CC=CC=CC1 GWYPDXLJACEENP-UHFFFAOYSA-N 0.000 description 1
- 239000005968 1-Decanol Substances 0.000 description 1
- WZMQOSYJAAMGTB-UHFFFAOYSA-N 1-ethylcyclohexa-1,3-diene Chemical compound CCC1=CC=CCC1 WZMQOSYJAAMGTB-UHFFFAOYSA-N 0.000 description 1
- RNVJDIGFTGLKCE-UHFFFAOYSA-N 2,3,3-trifluoro-2-(trifluoromethyl)bicyclo[2.2.1]hept-5-ene Chemical compound C1C2C=CC1C(C(F)(F)F)(F)C2(F)F RNVJDIGFTGLKCE-UHFFFAOYSA-N 0.000 description 1
- FEEIOCGOXYNQIM-UHFFFAOYSA-N 2,3-di(propan-2-ylidene)bicyclo[2.2.1]hept-5-ene Chemical compound C1C2C=CC1C(=C(C)C)C2=C(C)C FEEIOCGOXYNQIM-UHFFFAOYSA-N 0.000 description 1
- QNVRIHYSUZMSGM-LURJTMIESA-N 2-Hexanol Natural products CCCC[C@H](C)O QNVRIHYSUZMSGM-LURJTMIESA-N 0.000 description 1
- QQBUHYQVKJQAOB-UHFFFAOYSA-N 2-ethenylfuran Chemical compound C=CC1=CC=CO1 QQBUHYQVKJQAOB-UHFFFAOYSA-N 0.000 description 1
- HLPIHRDZBHXTFJ-UHFFFAOYSA-N 2-ethylfuran Chemical compound CCC1=CC=CO1 HLPIHRDZBHXTFJ-UHFFFAOYSA-N 0.000 description 1
- INYHZQLKOKTDAI-UHFFFAOYSA-N 5-ethenylbicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(C=C)CC1C=C2 INYHZQLKOKTDAI-UHFFFAOYSA-N 0.000 description 1
- RBRGWYHSVYKUQT-UHFFFAOYSA-N 5-oxabicyclo[2.2.1]hept-2-ene Chemical compound C1C2COC1C=C2 RBRGWYHSVYKUQT-UHFFFAOYSA-N 0.000 description 1
- UGJBFMMPNVKBPX-UHFFFAOYSA-N 5-propan-2-ylidenebicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(=C(C)C)CC1C=C2 UGJBFMMPNVKBPX-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 239000007848 Bronsted acid Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 1
- 238000007259 addition reaction Methods 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- SRSXLGNVWSONIS-UHFFFAOYSA-N benzenesulfonic acid Chemical compound OS(=O)(=O)C1=CC=CC=C1 SRSXLGNVWSONIS-UHFFFAOYSA-N 0.000 description 1
- 229940092714 benzenesulfonic acid Drugs 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000012718 coordination polymerization Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000012776 electronic material Substances 0.000 description 1
- 238000006266 etherification reaction Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 150000002221 fluorine Chemical class 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000000887 hydrating effect Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- QQZOPKMRPOGIEB-UHFFFAOYSA-N n-butyl methyl ketone Natural products CCCCC(C)=O QQZOPKMRPOGIEB-UHFFFAOYSA-N 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical compound OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/38—Separation; Purification; Stabilisation; Use of additives
- C07C17/383—Separation; Purification; Stabilisation; Use of additives by distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/38—Separation; Purification; Stabilisation; Use of additives
- C07C17/395—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to a chemical modification of at least one compound
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C23/00—Compounds containing at least one halogen atom bound to a ring other than a six-membered aromatic ring
- C07C23/18—Polycyclic halogenated hydrocarbons
- C07C23/20—Polycyclic halogenated hydrocarbons with condensed rings none of which is aromatic
- C07C23/27—Polycyclic halogenated hydrocarbons with condensed rings none of which is aromatic with a bicyclo ring system containing seven carbon atoms
- C07C23/30—Mono-unsaturated bicyclo ring system
Definitions
- the present invention relates to a method for producing a fluorine-containing cyclic olefin composition and a fluorine-containing cyclic olefin composition.
- a fluorine-containing cyclic olefin compound that is a raw material for a fluorine-containing cyclic olefin polymer can be produced, for example, by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction.
- Examples of techniques related to the method for producing such fluorine-containing cyclic olefin compounds include those described in Patent Document 1.
- Patent Document 1 describes a process for producing a fluorine-containing cyclic olefin monomer, which includes a step (A) of continuously producing a fluorine-containing cyclic olefin monomer by continuously reacting a fluorine-containing olefin and a cyclic polyene in a reaction vessel.
- the cyclic polyene is continuously or intermittently supplied into the reaction vessel, and the fluorine-containing olefin is continuously or intermittently supplied into the reaction vessel, or
- the fluorine-containing olefin and the cyclic polyene can be continuously reacted, and the content of the fluorine-containing olefin relative to the content of the cyclic polyene in the reaction vessel X 1 .
- a method for producing a fluorine-containing cyclic olefin monomer is described in which the molar ratio X 2 / X 1 of X 2 is adjusted within a range of 1.01 or more.
- Patent Document 1 describes that according to the production method, the target fluorine-containing cyclic olefin monomer can be obtained with high selectivity.
- the boiling point difference between the target product, the fluorine-containing cyclic olefin compound, and the by-product, the fluorine-free cyclic diolefin compound may be small. It was sometimes difficult to separate compounds.
- the present invention has been made in view of the above circumstances, and provides a manufacturing method capable of obtaining a fluorine-containing cyclic olefin composition with a reduced content of a fluorine-free cyclic diolefin compound.
- the present inventors have made extensive studies to solve the above problems. As a result, by hydrating and/or etherifying the by-product fluorine-free cyclic diolefin compound with the hydroxyl group-containing compound, the target fluorine-containing cyclic olefin compound and the fluorine-free by-product It has been discovered that it is possible to obtain a fluorine-containing cyclic olefin composition that can be easily separated from a fluorine-containing cyclic diolefin compound and has a reduced content of a fluorine-free cyclic diolefin compound as a by-product, and has developed the present invention. Completed. According to the present invention, a method for producing a fluorine-containing cyclic olefin composition and a fluorine-containing cyclic olefin composition shown below are provided.
- composition (X) containing a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1) represented by the following formula (1) an acid catalyst and a compound selected from the group consisting of water and an alkyl alcohol.
- a mixing step of mixing at least one selected hydroxyl group-containing compound (C) By reacting the fluorine-free cyclic diolefin compound (B1) with the hydroxyl group-containing compound (C), a compound selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3) is produced.
- R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or It is an alkoxyalkyl group having 2 to 10 carbon atoms containing fluorine, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or selected from alkoxy groups having 1 to 10 carbon atoms or alkoxyalkyl groups having 2 to 10 carbon atoms, R 1 to R 4 may be bonded to each other to form a ring structure, and X is -CH 2 - or O -, n indicates 0 or 1) [2] The fluorine-containing cyclic olefin according to [1] above,
- the fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1).
- the method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [5] above, comprising both of the above.
- the method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [7] above, further comprising a separation step of separating.
- the content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is 5.0% by mass or less when the entire fluorine-containing cyclic olefin composition is 100% by mass.
- the method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [8] above.
- a fluorine-containing cyclic olefin composition comprising a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1) represented by the following formula (1),
- the content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is more than 0% by mass and 1.0% by mass when the entire fluorine-containing cyclic olefin composition is 100% by mass. % or less.
- R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or It is an alkoxyalkyl group having 2 to 10 carbon atoms containing fluorine, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or selected from alkoxy groups having 1 to 10 carbon atoms or alkoxyalkyl groups having 2 to 10 carbon atoms, R 1 to R 4 may be bonded to each other to form a ring structure, and X is -CH 2 - or O -, n indicates 0 or 1)
- the present invention it is possible to provide a manufacturing method capable of obtaining a fluorine-containing cyclic olefin composition with a reduced content of a fluorine-free cyclic diolefin compound.
- Method for producing a fluorine-containing cyclic olefin composition comprises a fluorine-containing cyclic olefin compound (A) represented by the following formula (1) and a fluorine-free cyclic diolefin compound (B1).
- the reaction product of the fluorine-free cyclic diolefin compound (B1) and water is referred to as the fluorine-free hydrated compound (B2), and the fluorine-free cyclic diolefin compound (B1) and the alkyl
- the reaction product with alcohol is called a fluorine-free ether compound (B3). That is, in the method for producing a fluorine-containing cyclic olefin composition of the present invention, when the hydroxyl group-containing compound (C) contains water, the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) are reacted.
- the method includes a reaction step of obtaining a fluorine-free ether compound (B3) by reacting the following.
- R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or fluorine. is an alkoxyalkyl group having 2 to 10 carbon atoms, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or an alkoxyalkyl group having 1 to 10 carbon atoms.
- R 1 to R 4 may be bonded to each other to form a ring structure, and X is -CH 2 - or O- , and n represents 0 or 1.
- the method for producing a fluorine-containing cyclic olefin composition according to the present invention it is possible to obtain a fluorine-containing cyclic olefin composition in which the content of a fluorine-free cyclic diolefin compound is reduced.
- the reason why such an effect is obtained is presumed to be as follows.
- the addition produces a fluorine-free hydrated compound (B2) or a fluorine-free ether compound (B3).
- the content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition can be reduced.
- the boiling point difference between the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3) and the fluorine-containing cyclic olefin compound (A) is the same as that between the fluorine-free cyclic diolefin compound (B1) and the fluorine-containing cyclic olefin compound.
- the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3) can be easily separated from the fluorine-containing cyclic olefin composition by distillation. Therefore, according to the method for producing a fluorine-containing cyclic olefin composition according to the present invention, by-products can be easily separated, so it is possible to obtain a fluorine-containing cyclic olefin composition with improved purity. Each step will be explained below.
- the method for producing a fluorine-containing cyclic olefin composition according to the present invention includes a composition (X) containing a fluorine-containing cyclic olefin compound (A) represented by the above formula (1) and a fluorine-free cyclic diolefin compound (B1). On the other hand, it includes a mixing step of mixing an acid catalyst and at least one hydroxyl group-containing compound (C) selected from the group consisting of water and alkyl alcohol.
- Composition (X) contains a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1).
- Composition (X) is, for example, a composition obtained by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction.
- R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or fluorine. is an alkoxyalkyl group having 2 to 10 carbon atoms, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or an alkoxyalkyl group having 1 to 10 carbon atoms.
- R 1 to R 4 may be bonded to each other to form a ring structure.
- R 1 to R 4 are preferably fluorine or a fluorine-containing alkyl group having 1 to 4 carbon atoms, more preferably fluorine or a trifluoromethyl group, and one of R 1 to R 4 is trifluoromethyl. It is more preferable that the remainder be fluorine.
- X represents -CH 2 - or O-, preferably -CH 2 -.
- n represents 0 or 1, preferably 1.
- R 1 to R 4 more specifically include fluorine; fluoromethyl group, difluoromethyl group, trifluoromethyl group, trifluoroethyl group, pentafluoroethyl group, heptafluoropropyl group. , hexafluoroisopropyl group, heptafluoroisopropyl group, hexafluoro-2-methylisopropyl group, perfluoro-2-methylisopropyl group, n-perfluorobutyl group, n-perfluoropentyl group, perfluorocyclopentyl group, etc.
- An alkyl group containing 1 to 10 carbon atoms containing fluorine such as an alkyl group partially or completely substituted with fluorine; a fluoromethoxy group, a difluoromethoxy group, a trifluoromethoxy group, a trifluoroethoxy group, a pentafluoroethoxy group, Heptafluoropropoxy group, hexafluoroisopropoxy group, heptafluoroisopropoxy group, hexafluoro-2-methylisopropoxy group, perfluoro-2-methylisopropoxy group, n-perfluorobutoxy group, n-perfluoropentoxy group, perfluoro
- R 1 to R 4 may be bonded to each other to form a ring structure, or may form a ring such as a perfluorocycloalkyl group or a perfluorocycloether group via oxygen.
- other R 1 to R 4 that do not contain fluorine include hydrogen; methyl group, ethyl group, propyl group, isopropyl group, 2-methylisopropyl group, n-butyl group, n-pentyl group, cyclopentyl group, etc.
- Alkyl group having 1 to 10 carbon atoms alkoxy group having 1 to 10 carbon atoms such as methoxy group, ethoxy group, propoxy group, butoxy group, pentoxy group, methoxymethyl group, ethoxymethyl group, propoxymethyl group, butoxymethyl group, Examples include alkoxyalkyl groups having 2 to 10 carbon atoms such as pentoxymethyl group.
- the fluorine-containing cyclic olefin compound (A) is, for example, a composition obtained by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction, and is a fluorine-containing cyclic olefin compound in which n is 0 in the formula (1) above.
- the fluorine-containing In the cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2), in the formula (1) X is -CH 2 -, and R 1 to R 4 are fluorine or a trifluoromethyl group.
- R 1 to R 4 is a trifluoromethyl group, and the remaining ones are more preferably fluorine.
- the fluorine-containing cyclic olefin compound (A) preferably contains at least one selected from fluorine-containing tetracyclododecene, fluorine-containing norbornene, fluorine-containing oxotetracyclododecene, and fluorine-containing oxonorbornene, and more preferably fluorine-containing It contains at least one selected from tetracyclododecene and fluorine-containing norbornene, and more preferably contains fluorine-containing tetracyclododecene.
- tetracyclododecene means tetracyclo[4.4.0.1 2,5 .
- the fluorine-containing tetracyclododecene is a fluorine-containing cyclic olefin in which X is -CH 2 - and n is 1 in the formula (1).
- the fluorine-containing norbornene is a fluorine-containing cyclic olefin in which, in the formula (1), X is -CH 2 - and n is 0.
- the fluorine-containing oxotetracyclododecene is a fluorine-containing cyclic olefin in which X is -O- and n is 1 in the formula (1).
- the fluorine-containing oxonorbornene is a fluorine-containing cyclic olefin in which X is -O- and n is 0 in the formula (1).
- fluorine-containing olefin As the fluorine-containing olefin, for example, a fluorine-containing olefin represented by the following formula (2) can be used.
- R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or fluorine. is an alkoxyalkyl group having 2 to 10 carbon atoms, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or an alkoxyalkyl group having 1 to 10 carbon atoms.
- R 1 to R 4 may be bonded to each other to form a ring structure.
- R 1 to R 4 are preferably fluorine or a fluorine-containing alkyl group having 1 to 4 carbon atoms, more preferably fluorine or a trifluoromethyl group, and one of R 1 to R 4 is trifluoromethyl. It is more preferable that the remainder be fluorine.
- R 1 to R 4 more specifically include fluorine; fluoromethyl group, difluoromethyl group, trifluoromethyl group, trifluoroethyl group, pentafluoroethyl group, heptafluoropropyl group. , hexafluoroisopropyl group, heptafluoroisopropyl group, hexafluoro-2-methylisopropyl group, perfluoro-2-methylisopropyl group, n-perfluorobutyl group, n-perfluoropentyl group, perfluorocyclopentyl group, etc.
- An alkyl group containing 1 to 10 carbon atoms containing fluorine such as an alkyl group partially or completely substituted with fluorine; a fluoromethoxy group, a difluoromethoxy group, a trifluoromethoxy group, a trifluoroethoxy group, a pentafluoroethoxy group, Heptafluoropropoxy group, hexafluoroisopropoxy group, heptafluoroisopropoxy group, hexafluoro-2-methylisopropoxy group, perfluoro-2-methylisopropoxy group, n-perfluorobutoxy group, n-perfluoropentoxy group, perfluoro
- R 1 to R 4 may be bonded to each other to form a ring structure, or may form a ring such as a perfluorocycloalkyl group or a perfluorocycloether group via oxygen.
- other R 1 to R 4 that do not contain fluorine include hydrogen; methyl group, ethyl group, propyl group, isopropyl group, 2-methylisopropyl group, n-butyl group, n-pentyl group, cyclopentyl group, etc.
- Alkyl group having 1 to 10 carbon atoms alkoxy group having 1 to 10 carbon atoms such as methoxy group, ethoxy group, propoxy group, butoxy group, pentoxy group, methoxymethyl group, ethoxymethyl group, propoxymethyl group, butoxymethyl group, Examples include alkoxyalkyl groups having 2 to 10 carbon atoms such as pentoxymethyl group.
- cyclic polyene examples include cyclopentadiene, cyclohexadiene, ethylcyclohexadiene, cycloheptadiene, dicyclopentadiene, dicyclohexadiene, 1-oxa-2,4-cyclopentadiene, 1-oxa-2-ethyl-2, 4-cyclopentadiene, 1-oxa-2-vinyl-2,4-cyclopentadiene, ethylidenenorbornene, vinylnorbornene, isopropylidenenorbornene, methylhydroindene, diisopropylidenenorbornene, propenylisonorbornadiene, and the like can be used.
- cyclic polyenes may be used singly or in combination of two or more.
- cyclopentadiene, dicyclopentadiene, and 1-oxa-2,4-cyclopentadiene are preferred, dicyclopentadiene and furan are more preferred, and dicyclopentadiene is preferred. is even more preferable.
- the fluorine-free cyclic diolefin compound (B1) is, for example, a compound obtained by a Diels-Alder reaction between the cyclic polyenes, and examples thereof include dicyclopentadiene, tricyclopentadiene, and the like.
- the fluorine-free cyclic diolefin compound (B1) may contain at least one selected from dicyclopentadiene and tricyclopentadiene.
- the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free cyclic diolefin compound (B1) are 10°C or less, the fluorine-containing cyclic olefin compound is removed by distillation. Since it is difficult to separate the olefin compound (A) and the fluorine-free cyclic diolefin compound (B1), from the viewpoint of obtaining a fluorine-containing cyclic olefin composition with improved purity, the fluorine-containing cyclic olefin composition according to the present invention is The manufacturing method is effective.
- the boiling point refers to the boiling point at 1 atmosphere.
- the acid catalyst is not particularly limited as long as it is a Br ⁇ nsted acid, and includes at least one selected from the group consisting of inorganic acids, organic acids, and solid acids.
- inorganic acid include hydrochloric acid, sulfuric acid, nitric acid, and phosphoric acid.
- organic acid include methanesulfonic acid, trifluoromethanesulfonic acid, benzenesulfonic acid, p-toluenesulfonic acid, 10-camphorsulfonic acid, and trifluoroacetic acid.
- the solid acid include strong acidic cation exchange resins having sulfonic acid groups.
- strongly acidic cation exchange resins are preferred from the viewpoint that the acid catalyst can be separated by filtration without performing a step of neutralizing and extracting the used acid with an alkaline solution such as an aqueous sodium hydroxide solution after the reaction. Furthermore, from the viewpoint of increasing the contact area with the reaction substrate, a strongly acidic cation exchange resin having a macroporous structure with a large surface area is preferred.
- the acid dissociation constant (pKa) of the acid catalyst is preferably 2 or less from the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C).
- the mixing amount of the acid catalyst in the mixing step is preferably from the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) based on 100 parts by mass of the composition (X). is 0.01 parts by mass or more, more preferably 0.05 parts by mass or more, even more preferably 0.1 parts by mass or more, even more preferably 0.5 parts by mass or more, still more preferably 1.0 parts by mass or more, and even more preferably is 1.5 parts by mass or more, and preferably 50 parts by mass or less, more preferably 30 parts by mass or less, still more preferably 25 parts by mass or less, still more preferably 20 parts by mass or less, and even more preferably 15 parts by mass or less. , more preferably 10 parts by mass or less.
- the hydroxyl group-containing compound (C) is at least one selected from the group consisting of water and alkyl alcohol.
- Alkyl alcohol is preferred because it increases the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free ether compound (B3) to facilitate separation in the separation step.
- the number of carbon atoms in the alkyl alcohol is determined from the viewpoints of increasing the reaction temperature by increasing the boiling point of the alkyl alcohol to further improve the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C), and From the viewpoint of increasing the difference in boiling point from the containing cyclic olefin compound (A) to facilitate separation in the separation step, it is preferably 3 or more, and preferably 10 or less, more preferably 8 or less, and even more preferably 6 It is as follows.
- the number of carbon atoms in the alkyl alcohol is preferably 3 or more and 10 or less, more preferably 3 or more and 8 or less, and still more preferably 3 or more and 6 or less.
- the alkyl alcohol is preferably 1-propanol, 2-propanol, 1-butanol, or 2-butanol.
- the amount of the hydroxyl group-containing compound (C) mixed in the mixing step is such that the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) is further improved based on 100 parts by mass of the composition (X). From this point of view, it is preferably 1 part by mass or more, more preferably 5 parts by mass or more, even more preferably 10 parts by mass or more, still more preferably 20 parts by mass or more, even more preferably 30 parts by mass or more, and preferably 1000 parts by mass. parts by weight or less, more preferably 500 parts by weight or less, still more preferably 250 parts by weight or less, still more preferably 150 parts by weight or less, still more preferably 100 parts by weight or less, still more preferably 60 parts by weight or less.
- any method may be used to mix each component.
- the mixing may be carried out in any manner such as all at once or divided.
- the device for mixing each component and any device capable of stirring and mixing, batch type or continuous type, may be used.
- the temperature at which each component is mixed can be arbitrarily selected within the range from room temperature to the boiling point of the solvent.
- the mixing step may be performed simultaneously with the reaction step described below, or may be performed before the reaction step.
- the method for producing a fluorine-containing cyclic olefin composition according to the present invention includes reacting a fluorine-free cyclic diolefin compound (B1) with a hydroxyl group-containing compound (C) to produce a fluorine-free hydrated compound (B2) and It includes a reaction step for obtaining at least one selected from the group consisting of fluorine-free ether compounds (B3).
