WO2021254372A1 - Method for preparing hexafluoro-1,3-butadiene and intermediate thereof - Google Patents
Method for preparing hexafluoro-1,3-butadiene and intermediate thereof Download PDFInfo
- Publication number
- WO2021254372A1 WO2021254372A1 PCT/CN2021/100290 CN2021100290W WO2021254372A1 WO 2021254372 A1 WO2021254372 A1 WO 2021254372A1 CN 2021100290 W CN2021100290 W CN 2021100290W WO 2021254372 A1 WO2021254372 A1 WO 2021254372A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- hexafluoro
- dibromo
- chloro
- butadiene
- reaction
- Prior art date
Links
- LGPPATCNSOSOQH-UHFFFAOYSA-N 1,1,2,3,4,4-hexafluorobuta-1,3-diene Chemical compound FC(F)=C(F)C(F)=C(F)F LGPPATCNSOSOQH-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 238000000034 method Methods 0.000 title claims abstract description 43
- 238000006243 chemical reaction Methods 0.000 claims abstract description 68
- 238000002360 preparation method Methods 0.000 claims abstract description 43
- 239000003999 initiator Substances 0.000 claims abstract description 24
- OVZATIUQXBLIQT-UHFFFAOYSA-N 1,2-dibromo-1-chloro-1,2,2-trifluoroethane Chemical compound FC(F)(Br)C(F)(Cl)Br OVZATIUQXBLIQT-UHFFFAOYSA-N 0.000 claims abstract description 15
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- CIHOLLKRGTVIJN-UHFFFAOYSA-N tert‐butyl hydroperoxide Chemical compound CC(C)(C)OO CIHOLLKRGTVIJN-UHFFFAOYSA-N 0.000 claims abstract description 14
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052740 iodine Inorganic materials 0.000 claims abstract description 13
- 235000019400 benzoyl peroxide Nutrition 0.000 claims abstract description 12
- LSXWFXONGKSEMY-UHFFFAOYSA-N di-tert-butyl peroxide Chemical compound CC(C)(C)OOC(C)(C)C LSXWFXONGKSEMY-UHFFFAOYSA-N 0.000 claims abstract description 12
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims abstract description 10
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 8
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims abstract description 7
- 239000003880 polar aprotic solvent Substances 0.000 claims abstract description 7
- 230000009471 action Effects 0.000 claims abstract description 6
- 229910052794 bromium Inorganic materials 0.000 claims abstract description 5
- 238000005695 dehalogenation reaction Methods 0.000 claims abstract description 5
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims abstract description 5
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 21
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 15
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 15
- 239000003054 catalyst Substances 0.000 claims description 13
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 10
- 239000000460 chlorine Substances 0.000 claims description 10
- -1 trifluoroethylene halide Chemical class 0.000 claims description 9
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 239000011630 iodine Substances 0.000 claims description 8
- UAYWVJHJZHQCIE-UHFFFAOYSA-L zinc iodide Chemical compound I[Zn]I UAYWVJHJZHQCIE-UHFFFAOYSA-L 0.000 claims description 8
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 claims description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 6
- 239000011261 inert gas Substances 0.000 claims description 6
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 239000003960 organic solvent Substances 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 4
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 4
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical group C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 claims description 4
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 claims description 4
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 3
- 238000004821 distillation Methods 0.000 claims description 3