- the fluorine-containing cyclic olefin compound (A) and the fluorine-free cyclic diolefin compound (B1) usually have different electron densities at the double bond part, and the fluorine-free cyclic diolefin compound (B1) is better than the fluorine-containing cyclic diolefin compound (B1). expensive.
- composition (X) containing the fluorine-containing cyclic olefin compound (A) and the fluorine-free cyclic diolefin compound (B1) is reacted with the hydroxyl group-containing compound (C) in the presence of an acid catalyst, fluorine
- the addition reaction of the hydroxyl group-containing compound (C) proceeds more selectively in the non-containing cyclic diolefin compound (B1), so that it can be hydrated or etherified.
- the absolute difference between the HOMO energy (E 1 ) of the fluorine-containing cyclic olefin compound (A) and the HOMO energy (E 2 ) of the fluorine-free cyclic diolefin compound (B1) The value
- HOMO is the highest occupied molecular orbital, and the HOMO energy of each compound can be calculated using long-range corrected density functional theory. Using Gaussian16 Rev.B.01, ⁇ B97X-D is selected as the functional, 6-31G(d) is used as the basis function, and the structure is optimized for calculation.
- the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) can be carried out, for example, by the reaction between the composition (X), the acid catalyst, and the hydroxyl group-containing compound (C) obtained in the mixing step. This can be done by heating the mixture.
- the heating temperature in the reaction step is not particularly limited as it is set appropriately depending on the type and amount of each component to be treated, but from the viewpoint of further promoting the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C).
- the temperature in the reaction step is preferably 60°C or more and 150°C or less, more preferably 80°C or more and 130°C or less, and even more preferably 90°C or more and 120°C or less.
- the heating time (reaction time) in the reaction step is not particularly limited as it is appropriately set depending on the type and amount of each component to be treated, but the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C)
- the time period is preferably 1 hour or more, more preferably 2 hours or more, still more preferably 4 hours or more, even more preferably 8 hours or more, and from the viewpoint of improving productivity, preferably 48 hours or less, More preferably 24 hours or less, still more preferably 20 hours or less.
- the heating time (reaction time) in the reaction step is preferably 1 hour or more and 48 hours or less, more preferably 2 hours or more and 24 hours or less, even more preferably 4 hours or more and 20 hours or less, and even more preferably 8 hours.
- the duration is 20 hours or less.
- the reaction step can be carried out, for example, in an inert gas atmosphere such as nitrogen gas, and under normal pressure (atmospheric pressure).
- the method for producing a fluorine-containing cyclic olefin composition according to the present invention is aimed at controlling the purity of the obtained fluorine-containing cyclic olefin composition, that is, the content of the fluorine-containing cyclic olefin compound (A), which is the target substance in the fluorine-containing cyclic olefin composition.
- the reaction step at least one selected from the group consisting of the fluorine-containing cyclic olefin compound (A), the fluorine-free hydrated compound (B2), and the fluorine-free ether compound (B3) is removed by distillation. It is preferable to further include a separation step of separating one type.
- the distillation method is not particularly limited as long as it is a distillation method that can separate the fluorine-containing cyclic olefin compound (A) and the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3), but for example, atmospheric pressure.
- distillation under normal pressure may be carried out under reduced pressure
- vacuum distillation may be carried out under reduced pressure in the system, and the like.
- the fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1).
- the method for producing a fluorine-containing cyclic olefin composition according to the present invention improves the purity of the obtained fluorine-containing cyclic olefin composition, that is, the fluorine-containing cyclic olefin compound that is the target substance in the fluorine-containing cyclic olefin composition.
- the distillation method is not particularly limited as long as it is a distillation method that can separate the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2), but examples include atmospheric distillation conducted under atmospheric pressure, Examples include vacuum distillation performed under reduced pressure.
- the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is determined based on the entire fluorine-containing cyclic olefin composition.
- the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is determined based on the entire fluorine-containing cyclic olefin composition.
- 100% by mass preferably 5.0% by mass or less, more preferably 3.0% by mass or less, even more preferably 2.0% by mass or less, even more preferably 1.0% by mass or less, even more preferably 0 .8% by mass or less, more preferably 0.3% by mass or less.
- the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is preferably as small as possible, the lower limit of the content is not particularly limited, but for example, it is more than 0% by mass.
- the content may be 0.01% by mass or more, 0.05% by mass or more, or 0.1% by mass or more.
- the content of the fluorine-containing cyclic olefin compound (A), which is the target substance in the obtained fluorine-containing cyclic olefin composition is Preferably 75.0% by mass or more, more preferably 80.0% by mass or more, even more preferably 85.0% by mass or more, still more preferably 90.0% by mass or more, when the whole product is 100% by mass. be.
- the content of the target fluorine-containing cyclic olefin compound (A) in the obtained fluorine-containing cyclic olefin composition is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably It is 99.5% by mass or more, more preferably 99.7% by mass or more.
- a fluorine-containing cyclic olefin compound (A1 ) is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably 99.5% by mass or more, when the entire fluorine-containing cyclic olefin composition is 100% by mass. , more preferably 99.7% by mass or more.
- a fluorine-containing cyclic olefin compound (A2 ) is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably 99.5% by mass or more, when the entire fluorine-containing cyclic olefin composition is 100% by mass. , more preferably 99.7% by mass or more.
- the content of each component in the fluorine-containing cyclic olefin composition can be measured, for example, by gas chromatography.
- the measurement method is to use "GC-2010Plus” manufactured by Shimadzu Corporation, and "DB-5" (length 30 m x diameter 0.25 mm x film thickness 0.5 ⁇ m, manufactured by Agilent Technologies) as a capillary column. I can do it.
- the concentration of each component can be measured under conditions of holding the temperature at 40°C for 2 minutes and then increasing the temperature to 250°C at a rate of 10°C/min.
- the concentration of each component can be determined by the peak area ratio (mass %) of each component to the total peak area in the obtained chromatogram.
- fluorine-containing cyclic olefin composition of the present invention for example, coordination polymerization in which a polymer is synthesized using a transition metal catalyst in the coexistence of an alkali metal as a promoter; Radical polymerization, which synthesizes polymers by generating
- a fluorine-containing cyclic olefin polymer can be synthesized by a method such as metathesis polymerization, in which a polymer is synthesized using a method such as metathesis polymerization.
- two or more types of fluorine-containing cyclic olefin compositions according to the present invention may be used together.
- non-fluorine-based cyclic or chain olefins may be present and copolymerized with the fluorine-containing cyclic olefin composition of the present invention. It may also be used as a transfer agent.
- the molded product exhibits low refractive and highly transparent resin properties, such as lenses. It can be widely used in the fields of optical and electronic materials in the form of films, optical waveguides, fibers, etc.
- Example 1 Under a nitrogen atmosphere, 5.8 kg of dicyclopentadiene (manufactured by Tokyo Kasei Kogyo Co., Ltd., hereinafter also referred to as "DCp") and 16.8 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device. 6 kg was added thereto, heated and stirred at 160°C for 24 hours, and then heated and stirred at 180°C for 15 hours. After cooling, 3.9 kg of unreacted hexafluoropropene was collected, and 17.9 kg of the reaction solution was taken out.
- DCp dicyclopentadiene
- hexafluoropropene manufactured by Takachiho Kagaku Kogyo Co., Ltd.
- the boiling point of TDF 6 is 240°C
- the boiling point of NBF 6 is 165°C
- the boiling point of DCp is 170°C
- the boiling point of TCPD is 248°C.
- the HOMO energy of TDF 6 is -8.7 eV
- the HOMO energy of NBF 6 is -9.3 eV
- the HOMO energy of DCp is -8.4 eV
- the HOMO energy of TCPD is -8.2 eV.
- HOMO is the highest occupied molecular orbital
- the HOMO energy of each compound can be calculated using long-range corrected density functional theory. Using Gaussian16 Rev.B.01, ⁇ B97X-D was selected as the functional, 6-31G(d) was used as the basis function, and structure optimization was performed.
- composition (X1) 250 g of composition (X1), 100 g of water as a hydroxyl group-containing compound (C), and 5 g of sulfuric acid as an acid catalyst were placed in a 1000 mL glass reactor equipped with a stirrer and a condenser, and under a nitrogen atmosphere, The mixture was heated and stirred at 100°C for 18 hours to carry out a hydration reaction of DCp and TCPD in composition (X1) (hereinafter also referred to as "reaction step"). Next, the obtained reaction solution was cooled to room temperature, and then neutralized and extracted with a 5% NaOH aqueous solution to obtain a fluorine-containing cyclic olefin composition before purification by distillation.
- Example 2 to 6 Example except that the types of acid catalyst and hydroxyl group-containing compound (C) were changed to those listed in Table 1, the amount of acid catalyst input was 13 g, and the heating conditions in the reaction step were changed to those listed in Table 1.
- a TDF 6- containing composition and a NBF 6- containing composition were manufactured and evaluated, respectively.
- Examples 4 and 5 used composition (X2) instead of composition (X1), and
- Example 6 used composition (X3) instead of composition (X1).
- the solid acid catalyst was removed by vacuum filtration and used as a measurement sample for gas chromatography analysis. Details of solid acids A and B in Table 1 are as follows.
- DCp-OPr or -OHx and TCPD-OPr in Table 1 mean alkyl etherified products of DCp and TCPD, respectively.
- composition (X2) (Preparation of composition (X2)) Under a nitrogen atmosphere, 3.8 kg of DCp (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and 11.5 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device, and heated at 160°C for 24 hours. The mixture was stirred and then heated and stirred at 180° C. for 15 hours. After cooling, 2.5 kg of unreacted hexafluoropropene was collected, and 12.4 kg of the reaction solution was taken out.
- DCp manufactured by Tokyo Kasei Kogyo Co., Ltd.
- hexafluoropropene manufactured by Takachiho Kagaku Kogyo Co., Ltd.
- composition (X3) (Preparation of composition (X3)) Under a nitrogen atmosphere, 5.2 kg of DCp (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and 14.2 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device, and heated at 160°C for 24 hours. The mixture was stirred and then heated and stirred at 180° C. for 15 hours. After cooling, 1.9 kg of unreacted hexafluoropropene was collected, and 16.3 kg of the reaction solution was taken out.
- DCp manufactured by Tokyo Kasei Kogyo Co., Ltd.
- hexafluoropropene manufactured by Takachiho Kagaku Kogyo Co., Ltd.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
This method for producing a fluorine-containing cyclic olefin composition includes: a mixing step for mixing an acid catalyst and one or more types of hydroxyl group-containing compounds (C) which are selected from the group consisting of water and alkyl alcohol into a composition (X) which contains a fluorine-containing cyclic olefin compound (A) represented by formula (1) and a cyclic diolefin compound (B1) which does not contain fluorine; and a reaction step for obtaining one or more types of compound selected from the group consisting of a hydrate compound (B2) which does not contain fluorine and an ether compound (B3) which does not contain fluorine, by reacting the cyclic diolefin compound (B1) which does not contain fluorine and the hydroxyl group-containing compounds (C) with one another.
Description
本発明は、フッ素含有環状オレフィン組成物の製造方法及びフッ素含有環状オレフィン組成物に関する。
The present invention relates to a method for producing a fluorine-containing cyclic olefin composition and a fluorine-containing cyclic olefin composition.
フッ素含有環状オレフィンポリマーの原材料であるフッ素含有環状オレフィン化合物は、例えば、フッ素含有オレフィンと環状ポリエンとをDiels-Alder反応させることにより製造することができる。
このようなフッ素含有環状オレフィン化合物の製造方法に関する技術としては、例えば、特許文献1に記載されたものが挙げられる。 A fluorine-containing cyclic olefin compound that is a raw material for a fluorine-containing cyclic olefin polymer can be produced, for example, by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction.
Examples of techniques related to the method for producing such fluorine-containing cyclic olefin compounds include those described in Patent Document 1.
このようなフッ素含有環状オレフィン化合物の製造方法に関する技術としては、例えば、特許文献1に記載されたものが挙げられる。 A fluorine-containing cyclic olefin compound that is a raw material for a fluorine-containing cyclic olefin polymer can be produced, for example, by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction.
Examples of techniques related to the method for producing such fluorine-containing cyclic olefin compounds include those described in Patent Document 1.
特許文献1には、反応容器内でフッ素含有オレフィンと環状ポリエンとを連続的に反応させることによって、フッ素含有環状オレフィンモノマーを連続的に製造する工程(A)を含むフッ素含有環状オレフィンモノマーの製造方法であって、前記工程(A)において、前記環状ポリエンを前記反応容器内に連続的又は断続的に供給するとともに、前記フッ素含有オレフィンを前記反応容器内に連続的又は断続的に供給するあるいは前記反応容器内に仕込んでおくことによって、前記フッ素含有オレフィンと前記環状ポリエンとを連続的に反応させ、かつ、前記反応容器内の前記環状ポリエンの含有量X1に対する前記フッ素含有オレフィンの含有量X2のモル比X2/X1を1.01以上の範囲内に調整するフッ素含有環状オレフィンモノマーの製造方法が記載されている。特許文献1には、前記製造方法によれば、目的のフッ素含有環状オレフィンモノマーを高選択的に得ることができると記載されている。
Patent Document 1 describes a process for producing a fluorine-containing cyclic olefin monomer, which includes a step (A) of continuously producing a fluorine-containing cyclic olefin monomer by continuously reacting a fluorine-containing olefin and a cyclic polyene in a reaction vessel. In the step (A), the cyclic polyene is continuously or intermittently supplied into the reaction vessel, and the fluorine-containing olefin is continuously or intermittently supplied into the reaction vessel, or By charging the fluorine-containing olefin and the cyclic polyene into the reaction vessel, the fluorine-containing olefin and the cyclic polyene can be continuously reacted, and the content of the fluorine-containing olefin relative to the content of the cyclic polyene in the reaction vessel X 1 . A method for producing a fluorine-containing cyclic olefin monomer is described in which the molar ratio X 2 / X 1 of X 2 is adjusted within a range of 1.01 or more. Patent Document 1 describes that according to the production method, the target fluorine-containing cyclic olefin monomer can be obtained with high selectivity.
本発明者らの検討によれば、フッ素含有オレフィン及び環状ポリエンを用いてフッ素含有環状オレフィン化合物を製造する際に、環状ポリエン同士がDiels-Alder反応してフッ素非含有環状ジオレフィン化合物が副生成物として生じてしまうことが明らかになった。フッ素非含有環状ジオレフィン化合物は反応性に富んでいるため、副生成物としてフッ素非含有環状ジオレフィン化合物を含むフッ素含有環状オレフィン化合物を用いるときに、望んでいない副反応が起きてしまう場合があった。
一方で、目的物であるフッ素含有環状オレフィン化合物と、副生成物であるフッ素非含有環状ジオレフィン化合物とは沸点差が小さい場合があり、蒸留によってフッ素含有環状オレフィン化合物とフッ素非含有環状ジオレフィン化合物を分離することが難しい場合があった。 According to the studies of the present inventors, when producing a fluorine-containing cyclic olefin compound using a fluorine-containing olefin and a cyclic polyene, the cyclic polyenes undergo a Diels-Alder reaction with each other, and a fluorine-free cyclic diolefin compound is produced as a by-product. It became clear that it would occur as a thing. Since fluorine-free cyclic diolefin compounds are highly reactive, undesired side reactions may occur when using fluorine-containing cyclic olefin compounds containing fluorine-free cyclic diolefin compounds as by-products. there were.
On the other hand, the boiling point difference between the target product, the fluorine-containing cyclic olefin compound, and the by-product, the fluorine-free cyclic diolefin compound, may be small. It was sometimes difficult to separate compounds.
一方で、目的物であるフッ素含有環状オレフィン化合物と、副生成物であるフッ素非含有環状ジオレフィン化合物とは沸点差が小さい場合があり、蒸留によってフッ素含有環状オレフィン化合物とフッ素非含有環状ジオレフィン化合物を分離することが難しい場合があった。 According to the studies of the present inventors, when producing a fluorine-containing cyclic olefin compound using a fluorine-containing olefin and a cyclic polyene, the cyclic polyenes undergo a Diels-Alder reaction with each other, and a fluorine-free cyclic diolefin compound is produced as a by-product. It became clear that it would occur as a thing. Since fluorine-free cyclic diolefin compounds are highly reactive, undesired side reactions may occur when using fluorine-containing cyclic olefin compounds containing fluorine-free cyclic diolefin compounds as by-products. there were.
On the other hand, the boiling point difference between the target product, the fluorine-containing cyclic olefin compound, and the by-product, the fluorine-free cyclic diolefin compound, may be small. It was sometimes difficult to separate compounds.
本発明は上記事情を鑑みなされたものであり、フッ素非含有環状ジオレフィン化合物の含有量が低減したフッ素含有環状オレフィン組成物を得ることが可能な製造方法を提供するものである。
The present invention has been made in view of the above circumstances, and provides a manufacturing method capable of obtaining a fluorine-containing cyclic olefin composition with a reduced content of a fluorine-free cyclic diolefin compound.
本発明者らは上記課題を解決すべく鋭意検討を重ねた。その結果、副生成物であるフッ素非含有環状ジオレフィン化合物を水酸基含有化合物により水和させる及び/又はエーテル化させることにより、目的物であるフッ素含有環状オレフィン化合物と、副生成物であるフッ素非含有環状ジオレフィン化合物との分離が容易となり、副生成物であるフッ素非含有環状ジオレフィン化合物の含有量が低減したフッ素含有環状オレフィン組成物を得ることが可能であることを見出し、本発明を完成させた。
本発明によれば、以下に示すフッ素含有環状オレフィン組成物の製造方法及びフッ素含有環状オレフィン組成物が提供される。 The present inventors have made extensive studies to solve the above problems. As a result, by hydrating and/or etherifying the by-product fluorine-free cyclic diolefin compound with the hydroxyl group-containing compound, the target fluorine-containing cyclic olefin compound and the fluorine-free by-product It has been discovered that it is possible to obtain a fluorine-containing cyclic olefin composition that can be easily separated from a fluorine-containing cyclic diolefin compound and has a reduced content of a fluorine-free cyclic diolefin compound as a by-product, and has developed the present invention. Completed.
According to the present invention, a method for producing a fluorine-containing cyclic olefin composition and a fluorine-containing cyclic olefin composition shown below are provided.
本発明によれば、以下に示すフッ素含有環状オレフィン組成物の製造方法及びフッ素含有環状オレフィン組成物が提供される。 The present inventors have made extensive studies to solve the above problems. As a result, by hydrating and/or etherifying the by-product fluorine-free cyclic diolefin compound with the hydroxyl group-containing compound, the target fluorine-containing cyclic olefin compound and the fluorine-free by-product It has been discovered that it is possible to obtain a fluorine-containing cyclic olefin composition that can be easily separated from a fluorine-containing cyclic diolefin compound and has a reduced content of a fluorine-free cyclic diolefin compound as a by-product, and has developed the present invention. Completed.
According to the present invention, a method for producing a fluorine-containing cyclic olefin composition and a fluorine-containing cyclic olefin composition shown below are provided.
[1]
下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程と、
前記フッ素非含有環状ジオレフィン化合物(B1)と、前記水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程と、
を含むフッ素含有環状オレフィン組成物の製造方法。
(前記式(1)中、R1~R4のうち、少なくとも1つは、フッ素、フッ素を含有する炭素数1~10のアルキル基、フッ素を含有する炭素数1~10のアルコキシ基、又はフッ素を含有する炭素数2~10のアルコキシアルキル基であり、R1~R4がフッ素を含有しない基である場合、R1~R4は、水素、炭素数1~10のアルキル基、炭素数1~10のアルコキシ基、又は炭素数2~10のアルコキシアルキル基から選ばれ、R1~R4は互いに結合して環構造を形成していてもよく、Xは-CH2-又はO-を示し、nは0又は1を示す。)
[2]
前記フッ素含有環状オレフィン化合物(A)の沸点と、前記フッ素非含有環状ジオレフィン化合物(B1)の沸点との差の絶対値が10℃以下である、前記[1]に記載のフッ素含有環状オレフィン組成物の製造方法。
[3]
前記アルキルアルコールの炭素数が3以上10以下である、前記[1]又は[2]に記載のフッ素含有環状オレフィン組成物の製造方法。
[4]
前記酸触媒が無機酸、有機酸及び固体酸からなる群から選択される少なくとも一種を含む、前記[1]~[3]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[5]
前記フッ素含有環状オレフィン化合物(A)のHOMOエネルギー(E1)と、前記フッ素非含有環状ジオレフィン化合物(B1)のHOMOエネルギー(E2)との差の絶対値|E2-E1|が0.3eV以上である、前記[1]~[4]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[6]
前記フッ素含有環状オレフィン化合物(A)は、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む、前記[1]~[5]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[7]
前記反応工程の後に、蒸留により、前記フッ素含有環状オレフィン化合物(A1)と前記フッ素含有環状オレフィン化合物(A2)とを分離する分離工程を更に含む、前記[6]に記載のフッ素含有環状オレフィン組成物の製造方法。
[8]
前記反応工程の後に、蒸留により、前記フッ素含有環状オレフィン化合物(A)と前記フッ素非含有水和化合物(B2)及び前記フッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程を更に含む、前記[1]~[7]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[9]
前記フッ素含有環状オレフィン組成物中の前記フッ素非含有環状ジオレフィン化合物(B1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、5.0質量%以下である、前記[1]~[8]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[10]
前記フッ素含有環状オレフィン組成物中の、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、99.0質量%以上である、前記[8]に記載のフッ素含有環状オレフィン組成物の製造方法。
[11]
前記フッ素含有環状オレフィン組成物中の、前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、99.0質量%以上である、前記[8]に記載のフッ素含有環状オレフィン組成物の製造方法。
[12]
下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含むフッ素含有環状オレフィン組成物であって、
前記フッ素含有環状オレフィン組成物中の前記フッ素非含有環状ジオレフィン化合物(B1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、0質量%超1.0質量%以下であるフッ素含有環状オレフィン組成物。
(前記式(1)中、R1~R4のうち、少なくとも1つは、フッ素、フッ素を含有する炭素数1~10のアルキル基、フッ素を含有する炭素数1~10のアルコキシ基、又はフッ素を含有する炭素数2~10のアルコキシアルキル基であり、R1~R4がフッ素を含有しない基である場合、R1~R4は、水素、炭素数1~10のアルキル基、炭素数1~10のアルコキシ基、又は炭素数2~10のアルコキシアルキル基から選ばれ、R1~R4は互いに結合して環構造を形成していてもよく、Xは-CH2-又はO-を示し、nは0又は1を示す。)
[1]
For a composition (X) containing a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1) represented by the following formula (1), an acid catalyst and a compound selected from the group consisting of water and an alkyl alcohol. a mixing step of mixing at least one selected hydroxyl group-containing compound (C);
By reacting the fluorine-free cyclic diolefin compound (B1) with the hydroxyl group-containing compound (C), a compound selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3) is produced. a reaction step for obtaining at least one type of
A method for producing a fluorine-containing cyclic olefin composition.
(In the above formula (1), at least one of R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or It is an alkoxyalkyl group having 2 to 10 carbon atoms containing fluorine, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or selected from alkoxy groups having 1 to 10 carbon atoms or alkoxyalkyl groups having 2 to 10 carbon atoms, R 1 to R 4 may be bonded to each other to form a ring structure, and X is -CH 2 - or O -, n indicates 0 or 1)
[2]
The fluorine-containing cyclic olefin according to [1] above, wherein the absolute value of the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the non-fluorine-containing cyclic diolefin compound (B1) is 10°C or less Method for manufacturing the composition.
[3]
The method for producing a fluorine-containing cyclic olefin composition according to [1] or [2] above, wherein the alkyl alcohol has 3 or more and 10 or less carbon atoms.
[4]
The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [3] above, wherein the acid catalyst contains at least one selected from the group consisting of inorganic acids, organic acids, and solid acids.
[5]
The absolute value of the difference between the HOMO energy (E 1 ) of the fluorine-containing cyclic olefin compound (A) and the HOMO energy (E 2 ) of the fluorine-free cyclic diolefin compound (B1) |E 2 −E 1 | The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [4] above, which has a voltage of 0.3 eV or more.
[6]
The fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1). The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [5] above, comprising both of the above.
[7]
The fluorine-containing cyclic olefin composition according to [6], further comprising a separation step of separating the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2) by distillation after the reaction step. How things are manufactured.
[8]
After the reaction step, separation of the fluorine-containing cyclic olefin compound (A), at least one selected from the group consisting of the fluorine-free hydrated compound (B2) and the fluorine-free ether compound (B3) is performed by distillation. The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [7] above, further comprising a separation step of separating.
[9]
The content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is 5.0% by mass or less when the entire fluorine-containing cyclic olefin composition is 100% by mass. , the method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [8] above.
[10]
When the content of the fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) in the fluorine-containing cyclic olefin composition is 100% by mass of the entire fluorine-containing cyclic olefin composition. , 99.0% by mass or more, the method for producing a fluorine-containing cyclic olefin composition according to [8] above.
[11]
When the content of the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1) in the fluorine-containing cyclic olefin composition is 100% by mass of the entire fluorine-containing cyclic olefin composition. , 99.0% by mass or more, the method for producing a fluorine-containing cyclic olefin composition according to [8] above.
[12]
A fluorine-containing cyclic olefin composition comprising a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1) represented by the following formula (1),
The content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is more than 0% by mass and 1.0% by mass when the entire fluorine-containing cyclic olefin composition is 100% by mass. % or less.
(In the above formula (1), at least one of R 1 to R 4 is fluorine, a fluorine-containing alkyl group having 1 to 10 carbon atoms, a fluorine-containing alkoxy group having 1 to 10 carbon atoms, or It is an alkoxyalkyl group having 2 to 10 carbon atoms containing fluorine, and when R 1 to R 4 are groups not containing fluorine, R 1 to R 4 are hydrogen, an alkyl group having 1 to 10 carbon atoms, or selected from alkoxy groups having 1 to 10 carbon atoms or alkoxyalkyl groups having 2 to 10 carbon atoms, R 1 to R 4 may be bonded to each other to form a ring structure, and X is -CH 2 - or O -, n indicates 0 or 1)
下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程と、
前記フッ素非含有環状ジオレフィン化合物(B1)と、前記水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程と、
を含むフッ素含有環状オレフィン組成物の製造方法。
[2]
前記フッ素含有環状オレフィン化合物(A)の沸点と、前記フッ素非含有環状ジオレフィン化合物(B1)の沸点との差の絶対値が10℃以下である、前記[1]に記載のフッ素含有環状オレフィン組成物の製造方法。
[3]
前記アルキルアルコールの炭素数が3以上10以下である、前記[1]又は[2]に記載のフッ素含有環状オレフィン組成物の製造方法。
[4]
前記酸触媒が無機酸、有機酸及び固体酸からなる群から選択される少なくとも一種を含む、前記[1]~[3]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[5]
前記フッ素含有環状オレフィン化合物(A)のHOMOエネルギー(E1)と、前記フッ素非含有環状ジオレフィン化合物(B1)のHOMOエネルギー(E2)との差の絶対値|E2-E1|が0.3eV以上である、前記[1]~[4]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[6]
前記フッ素含有環状オレフィン化合物(A)は、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む、前記[1]~[5]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[7]
前記反応工程の後に、蒸留により、前記フッ素含有環状オレフィン化合物(A1)と前記フッ素含有環状オレフィン化合物(A2)とを分離する分離工程を更に含む、前記[6]に記載のフッ素含有環状オレフィン組成物の製造方法。
[8]
前記反応工程の後に、蒸留により、前記フッ素含有環状オレフィン化合物(A)と前記フッ素非含有水和化合物(B2)及び前記フッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程を更に含む、前記[1]~[7]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[9]
前記フッ素含有環状オレフィン組成物中の前記フッ素非含有環状ジオレフィン化合物(B1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、5.0質量%以下である、前記[1]~[8]のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。
[10]
前記フッ素含有環状オレフィン組成物中の、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、99.0質量%以上である、前記[8]に記載のフッ素含有環状オレフィン組成物の製造方法。
[11]
前記フッ素含有環状オレフィン組成物中の、前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、99.0質量%以上である、前記[8]に記載のフッ素含有環状オレフィン組成物の製造方法。
[12]
下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含むフッ素含有環状オレフィン組成物であって、
前記フッ素含有環状オレフィン組成物中の前記フッ素非含有環状ジオレフィン化合物(B1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、0質量%超1.0質量%以下であるフッ素含有環状オレフィン組成物。
For a composition (X) containing a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1) represented by the following formula (1), an acid catalyst and a compound selected from the group consisting of water and an alkyl alcohol. a mixing step of mixing at least one selected hydroxyl group-containing compound (C);
By reacting the fluorine-free cyclic diolefin compound (B1) with the hydroxyl group-containing compound (C), a compound selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3) is produced. a reaction step for obtaining at least one type of
A method for producing a fluorine-containing cyclic olefin composition.
[2]
The fluorine-containing cyclic olefin according to [1] above, wherein the absolute value of the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the non-fluorine-containing cyclic diolefin compound (B1) is 10°C or less Method for manufacturing the composition.
[3]
The method for producing a fluorine-containing cyclic olefin composition according to [1] or [2] above, wherein the alkyl alcohol has 3 or more and 10 or less carbon atoms.
[4]
The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [3] above, wherein the acid catalyst contains at least one selected from the group consisting of inorganic acids, organic acids, and solid acids.
[5]
The absolute value of the difference between the HOMO energy (E 1 ) of the fluorine-containing cyclic olefin compound (A) and the HOMO energy (E 2 ) of the fluorine-free cyclic diolefin compound (B1) |E 2 −E 1 | The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [4] above, which has a voltage of 0.3 eV or more.
[6]
The fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1). The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [5] above, comprising both of the above.
[7]
The fluorine-containing cyclic olefin composition according to [6], further comprising a separation step of separating the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2) by distillation after the reaction step. How things are manufactured.
[8]
After the reaction step, separation of the fluorine-containing cyclic olefin compound (A), at least one selected from the group consisting of the fluorine-free hydrated compound (B2) and the fluorine-free ether compound (B3) is performed by distillation. The method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [7] above, further comprising a separation step of separating.
[9]
The content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is 5.0% by mass or less when the entire fluorine-containing cyclic olefin composition is 100% by mass. , the method for producing a fluorine-containing cyclic olefin composition according to any one of [1] to [8] above.
[10]
When the content of the fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) in the fluorine-containing cyclic olefin composition is 100% by mass of the entire fluorine-containing cyclic olefin composition. , 99.0% by mass or more, the method for producing a fluorine-containing cyclic olefin composition according to [8] above.
[11]
When the content of the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1) in the fluorine-containing cyclic olefin composition is 100% by mass of the entire fluorine-containing cyclic olefin composition. , 99.0% by mass or more, the method for producing a fluorine-containing cyclic olefin composition according to [8] above.
[12]
A fluorine-containing cyclic olefin composition comprising a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1) represented by the following formula (1),
The content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is more than 0% by mass and 1.0% by mass when the entire fluorine-containing cyclic olefin composition is 100% by mass. % or less.
本発明によれば、フッ素非含有環状ジオレフィン化合物の含有量が低減したフッ素含有環状オレフィン組成物を得ることが可能な製造方法を提供することができる。
According to the present invention, it is possible to provide a manufacturing method capable of obtaining a fluorine-containing cyclic olefin composition with a reduced content of a fluorine-free cyclic diolefin compound.
以下、本発明を実施形態に基づいて説明する。なお、本実施形態では、数値範囲を示す「A~B」は特に断りがなければ、A以上B以下を表す。また、数値範囲が段階的に記載されている場合、各数値範囲の上限及び下限は任意に組み合わせることができる。
Hereinafter, the present invention will be described based on embodiments. In this embodiment, unless otherwise specified, "A to B" indicating a numerical range represents A or more and B or less. Moreover, when numerical ranges are described in stages, the upper and lower limits of each numerical range can be arbitrarily combined.
1.フッ素含有環状オレフィン組成物の製造方法
本発明のフッ素含有環状オレフィン組成物の製造方法は、下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程と、前記フッ素非含有環状ジオレフィン化合物(B1)と、前記水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程と、を含む。
ここで、本明細書において、フッ素非含有環状ジオレフィン化合物(B1)と水との反応物をフッ素非含有水和化合物(B2)と呼び、フッ素非含有環状ジオレフィン化合物(B1)と、アルキルアルコールとの反応物をフッ素非含有エーテル化合物(B3)と呼ぶ。すなわち、本発明のフッ素含有環状オレフィン組成物の製造方法は、水酸基含有化合物(C)が水を含む場合は、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)とを反応させることによりフッ素非含有水和化合物(B2)を得る反応工程を含み、水酸基含有化合物(C)がアルキルアルコールを含む場合は、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)とを反応させることによりフッ素非含有エーテル化合物(B3)を得る反応工程を含む。 1. Method for producing a fluorine-containing cyclic olefin composition The method for producing a fluorine-containing cyclic olefin composition of the present invention comprises a fluorine-containing cyclic olefin compound (A) represented by the following formula (1) and a fluorine-free cyclic diolefin compound (B1). a mixing step of mixing an acid catalyst and at least one hydroxyl group-containing compound (C) selected from the group consisting of water and an alkyl alcohol; By reacting the olefin compound (B1) with the hydroxyl group-containing compound (C), at least one selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3) is obtained. A reaction step.
Here, in this specification, the reaction product of the fluorine-free cyclic diolefin compound (B1) and water is referred to as the fluorine-free hydrated compound (B2), and the fluorine-free cyclic diolefin compound (B1) and the alkyl The reaction product with alcohol is called a fluorine-free ether compound (B3). That is, in the method for producing a fluorine-containing cyclic olefin composition of the present invention, when the hydroxyl group-containing compound (C) contains water, the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) are reacted. When the hydroxyl group-containing compound (C) contains an alkyl alcohol, the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) are combined. The method includes a reaction step of obtaining a fluorine-free ether compound (B3) by reacting the following.
本発明のフッ素含有環状オレフィン組成物の製造方法は、下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程と、前記フッ素非含有環状ジオレフィン化合物(B1)と、前記水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程と、を含む。
ここで、本明細書において、フッ素非含有環状ジオレフィン化合物(B1)と水との反応物をフッ素非含有水和化合物(B2)と呼び、フッ素非含有環状ジオレフィン化合物(B1)と、アルキルアルコールとの反応物をフッ素非含有エーテル化合物(B3)と呼ぶ。すなわち、本発明のフッ素含有環状オレフィン組成物の製造方法は、水酸基含有化合物(C)が水を含む場合は、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)とを反応させることによりフッ素非含有水和化合物(B2)を得る反応工程を含み、水酸基含有化合物(C)がアルキルアルコールを含む場合は、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)とを反応させることによりフッ素非含有エーテル化合物(B3)を得る反応工程を含む。 1. Method for producing a fluorine-containing cyclic olefin composition The method for producing a fluorine-containing cyclic olefin composition of the present invention comprises a fluorine-containing cyclic olefin compound (A) represented by the following formula (1) and a fluorine-free cyclic diolefin compound (B1). a mixing step of mixing an acid catalyst and at least one hydroxyl group-containing compound (C) selected from the group consisting of water and an alkyl alcohol; By reacting the olefin compound (B1) with the hydroxyl group-containing compound (C), at least one selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3) is obtained. A reaction step.
Here, in this specification, the reaction product of the fluorine-free cyclic diolefin compound (B1) and water is referred to as the fluorine-free hydrated compound (B2), and the fluorine-free cyclic diolefin compound (B1) and the alkyl The reaction product with alcohol is called a fluorine-free ether compound (B3). That is, in the method for producing a fluorine-containing cyclic olefin composition of the present invention, when the hydroxyl group-containing compound (C) contains water, the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) are reacted. When the hydroxyl group-containing compound (C) contains an alkyl alcohol, the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) are combined. The method includes a reaction step of obtaining a fluorine-free ether compound (B3) by reacting the following.
本発明に係るフッ素含有環状オレフィン組成物の製造方法によれば、フッ素非含有環状ジオレフィン化合物の含有量が低減したフッ素含有環状オレフィン組成物を得ることができる。
このような効果が得られる理由は、以下の通りであると推察される。
酸触媒の存在下で、フッ素非含有環状ジオレフィン化合物(B1)と、水酸基含有化合物(C)とを反応させることにより、フッ素非含有環状ジオレフィン化合物(B1)に水酸基含有化合物(C)が付加してフッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)が生成する。これにより、フッ素含有環状オレフィン組成物中のフッ素非含有環状ジオレフィン化合物(B1)の含有量を低減することができる。
さらに、フッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)とフッ素含有環状オレフィン化合物(A)との沸点差が、フッ素非含有環状ジオレフィン化合物(B1)とフッ素含有環状オレフィン化合物(A)との沸点差よりも大きくなるため、フッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)は、蒸留によって、フッ素含有環状オレフィン組成物から分離しやすくなる。そのため、本発明に係るフッ素含有環状オレフィン組成物の製造方法によれば、副生成物を分離しやすくなるため、純度が向上したフッ素含有環状オレフィン組成物を得ることが可能である。
以下、各工程について説明する。 According to the method for producing a fluorine-containing cyclic olefin composition according to the present invention, it is possible to obtain a fluorine-containing cyclic olefin composition in which the content of a fluorine-free cyclic diolefin compound is reduced.
The reason why such an effect is obtained is presumed to be as follows.
By reacting the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) in the presence of an acid catalyst, the hydroxyl group-containing compound (C) is added to the fluorine-free cyclic diolefin compound (B1). The addition produces a fluorine-free hydrated compound (B2) or a fluorine-free ether compound (B3). Thereby, the content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition can be reduced.
Furthermore, the boiling point difference between the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3) and the fluorine-containing cyclic olefin compound (A) is the same as that between the fluorine-free cyclic diolefin compound (B1) and the fluorine-containing cyclic olefin compound. Since the boiling point difference is larger than that of compound (A), the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3) can be easily separated from the fluorine-containing cyclic olefin composition by distillation. Therefore, according to the method for producing a fluorine-containing cyclic olefin composition according to the present invention, by-products can be easily separated, so it is possible to obtain a fluorine-containing cyclic olefin composition with improved purity.
Each step will be explained below.
このような効果が得られる理由は、以下の通りであると推察される。
酸触媒の存在下で、フッ素非含有環状ジオレフィン化合物(B1)と、水酸基含有化合物(C)とを反応させることにより、フッ素非含有環状ジオレフィン化合物(B1)に水酸基含有化合物(C)が付加してフッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)が生成する。これにより、フッ素含有環状オレフィン組成物中のフッ素非含有環状ジオレフィン化合物(B1)の含有量を低減することができる。
さらに、フッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)とフッ素含有環状オレフィン化合物(A)との沸点差が、フッ素非含有環状ジオレフィン化合物(B1)とフッ素含有環状オレフィン化合物(A)との沸点差よりも大きくなるため、フッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)は、蒸留によって、フッ素含有環状オレフィン組成物から分離しやすくなる。そのため、本発明に係るフッ素含有環状オレフィン組成物の製造方法によれば、副生成物を分離しやすくなるため、純度が向上したフッ素含有環状オレフィン組成物を得ることが可能である。
以下、各工程について説明する。 According to the method for producing a fluorine-containing cyclic olefin composition according to the present invention, it is possible to obtain a fluorine-containing cyclic olefin composition in which the content of a fluorine-free cyclic diolefin compound is reduced.
The reason why such an effect is obtained is presumed to be as follows.
By reacting the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) in the presence of an acid catalyst, the hydroxyl group-containing compound (C) is added to the fluorine-free cyclic diolefin compound (B1). The addition produces a fluorine-free hydrated compound (B2) or a fluorine-free ether compound (B3). Thereby, the content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition can be reduced.
Furthermore, the boiling point difference between the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3) and the fluorine-containing cyclic olefin compound (A) is the same as that between the fluorine-free cyclic diolefin compound (B1) and the fluorine-containing cyclic olefin compound. Since the boiling point difference is larger than that of compound (A), the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3) can be easily separated from the fluorine-containing cyclic olefin composition by distillation. Therefore, according to the method for producing a fluorine-containing cyclic olefin composition according to the present invention, by-products can be easily separated, so it is possible to obtain a fluorine-containing cyclic olefin composition with improved purity.
Each step will be explained below.
[混合工程]
本発明に係るフッ素含有環状オレフィン組成物の製造方法は、前記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程を含む。 [Mixing process]
The method for producing a fluorine-containing cyclic olefin composition according to the present invention includes a composition (X) containing a fluorine-containing cyclic olefin compound (A) represented by the above formula (1) and a fluorine-free cyclic diolefin compound (B1). On the other hand, it includes a mixing step of mixing an acid catalyst and at least one hydroxyl group-containing compound (C) selected from the group consisting of water and alkyl alcohol.
本発明に係るフッ素含有環状オレフィン組成物の製造方法は、前記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程を含む。 [Mixing process]
The method for producing a fluorine-containing cyclic olefin composition according to the present invention includes a composition (X) containing a fluorine-containing cyclic olefin compound (A) represented by the above formula (1) and a fluorine-free cyclic diolefin compound (B1). On the other hand, it includes a mixing step of mixing an acid catalyst and at least one hydroxyl group-containing compound (C) selected from the group consisting of water and alkyl alcohol.
(組成物(X))
組成物(X)は、フッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む。
組成物(X)は、例えば、フッ素含有オレフィンと環状ポリエンとをDiels-Alder反応させることにより得られる組成物である。 (Composition (X))
Composition (X) contains a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1).
Composition (X) is, for example, a composition obtained by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction.
組成物(X)は、フッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む。
組成物(X)は、例えば、フッ素含有オレフィンと環状ポリエンとをDiels-Alder反応させることにより得られる組成物である。 (Composition (X))
Composition (X) contains a fluorine-containing cyclic olefin compound (A) and a fluorine-free cyclic diolefin compound (B1).
Composition (X) is, for example, a composition obtained by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction.
Xは-CH2-又はO-を示し、-CH2-が好ましい。
nは0又は1を示し、1が好ましい。
X represents -CH 2 - or O-, preferably -CH 2 -.
n represents 0 or 1, preferably 1.