- 229910052734 helium Inorganic materials 0.000 claims description 3
- 239000001307 helium Substances 0.000 claims description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 3
- VNDYJBBGRKZCSX-UHFFFAOYSA-L zinc bromide Chemical group Br[Zn]Br VNDYJBBGRKZCSX-UHFFFAOYSA-L 0.000 claims description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims description 2
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 235000019253 formic acid Nutrition 0.000 claims description 2
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims 2
- 239000003795 chemical substances by application Substances 0.000 claims 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims 1
- 229940102001 zinc bromide Drugs 0.000 claims 1
- 230000008569 process Effects 0.000 abstract description 11
- 238000009776 industrial production Methods 0.000 abstract description 3
- 239000000543 intermediate Substances 0.000 description 28
- 239000002994 raw material Substances 0.000 description 11
- 239000007789 gas Substances 0.000 description 9
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 description 7
- 239000002904 solvent Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- AYCANDRGVPTASA-UHFFFAOYSA-N 1-bromo-1,2,2-trifluoroethene Chemical group FC(F)=C(F)Br AYCANDRGVPTASA-UHFFFAOYSA-N 0.000 description 5
- 238000005530 etching Methods 0.000 description 5
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 5
- 230000000977 initiatory effect Effects 0.000 description 5
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 4
- SBZXBUIDTXKZTM-UHFFFAOYSA-N diglyme Chemical compound COCCOCCOC SBZXBUIDTXKZTM-UHFFFAOYSA-N 0.000 description 4
- 229910052731 fluorine Inorganic materials 0.000 description 4
- 239000011737 fluorine Substances 0.000 description 4
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 4
- 238000003760 magnetic stirring Methods 0.000 description 4
- 150000003254 radicals Chemical class 0.000 description 4
- 230000002194 synthesizing effect Effects 0.000 description 4
- PFSLUJSDDNGKIZ-UHFFFAOYSA-N 1,4-dibromo-2,3-dichloro-1,1,2,3,4,4-hexafluorobutane Chemical compound FC(F)(Br)C(F)(Cl)C(F)(Cl)C(F)(F)Br PFSLUJSDDNGKIZ-UHFFFAOYSA-N 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- QZRGKCOWNLSUDK-UHFFFAOYSA-N Iodochlorine Chemical compound ICl QZRGKCOWNLSUDK-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical compound ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000006471 dimerization reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- CNRGDMNPQKVTJP-UHFFFAOYSA-N 1,1,4,4-tetrachloro-2,3-difluorobuta-1,3-diene Chemical compound C(=C(Cl)Cl)(C(=C(Cl)Cl)F)F CNRGDMNPQKVTJP-UHFFFAOYSA-N 0.000 description 2
- YLYSNAJRDKXSGQ-UHFFFAOYSA-N 1,2,4-tribromo-3-chloro-1,1,2,3,4,4-hexafluorobutane Chemical compound C(C(C(F)(F)Br)(F)Br)(C(F)(F)Br)(F)Cl YLYSNAJRDKXSGQ-UHFFFAOYSA-N 0.000 description 2
- PAAZPARNPHGIKF-UHFFFAOYSA-N 1,2-dibromoethane Chemical compound BrCCBr PAAZPARNPHGIKF-UHFFFAOYSA-N 0.000 description 2
- BZBLUUDREZEDDJ-UHFFFAOYSA-N 2,2,3,3-tetrachloro-1,1,1,4,4,4-hexafluorobutane Chemical compound FC(F)(F)C(Cl)(Cl)C(Cl)(Cl)C(F)(F)F BZBLUUDREZEDDJ-UHFFFAOYSA-N 0.000 description 2
- KWXXMLHQBFNLOR-UHFFFAOYSA-N 3,4-dichloro-1,1,2,3,4,4-hexafluorobut-1-ene Chemical compound FC(F)=C(F)C(F)(Cl)C(F)(F)Cl KWXXMLHQBFNLOR-UHFFFAOYSA-N 0.000 description 2
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000012295 chemical reaction liquid Substances 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229910000856 hastalloy Inorganic materials 0.000 description 2
- 238000010907 mechanical stirring Methods 0.000 description 2
- 239000002798 polar solvent Substances 0.000 description 2