前記式(1)において、R1~R4としては、より具体的には、フッ素;フルオロメチル基、ジフルオロメチル基、トリフルオロメチル基、トリフルオロエチル基、ペンタフルオロエチル基、ヘプタフルオロプロピル基、ヘキサフルオロイソプロピル基、ヘプタフルオロイソプロピル基、ヘキサフルオロ-2-メチルイソプロピル基、ペルフルオロ-2-メチルイソプロピル基、n-ペルフルオロブチル基、n-ペルフルオロペンチル基、ペルフルオロシクロペンチル基等のアルキル基の水素の一部又は全てがフッ素で置換されたアルキル基等のフッ素を含有する炭素数1~10のアルキル基;フルオロメトキシ基、ジフルオロメトキシ基、トリフルオロメトキシ基、トリフルオロエトキシ基、ペンタフルオロエトキシ基、ヘプタフルオロプロポキシ基、ヘキサフルオロイソプロポキシ基、ヘプタフルオロイソプロポキシ基、ヘキサフルオロ-2-メチルイソプロポキシ基、ペルフルオロ-2-メチルイソプロポキシ基、n-ペルフルオロブトキシ基、n-ペルフルオロペントキシ基、ペルフルオロシクロペントキシ基等のアルコキシ基の水素の一部又は全てがフッ素で置換されたアルコキシ基等のフッ素を含有する炭素数1~10のアルコキシ基;フルオロメトキシメチル基、ジフルオロメトキシメチル基、トリフルオロメトキシメチル基、トリフルオロエトキシメチル基、ペンタフルオロエトキシメチル基、ヘプタフルオロプロポキシメチル基、ヘキサフルオロイソプロポキシメチル基、ヘプタフルオロイソプロポキシメチル基、ヘキサフルオロ-2-メチルイソプロポキシメチル基、ペルフルオロ-2-メチルイソプロポキシメチル基、n-ペルフルオロブトキシメチル基、n-ペルフルオロペントキシメチル基、ペルフルオロシクロペントキシメチル基等のアルコキシ基の水素の一部又は全てがフッ素で置換されたアルコキシアルキル基等のフッ素を含有する炭素数2~10のアルコキシアルキル基等が例示される。
In the formula (1), R 1 to R 4 more specifically include fluorine; fluoromethyl group, difluoromethyl group, trifluoromethyl group, trifluoroethyl group, pentafluoroethyl group, heptafluoropropyl group. , hexafluoroisopropyl group, heptafluoroisopropyl group, hexafluoro-2-methylisopropyl group, perfluoro-2-methylisopropyl group, n-perfluorobutyl group, n-perfluoropentyl group, perfluorocyclopentyl group, etc. An alkyl group containing 1 to 10 carbon atoms containing fluorine, such as an alkyl group partially or completely substituted with fluorine; a fluoromethoxy group, a difluoromethoxy group, a trifluoromethoxy group, a trifluoroethoxy group, a pentafluoroethoxy group, Heptafluoropropoxy group, hexafluoroisopropoxy group, heptafluoroisopropoxy group, hexafluoro-2-methylisopropoxy group, perfluoro-2-methylisopropoxy group, n-perfluorobutoxy group, n-perfluoropentoxy group, perfluoro A fluorine-containing alkoxy group having 1 to 10 carbon atoms, such as an alkoxy group in which some or all of the hydrogen atoms of an alkoxy group such as a cyclopentoxy group are substituted with fluorine; fluoromethoxymethyl group, difluoromethoxymethyl group, trifluoro Methoxymethyl group, trifluoroethoxymethyl group, pentafluoroethoxymethyl group, heptafluoropropoxymethyl group, hexafluoroisopropoxymethyl group, heptafluoroisopropoxymethyl group, hexafluoro-2-methylisopropoxymethyl group, perfluoro-2 - Alkoxyalkyl groups in which some or all of the hydrogen atoms of an alkoxy group are substituted with fluorine, such as methylisopropoxymethyl group, n-perfluorobutoxymethyl group, n-perfluoropentoxymethyl group, perfluorocyclopentoxymethyl group, etc. Examples include fluorine-containing alkoxyalkyl groups having 2 to 10 carbon atoms.
また、R1~R4が互いに結合して環構造を形成していてもよく、ペルフルオロシクロアルキル基、酸素を介したペルフルオロシクロエーテル基等の環を形成してもよい。
さらに、フッ素を含有しないその他のR1~R4としては、水素;メチル基、エチル基、プロピル基、イソプロピル基、2-メチルイソプロピル基、n-ブチル基、n-ペンチル基、シクロペンチル基等の炭素数1~10のアルキル基;メトキシ基、エトキシ基、プロポキシ基、ブトキシ基、ペントキシ基等の炭素数1~10のアルコキシ基、メトキシメチル基、エトキシメチル基、プロポキシメチル基、ブトキシメチル基、ペントキシメチル基等の炭素数2~10のアルコキシアルキル基等が例示される。 Further, R 1 to R 4 may be bonded to each other to form a ring structure, or may form a ring such as a perfluorocycloalkyl group or a perfluorocycloether group via oxygen.
Furthermore, other R 1 to R 4 that do not contain fluorine include hydrogen; methyl group, ethyl group, propyl group, isopropyl group, 2-methylisopropyl group, n-butyl group, n-pentyl group, cyclopentyl group, etc. Alkyl group having 1 to 10 carbon atoms; alkoxy group having 1 to 10 carbon atoms such as methoxy group, ethoxy group, propoxy group, butoxy group, pentoxy group, methoxymethyl group, ethoxymethyl group, propoxymethyl group, butoxymethyl group, Examples include alkoxyalkyl groups having 2 to 10 carbon atoms such as pentoxymethyl group.
さらに、フッ素を含有しないその他のR1~R4としては、水素;メチル基、エチル基、プロピル基、イソプロピル基、2-メチルイソプロピル基、n-ブチル基、n-ペンチル基、シクロペンチル基等の炭素数1~10のアルキル基;メトキシ基、エトキシ基、プロポキシ基、ブトキシ基、ペントキシ基等の炭素数1~10のアルコキシ基、メトキシメチル基、エトキシメチル基、プロポキシメチル基、ブトキシメチル基、ペントキシメチル基等の炭素数2~10のアルコキシアルキル基等が例示される。 Further, R 1 to R 4 may be bonded to each other to form a ring structure, or may form a ring such as a perfluorocycloalkyl group or a perfluorocycloether group via oxygen.
Furthermore, other R 1 to R 4 that do not contain fluorine include hydrogen; methyl group, ethyl group, propyl group, isopropyl group, 2-methylisopropyl group, n-butyl group, n-pentyl group, cyclopentyl group, etc. Alkyl group having 1 to 10 carbon atoms; alkoxy group having 1 to 10 carbon atoms such as methoxy group, ethoxy group, propoxy group, butoxy group, pentoxy group, methoxymethyl group, ethoxymethyl group, propoxymethyl group, butoxymethyl group, Examples include alkoxyalkyl groups having 2 to 10 carbon atoms such as pentoxymethyl group.
フッ素含有環状オレフィン化合物(A)は、例えば、フッ素含有オレフィンと環状ポリエンとをDiels-Alder反応させることにより得られる組成物であり、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む混合物の場合がある。
前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む混合物の場合において、フッ素含有環状オレフィン化合物(A1)及びフッ素含有環状オレフィン化合物(A2)は、前記式(1)中、Xが-CH2-であって、R1~R4がフッ素又はトリフルオロメチル基であることが好ましく、R1~R4のうち1つがトリフルオロメチル基であり、残りがフッ素であることがより好ましい。 The fluorine-containing cyclic olefin compound (A) is, for example, a composition obtained by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction, and is a fluorine-containing cyclic olefin compound in which n is 0 in the formula (1) above. There may be a mixture containing both (A1) and the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1).
In the case of a mixture containing both the fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1), the fluorine-containing In the cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2), in the formula (1), X is -CH 2 -, and R 1 to R 4 are fluorine or a trifluoromethyl group. Preferably, one of R 1 to R 4 is a trifluoromethyl group, and the remaining ones are more preferably fluorine.
前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む混合物の場合において、フッ素含有環状オレフィン化合物(A1)及びフッ素含有環状オレフィン化合物(A2)は、前記式(1)中、Xが-CH2-であって、R1~R4がフッ素又はトリフルオロメチル基であることが好ましく、R1~R4のうち1つがトリフルオロメチル基であり、残りがフッ素であることがより好ましい。 The fluorine-containing cyclic olefin compound (A) is, for example, a composition obtained by subjecting a fluorine-containing olefin and a cyclic polyene to a Diels-Alder reaction, and is a fluorine-containing cyclic olefin compound in which n is 0 in the formula (1) above. There may be a mixture containing both (A1) and the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1).
In the case of a mixture containing both the fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1), the fluorine-containing In the cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2), in the formula (1), X is -CH 2 -, and R 1 to R 4 are fluorine or a trifluoromethyl group. Preferably, one of R 1 to R 4 is a trifluoromethyl group, and the remaining ones are more preferably fluorine.
フッ素含有環状オレフィン化合物(A)としては、好ましくはフッ素含有テトラシクロドデセン、フッ素含有ノルボルネン、フッ素含有オキソテトラシクロドデセン及びフッ素含有オキソノルボルネンから選択される少なくとも一種を含み、より好ましくはフッ素含有テトラシクロドデセン及びフッ素含有ノルボルネンから選択される少なくとも一種を含み、更に好ましくはフッ素含有テトラシクロドデセンを含む。
ここで、テトラシクロドデセンとはテトラシクロ[4.4.0.12,5.17,10]-3-ドデセンのことをいう。ノルボルネンとは、ビシクロ[2.2.1]ヘプト-2-エンのことをいう。また、オキソノルボルネンとは、オキサビシクロ[2.2.1]ヘプト-2-エンのことをいう。
フッ素含有テトラシクロドデセンとは、前記式(1)中、Xが-CH2-でありnが1であるフッ素含有環状オレフィンである。
フッ素含有ノルボルネンとは、前記式(1)中、Xが-CH2-でありnが0であるフッ素含有環状オレフィンである。
フッ素含有オキソテトラシクロドデセンとは、前記式(1)中、Xが-O-でありnが1であるフッ素含有環状オレフィンである。
フッ素含有オキソノルボルネンとは、前記式(1)中、Xが-O-でありnが0であるフッ素含有環状オレフィンである。 The fluorine-containing cyclic olefin compound (A) preferably contains at least one selected from fluorine-containing tetracyclododecene, fluorine-containing norbornene, fluorine-containing oxotetracyclododecene, and fluorine-containing oxonorbornene, and more preferably fluorine-containing It contains at least one selected from tetracyclododecene and fluorine-containing norbornene, and more preferably contains fluorine-containing tetracyclododecene.
Here, tetracyclododecene means tetracyclo[4.4.0.1 2,5 . 1 7,10 ]-3-dodecene. Norbornene refers to bicyclo[2.2.1]hept-2-ene. Further, oxonorbornene refers to oxabicyclo[2.2.1]hept-2-ene.
The fluorine-containing tetracyclododecene is a fluorine-containing cyclic olefin in which X is -CH 2 - and n is 1 in the formula (1).
The fluorine-containing norbornene is a fluorine-containing cyclic olefin in which, in the formula (1), X is -CH 2 - and n is 0.
The fluorine-containing oxotetracyclododecene is a fluorine-containing cyclic olefin in which X is -O- and n is 1 in the formula (1).
The fluorine-containing oxonorbornene is a fluorine-containing cyclic olefin in which X is -O- and n is 0 in the formula (1).
ここで、テトラシクロドデセンとはテトラシクロ[4.4.0.12,5.17,10]-3-ドデセンのことをいう。ノルボルネンとは、ビシクロ[2.2.1]ヘプト-2-エンのことをいう。また、オキソノルボルネンとは、オキサビシクロ[2.2.1]ヘプト-2-エンのことをいう。
フッ素含有テトラシクロドデセンとは、前記式(1)中、Xが-CH2-でありnが1であるフッ素含有環状オレフィンである。
フッ素含有ノルボルネンとは、前記式(1)中、Xが-CH2-でありnが0であるフッ素含有環状オレフィンである。
フッ素含有オキソテトラシクロドデセンとは、前記式(1)中、Xが-O-でありnが1であるフッ素含有環状オレフィンである。
フッ素含有オキソノルボルネンとは、前記式(1)中、Xが-O-でありnが0であるフッ素含有環状オレフィンである。 The fluorine-containing cyclic olefin compound (A) preferably contains at least one selected from fluorine-containing tetracyclododecene, fluorine-containing norbornene, fluorine-containing oxotetracyclododecene, and fluorine-containing oxonorbornene, and more preferably fluorine-containing It contains at least one selected from tetracyclododecene and fluorine-containing norbornene, and more preferably contains fluorine-containing tetracyclododecene.
Here, tetracyclododecene means tetracyclo[4.4.0.1 2,5 . 1 7,10 ]-3-dodecene. Norbornene refers to bicyclo[2.2.1]hept-2-ene. Further, oxonorbornene refers to oxabicyclo[2.2.1]hept-2-ene.
The fluorine-containing tetracyclododecene is a fluorine-containing cyclic olefin in which X is -CH 2 - and n is 1 in the formula (1).
The fluorine-containing norbornene is a fluorine-containing cyclic olefin in which, in the formula (1), X is -CH 2 - and n is 0.
The fluorine-containing oxotetracyclododecene is a fluorine-containing cyclic olefin in which X is -O- and n is 1 in the formula (1).
The fluorine-containing oxonorbornene is a fluorine-containing cyclic olefin in which X is -O- and n is 0 in the formula (1).
(フッ素含有オレフィン)
フッ素含有オレフィンは、例えば、下記式(2)で表わされるフッ素含有オレフィンを用いることができる。 (Fluorine-containing olefin)
As the fluorine-containing olefin, for example, a fluorine-containing olefin represented by the following formula (2) can be used.
フッ素含有オレフィンは、例えば、下記式(2)で表わされるフッ素含有オレフィンを用いることができる。 (Fluorine-containing olefin)
As the fluorine-containing olefin, for example, a fluorine-containing olefin represented by the following formula (2) can be used.
前記式(2)において、R1~R4としては、より具体的には、フッ素;フルオロメチル基、ジフルオロメチル基、トリフルオロメチル基、トリフルオロエチル基、ペンタフルオロエチル基、ヘプタフルオロプロピル基、ヘキサフルオロイソプロピル基、ヘプタフルオロイソプロピル基、ヘキサフルオロ-2-メチルイソプロピル基、ペルフルオロ-2-メチルイソプロピル基、n-ペルフルオロブチル基、n-ペルフルオロペンチル基、ペルフルオロシクロペンチル基等のアルキル基の水素の一部又は全てがフッ素で置換されたアルキル基等のフッ素を含有する炭素数1~10のアルキル基;フルオロメトキシ基、ジフルオロメトキシ基、トリフルオロメトキシ基、トリフルオロエトキシ基、ペンタフルオロエトキシ基、ヘプタフルオロプロポキシ基、ヘキサフルオロイソプロポキシ基、ヘプタフルオロイソプロポキシ基、ヘキサフルオロ-2-メチルイソプロポキシ基、ペルフルオロ-2-メチルイソプロポキシ基、n-ペルフルオロブトキシ基、n-ペルフルオロペントキシ基、ペルフルオロシクロペントキシ基等のアルコキシ基の水素の一部又は全てがフッ素で置換されたアルコキシ基等のフッ素を含有する炭素数1~10のアルコキシ基;フルオロメトキシメチル基、ジフルオロメトキシメチル基、トリフルオロメトキシメチル基、トリフルオロエトキシメチル基、ペンタフルオロエトキシメチル基、ヘプタフルオロプロポキシメチル基、ヘキサフルオロイソプロポキシメチル基、ヘプタフルオロイソプロポキシメチル基、ヘキサフルオロ-2-メチルイソプロポキシメチル基、ペルフルオロ-2-メチルイソプロポキシメチル基、n-ペルフルオロブトキシメチル基、n-ペルフルオロペントキシメチル基、ペルフルオロシクロペントキシメチル基等のアルコキシ基の水素の一部又は全てがフッ素で置換されたアルコキシアルキル基等のフッ素を含有する炭素数2~10のアルコキシアルキル基等が例示される。
In the formula (2), R 1 to R 4 more specifically include fluorine; fluoromethyl group, difluoromethyl group, trifluoromethyl group, trifluoroethyl group, pentafluoroethyl group, heptafluoropropyl group. , hexafluoroisopropyl group, heptafluoroisopropyl group, hexafluoro-2-methylisopropyl group, perfluoro-2-methylisopropyl group, n-perfluorobutyl group, n-perfluoropentyl group, perfluorocyclopentyl group, etc. An alkyl group containing 1 to 10 carbon atoms containing fluorine, such as an alkyl group partially or completely substituted with fluorine; a fluoromethoxy group, a difluoromethoxy group, a trifluoromethoxy group, a trifluoroethoxy group, a pentafluoroethoxy group, Heptafluoropropoxy group, hexafluoroisopropoxy group, heptafluoroisopropoxy group, hexafluoro-2-methylisopropoxy group, perfluoro-2-methylisopropoxy group, n-perfluorobutoxy group, n-perfluoropentoxy group, perfluoro A fluorine-containing alkoxy group having 1 to 10 carbon atoms, such as an alkoxy group in which some or all of the hydrogen atoms of an alkoxy group such as a cyclopentoxy group are substituted with fluorine; fluoromethoxymethyl group, difluoromethoxymethyl group, trifluoro Methoxymethyl group, trifluoroethoxymethyl group, pentafluoroethoxymethyl group, heptafluoropropoxymethyl group, hexafluoroisopropoxymethyl group, heptafluoroisopropoxymethyl group, hexafluoro-2-methylisopropoxymethyl group, perfluoro-2 - Alkoxyalkyl groups in which some or all of the hydrogen atoms of an alkoxy group are substituted with fluorine, such as methylisopropoxymethyl group, n-perfluorobutoxymethyl group, n-perfluoropentoxymethyl group, perfluorocyclopentoxymethyl group, etc. Examples include fluorine-containing alkoxyalkyl groups having 2 to 10 carbon atoms.
また、R1~R4が互いに結合して環構造を形成していてもよく、ペルフルオロシクロアルキル基、酸素を介したペルフルオロシクロエーテル基等の環を形成してもよい。
さらに、フッ素を含有しないその他のR1~R4としては、水素;メチル基、エチル基、プロピル基、イソプロピル基、2-メチルイソプロピル基、n-ブチル基、n-ペンチル基、シクロペンチル基等の炭素数1~10のアルキル基;メトキシ基、エトキシ基、プロポキシ基、ブトキシ基、ペントキシ基等の炭素数1~10のアルコキシ基、メトキシメチル基、エトキシメチル基、プロポキシメチル基、ブトキシメチル基、ペントキシメチル基等の炭素数2~10のアルコキシアルキル基等が例示される。 Further, R 1 to R 4 may be bonded to each other to form a ring structure, or may form a ring such as a perfluorocycloalkyl group or a perfluorocycloether group via oxygen.
Furthermore, other R 1 to R 4 that do not contain fluorine include hydrogen; methyl group, ethyl group, propyl group, isopropyl group, 2-methylisopropyl group, n-butyl group, n-pentyl group, cyclopentyl group, etc. Alkyl group having 1 to 10 carbon atoms; alkoxy group having 1 to 10 carbon atoms such as methoxy group, ethoxy group, propoxy group, butoxy group, pentoxy group, methoxymethyl group, ethoxymethyl group, propoxymethyl group, butoxymethyl group, Examples include alkoxyalkyl groups having 2 to 10 carbon atoms such as pentoxymethyl group.
さらに、フッ素を含有しないその他のR1~R4としては、水素;メチル基、エチル基、プロピル基、イソプロピル基、2-メチルイソプロピル基、n-ブチル基、n-ペンチル基、シクロペンチル基等の炭素数1~10のアルキル基;メトキシ基、エトキシ基、プロポキシ基、ブトキシ基、ペントキシ基等の炭素数1~10のアルコキシ基、メトキシメチル基、エトキシメチル基、プロポキシメチル基、ブトキシメチル基、ペントキシメチル基等の炭素数2~10のアルコキシアルキル基等が例示される。 Further, R 1 to R 4 may be bonded to each other to form a ring structure, or may form a ring such as a perfluorocycloalkyl group or a perfluorocycloether group via oxygen.
Furthermore, other R 1 to R 4 that do not contain fluorine include hydrogen; methyl group, ethyl group, propyl group, isopropyl group, 2-methylisopropyl group, n-butyl group, n-pentyl group, cyclopentyl group, etc. Alkyl group having 1 to 10 carbon atoms; alkoxy group having 1 to 10 carbon atoms such as methoxy group, ethoxy group, propoxy group, butoxy group, pentoxy group, methoxymethyl group, ethoxymethyl group, propoxymethyl group, butoxymethyl group, Examples include alkoxyalkyl groups having 2 to 10 carbon atoms such as pentoxymethyl group.
(環状ポリエン)
環状ポリエンとしては、例えば、シクロペンタジエン、シクロヘキサジエン、エチルシクロヘキサジエン、シクロヘプタジエン、ジシクロペンタジエン、ジシクロヘキサジエン、1-オキサ-2,4-シクロペンタジエン、1-オキサ-2-エチル-2,4-シクロペンタジエン、1-オキサ-2-ビニル-2,4-シクロペンタジエン、エチリデンノルボルネン、ビニルノルボルネン、イソプロピリデンノルボルネン、メチルヒドロインデン、ジイソプロピリデンノルボルネン、プロペニルイソノルボルナジエン等を用いることができる。
これらの環状ポリエンは、1種類を単独で用いてもよいし、2種以上を組み合せて用いてもよい。
これらの中でも、環状ポリエンとしては、シクロペンタジエン、ジシクロペンタジエン及び1-オキサ-2,4-シクロペンタジエン(慣用名で通常フランと称す)が好ましく、ジシクロペンタジエン及びフランがより好ましく、ジシクロペンタジエンが更に好ましい。 (cyclic polyene)
Examples of the cyclic polyene include cyclopentadiene, cyclohexadiene, ethylcyclohexadiene, cycloheptadiene, dicyclopentadiene, dicyclohexadiene, 1-oxa-2,4-cyclopentadiene, 1-oxa-2-ethyl-2, 4-cyclopentadiene, 1-oxa-2-vinyl-2,4-cyclopentadiene, ethylidenenorbornene, vinylnorbornene, isopropylidenenorbornene, methylhydroindene, diisopropylidenenorbornene, propenylisonorbornadiene, and the like can be used.
These cyclic polyenes may be used singly or in combination of two or more.
Among these, as the cyclic polyene, cyclopentadiene, dicyclopentadiene, and 1-oxa-2,4-cyclopentadiene (commonly referred to as furan) are preferred, dicyclopentadiene and furan are more preferred, and dicyclopentadiene is preferred. is even more preferable.
環状ポリエンとしては、例えば、シクロペンタジエン、シクロヘキサジエン、エチルシクロヘキサジエン、シクロヘプタジエン、ジシクロペンタジエン、ジシクロヘキサジエン、1-オキサ-2,4-シクロペンタジエン、1-オキサ-2-エチル-2,4-シクロペンタジエン、1-オキサ-2-ビニル-2,4-シクロペンタジエン、エチリデンノルボルネン、ビニルノルボルネン、イソプロピリデンノルボルネン、メチルヒドロインデン、ジイソプロピリデンノルボルネン、プロペニルイソノルボルナジエン等を用いることができる。
これらの環状ポリエンは、1種類を単独で用いてもよいし、2種以上を組み合せて用いてもよい。
これらの中でも、環状ポリエンとしては、シクロペンタジエン、ジシクロペンタジエン及び1-オキサ-2,4-シクロペンタジエン(慣用名で通常フランと称す)が好ましく、ジシクロペンタジエン及びフランがより好ましく、ジシクロペンタジエンが更に好ましい。 (cyclic polyene)
Examples of the cyclic polyene include cyclopentadiene, cyclohexadiene, ethylcyclohexadiene, cycloheptadiene, dicyclopentadiene, dicyclohexadiene, 1-oxa-2,4-cyclopentadiene, 1-oxa-2-ethyl-2, 4-cyclopentadiene, 1-oxa-2-vinyl-2,4-cyclopentadiene, ethylidenenorbornene, vinylnorbornene, isopropylidenenorbornene, methylhydroindene, diisopropylidenenorbornene, propenylisonorbornadiene, and the like can be used.
These cyclic polyenes may be used singly or in combination of two or more.
Among these, as the cyclic polyene, cyclopentadiene, dicyclopentadiene, and 1-oxa-2,4-cyclopentadiene (commonly referred to as furan) are preferred, dicyclopentadiene and furan are more preferred, and dicyclopentadiene is preferred. is even more preferable.
(フッ素非含有環状ジオレフィン化合物(B1))
フッ素非含有環状ジオレフィン化合物(B1)は、例えば、前記環状ポリエン同士がDiels-Alder反応して得られる化合物であり、ジシクロペンタジエン、トリシクロペンタジエン等が挙げられる。フッ素非含有環状ジオレフィン化合物(B1)は、ジシクロペンタジエン及びトリシクロペンタジエンから選択される少なくとも一種が含まれていてもよい。 (Fluorine-free cyclic diolefin compound (B1))
The fluorine-free cyclic diolefin compound (B1) is, for example, a compound obtained by a Diels-Alder reaction between the cyclic polyenes, and examples thereof include dicyclopentadiene, tricyclopentadiene, and the like. The fluorine-free cyclic diolefin compound (B1) may contain at least one selected from dicyclopentadiene and tricyclopentadiene.
フッ素非含有環状ジオレフィン化合物(B1)は、例えば、前記環状ポリエン同士がDiels-Alder反応して得られる化合物であり、ジシクロペンタジエン、トリシクロペンタジエン等が挙げられる。フッ素非含有環状ジオレフィン化合物(B1)は、ジシクロペンタジエン及びトリシクロペンタジエンから選択される少なくとも一種が含まれていてもよい。 (Fluorine-free cyclic diolefin compound (B1))
The fluorine-free cyclic diolefin compound (B1) is, for example, a compound obtained by a Diels-Alder reaction between the cyclic polyenes, and examples thereof include dicyclopentadiene, tricyclopentadiene, and the like. The fluorine-free cyclic diolefin compound (B1) may contain at least one selected from dicyclopentadiene and tricyclopentadiene.
組成物(X)において、フッ素含有環状オレフィン化合物(A)の沸点と、フッ素非含有環状ジオレフィン化合物(B1)の沸点との差の絶対値が10℃以下である場合、蒸留によってフッ素含有環状オレフィン化合物(A)とフッ素非含有環状ジオレフィン化合物(B1)を分離することが難しいため、純度が向上したフッ素含有環状オレフィン組成物を得る観点から、本発明に係るフッ素含有環状オレフィン組成物の製造方法は効果的である。
本明細書において、沸点は1気圧での沸点を示す。 In the composition (X), when the absolute value of the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free cyclic diolefin compound (B1) is 10°C or less, the fluorine-containing cyclic olefin compound is removed by distillation. Since it is difficult to separate the olefin compound (A) and the fluorine-free cyclic diolefin compound (B1), from the viewpoint of obtaining a fluorine-containing cyclic olefin composition with improved purity, the fluorine-containing cyclic olefin composition according to the present invention is The manufacturing method is effective.
In this specification, the boiling point refers to the boiling point at 1 atmosphere.
本明細書において、沸点は1気圧での沸点を示す。 In the composition (X), when the absolute value of the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free cyclic diolefin compound (B1) is 10°C or less, the fluorine-containing cyclic olefin compound is removed by distillation. Since it is difficult to separate the olefin compound (A) and the fluorine-free cyclic diolefin compound (B1), from the viewpoint of obtaining a fluorine-containing cyclic olefin composition with improved purity, the fluorine-containing cyclic olefin composition according to the present invention is The manufacturing method is effective.
In this specification, the boiling point refers to the boiling point at 1 atmosphere.
(酸触媒)
酸触媒としてはブレンステッド酸であれば特に限定されず、無機酸、有機酸及び固体酸からなる群から選択される少なくとも一種が挙げられる。
無機酸としては、例えば、塩酸、硫酸、硝酸、リン酸等が挙げられる。
有機酸としては、例えば、メタンスルホン酸、トリフルオロメタンスルホン酸、ベンゼンスルホン酸、p-トルエンスルホン酸、10-カンファースルホン酸、トリフルオロ酢酸等が挙げられる。
固体酸としては、例えば、スルホン酸基を有する強酸性陽イオン交換樹脂等が挙げられる。
これらの中でも、反応後に、使用した酸を水酸化ナトリウム水溶液等のアルカリ溶液で中和、抽出する工程を行わずに、ろ過により酸触媒を分離できる観点から、強酸性陽イオン交換樹脂が好ましい。さらに反応基質との接触面積を大きくできる観点から、表面積の大きいマクロポーラス構造を有する強酸性陽イオン交換樹脂が好ましい。
酸触媒の酸解離定数(pKa)は、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点から、好ましくは2以下である。 (acid catalyst)
The acid catalyst is not particularly limited as long as it is a Brønsted acid, and includes at least one selected from the group consisting of inorganic acids, organic acids, and solid acids.
Examples of the inorganic acid include hydrochloric acid, sulfuric acid, nitric acid, and phosphoric acid.
Examples of the organic acid include methanesulfonic acid, trifluoromethanesulfonic acid, benzenesulfonic acid, p-toluenesulfonic acid, 10-camphorsulfonic acid, and trifluoroacetic acid.
Examples of the solid acid include strong acidic cation exchange resins having sulfonic acid groups.
Among these, strongly acidic cation exchange resins are preferred from the viewpoint that the acid catalyst can be separated by filtration without performing a step of neutralizing and extracting the used acid with an alkaline solution such as an aqueous sodium hydroxide solution after the reaction. Furthermore, from the viewpoint of increasing the contact area with the reaction substrate, a strongly acidic cation exchange resin having a macroporous structure with a large surface area is preferred.
The acid dissociation constant (pKa) of the acid catalyst is preferably 2 or less from the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C).
酸触媒としてはブレンステッド酸であれば特に限定されず、無機酸、有機酸及び固体酸からなる群から選択される少なくとも一種が挙げられる。
無機酸としては、例えば、塩酸、硫酸、硝酸、リン酸等が挙げられる。
有機酸としては、例えば、メタンスルホン酸、トリフルオロメタンスルホン酸、ベンゼンスルホン酸、p-トルエンスルホン酸、10-カンファースルホン酸、トリフルオロ酢酸等が挙げられる。
固体酸としては、例えば、スルホン酸基を有する強酸性陽イオン交換樹脂等が挙げられる。
これらの中でも、反応後に、使用した酸を水酸化ナトリウム水溶液等のアルカリ溶液で中和、抽出する工程を行わずに、ろ過により酸触媒を分離できる観点から、強酸性陽イオン交換樹脂が好ましい。さらに反応基質との接触面積を大きくできる観点から、表面積の大きいマクロポーラス構造を有する強酸性陽イオン交換樹脂が好ましい。
酸触媒の酸解離定数(pKa)は、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点から、好ましくは2以下である。 (acid catalyst)
The acid catalyst is not particularly limited as long as it is a Brønsted acid, and includes at least one selected from the group consisting of inorganic acids, organic acids, and solid acids.
Examples of the inorganic acid include hydrochloric acid, sulfuric acid, nitric acid, and phosphoric acid.
Examples of the organic acid include methanesulfonic acid, trifluoromethanesulfonic acid, benzenesulfonic acid, p-toluenesulfonic acid, 10-camphorsulfonic acid, and trifluoroacetic acid.
Examples of the solid acid include strong acidic cation exchange resins having sulfonic acid groups.
Among these, strongly acidic cation exchange resins are preferred from the viewpoint that the acid catalyst can be separated by filtration without performing a step of neutralizing and extracting the used acid with an alkaline solution such as an aqueous sodium hydroxide solution after the reaction. Furthermore, from the viewpoint of increasing the contact area with the reaction substrate, a strongly acidic cation exchange resin having a macroporous structure with a large surface area is preferred.
The acid dissociation constant (pKa) of the acid catalyst is preferably 2 or less from the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C).
混合工程における酸触媒の混合量は、組成物(X)100質量部に対し、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点から、好ましくは0.01質量部以上、より好ましくは0.05質量部以上、更に好ましくは0.1質量部以上、更に好ましくは0.5質量部以上、更に好ましくは1.0質量部以上、更に好ましくは1.5質量部以上であり、そして、好ましくは50質量部以下、より好ましくは30質量部以下、更に好ましくは25質量部以下、更に好ましくは20質量部以下、更に好ましくは15質量部以下、更に好ましくは10質量部以下である。
The mixing amount of the acid catalyst in the mixing step is preferably from the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) based on 100 parts by mass of the composition (X). is 0.01 parts by mass or more, more preferably 0.05 parts by mass or more, even more preferably 0.1 parts by mass or more, even more preferably 0.5 parts by mass or more, still more preferably 1.0 parts by mass or more, and even more preferably is 1.5 parts by mass or more, and preferably 50 parts by mass or less, more preferably 30 parts by mass or less, still more preferably 25 parts by mass or less, still more preferably 20 parts by mass or less, and even more preferably 15 parts by mass or less. , more preferably 10 parts by mass or less.
(水酸基含有化合物(C))
水酸基含有化合物(C)は、水及びアルキルアルコールからなる群から選択される少なくとも一種である。フッ素含有環状オレフィン化合物(A)の沸点とフッ素非含有エーテル化合物(B3)の沸点の差を大きくして分離工程で分離しやすくするため、アルキルアルコールが好ましい。
アルキルアルコールの炭素数は、アルキルアルコールの沸点を上げることにより反応温度を上げてフッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点、及び、フッ素含有環状オレフィン化合物(A)との沸点の差を大きくして分離工程で分離しやすくする観点から、好ましくは3以上であり、そして、好ましくは10以下、より好ましくは8以下、更に好ましくは6以下である。これらの観点から、アルキルアルコールの炭素数は、好ましくは3以上10以下、より好ましくは3以上8以下、更に好ましくは3以上6以下である。
アルキルアルコールとしては、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点から、好ましくは1-プロパノール、2-プロパノール、1-ブタノール、2-ブタノール、2-メチル-1-プロパノール、2-メチル-2-プロパノール、1-ペンタノール、2-ペンタノール、1-ヘキサノール、2-ヘキサノール、1-ヘプタノール、2-ヘプタノール、1-オクタノール、1-ノナノール及び1-デカノールからなる群から選択される少なくとも一種であり、より好ましくは1-プロパノール、1-ブタノール、1-ペンタノール及び1-ヘキサノールからなる群から選択される少なくとも一種である。 (Hydroxy group-containing compound (C))
The hydroxyl group-containing compound (C) is at least one selected from the group consisting of water and alkyl alcohol. Alkyl alcohol is preferred because it increases the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free ether compound (B3) to facilitate separation in the separation step.
The number of carbon atoms in the alkyl alcohol is determined from the viewpoints of increasing the reaction temperature by increasing the boiling point of the alkyl alcohol to further improve the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C), and From the viewpoint of increasing the difference in boiling point from the containing cyclic olefin compound (A) to facilitate separation in the separation step, it is preferably 3 or more, and preferably 10 or less, more preferably 8 or less, and even more preferably 6 It is as follows. From these viewpoints, the number of carbon atoms in the alkyl alcohol is preferably 3 or more and 10 or less, more preferably 3 or more and 8 or less, and still more preferably 3 or more and 6 or less.
From the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C), the alkyl alcohol is preferably 1-propanol, 2-propanol, 1-butanol, or 2-butanol. , 2-methyl-1-propanol, 2-methyl-2-propanol, 1-pentanol, 2-pentanol, 1-hexanol, 2-hexanol, 1-heptanol, 2-heptanol, 1-octanol, 1-nonanol and 1-decanol, more preferably at least one selected from the group consisting of 1-propanol, 1-butanol, 1-pentanol, and 1-hexanol.
水酸基含有化合物(C)は、水及びアルキルアルコールからなる群から選択される少なくとも一種である。フッ素含有環状オレフィン化合物(A)の沸点とフッ素非含有エーテル化合物(B3)の沸点の差を大きくして分離工程で分離しやすくするため、アルキルアルコールが好ましい。
アルキルアルコールの炭素数は、アルキルアルコールの沸点を上げることにより反応温度を上げてフッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点、及び、フッ素含有環状オレフィン化合物(A)との沸点の差を大きくして分離工程で分離しやすくする観点から、好ましくは3以上であり、そして、好ましくは10以下、より好ましくは8以下、更に好ましくは6以下である。これらの観点から、アルキルアルコールの炭素数は、好ましくは3以上10以下、より好ましくは3以上8以下、更に好ましくは3以上6以下である。
アルキルアルコールとしては、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点から、好ましくは1-プロパノール、2-プロパノール、1-ブタノール、2-ブタノール、2-メチル-1-プロパノール、2-メチル-2-プロパノール、1-ペンタノール、2-ペンタノール、1-ヘキサノール、2-ヘキサノール、1-ヘプタノール、2-ヘプタノール、1-オクタノール、1-ノナノール及び1-デカノールからなる群から選択される少なくとも一種であり、より好ましくは1-プロパノール、1-ブタノール、1-ペンタノール及び1-ヘキサノールからなる群から選択される少なくとも一種である。 (Hydroxy group-containing compound (C))
The hydroxyl group-containing compound (C) is at least one selected from the group consisting of water and alkyl alcohol. Alkyl alcohol is preferred because it increases the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free ether compound (B3) to facilitate separation in the separation step.
The number of carbon atoms in the alkyl alcohol is determined from the viewpoints of increasing the reaction temperature by increasing the boiling point of the alkyl alcohol to further improve the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C), and From the viewpoint of increasing the difference in boiling point from the containing cyclic olefin compound (A) to facilitate separation in the separation step, it is preferably 3 or more, and preferably 10 or less, more preferably 8 or less, and even more preferably 6 It is as follows. From these viewpoints, the number of carbon atoms in the alkyl alcohol is preferably 3 or more and 10 or less, more preferably 3 or more and 8 or less, and still more preferably 3 or more and 6 or less.
From the viewpoint of further improving the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C), the alkyl alcohol is preferably 1-propanol, 2-propanol, 1-butanol, or 2-butanol. , 2-methyl-1-propanol, 2-methyl-2-propanol, 1-pentanol, 2-pentanol, 1-hexanol, 2-hexanol, 1-heptanol, 2-heptanol, 1-octanol, 1-nonanol and 1-decanol, more preferably at least one selected from the group consisting of 1-propanol, 1-butanol, 1-pentanol, and 1-hexanol.
混合工程における水酸基含有化合物(C)の混合量は、組成物(X)100質量部に対し、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応性をより向上させる観点から、好ましくは1質量部以上、より好ましくは5質量部以上、更に好ましくは10質量部以上、更に好ましくは20質量部以上、更に好ましくは30質量部以上であり、そして、好ましくは1000質量部以下、より好ましくは500質量部以下、更に好ましくは250質量部以下、更に好ましくは150質量部以下、更に好ましくは100質量部以下、更に好ましくは60質量部以下である。
The amount of the hydroxyl group-containing compound (C) mixed in the mixing step is such that the reactivity between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) is further improved based on 100 parts by mass of the composition (X). From this point of view, it is preferably 1 part by mass or more, more preferably 5 parts by mass or more, even more preferably 10 parts by mass or more, still more preferably 20 parts by mass or more, even more preferably 30 parts by mass or more, and preferably 1000 parts by mass. parts by weight or less, more preferably 500 parts by weight or less, still more preferably 250 parts by weight or less, still more preferably 150 parts by weight or less, still more preferably 100 parts by weight or less, still more preferably 60 parts by weight or less.
混合工程において、各成分を混合する方法としては、いかなる方法で実施してもよい。各成分の混合については、その順序に制限はなく、一括又は分割等のいかなる方式でも実施することができる。各成分を混合する装置としても、制限はなく、撹拌、混合が可能な、バッチ式、もしくは連続式の、いかなる装置で実施してもよい。各成分を混合する際の温度は、室温から溶媒の沸点までの範囲で任意に選択することができる。
また、混合工程は、後述の反応工程と同時におこなってもよいし、反応工程の前におこなってもよい。 In the mixing step, any method may be used to mix each component. There is no restriction on the order of mixing the components, and the mixing may be carried out in any manner such as all at once or divided. There is no restriction on the device for mixing each component, and any device capable of stirring and mixing, batch type or continuous type, may be used. The temperature at which each component is mixed can be arbitrarily selected within the range from room temperature to the boiling point of the solvent.
Further, the mixing step may be performed simultaneously with the reaction step described below, or may be performed before the reaction step.
また、混合工程は、後述の反応工程と同時におこなってもよいし、反応工程の前におこなってもよい。 In the mixing step, any method may be used to mix each component. There is no restriction on the order of mixing the components, and the mixing may be carried out in any manner such as all at once or divided. There is no restriction on the device for mixing each component, and any device capable of stirring and mixing, batch type or continuous type, may be used. The temperature at which each component is mixed can be arbitrarily selected within the range from room temperature to the boiling point of the solvent.
Further, the mixing step may be performed simultaneously with the reaction step described below, or may be performed before the reaction step.
[反応工程]
本発明に係るフッ素含有環状オレフィン組成物の製造方法は、フッ素非含有環状ジオレフィン化合物(B1)と、水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程を含む。
ここで、フッ素含有環状オレフィン化合物(A)とフッ素非含有環状ジオレフィン化合物(B1)は、通常は、二重結合部分の電子密度が異なり、フッ素非含有環状ジオレフィン化合物(B1)の方が高い。そのため、酸触媒の存在下で、フッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)と、水酸基含有化合物(C)とを反応させると、フッ素非含有環状ジオレフィン化合物(B1)の方が選択的に水酸基含有化合物(C)の付加反応が進行して水和あるいはエーテル化することができる。 [Reaction process]
The method for producing a fluorine-containing cyclic olefin composition according to the present invention includes reacting a fluorine-free cyclic diolefin compound (B1) with a hydroxyl group-containing compound (C) to produce a fluorine-free hydrated compound (B2) and It includes a reaction step for obtaining at least one selected from the group consisting of fluorine-free ether compounds (B3).
Here, the fluorine-containing cyclic olefin compound (A) and the fluorine-free cyclic diolefin compound (B1) usually have different electron densities at the double bond part, and the fluorine-free cyclic diolefin compound (B1) is better than the fluorine-containing cyclic diolefin compound (B1). expensive. Therefore, when the composition (X) containing the fluorine-containing cyclic olefin compound (A) and the fluorine-free cyclic diolefin compound (B1) is reacted with the hydroxyl group-containing compound (C) in the presence of an acid catalyst, fluorine The addition reaction of the hydroxyl group-containing compound (C) proceeds more selectively in the non-containing cyclic diolefin compound (B1), so that it can be hydrated or etherified.
本発明に係るフッ素含有環状オレフィン組成物の製造方法は、フッ素非含有環状ジオレフィン化合物(B1)と、水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程を含む。
ここで、フッ素含有環状オレフィン化合物(A)とフッ素非含有環状ジオレフィン化合物(B1)は、通常は、二重結合部分の電子密度が異なり、フッ素非含有環状ジオレフィン化合物(B1)の方が高い。そのため、酸触媒の存在下で、フッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)と、水酸基含有化合物(C)とを反応させると、フッ素非含有環状ジオレフィン化合物(B1)の方が選択的に水酸基含有化合物(C)の付加反応が進行して水和あるいはエーテル化することができる。 [Reaction process]
The method for producing a fluorine-containing cyclic olefin composition according to the present invention includes reacting a fluorine-free cyclic diolefin compound (B1) with a hydroxyl group-containing compound (C) to produce a fluorine-free hydrated compound (B2) and It includes a reaction step for obtaining at least one selected from the group consisting of fluorine-free ether compounds (B3).
Here, the fluorine-containing cyclic olefin compound (A) and the fluorine-free cyclic diolefin compound (B1) usually have different electron densities at the double bond part, and the fluorine-free cyclic diolefin compound (B1) is better than the fluorine-containing cyclic diolefin compound (B1). expensive. Therefore, when the composition (X) containing the fluorine-containing cyclic olefin compound (A) and the fluorine-free cyclic diolefin compound (B1) is reacted with the hydroxyl group-containing compound (C) in the presence of an acid catalyst, fluorine The addition reaction of the hydroxyl group-containing compound (C) proceeds more selectively in the non-containing cyclic diolefin compound (B1), so that it can be hydrated or etherified.