- 238000007348 radical reaction Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- KHFGPBNEILANTD-UHFFFAOYSA-N 1,1,1,2-tetrachloro-2,3,3,4,4,4-hexafluorobutane Chemical compound FC(F)(F)C(F)(F)C(F)(Cl)C(Cl)(Cl)Cl KHFGPBNEILANTD-UHFFFAOYSA-N 0.000 description 1
- MIZLGWKEZAPEFJ-UHFFFAOYSA-N 1,1,2-trifluoroethene Chemical group FC=C(F)F MIZLGWKEZAPEFJ-UHFFFAOYSA-N 0.000 description 1
- IRHYACQPDDXBCB-UHFFFAOYSA-N 1,2,3,4-tetrachloro-1,1,2,3,4,4-hexafluorobutane Chemical compound FC(F)(Cl)C(F)(Cl)C(F)(Cl)C(F)(F)Cl IRHYACQPDDXBCB-UHFFFAOYSA-N 0.000 description 1
- UREJNEBJDURREH-UHFFFAOYSA-N 1,2-dibromo-1,1,2-trifluoroethane Chemical compound FC(Br)C(F)(F)Br UREJNEBJDURREH-UHFFFAOYSA-N 0.000 description 1
- HCUGPHQZDLROAY-UHFFFAOYSA-N 1,2-dichloro-1,1,2-trifluoro-2-iodoethane Chemical compound FC(F)(Cl)C(F)(Cl)I HCUGPHQZDLROAY-UHFFFAOYSA-N 0.000 description 1
- LMHAGAHDHRQIMB-UHFFFAOYSA-N 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane Chemical compound FC1(F)C(F)(F)C(F)(Cl)C1(F)Cl LMHAGAHDHRQIMB-UHFFFAOYSA-N 0.000 description 1
- ZMHBVZQKSVXDMZ-UHFFFAOYSA-N 2,3-dichloro-1,1,2,3,4,4-hexafluorobutane Chemical compound ClC(C(F)F)(C(C(F)F)(F)Cl)F ZMHBVZQKSVXDMZ-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- AFLIPEBFYDIRNJ-UHFFFAOYSA-N FC(F)=C(F)[Zn] Chemical compound FC(F)=C(F)[Zn] AFLIPEBFYDIRNJ-UHFFFAOYSA-N 0.000 description 1
- WYEPLZROMPCSKP-UHFFFAOYSA-N [He].[F] Chemical compound [He].[F] WYEPLZROMPCSKP-UHFFFAOYSA-N 0.000 description 1
- MBYNTKPBDYZMAQ-UHFFFAOYSA-N [benzhydrylperoxy(phenyl)methyl]benzene Chemical compound C=1C=CC=CC=1C(C=1C=CC=CC=1)OOC(C=1C=CC=CC=1)C1=CC=CC=C1 MBYNTKPBDYZMAQ-UHFFFAOYSA-N 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 208000012839 conversion disease Diseases 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
- 238000001312 dry etching Methods 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000003682 fluorination reaction Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007116 intermolecular coupling reaction Methods 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/26—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton
- C07C17/272—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by addition reactions
- C07C17/278—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by addition reactions of only halogenated hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/25—Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C19/00—Acyclic saturated compounds containing halogen atoms
- C07C19/08—Acyclic saturated compounds containing halogen atoms containing fluorine
- C07C19/10—Acyclic saturated compounds containing halogen atoms containing fluorine and chlorine
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C19/00—Acyclic saturated compounds containing halogen atoms
- C07C19/08—Acyclic saturated compounds containing halogen atoms containing fluorine
- C07C19/14—Acyclic saturated compounds containing halogen atoms containing fluorine and bromine
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C21/00—Acyclic unsaturated compounds containing halogen atoms
- C07C21/02—Acyclic unsaturated compounds containing halogen atoms containing carbon-to-carbon double bonds
- C07C21/19—Halogenated dienes
- C07C21/20—Halogenated butadienes
Definitions
- Hexafluoro-1,3-butadiene English name Hexafluoro-1,3-butadiene, HFBD for short, boiling point 5.5°C, freezing point -130°C, liquid density at 15°C is 1.44kg/L.
- Hexafluoro-1,3-butadiene is a new generation of green dry etching gas, with excellent environmental performance and working performance, its existence time in the atmosphere (ALT) is only 1.9 days, and the GWP 100 value is 290. Because hexafluoro-1,3-butadiene has a low fluorine-to-carbon ratio, it exhibits excellent etching performance. It is used for the etching of rectifier circuit boards containing Cu and low K dielectric constant.