ここで、前記組成物(X)において、フッ素含有環状オレフィン化合物(A)のHOMOエネルギー(E1)と、フッ素非含有環状ジオレフィン化合物(B1)のHOMOエネルギー(E2)との差の絶対値|E2-E1|は、反応工程において水酸基含有化合物(C)とフッ素非含有環状ジオレフィン化合物(B1)との選択的反応性をより向上させる観点から、好ましくは0.3eV以上、より好ましくは0.5eV以上である。
ここで、HOMOとは最高被占分子軌道(Highest Occupied Molecular Orbital)であり、各化合物のHOMOエネルギーは、長距離補正密度汎関数法で計算することができ、具体的には、量子化学計算ソフトウエアGaussian16 Rev.B.01を用い、汎関数としてωB97X-Dを選定し基底関数とてして6-31G(d)を採用した上で構造最適化を行って計算することができる。 Here, in the composition (X), the absolute difference between the HOMO energy (E 1 ) of the fluorine-containing cyclic olefin compound (A) and the HOMO energy (E 2 ) of the fluorine-free cyclic diolefin compound (B1) The value |E 2 −E 1 | is preferably 0.3 eV or more, from the viewpoint of further improving the selective reactivity between the hydroxyl group-containing compound (C) and the fluorine-free cyclic diolefin compound (B1) in the reaction step, More preferably, it is 0.5 eV or more.
Here, HOMO is the highest occupied molecular orbital, and the HOMO energy of each compound can be calculated using long-range corrected density functional theory. Using Gaussian16 Rev.B.01, ωB97X-D is selected as the functional, 6-31G(d) is used as the basis function, and the structure is optimized for calculation.
ここで、HOMOとは最高被占分子軌道(Highest Occupied Molecular Orbital)であり、各化合物のHOMOエネルギーは、長距離補正密度汎関数法で計算することができ、具体的には、量子化学計算ソフトウエアGaussian16 Rev.B.01を用い、汎関数としてωB97X-Dを選定し基底関数とてして6-31G(d)を採用した上で構造最適化を行って計算することができる。 Here, in the composition (X), the absolute difference between the HOMO energy (E 1 ) of the fluorine-containing cyclic olefin compound (A) and the HOMO energy (E 2 ) of the fluorine-free cyclic diolefin compound (B1) The value |E 2 −E 1 | is preferably 0.3 eV or more, from the viewpoint of further improving the selective reactivity between the hydroxyl group-containing compound (C) and the fluorine-free cyclic diolefin compound (B1) in the reaction step, More preferably, it is 0.5 eV or more.
Here, HOMO is the highest occupied molecular orbital, and the HOMO energy of each compound can be calculated using long-range corrected density functional theory. Using Gaussian16 Rev.B.01, ωB97X-D is selected as the functional, 6-31G(d) is used as the basis function, and the structure is optimized for calculation.
フッ素非含有環状ジオレフィン化合物(B1)と、水酸基含有化合物(C)との反応は、例えば、前記混合工程で得られた、組成物(X)と酸触媒と水酸基含有化合物(C)との混合物を加熱することにより行うことができる。
反応工程における加熱温度は各成分の種類や処理量によって適宜設定されるため特に限定されないが、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応をより促進させる観点から、好ましくは60℃以上、より好ましくは80℃以上、更に好ましくは90℃以上であり、酸触媒の揮発や各成分の分解等をより抑制する観点から、好ましくは150℃以下、より好ましくは130℃以下、更に好ましくは120℃以下である。これらの観点から、反応工程における加熱温度は、好ましくは60℃以上150℃以下、より好ましくは80℃以上130℃以下、更に好ましくは90℃以上120℃以下である。 The reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) can be carried out, for example, by the reaction between the composition (X), the acid catalyst, and the hydroxyl group-containing compound (C) obtained in the mixing step. This can be done by heating the mixture.
The heating temperature in the reaction step is not particularly limited as it is set appropriately depending on the type and amount of each component to be treated, but from the viewpoint of further promoting the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C). , preferably 60°C or higher, more preferably 80°C or higher, even more preferably 90°C or higher, and from the viewpoint of further suppressing volatilization of the acid catalyst and decomposition of each component, preferably 150°C or lower, more preferably 130°C or higher. The temperature is preferably 120°C or lower, more preferably 120°C or lower. From these viewpoints, the heating temperature in the reaction step is preferably 60°C or more and 150°C or less, more preferably 80°C or more and 130°C or less, and even more preferably 90°C or more and 120°C or less.
反応工程における加熱温度は各成分の種類や処理量によって適宜設定されるため特に限定されないが、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応をより促進させる観点から、好ましくは60℃以上、より好ましくは80℃以上、更に好ましくは90℃以上であり、酸触媒の揮発や各成分の分解等をより抑制する観点から、好ましくは150℃以下、より好ましくは130℃以下、更に好ましくは120℃以下である。これらの観点から、反応工程における加熱温度は、好ましくは60℃以上150℃以下、より好ましくは80℃以上130℃以下、更に好ましくは90℃以上120℃以下である。 The reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) can be carried out, for example, by the reaction between the composition (X), the acid catalyst, and the hydroxyl group-containing compound (C) obtained in the mixing step. This can be done by heating the mixture.
The heating temperature in the reaction step is not particularly limited as it is set appropriately depending on the type and amount of each component to be treated, but from the viewpoint of further promoting the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C). , preferably 60°C or higher, more preferably 80°C or higher, even more preferably 90°C or higher, and from the viewpoint of further suppressing volatilization of the acid catalyst and decomposition of each component, preferably 150°C or lower, more preferably 130°C or higher. The temperature is preferably 120°C or lower, more preferably 120°C or lower. From these viewpoints, the heating temperature in the reaction step is preferably 60°C or more and 150°C or less, more preferably 80°C or more and 130°C or less, and even more preferably 90°C or more and 120°C or less.
また、反応工程における加熱時間(反応時間)は各成分の種類や処理量によって適宜設定されるため特に限定されないが、フッ素非含有環状ジオレフィン化合物(B1)と水酸基含有化合物(C)との反応をより促進させる観点から、好ましくは1時間以上、より好ましくは2時間以上、更に好ましくは4時間以上、更に好ましくは8時間以上であり、生産性を向上させる観点から、好ましくは48時間以下、より好ましくは24時間以下、更に好ましくは20時間以下である。これらの観点から、反応工程における加熱時間(反応時間)は、好ましくは1時間以上48時間以下、より好ましくは2時間以上24時間以下、更に好ましくは4時間以上20時間以下、更に好ましくは8時間以上20時間以下である。
また、反応工程は、例えば、窒素ガス等の不活性ガス雰囲気、常圧(大気圧)下でおこなうことができる。 In addition, the heating time (reaction time) in the reaction step is not particularly limited as it is appropriately set depending on the type and amount of each component to be treated, but the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) From the viewpoint of further promoting the process, the time period is preferably 1 hour or more, more preferably 2 hours or more, still more preferably 4 hours or more, even more preferably 8 hours or more, and from the viewpoint of improving productivity, preferably 48 hours or less, More preferably 24 hours or less, still more preferably 20 hours or less. From these viewpoints, the heating time (reaction time) in the reaction step is preferably 1 hour or more and 48 hours or less, more preferably 2 hours or more and 24 hours or less, even more preferably 4 hours or more and 20 hours or less, and even more preferably 8 hours. The duration is 20 hours or less.
Further, the reaction step can be carried out, for example, in an inert gas atmosphere such as nitrogen gas, and under normal pressure (atmospheric pressure).
また、反応工程は、例えば、窒素ガス等の不活性ガス雰囲気、常圧(大気圧)下でおこなうことができる。 In addition, the heating time (reaction time) in the reaction step is not particularly limited as it is appropriately set depending on the type and amount of each component to be treated, but the reaction between the fluorine-free cyclic diolefin compound (B1) and the hydroxyl group-containing compound (C) From the viewpoint of further promoting the process, the time period is preferably 1 hour or more, more preferably 2 hours or more, still more preferably 4 hours or more, even more preferably 8 hours or more, and from the viewpoint of improving productivity, preferably 48 hours or less, More preferably 24 hours or less, still more preferably 20 hours or less. From these viewpoints, the heating time (reaction time) in the reaction step is preferably 1 hour or more and 48 hours or less, more preferably 2 hours or more and 24 hours or less, even more preferably 4 hours or more and 20 hours or less, and even more preferably 8 hours. The duration is 20 hours or less.
Further, the reaction step can be carried out, for example, in an inert gas atmosphere such as nitrogen gas, and under normal pressure (atmospheric pressure).
[分離工程]
本発明に係るフッ素含有環状オレフィン組成物の製造方法は、得られるフッ素含有環状オレフィン組成物の純度すなわちフッ素含有環状オレフィン組成物中の目的物であるフッ素含有環状オレフィン化合物(A)の含有量をより向上させる観点から、前記反応工程の後に、蒸留により、フッ素含有環状オレフィン化合物(A)とフッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程を更に含むことが好ましい。
蒸留の方法としてはフッ素含有環状オレフィン化合物(A)とフッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)とを分離できる蒸留方法であれば特に限定されないが、例えば、大気圧下で実施する常圧蒸留、系内を減圧にして行う減圧蒸留等が挙げられる。 [Separation process]
The method for producing a fluorine-containing cyclic olefin composition according to the present invention is aimed at controlling the purity of the obtained fluorine-containing cyclic olefin composition, that is, the content of the fluorine-containing cyclic olefin compound (A), which is the target substance in the fluorine-containing cyclic olefin composition. From the viewpoint of further improvement, after the reaction step, at least one selected from the group consisting of the fluorine-containing cyclic olefin compound (A), the fluorine-free hydrated compound (B2), and the fluorine-free ether compound (B3) is removed by distillation. It is preferable to further include a separation step of separating one type.
The distillation method is not particularly limited as long as it is a distillation method that can separate the fluorine-containing cyclic olefin compound (A) and the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3), but for example, atmospheric pressure. For example, distillation under normal pressure may be carried out under reduced pressure, vacuum distillation may be carried out under reduced pressure in the system, and the like.
本発明に係るフッ素含有環状オレフィン組成物の製造方法は、得られるフッ素含有環状オレフィン組成物の純度すなわちフッ素含有環状オレフィン組成物中の目的物であるフッ素含有環状オレフィン化合物(A)の含有量をより向上させる観点から、前記反応工程の後に、蒸留により、フッ素含有環状オレフィン化合物(A)とフッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程を更に含むことが好ましい。
蒸留の方法としてはフッ素含有環状オレフィン化合物(A)とフッ素非含有水和化合物(B2)あるいはフッ素非含有エーテル化合物(B3)とを分離できる蒸留方法であれば特に限定されないが、例えば、大気圧下で実施する常圧蒸留、系内を減圧にして行う減圧蒸留等が挙げられる。 [Separation process]
The method for producing a fluorine-containing cyclic olefin composition according to the present invention is aimed at controlling the purity of the obtained fluorine-containing cyclic olefin composition, that is, the content of the fluorine-containing cyclic olefin compound (A), which is the target substance in the fluorine-containing cyclic olefin composition. From the viewpoint of further improvement, after the reaction step, at least one selected from the group consisting of the fluorine-containing cyclic olefin compound (A), the fluorine-free hydrated compound (B2), and the fluorine-free ether compound (B3) is removed by distillation. It is preferable to further include a separation step of separating one type.
The distillation method is not particularly limited as long as it is a distillation method that can separate the fluorine-containing cyclic olefin compound (A) and the fluorine-free hydrated compound (B2) or the fluorine-free ether compound (B3), but for example, atmospheric pressure. For example, distillation under normal pressure may be carried out under reduced pressure, vacuum distillation may be carried out under reduced pressure in the system, and the like.
また、フッ素含有環状オレフィン化合物(A)が、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む場合、本発明に係るフッ素含有環状オレフィン組成物の製造方法は、得られるフッ素含有環状オレフィン組成物の純度すなわちフッ素含有環状オレフィン組成物中の目的物であるフッ素含有環状オレフィン化合物(A)の含有量をより向上させる観点から、前記反応工程の後に、蒸留により、フッ素含有環状オレフィン化合物(A1)とフッ素含有環状オレフィン化合物(A2)とを分離する分離工程を更に含むことが好ましい。
蒸留の方法としてはフッ素含有環状オレフィン化合物(A1)とフッ素含有環状オレフィン化合物(A2)とを分離できる蒸留方法であれば特に限定されないが、例えば、大気圧下で実施する常圧蒸留、系内を減圧にして行う減圧蒸留等が挙げられる。 Further, the fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1). ), the method for producing a fluorine-containing cyclic olefin composition according to the present invention improves the purity of the obtained fluorine-containing cyclic olefin composition, that is, the fluorine-containing cyclic olefin compound that is the target substance in the fluorine-containing cyclic olefin composition. From the viewpoint of further increasing the content of (A), it is possible to further include a separation step of separating the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2) by distillation after the reaction step. preferable.
The distillation method is not particularly limited as long as it is a distillation method that can separate the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2), but examples include atmospheric distillation conducted under atmospheric pressure, Examples include vacuum distillation performed under reduced pressure.
蒸留の方法としてはフッ素含有環状オレフィン化合物(A1)とフッ素含有環状オレフィン化合物(A2)とを分離できる蒸留方法であれば特に限定されないが、例えば、大気圧下で実施する常圧蒸留、系内を減圧にして行う減圧蒸留等が挙げられる。 Further, the fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1). ), the method for producing a fluorine-containing cyclic olefin composition according to the present invention improves the purity of the obtained fluorine-containing cyclic olefin composition, that is, the fluorine-containing cyclic olefin compound that is the target substance in the fluorine-containing cyclic olefin composition. From the viewpoint of further increasing the content of (A), it is possible to further include a separation step of separating the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2) by distillation after the reaction step. preferable.
The distillation method is not particularly limited as long as it is a distillation method that can separate the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2), but examples include atmospheric distillation conducted under atmospheric pressure, Examples include vacuum distillation performed under reduced pressure.
本発明に係るフッ素含有環状オレフィン組成物の製造方法において、得られたフッ素含有環状オレフィン組成物中のフッ素非含有環状ジオレフィン化合物(B1)の含有量は、フッ素含有環状オレフィン組成物の全体を100質量%としたとき、好ましくは5.0質量%以下、より好ましくは3.0質量%以下、更に好ましくは2.0質量%以下、更に好ましくは1.0質量%以下、更に好ましくは0.8質量%以下、更に好ましくは0.3質量%以下である。
また、得られたフッ素含有環状オレフィン組成物中のフッ素非含有環状ジオレフィン化合物(B1)の含有量は少ないほど好ましいため前記含有量の下限値は特に限定されないが、例えば0質量%超であってもよく、0.01質量%以上であってもよく、0.05質量%以上であってもよく、0.1質量%以上であってもよい。 In the method for producing a fluorine-containing cyclic olefin composition according to the present invention, the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is determined based on the entire fluorine-containing cyclic olefin composition. When taken as 100% by mass, preferably 5.0% by mass or less, more preferably 3.0% by mass or less, even more preferably 2.0% by mass or less, even more preferably 1.0% by mass or less, even more preferably 0 .8% by mass or less, more preferably 0.3% by mass or less.
Further, since the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is preferably as small as possible, the lower limit of the content is not particularly limited, but for example, it is more than 0% by mass. The content may be 0.01% by mass or more, 0.05% by mass or more, or 0.1% by mass or more.
また、得られたフッ素含有環状オレフィン組成物中のフッ素非含有環状ジオレフィン化合物(B1)の含有量は少ないほど好ましいため前記含有量の下限値は特に限定されないが、例えば0質量%超であってもよく、0.01質量%以上であってもよく、0.05質量%以上であってもよく、0.1質量%以上であってもよい。 In the method for producing a fluorine-containing cyclic olefin composition according to the present invention, the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is determined based on the entire fluorine-containing cyclic olefin composition. When taken as 100% by mass, preferably 5.0% by mass or less, more preferably 3.0% by mass or less, even more preferably 2.0% by mass or less, even more preferably 1.0% by mass or less, even more preferably 0 .8% by mass or less, more preferably 0.3% by mass or less.
Further, since the content of the fluorine-free cyclic diolefin compound (B1) in the obtained fluorine-containing cyclic olefin composition is preferably as small as possible, the lower limit of the content is not particularly limited, but for example, it is more than 0% by mass. The content may be 0.01% by mass or more, 0.05% by mass or more, or 0.1% by mass or more.
また、本発明に係るフッ素含有環状オレフィン組成物の製造方法において、得られたフッ素含有環状オレフィン組成物中の目的物であるフッ素含有環状オレフィン化合物(A)の含有量は、フッ素含有環状オレフィン組成物の全体を100質量%としたとき、好ましくは75.0質量%以上、より好ましくは80.0質量%以上、更に好ましくは85.0質量%以上、更に好ましくは90.0質量%以上である。
本発明に係るフッ素含有環状オレフィン組成物の製造方法において、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程後での得られたフッ素含有環状オレフィン組成物中の目的物であるフッ素含有環状オレフィン化合物(A)の含有量は、好ましくは99.0量%以上、より好ましくは99.2質量%以上、更に好ましくは99.5質量%以上、更に好ましくは99.7質量%以上である。
また、本発明に係るフッ素含有環状オレフィン組成物の製造方法において、得られたフッ素含有環状オレフィン組成物中の目的物である前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)の含有量は、フッ素含有環状オレフィン組成物の全体を100質量%としたとき、好ましくは99.0質量%以上、より好ましくは99.2質量%以上、更に好ましくは99.5質量%以上、更に好ましくは99.7質量%以上である。
また、本発明に係るフッ素含有環状オレフィン組成物の製造方法において、得られたフッ素含有環状オレフィン組成物中の目的物である前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の含有量は、フッ素含有環状オレフィン組成物の全体を100質量%としたとき、好ましくは99.0質量%以上、より好ましくは99.2質量%以上、更に好ましくは99.5質量%以上、更に好ましくは99.7質量%以上である。
ここで、フッ素含有環状オレフィン組成物中の各成分の含有量は、例えば、ガスクロマトグラフィーによって測定することができる。測定方法は、株式会社島津製作所製「GC-2010Plus」を使用し、キャピラリーカラムとして「DB-5」(長さ30m×直径0.25mm×膜厚0.5μm、Agilent Technologies社製)を使用することができる。測定条件は、40℃で2分間保持後、10℃/分で250℃まで昇温する条件で各成分の濃度を測定できる。各成分の濃度は、得られたクロマトグラムにおいて、全ピーク面積に対する各成分のピーク面積割合(質量%)をその成分の濃度とできる。 In addition, in the method for producing a fluorine-containing cyclic olefin composition according to the present invention, the content of the fluorine-containing cyclic olefin compound (A), which is the target substance in the obtained fluorine-containing cyclic olefin composition, is Preferably 75.0% by mass or more, more preferably 80.0% by mass or more, even more preferably 85.0% by mass or more, still more preferably 90.0% by mass or more, when the whole product is 100% by mass. be.
In the method for producing a fluorine-containing cyclic olefin composition according to the present invention, after the separation step of separating at least one selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3), The content of the target fluorine-containing cyclic olefin compound (A) in the obtained fluorine-containing cyclic olefin composition is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably It is 99.5% by mass or more, more preferably 99.7% by mass or more.
In addition, in the method for producing a fluorine-containing cyclic olefin composition according to the present invention, a fluorine-containing cyclic olefin compound (A1 ) is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably 99.5% by mass or more, when the entire fluorine-containing cyclic olefin composition is 100% by mass. , more preferably 99.7% by mass or more.
In addition, in the method for producing a fluorine-containing cyclic olefin composition according to the present invention, a fluorine-containing cyclic olefin compound (A2 ) is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably 99.5% by mass or more, when the entire fluorine-containing cyclic olefin composition is 100% by mass. , more preferably 99.7% by mass or more.
Here, the content of each component in the fluorine-containing cyclic olefin composition can be measured, for example, by gas chromatography. The measurement method is to use "GC-2010Plus" manufactured by Shimadzu Corporation, and "DB-5" (length 30 m x diameter 0.25 mm x film thickness 0.5 μm, manufactured by Agilent Technologies) as a capillary column. I can do it. The concentration of each component can be measured under conditions of holding the temperature at 40°C for 2 minutes and then increasing the temperature to 250°C at a rate of 10°C/min. The concentration of each component can be determined by the peak area ratio (mass %) of each component to the total peak area in the obtained chromatogram.
本発明に係るフッ素含有環状オレフィン組成物の製造方法において、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程後での得られたフッ素含有環状オレフィン組成物中の目的物であるフッ素含有環状オレフィン化合物(A)の含有量は、好ましくは99.0量%以上、より好ましくは99.2質量%以上、更に好ましくは99.5質量%以上、更に好ましくは99.7質量%以上である。
また、本発明に係るフッ素含有環状オレフィン組成物の製造方法において、得られたフッ素含有環状オレフィン組成物中の目的物である前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)の含有量は、フッ素含有環状オレフィン組成物の全体を100質量%としたとき、好ましくは99.0質量%以上、より好ましくは99.2質量%以上、更に好ましくは99.5質量%以上、更に好ましくは99.7質量%以上である。
また、本発明に係るフッ素含有環状オレフィン組成物の製造方法において、得られたフッ素含有環状オレフィン組成物中の目的物である前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の含有量は、フッ素含有環状オレフィン組成物の全体を100質量%としたとき、好ましくは99.0質量%以上、より好ましくは99.2質量%以上、更に好ましくは99.5質量%以上、更に好ましくは99.7質量%以上である。
ここで、フッ素含有環状オレフィン組成物中の各成分の含有量は、例えば、ガスクロマトグラフィーによって測定することができる。測定方法は、株式会社島津製作所製「GC-2010Plus」を使用し、キャピラリーカラムとして「DB-5」(長さ30m×直径0.25mm×膜厚0.5μm、Agilent Technologies社製)を使用することができる。測定条件は、40℃で2分間保持後、10℃/分で250℃まで昇温する条件で各成分の濃度を測定できる。各成分の濃度は、得られたクロマトグラムにおいて、全ピーク面積に対する各成分のピーク面積割合(質量%)をその成分の濃度とできる。 In addition, in the method for producing a fluorine-containing cyclic olefin composition according to the present invention, the content of the fluorine-containing cyclic olefin compound (A), which is the target substance in the obtained fluorine-containing cyclic olefin composition, is Preferably 75.0% by mass or more, more preferably 80.0% by mass or more, even more preferably 85.0% by mass or more, still more preferably 90.0% by mass or more, when the whole product is 100% by mass. be.
In the method for producing a fluorine-containing cyclic olefin composition according to the present invention, after the separation step of separating at least one selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3), The content of the target fluorine-containing cyclic olefin compound (A) in the obtained fluorine-containing cyclic olefin composition is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably It is 99.5% by mass or more, more preferably 99.7% by mass or more.
In addition, in the method for producing a fluorine-containing cyclic olefin composition according to the present invention, a fluorine-containing cyclic olefin compound (A1 ) is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably 99.5% by mass or more, when the entire fluorine-containing cyclic olefin composition is 100% by mass. , more preferably 99.7% by mass or more.
In addition, in the method for producing a fluorine-containing cyclic olefin composition according to the present invention, a fluorine-containing cyclic olefin compound (A2 ) is preferably 99.0% by mass or more, more preferably 99.2% by mass or more, even more preferably 99.5% by mass or more, when the entire fluorine-containing cyclic olefin composition is 100% by mass. , more preferably 99.7% by mass or more.
Here, the content of each component in the fluorine-containing cyclic olefin composition can be measured, for example, by gas chromatography. The measurement method is to use "GC-2010Plus" manufactured by Shimadzu Corporation, and "DB-5" (length 30 m x diameter 0.25 mm x film thickness 0.5 μm, manufactured by Agilent Technologies) as a capillary column. I can do it. The concentration of each component can be measured under conditions of holding the temperature at 40°C for 2 minutes and then increasing the temperature to 250°C at a rate of 10°C/min. The concentration of each component can be determined by the peak area ratio (mass %) of each component to the total peak area in the obtained chromatogram.
本発明に係るフッ素含有環状オレフィン組成物によれば、例えば、遷移金属触媒を用いてアルカリ金属類を助触媒として共存させポリマーを合成する配位重合;ラジカル開始剤を用いて光又は熱によりラジカルを発生させポリマーを合成するラジカル重合;タングステン塩化物又はモルリブデン塩化物を用いてアルカリ金属類を助触媒として共存させポリマーを合成するメタセシス重合;タングステン、モルリブデン、ルテニウムを中心金属とするアルキリデン触媒を用いてポリマーを合成するメタセシス重合等の方法で、フッ素含有環状オレフィンポリマーを合成することができる。それぞれの重合法において、本発明に係るフッ素含有環状オレフィン組成物を2種類以上共存させて用いてもよい。
さらに、種々の重合法において、非フッ素系の環状又は鎖状オレフィンを共存させて本発明に係るフッ素含有環状オレフィン組成物と共重合させてもよく、非フッ素系の環状又は鎖状オレフィンを連鎖移動剤として使用してもよい。
得られたポリマーは、環状オレフィンポリマーとしての特性に加え、フッ素原子、及び/又は、フッ素含有置換基の効果によりその成型物は、例えば、低屈折で高透明な樹脂特性を示し、例えば、レンズ、フィルム、光導波路、ファイバー等の形態で光学、電子材料分野を中心に広く展開することができる。 According to the fluorine-containing cyclic olefin composition of the present invention, for example, coordination polymerization in which a polymer is synthesized using a transition metal catalyst in the coexistence of an alkali metal as a promoter; Radical polymerization, which synthesizes polymers by generating A fluorine-containing cyclic olefin polymer can be synthesized by a method such as metathesis polymerization, in which a polymer is synthesized using a method such as metathesis polymerization. In each polymerization method, two or more types of fluorine-containing cyclic olefin compositions according to the present invention may be used together.
Furthermore, in various polymerization methods, non-fluorine-based cyclic or chain olefins may be present and copolymerized with the fluorine-containing cyclic olefin composition of the present invention. It may also be used as a transfer agent.
In addition to the properties of the obtained polymer as a cyclic olefin polymer, due to the effect of the fluorine atom and/or the fluorine-containing substituent, the molded product exhibits low refractive and highly transparent resin properties, such as lenses. It can be widely used in the fields of optical and electronic materials in the form of films, optical waveguides, fibers, etc.
さらに、種々の重合法において、非フッ素系の環状又は鎖状オレフィンを共存させて本発明に係るフッ素含有環状オレフィン組成物と共重合させてもよく、非フッ素系の環状又は鎖状オレフィンを連鎖移動剤として使用してもよい。
得られたポリマーは、環状オレフィンポリマーとしての特性に加え、フッ素原子、及び/又は、フッ素含有置換基の効果によりその成型物は、例えば、低屈折で高透明な樹脂特性を示し、例えば、レンズ、フィルム、光導波路、ファイバー等の形態で光学、電子材料分野を中心に広く展開することができる。 According to the fluorine-containing cyclic olefin composition of the present invention, for example, coordination polymerization in which a polymer is synthesized using a transition metal catalyst in the coexistence of an alkali metal as a promoter; Radical polymerization, which synthesizes polymers by generating A fluorine-containing cyclic olefin polymer can be synthesized by a method such as metathesis polymerization, in which a polymer is synthesized using a method such as metathesis polymerization. In each polymerization method, two or more types of fluorine-containing cyclic olefin compositions according to the present invention may be used together.
Furthermore, in various polymerization methods, non-fluorine-based cyclic or chain olefins may be present and copolymerized with the fluorine-containing cyclic olefin composition of the present invention. It may also be used as a transfer agent.
In addition to the properties of the obtained polymer as a cyclic olefin polymer, due to the effect of the fluorine atom and/or the fluorine-containing substituent, the molded product exhibits low refractive and highly transparent resin properties, such as lenses. It can be widely used in the fields of optical and electronic materials in the form of films, optical waveguides, fibers, etc.
以上、本発明の実施形態について述べたが、これらは本発明の例示であり、上記以外の様々な構成を採用することもできる。
また、本発明は前述の実施形態に限定されるものではなく、本発明の効果を損なわない範囲での変形、改良等は本発明に含まれるものである。 Although the embodiments of the present invention have been described above, these are merely examples of the present invention, and various configurations other than those described above may also be adopted.
Further, the present invention is not limited to the above-described embodiments, and modifications, improvements, etc. are included within the scope of the present invention without impairing the effects of the present invention.
また、本発明は前述の実施形態に限定されるものではなく、本発明の効果を損なわない範囲での変形、改良等は本発明に含まれるものである。 Although the embodiments of the present invention have been described above, these are merely examples of the present invention, and various configurations other than those described above may also be adopted.
Further, the present invention is not limited to the above-described embodiments, and modifications, improvements, etc. are included within the scope of the present invention without impairing the effects of the present invention.
以下、本実施形態を、実施例等を参照して詳細に説明する。なお、本実施形態は、これらの実施例の記載に何ら限定されるものではない。
Hereinafter, this embodiment will be described in detail with reference to examples and the like. Note that this embodiment is in no way limited to the description of these examples.
[蒸留精製前後におけるフッ素含有環状オレフィン組成物中の各組成物の含有量の測定]
蒸留精製前後におけるフッ素含有環状オレフィン組成物中の各組成物の含有量(質量%)はガスクロマトグラフィー測定により行った。
ガスクロマトグラフィー装置としては島津製作所社製の「GC-2010Plus」を使用し、キャピラリーカラムとしてはAgilent Technologies社製の「DB-5」(長さ30m×直径0.25mm×膜厚0.5μm)を使用した。測定は、40℃で2分間保持後、10℃/分で250℃まで昇温する条件で測定を行った。各成分の濃度は、得られたクロマトグラムにおいて、全ピーク面積に対する各成分のピーク面積割合(質量%)をその成分の濃度であるとした。 [Measurement of the content of each composition in the fluorine-containing cyclic olefin composition before and after distillation purification]
The content (% by mass) of each composition in the fluorine-containing cyclic olefin composition before and after distillation purification was measured by gas chromatography.
As the gas chromatography device, "GC-2010Plus" manufactured by Shimadzu Corporation was used, and as the capillary column, "DB-5" manufactured by Agilent Technologies (length 30 m x diameter 0.25 mm x film thickness 0.5 μm) was used. used. The measurement was carried out under conditions of holding the temperature at 40°C for 2 minutes and then increasing the temperature to 250°C at a rate of 10°C/min. The concentration of each component was determined by the peak area ratio (mass %) of each component to the total peak area in the obtained chromatogram.
蒸留精製前後におけるフッ素含有環状オレフィン組成物中の各組成物の含有量(質量%)はガスクロマトグラフィー測定により行った。
ガスクロマトグラフィー装置としては島津製作所社製の「GC-2010Plus」を使用し、キャピラリーカラムとしてはAgilent Technologies社製の「DB-5」(長さ30m×直径0.25mm×膜厚0.5μm)を使用した。測定は、40℃で2分間保持後、10℃/分で250℃まで昇温する条件で測定を行った。各成分の濃度は、得られたクロマトグラムにおいて、全ピーク面積に対する各成分のピーク面積割合(質量%)をその成分の濃度であるとした。 [Measurement of the content of each composition in the fluorine-containing cyclic olefin composition before and after distillation purification]
The content (% by mass) of each composition in the fluorine-containing cyclic olefin composition before and after distillation purification was measured by gas chromatography.
As the gas chromatography device, "GC-2010Plus" manufactured by Shimadzu Corporation was used, and as the capillary column, "DB-5" manufactured by Agilent Technologies (length 30 m x diameter 0.25 mm x film thickness 0.5 μm) was used. used. The measurement was carried out under conditions of holding the temperature at 40°C for 2 minutes and then increasing the temperature to 250°C at a rate of 10°C/min. The concentration of each component was determined by the peak area ratio (mass %) of each component to the total peak area in the obtained chromatogram.
[実施例1]
窒素雰囲気下、磁気攪拌装置を備えた25Lのオートクレーブ内に、ジシクロペンタジエン(東京化成工業社製、以下、「DCp」ともいう)5.8kg、ヘキサフルオロプロペン(高千穂化学工業社製)16.6kgを入れ、160℃で24時間加熱攪拌し、次いで、180℃で15時間加熱攪拌した。冷却後、未反応のヘキサフルオロプロペン3.9kgを回収し、反応液17.9kgを取り出した。
次いで、得られた反応液を蒸留することにより、5,5,6-トリフルオロ-6-トリフルオロメチル-ビシクロ[2.2.1]ヘプト-2-エン(以下、「NBF6」ともいう)とDCpを含む組成物を15.5kg取得し、蒸留装置内の残留液より8,8,9-トリフルオロ-9-トリフルオロメチル-テトラシクロ[4.4.0.12,5.17,10]-3-ドデセン(以下。「TDF6」ともいう)とNBF6とDCpとトリシクロペンタジエン(以下、「TCPD」ともいう)とを含む組成物(X1)を2.2kg取得した。ここで、TDF6の沸点は240℃、NBF6の沸点は165℃、DCpの沸点は170℃、TCPDの沸点は248℃である。
また、TDF6のHOMOエネルギーは-8.7eV、NBF6のHOMOエネルギーは-9.3eV、DCpのHOMOエネルギーは-8.4eV、TCPDのHOMOエネルギーは-8.2eVである。
ここで、HOMOとは最高被占分子軌道(Highest Occupied Molecular Orbital)であり、各化合物のHOMOエネルギーは、長距離補正密度汎関数法で計算することができ、具体的には、量子化学計算ソフトウエアGaussian16 Rev.B.01を用い、汎関数としてωB97X-Dを選定し基底関数とてして6-31G(d)を採用した上で構造最適化を行って計算した。 [Example 1]
Under a nitrogen atmosphere, 5.8 kg of dicyclopentadiene (manufactured by Tokyo Kasei Kogyo Co., Ltd., hereinafter also referred to as "DCp") and 16.8 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device. 6 kg was added thereto, heated and stirred at 160°C for 24 hours, and then heated and stirred at 180°C for 15 hours. After cooling, 3.9 kg of unreacted hexafluoropropene was collected, and 17.9 kg of the reaction solution was taken out.
Next, the obtained reaction solution is distilled to obtain 5,5,6-trifluoro-6-trifluoromethyl-bicyclo[2.2.1]hept-2-ene (hereinafter also referred to as "NBF 6 "). ) and DCp were obtained, and 8,8,9-trifluoro-9-trifluoromethyl-tetracyclo[4.4.0.1 2,5 . 1 7,10 ]-3-dodecene (hereinafter also referred to as "TDF 6 "), NBF 6 , DCp, and tricyclopentadiene (hereinafter also referred to as "TCPD") 2.2 kg of composition (X1) was obtained. did. Here, the boiling point of TDF 6 is 240°C, the boiling point of NBF 6 is 165°C, the boiling point of DCp is 170°C, and the boiling point of TCPD is 248°C.
Further, the HOMO energy of TDF 6 is -8.7 eV, the HOMO energy of NBF 6 is -9.3 eV, the HOMO energy of DCp is -8.4 eV, and the HOMO energy of TCPD is -8.2 eV.
Here, HOMO is the highest occupied molecular orbital, and the HOMO energy of each compound can be calculated using long-range corrected density functional theory. Using Gaussian16 Rev.B.01, ωB97X-D was selected as the functional, 6-31G(d) was used as the basis function, and structure optimization was performed.
窒素雰囲気下、磁気攪拌装置を備えた25Lのオートクレーブ内に、ジシクロペンタジエン(東京化成工業社製、以下、「DCp」ともいう)5.8kg、ヘキサフルオロプロペン(高千穂化学工業社製)16.6kgを入れ、160℃で24時間加熱攪拌し、次いで、180℃で15時間加熱攪拌した。冷却後、未反応のヘキサフルオロプロペン3.9kgを回収し、反応液17.9kgを取り出した。
次いで、得られた反応液を蒸留することにより、5,5,6-トリフルオロ-6-トリフルオロメチル-ビシクロ[2.2.1]ヘプト-2-エン(以下、「NBF6」ともいう)とDCpを含む組成物を15.5kg取得し、蒸留装置内の残留液より8,8,9-トリフルオロ-9-トリフルオロメチル-テトラシクロ[4.4.0.12,5.17,10]-3-ドデセン(以下。「TDF6」ともいう)とNBF6とDCpとトリシクロペンタジエン(以下、「TCPD」ともいう)とを含む組成物(X1)を2.2kg取得した。ここで、TDF6の沸点は240℃、NBF6の沸点は165℃、DCpの沸点は170℃、TCPDの沸点は248℃である。
また、TDF6のHOMOエネルギーは-8.7eV、NBF6のHOMOエネルギーは-9.3eV、DCpのHOMOエネルギーは-8.4eV、TCPDのHOMOエネルギーは-8.2eVである。
ここで、HOMOとは最高被占分子軌道(Highest Occupied Molecular Orbital)であり、各化合物のHOMOエネルギーは、長距離補正密度汎関数法で計算することができ、具体的には、量子化学計算ソフトウエアGaussian16 Rev.B.01を用い、汎関数としてωB97X-Dを選定し基底関数とてして6-31G(d)を採用した上で構造最適化を行って計算した。 [Example 1]
Under a nitrogen atmosphere, 5.8 kg of dicyclopentadiene (manufactured by Tokyo Kasei Kogyo Co., Ltd., hereinafter also referred to as "DCp") and 16.8 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device. 6 kg was added thereto, heated and stirred at 160°C for 24 hours, and then heated and stirred at 180°C for 15 hours. After cooling, 3.9 kg of unreacted hexafluoropropene was collected, and 17.9 kg of the reaction solution was taken out.
Next, the obtained reaction solution is distilled to obtain 5,5,6-trifluoro-6-trifluoromethyl-bicyclo[2.2.1]hept-2-ene (hereinafter also referred to as "NBF 6 "). ) and DCp were obtained, and 8,8,9-trifluoro-9-trifluoromethyl-tetracyclo[4.4.0.1 2,5 . 1 7,10 ]-3-dodecene (hereinafter also referred to as "TDF 6 "), NBF 6 , DCp, and tricyclopentadiene (hereinafter also referred to as "TCPD") 2.2 kg of composition (X1) was obtained. did. Here, the boiling point of TDF 6 is 240°C, the boiling point of NBF 6 is 165°C, the boiling point of DCp is 170°C, and the boiling point of TCPD is 248°C.
Further, the HOMO energy of TDF 6 is -8.7 eV, the HOMO energy of NBF 6 is -9.3 eV, the HOMO energy of DCp is -8.4 eV, and the HOMO energy of TCPD is -8.2 eV.
Here, HOMO is the highest occupied molecular orbital, and the HOMO energy of each compound can be calculated using long-range corrected density functional theory. Using Gaussian16 Rev.B.01, ωB97X-D was selected as the functional, 6-31G(d) was used as the basis function, and structure optimization was performed.
次いで、攪拌機、及びコンデンサーを付した1000mLのガラス製反応器に、組成物(X1)を250g、水酸基含有化合物(C)である水を100g、酸触媒である硫酸を5g入れ、窒素雰囲気下、100℃で18時間加熱攪拌し、組成物(X1)中のDCp及びTCPDの水和反応をおこなった(以下、「反応工程」とも呼ぶ。)。次いで、得られた反応液を室温まで冷却後、5%NaOH水溶液で中和、抽出することにより、蒸留精製前のフッ素含有環状オレフィン組成物を得た。この蒸留精製前のフッ素含有環状オレフィン組成物をガスクロマトグラフィーにて分析を行った。
また、蒸留精製前のフッ素含有環状オレフィン組成物を入れた丸底フラスコにスニーダー分留管、リービッヒ冷却管を取り付け、減圧蒸留により、NBF6含有組成物とTDF6含有組成物を分留取得し、ガスクロマトグラフィーにてそれぞれ分析を行った。
ここで、表1におけるDCp-OH及びTCPD-OHはそれぞれDCp及びTCPDの水和化合物を意味する。 Next, 250 g of composition (X1), 100 g of water as a hydroxyl group-containing compound (C), and 5 g of sulfuric acid as an acid catalyst were placed in a 1000 mL glass reactor equipped with a stirrer and a condenser, and under a nitrogen atmosphere, The mixture was heated and stirred at 100°C for 18 hours to carry out a hydration reaction of DCp and TCPD in composition (X1) (hereinafter also referred to as "reaction step"). Next, the obtained reaction solution was cooled to room temperature, and then neutralized and extracted with a 5% NaOH aqueous solution to obtain a fluorine-containing cyclic olefin composition before purification by distillation. This fluorine-containing cyclic olefin composition before distillation purification was analyzed by gas chromatography.
In addition, a Sneader fractionator tube and a Liebig condenser tube were attached to a round bottom flask containing the fluorine-containing cyclic olefin composition before distillation purification, and a NBF 6- containing composition and a TDF 6- containing composition were obtained by fractional distillation by vacuum distillation. and gas chromatography.
Here, DCp-OH and TCPD-OH in Table 1 mean hydrated compounds of DCp and TCPD, respectively.
また、蒸留精製前のフッ素含有環状オレフィン組成物を入れた丸底フラスコにスニーダー分留管、リービッヒ冷却管を取り付け、減圧蒸留により、NBF6含有組成物とTDF6含有組成物を分留取得し、ガスクロマトグラフィーにてそれぞれ分析を行った。
ここで、表1におけるDCp-OH及びTCPD-OHはそれぞれDCp及びTCPDの水和化合物を意味する。 Next, 250 g of composition (X1), 100 g of water as a hydroxyl group-containing compound (C), and 5 g of sulfuric acid as an acid catalyst were placed in a 1000 mL glass reactor equipped with a stirrer and a condenser, and under a nitrogen atmosphere, The mixture was heated and stirred at 100°C for 18 hours to carry out a hydration reaction of DCp and TCPD in composition (X1) (hereinafter also referred to as "reaction step"). Next, the obtained reaction solution was cooled to room temperature, and then neutralized and extracted with a 5% NaOH aqueous solution to obtain a fluorine-containing cyclic olefin composition before purification by distillation. This fluorine-containing cyclic olefin composition before distillation purification was analyzed by gas chromatography.
In addition, a Sneader fractionator tube and a Liebig condenser tube were attached to a round bottom flask containing the fluorine-containing cyclic olefin composition before distillation purification, and a NBF 6- containing composition and a TDF 6- containing composition were obtained by fractional distillation by vacuum distillation. and gas chromatography.
Here, DCp-OH and TCPD-OH in Table 1 mean hydrated compounds of DCp and TCPD, respectively.
[実施例2~6]
酸触媒及び水酸基含有化合物(C)の種類を表1に記載のものに変更し、酸触媒の投入量を13gとし、反応工程における加熱条件を表1に記載の条件に変更した以外は実施例1と同様にして、TDF6含有組成物及びNBF6含有組成物の製造及び評価をそれぞれおこなった。ここで、実施例4及び5は組成物(X1)の代わりに組成物(X2)を使用し、実施例6は組成物(X1)の代わりに組成物(X3)を使用した。酸触媒として固体酸を用いた場合、減圧濾過により固体酸触媒を取り除いたものをガスクロマトグラフィー分析用の測定サンプルとした。
表1における固体酸A及びBの詳細は以下の通りである。
固体酸A:スルホン酸基を有する陽イオン交換樹脂(AmberLiteTM HPR2900 H Cation Exchange Resin、シグマアルドリッチ社製、酸解離定数pKa=2以下)
固体酸B:スルホン酸基を有する陽イオン交換樹脂(AMBERLYST 15JS-HG・DRY、オルガノ社製、酸解離定数pKa=2以下)
ここで、表1におけるDCp-OPr又は-OHx及びTCPD-OPrはそれぞれDCp及びTCPDのアルキルエーテル化物を意味する。 [Examples 2 to 6]
Example except that the types of acid catalyst and hydroxyl group-containing compound (C) were changed to those listed in Table 1, the amount of acid catalyst input was 13 g, and the heating conditions in the reaction step were changed to those listed in Table 1. In the same manner as in Example 1, a TDF 6- containing composition and a NBF 6- containing composition were manufactured and evaluated, respectively. Here, Examples 4 and 5 used composition (X2) instead of composition (X1), and Example 6 used composition (X3) instead of composition (X1). When a solid acid was used as the acid catalyst, the solid acid catalyst was removed by vacuum filtration and used as a measurement sample for gas chromatography analysis.