- hexafluoro-1,3-butadiene is a key etching gas for the new generation of storage technology 3D NAND flash memory. As the demand for high-end chips continues to increase, the market for hexafluoro-1,3-butadiene will continue to grow.
- Patent CN106336342A discloses a method for synthesizing hexafluoro-1,3-butadiene using chlorine and iodine as raw materials.
- the method includes the following steps: 1The reaction of chlorine and iodine to synthesize iodine chloride; 2Trichlorochloride The reaction of ethylene with iodine chloride gives 1,2-dichloro-1,1,2-trifluoro-2-iodoethane (CF 2 Cl-CFICl); 31,2-dichloro-1,1,2-tri Fluoro-2-iodoethane undergoes intermolecular coupling reaction in the presence of a catalyst to obtain 1,2,3,4-tetrachloro-hexafluorobutane (CF 2 Cl-CFCl-CFCl-CF 2 Cl); 41 ,2,3,4-Tetrachloro-hexafluorobutane undergoes intramolecular dehalogenation to obtain
- Russian patent RU0118462 discloses a method for synthesizing hexafluoro-1,3-butadiene with chlorotrifluoroethylene as a raw material.
- the method includes: dimerization of chlorotrifluoroethylene at high temperature to obtain 34% of 1,2- Dichlorohexafluorocyclobutane and 27% of 3,4-dichlorohexafluoro-1-butene, and the two products, 3,4-dichlorohexafluoro-1-butene, are separated through a high-efficiency rectification column Direct zinc powder dechlorination to obtain the target product hexafluoro-1,3-butadiene, the reaction equation is as follows:
- Zhejiang Lantian Environmental Protection Patent CN105732301A discloses that trifluoroethylene bromide is used as raw material to react with zinc powder to synthesize trifluorovinyl zinc reagent, and then under the action of trivalent iron salt or divalent copper salt, the self-coupling reaction obtains hexafluoro-
- the 1,3-butadiene method the reaction equation is as follows:
- Solvay patent WO2009087067A1 discloses a method for synthesizing hexafluoro-1,3-butadiene using trichloroethylene (TCE) and fluorine gas as raw materials.
- the present invention proposes a method for preparing hexafluoro-1,3-butadiene and its intermediates by a telomerization method.
- the method has simple process, mild reaction conditions, small amount of three wastes, safety and environmental protection, Suitable for industrial production.
- the initiator is selected from azobisisobutyronitrile (AIBN), di-tert-butyl peroxide (DTBP), dibenzoyl peroxide (BPO), dicumyl peroxide (DCP), tert-butyl peroxide At least one of hydrogen oxide (TBHP), potassium persulfate (KPS), and ammonium persulfate (APS);
- AIBN azobisisobutyronitrile
- DTBP di-tert-butyl peroxide
- BPO dibenzoyl peroxide
- DCP dicumyl peroxide
- TBHP hydrogen oxide
- KPS potassium persulfate
- APS ammonium persulfate
- step A1 can be regarded as a free radical reaction
- both photoinitiation and initiator initiation can initiate a free radical reaction.
- the initiation effect of the initiator is far better than that of photoinitiation for the reaction in step A1, and even different types of initiators have different initiation effects. That is, the use of initiators can increase the selectivity of intermediate A.
- the initiator is selected from at least one of di-tert-butyl peroxide, dibenzoyl peroxide, and tert-butyl hydroperoxide. More preferably, the initiator is dibenzoyl peroxide or tert-butyl hydroperoxide.
- the molar ratio of the 1,2-dibromo-1-chloro-1,2,2-trifluoroethane to the initiator is 1:0.01 to 1:0.1.
- the molar ratio of the 1,2-dibromo-1-chloro-1,2,2-trifluoroethane to the initiator is 1:0.03 to 1:0.06.
- the aprotic polar solvent is more conducive to the progress of the reaction.