Details of solid acids A and B in Table 1 are as follows.
Solid acid A: cation exchange resin having sulfonic acid groups (AmberLite TM HPR2900 H Cation Exchange Resin, manufactured by Sigma-Aldrich, acid dissociation constant pKa = 2 or less)
Solid acid B: Cation exchange resin with sulfonic acid group (AMBERLYST 15JS-HG・DRY, manufactured by Organo, acid dissociation constant pKa = 2 or less)
Here, DCp-OPr or -OHx and TCPD-OPr in Table 1 mean alkyl etherified products of DCp and TCPD, respectively.
酸触媒及び水酸基含有化合物(C)の種類を表1に記載のものに変更し、酸触媒の投入量を13gとし、反応工程における加熱条件を表1に記載の条件に変更した以外は実施例1と同様にして、TDF6含有組成物及びNBF6含有組成物の製造及び評価をそれぞれおこなった。ここで、実施例4及び5は組成物(X1)の代わりに組成物(X2)を使用し、実施例6は組成物(X1)の代わりに組成物(X3)を使用した。酸触媒として固体酸を用いた場合、減圧濾過により固体酸触媒を取り除いたものをガスクロマトグラフィー分析用の測定サンプルとした。
表1における固体酸A及びBの詳細は以下の通りである。
固体酸A:スルホン酸基を有する陽イオン交換樹脂(AmberLiteTM HPR2900 H Cation Exchange Resin、シグマアルドリッチ社製、酸解離定数pKa=2以下)
固体酸B:スルホン酸基を有する陽イオン交換樹脂(AMBERLYST 15JS-HG・DRY、オルガノ社製、酸解離定数pKa=2以下)
ここで、表1におけるDCp-OPr又は-OHx及びTCPD-OPrはそれぞれDCp及びTCPDのアルキルエーテル化物を意味する。 [Examples 2 to 6]
Example except that the types of acid catalyst and hydroxyl group-containing compound (C) were changed to those listed in Table 1, the amount of acid catalyst input was 13 g, and the heating conditions in the reaction step were changed to those listed in Table 1. In the same manner as in Example 1, a TDF 6- containing composition and a NBF 6- containing composition were manufactured and evaluated, respectively. Here, Examples 4 and 5 used composition (X2) instead of composition (X1), and Example 6 used composition (X3) instead of composition (X1). When a solid acid was used as the acid catalyst, the solid acid catalyst was removed by vacuum filtration and used as a measurement sample for gas chromatography analysis.
Details of solid acids A and B in Table 1 are as follows.
Solid acid A: cation exchange resin having sulfonic acid groups (AmberLite TM HPR2900 H Cation Exchange Resin, manufactured by Sigma-Aldrich, acid dissociation constant pKa = 2 or less)
Solid acid B: Cation exchange resin with sulfonic acid group (AMBERLYST 15JS-HG・DRY, manufactured by Organo, acid dissociation constant pKa = 2 or less)
Here, DCp-OPr or -OHx and TCPD-OPr in Table 1 mean alkyl etherified products of DCp and TCPD, respectively.
(組成物(X2)の調製)
窒素雰囲気下、磁気攪拌装置を備えた25Lのオートクレーブ内に、DCp(東京化成工業社製)3.8kg、ヘキサフルオロプロペン(高千穂化学工業社製)11.5kgを入れ、160℃で24時間加熱攪拌し、次いで、180℃で15時間加熱攪拌した。冷却後、未反応のヘキサフルオロプロペン2.5kgを回収し、反応液12.4kgを取り出した。
次いで、得られた反応液を蒸留することにより、NBF6とDCpを含む組成物を11.0kg取得し、蒸留装置内の残留液よりTDF6とNBF6とTCPDとを含む組成物(X2)を1.0kg取得した。 (Preparation of composition (X2))
Under a nitrogen atmosphere, 3.8 kg of DCp (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and 11.5 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device, and heated at 160°C for 24 hours. The mixture was stirred and then heated and stirred at 180° C. for 15 hours. After cooling, 2.5 kg of unreacted hexafluoropropene was collected, and 12.4 kg of the reaction solution was taken out.
Next, 11.0 kg of a composition containing NBF 6 and DCp was obtained by distilling the obtained reaction solution, and a composition containing TDF 6 , NBF 6 , and TCPD (X2) was obtained from the residual liquid in the distillation apparatus. 1.0 kg of was obtained.
窒素雰囲気下、磁気攪拌装置を備えた25Lのオートクレーブ内に、DCp(東京化成工業社製)3.8kg、ヘキサフルオロプロペン(高千穂化学工業社製)11.5kgを入れ、160℃で24時間加熱攪拌し、次いで、180℃で15時間加熱攪拌した。冷却後、未反応のヘキサフルオロプロペン2.5kgを回収し、反応液12.4kgを取り出した。
次いで、得られた反応液を蒸留することにより、NBF6とDCpを含む組成物を11.0kg取得し、蒸留装置内の残留液よりTDF6とNBF6とTCPDとを含む組成物(X2)を1.0kg取得した。 (Preparation of composition (X2))
Under a nitrogen atmosphere, 3.8 kg of DCp (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and 11.5 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device, and heated at 160°C for 24 hours. The mixture was stirred and then heated and stirred at 180° C. for 15 hours. After cooling, 2.5 kg of unreacted hexafluoropropene was collected, and 12.4 kg of the reaction solution was taken out.
Next, 11.0 kg of a composition containing NBF 6 and DCp was obtained by distilling the obtained reaction solution, and a composition containing TDF 6 , NBF 6 , and TCPD (X2) was obtained from the residual liquid in the distillation apparatus. 1.0 kg of was obtained.
(組成物(X3)の調製)
窒素雰囲気下、磁気攪拌装置を備えた25Lのオートクレーブ内に、DCp(東京化成工業社製)5.2kg、ヘキサフルオロプロペン(高千穂化学工業社製)14.2kgを入れ、160℃で24時間加熱攪拌し、次いで、180℃で15時間加熱攪拌した。冷却後、未反応のヘキサフルオロプロペン1.9kgを回収し、反応液16.3kgを取り出した。
次いで、得られた反応液を蒸留することにより、NBF6とDCpを含む組成物を14.7kg取得し、蒸留装置内の残留液よりTDF6とNBF6とTCPDとを含む組成物(X3)を1.3kg取得した。 (Preparation of composition (X3))
Under a nitrogen atmosphere, 5.2 kg of DCp (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and 14.2 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device, and heated at 160°C for 24 hours. The mixture was stirred and then heated and stirred at 180° C. for 15 hours. After cooling, 1.9 kg of unreacted hexafluoropropene was collected, and 16.3 kg of the reaction solution was taken out.
Next, 14.7 kg of a composition containing NBF 6 and DCp was obtained by distilling the obtained reaction solution, and a composition containing TDF 6 , NBF 6 , and TCPD (X3) was obtained from the residual liquid in the distillation apparatus. 1.3 kg of was obtained.
窒素雰囲気下、磁気攪拌装置を備えた25Lのオートクレーブ内に、DCp(東京化成工業社製)5.2kg、ヘキサフルオロプロペン(高千穂化学工業社製)14.2kgを入れ、160℃で24時間加熱攪拌し、次いで、180℃で15時間加熱攪拌した。冷却後、未反応のヘキサフルオロプロペン1.9kgを回収し、反応液16.3kgを取り出した。
次いで、得られた反応液を蒸留することにより、NBF6とDCpを含む組成物を14.7kg取得し、蒸留装置内の残留液よりTDF6とNBF6とTCPDとを含む組成物(X3)を1.3kg取得した。 (Preparation of composition (X3))
Under a nitrogen atmosphere, 5.2 kg of DCp (manufactured by Tokyo Kasei Kogyo Co., Ltd.) and 14.2 kg of hexafluoropropene (manufactured by Takachiho Kagaku Kogyo Co., Ltd.) were placed in a 25 L autoclave equipped with a magnetic stirring device, and heated at 160°C for 24 hours. The mixture was stirred and then heated and stirred at 180° C. for 15 hours. After cooling, 1.9 kg of unreacted hexafluoropropene was collected, and 16.3 kg of the reaction solution was taken out.
Next, 14.7 kg of a composition containing NBF 6 and DCp was obtained by distilling the obtained reaction solution, and a composition containing TDF 6 , NBF 6 , and TCPD (X3) was obtained from the residual liquid in the distillation apparatus. 1.3 kg of was obtained.
[比較例1]
エーテル化反応を行わない以外は、実施例1と同様にして、NBF6含有組成物及びTDF6含有組成物の製造及び評価をそれぞれおこなった。 [Comparative example 1]
An NBF 6- containing composition and a TDF 6 -containing composition were manufactured and evaluated in the same manner as in Example 1, except that the etherification reaction was not performed.
エーテル化反応を行わない以外は、実施例1と同様にして、NBF6含有組成物及びTDF6含有組成物の製造及び評価をそれぞれおこなった。 [Comparative example 1]
An NBF 6- containing composition and a TDF 6 -containing composition were manufactured and evaluated in the same manner as in Example 1, except that the etherification reaction was not performed.
以上の結果を表1に示す。
The above results are shown in Table 1.
この出願は、2022年3月29日に出願された日本出願特願2022-054139号を基礎とする優先権を主張し、その開示の全てをここに取り込む。
This application claims priority based on Japanese Patent Application No. 2022-054139 filed on March 29, 2022, and the entire disclosure thereof is incorporated herein.
Claims (12)
- 下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含む組成物(X)に対して、酸触媒と、水及びアルキルアルコールからなる群から選択される少なくとも一種の水酸基含有化合物(C)と、を混合する混合工程と、
前記フッ素非含有環状ジオレフィン化合物(B1)と、前記水酸基含有化合物(C)とを反応させることにより、フッ素非含有水和化合物(B2)及びフッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を得る反応工程と、
を含むフッ素含有環状オレフィン組成物の製造方法。
By reacting the fluorine-free cyclic diolefin compound (B1) with the hydroxyl group-containing compound (C), a compound selected from the group consisting of a fluorine-free hydrated compound (B2) and a fluorine-free ether compound (B3) is produced. a reaction step for obtaining at least one type of
A method for producing a fluorine-containing cyclic olefin composition.
- 前記フッ素含有環状オレフィン化合物(A)の沸点と、前記フッ素非含有環状ジオレフィン化合物(B1)の沸点との差の絶対値が10℃以下である、請求項1に記載のフッ素含有環状オレフィン組成物の製造方法。 The fluorine-containing cyclic olefin composition according to claim 1, wherein the absolute value of the difference between the boiling point of the fluorine-containing cyclic olefin compound (A) and the boiling point of the fluorine-free cyclic diolefin compound (B1) is 10° C. or less. How things are manufactured.
- 前記アルキルアルコールの炭素数が3以上10以下である、請求項1又は2に記載のフッ素含有環状オレフィン組成物の製造方法。 The method for producing a fluorine-containing cyclic olefin composition according to claim 1 or 2, wherein the alkyl alcohol has 3 or more and 10 or less carbon atoms.
- 前記酸触媒が無機酸、有機酸及び固体酸からなる群から選択される少なくとも一種を含む、請求項1~3のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。 The method for producing a fluorine-containing cyclic olefin composition according to any one of claims 1 to 3, wherein the acid catalyst contains at least one selected from the group consisting of inorganic acids, organic acids, and solid acids.
- 前記フッ素含有環状オレフィン化合物(A)のHOMOエネルギー(E1)と、前記フッ素非含有環状ジオレフィン化合物(B1)のHOMOエネルギー(E2)との差の絶対値|E2-E1|が0.3eV以上である、請求項1~4のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。 The absolute value of the difference between the HOMO energy (E 1 ) of the fluorine-containing cyclic olefin compound (A) and the HOMO energy (E 2 ) of the fluorine-free cyclic diolefin compound (B1) |E 2 −E 1 | The method for producing a fluorine-containing cyclic olefin composition according to any one of claims 1 to 4, wherein the fluorine-containing cyclic olefin composition is 0.3 eV or more.
- 前記フッ素含有環状オレフィン化合物(A)は、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)及び前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の両方を含む、請求項1~5のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。 The fluorine-containing cyclic olefin compound (A) is a fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) and a fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1). The method for producing a fluorine-containing cyclic olefin composition according to any one of claims 1 to 5, comprising both of the above.
- 前記反応工程の後に、蒸留により、前記フッ素含有環状オレフィン化合物(A1)と前記フッ素含有環状オレフィン化合物(A2)とを分離する分離工程を更に含む、請求項6に記載のフッ素含有環状オレフィン組成物の製造方法。 The fluorine-containing cyclic olefin composition according to claim 6, further comprising a separation step of separating the fluorine-containing cyclic olefin compound (A1) and the fluorine-containing cyclic olefin compound (A2) by distillation after the reaction step. manufacturing method.
- 前記反応工程の後に、蒸留により、前記フッ素含有環状オレフィン化合物(A)と前記フッ素非含有水和化合物(B2)及び前記フッ素非含有エーテル化合物(B3)からなる群から選択される少なくとも一種を分離する分離工程を更に含む、請求項1~7のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。 After the reaction step, separation of the fluorine-containing cyclic olefin compound (A), at least one selected from the group consisting of the fluorine-free hydrated compound (B2) and the fluorine-free ether compound (B3) is performed by distillation. The method for producing a fluorine-containing cyclic olefin composition according to any one of claims 1 to 7, further comprising a separation step of.
- 前記フッ素含有環状オレフィン組成物中の前記フッ素非含有環状ジオレフィン化合物(B1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、5.0質量%以下である、請求項1~8のいずれかに記載のフッ素含有環状オレフィン組成物の製造方法。 The content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is 5.0% by mass or less when the entire fluorine-containing cyclic olefin composition is 100% by mass. A method for producing a fluorine-containing cyclic olefin composition according to any one of claims 1 to 8.
- 前記フッ素含有環状オレフィン組成物中の、前記式(1)においてnが0であるフッ素含有環状オレフィン化合物(A1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、99.0質量%以上である、請求項8に記載のフッ素含有環状オレフィン組成物の製造方法。 When the content of the fluorine-containing cyclic olefin compound (A1) in which n is 0 in the formula (1) in the fluorine-containing cyclic olefin composition is 100% by mass of the entire fluorine-containing cyclic olefin composition. The method for producing a fluorine-containing cyclic olefin composition according to claim 8, wherein the fluorine-containing cyclic olefin composition is 99.0% by mass or more.
- 前記フッ素含有環状オレフィン組成物中の、前記式(1)においてnが1であるフッ素含有環状オレフィン化合物(A2)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、99.0質量%以上である、請求項8に記載のフッ素含有環状オレフィン組成物の製造方法。 When the content of the fluorine-containing cyclic olefin compound (A2) in which n is 1 in the formula (1) in the fluorine-containing cyclic olefin composition is 100% by mass of the entire fluorine-containing cyclic olefin composition. The method for producing a fluorine-containing cyclic olefin composition according to claim 8, wherein the fluorine-containing cyclic olefin composition is 99.0% by mass or more.
- 下記式(1)で示されるフッ素含有環状オレフィン化合物(A)及びフッ素非含有環状ジオレフィン化合物(B1)を含むフッ素含有環状オレフィン組成物であって、
前記フッ素含有環状オレフィン組成物中の前記フッ素非含有環状ジオレフィン化合物(B1)の含有量が、前記フッ素含有環状オレフィン組成物の全体を100質量%としたとき、0質量%超1.0質量%以下であるフッ素含有環状オレフィン組成物。
The content of the fluorine-free cyclic diolefin compound (B1) in the fluorine-containing cyclic olefin composition is more than 0% by mass and 1.0% by mass when the entire fluorine-containing cyclic olefin composition is 100% by mass. % or less.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2022054139 | 2022-03-29 | ||
JP2022-054139 | 2022-03-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2023189217A1 true WO2023189217A1 (en) | 2023-10-05 |
Family
ID=88201314
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2023/008150 WO2023189217A1 (en) | 2022-03-29 | 2023-03-03 | Method for producing fluorine-containing cyclic olefin composition, and fluorine-containing cyclic olefin composition |
Country Status (2)
Country | Link |
---|---|
TW (1) | TW202340125A (en) |
WO (1) | WO2023189217A1 (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002114723A (en) * | 2000-09-29 | 2002-04-16 | Asahi Glass Co Ltd | Method for producing fluorine-containing alcohol |
JP2008230981A (en) * | 2007-03-16 | 2008-10-02 | Daikin Ind Ltd | Method for producing highly pure fluorine-containing alkyl ether |
JP2010132600A (en) * | 2008-12-04 | 2010-06-17 | Nippon Zeon Co Ltd | Fluorine-containing cyclic olefin compound, method of producing the same, ring opening polymer of fluorine-containing cyclic olefin, and hydrogenated ring opening polymer of fluorine-containing cyclic olefin |
JP2019089714A (en) * | 2017-11-10 | 2019-06-13 | 三井化学株式会社 | Manufacturing method of fluorine-containing cyclic olefin monomer |
JP2021109828A (en) * | 2020-01-06 | 2021-08-02 | Agc株式会社 | Method for producing azeotropic or azeotrope-like composition of 1,3-dichloro-2,3,3-trifluoropropene and alcohol |
-
2023
- 2023-03-03 WO PCT/JP2023/008150 patent/WO2023189217A1/en unknown
- 2023-03-07 TW TW112108263A patent/TW202340125A/en unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002114723A (en) * | 2000-09-29 | 2002-04-16 | Asahi Glass Co Ltd | Method for producing fluorine-containing alcohol |
JP2008230981A (en) * | 2007-03-16 | 2008-10-02 | Daikin Ind Ltd | Method for producing highly pure fluorine-containing alkyl ether |
JP2010132600A (en) * | 2008-12-04 | 2010-06-17 | Nippon Zeon Co Ltd | Fluorine-containing cyclic olefin compound, method of producing the same, ring opening polymer of fluorine-containing cyclic olefin, and hydrogenated ring opening polymer of fluorine-containing cyclic olefin |
JP2019089714A (en) * | 2017-11-10 | 2019-06-13 | 三井化学株式会社 | Manufacturing method of fluorine-containing cyclic olefin monomer |
JP2021109828A (en) * | 2020-01-06 | 2021-08-02 | Agc株式会社 | Method for producing azeotropic or azeotrope-like composition of 1,3-dichloro-2,3,3-trifluoropropene and alcohol |
Also Published As
Publication number | Publication date |
---|---|
TW202340125A (en) | 2023-10-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3051350B1 (en) | Alcoholic compound and method for producing alcoholic compound | |
KR101394835B1 (en) | Alicyclic diepoxy compound, epoxy resin composition, and cured product | |
EP2349967B1 (en) | Methods of making fluorinated ethers, fluorinated ethers, and uses thereof | |
WO2005075406A1 (en) | Adamantane derivatives and process for producing the same | |
EP2578562A1 (en) | Cyclic compound purification method | |
KR20140097370A (en) | Method for preparing fluorine-containing vinyl ether | |
KR20150114939A (en) | Allyl ether resin and epoxy resin | |
EP3757678A1 (en) | Resist underlayer film forming composition and method for forming pattern | |
EP2444385B1 (en) | Method for producing fluorine-containing ether with high purity | |
CN111635341A (en) | Trifluoro sulfonamide octahydro-pentalene photoresist resin monomer and preparation method thereof | |
WO2023189217A1 (en) | Method for producing fluorine-containing cyclic olefin composition, and fluorine-containing cyclic olefin composition | |
US20200399210A1 (en) | Process for producing sulfonic acid group-containing monomer | |
CN111675720B (en) | Trifluoro sulfonamide hexahydrofuro [3,2-b ] furan photoresist resin monomer and preparation method thereof | |
JP5530084B2 (en) | Fullerene derivative, solution thereof, and film thereof | |
CN111675680A (en) | Trifluoro sulfonamide pyran type photoresist resin monomer and preparation method thereof | |
JP5824963B2 (en) | Purification method of fluoroalkyl vinyl ether | |
CN111689941A (en) | Trifluoro sulfonamide 1, 4-dioxospiro [4,5] decane photoresist resin monomer and preparation method thereof | |
JPS6222735A (en) | Manufacture of fluorine containing diol and tetrol | |
US9156762B2 (en) | 4,4-bis[(ethenyloxy)methyl]cyclohexene and method for producing same | |
JP4937530B2 (en) | Fluorine-containing compound and method for producing the same | |
JP5498753B2 (en) | Vinyl ether having both alicyclic and aromatic ring structures | |
TWI615195B (en) | Method for producing dicyclopentadiene-modified phenol resin and reusable fluorine-based ion exchange resin catalyst | |
CN111747966A (en) | Trifluoro sulfonamide 2-oxabicyclo [2.2.1] heptane photoresist resin monomer and preparation method thereof | |
WO2024002860A1 (en) | Process for producing hydrofluoroethers | |
JP3493401B2 (en) | Glycol ether containing cyclohexyl group |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 23779246 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2024511566 Country of ref document: JP Kind code of ref document: A |