- the aprotic polar solvent is selected from tetrahydrofuran, 1,4-dioxane, acetonitrile, diethylene glycol dimethyl ether, N,N-dimethylformamide, N,N-dimethyl At least one of acetamide. More preferably, the polar aprotic solvent is selected from at least one of 1,4-dioxane, acetonitrile, and diethylene glycol dimethyl ether.
- the purification of the reaction solution can be carried out by a conventional purification method, such as atmospheric distillation or vacuum distillation.
- the reaction can be carried out in a solvent-free state.
- the reaction effect is better in organic solvents.
- the organic solvent is selected from formic acid, acetic acid, trifluoroacetic acid, propionic acid, dichloromethane, chloroform, carbon tetrachloride, dichloroethane, 1,1,1-trichloroethane, isopropyl
- the organic solvent is selected from at least one of acetic acid, N,N-dimethylformamide or isopropanol.
- the reaction temperature in the A1 step is 80°C to 160°C, and the temperature is kept for 6-12 hours; the reaction temperature in the A2 step is 60°C to 90°C, and the temperature is kept for 3 to 6 hours. .
- the initiator is selected from azobisisobutyronitrile (AIBN), di-tert-butyl peroxide (DTBP), dibenzoyl peroxide (BPO), dicumyl peroxide (DCP), tert-butyl peroxide At least one of hydrogen oxide (TBHP), potassium persulfate (KPS), and ammonium persulfate (APS).
- AIBN azobisisobutyronitrile
- DTBP di-tert-butyl peroxide
- BPO dibenzoyl peroxide
- DCP dicumyl peroxide
- TBHP hydrogen oxide
- KPS potassium persulfate
- APS ammonium persulfate
- the present invention has the following beneficial effects:
- the present invention uses a free radical initiator to initiate the telomerization reaction, which not only can control the rate of free radical generation and the degree of telomerization reaction, but also greatly improves the selectivity of the intermediate compared with photoinitiation.
- the reaction liquid was analyzed by GC-MS, and calculations showed that the conversion rate of the raw material 1,2-dibromo-1-chloro-1,2,2-trifluoroethane was 97.6%, and the intermediate 1,2,4-trifluoroethane The selectivity of bromo-3-chloro-1,1,2,3,4,4-hexafluorobutane is 73.9%. The results are shown in Table 2.
- the reaction solution is subjected to vacuum distillation to obtain high-purity intermediate A.
- Example 7 During the preparation of the intermediate, the type of solvent was changed, and the acetonitrile in Example 7 was replaced with 150 g of diethylene glycol dimethyl ether. The results of the reaction are shown in Table 2.
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Abstract
Disclosed is a method for preparing hexafluoro-1,3-butadiene and an intermediate thereof. The method for preparing hexafluoro-1,3-butadiene comprises: A1, reacting 1,2-dibromo-1-chloro-1,2,2-trifluoroethane with a trifluorohaloethylene in a polar aprotic solvent under the action of an initiator, and rectifying and purifying the reaction solution to obtain 1,4-dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane, wherein the structural formula of the trifluorohaloethylene is CF2=CFX, with X being Cl, Br or I, and the initiator is selected from at least one of azodiisobutyronitrile, di-tert-butyl peroxide, dibenzoyl peroxide, dicumyl peroxide, tert-butyl hydroperoxide, potassium persulfate and ammonium persulfate; and A2, subjecting 1,4-dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane and zinc powder to a dehalogenation reaction, in order to obtain hexafluoro-1,3-butadiene. The preparation method has advantages such as a simple process, mild reaction conditions, and being suitable for industrial production.
Description
本发明涉及含氟电子气体,特别涉及一种调聚法合成六氟-1,3-丁二烯及其中间体的方法。The invention relates to a fluorine-containing electronic gas, in particular to a method for synthesizing hexafluoro-1,3-butadiene and its intermediates by a telomerization method.
六氟-1,3-丁二烯,英文名为Hexafluoro-1,3-butadiene,简称HFBD,沸点5.5℃,凝固点-130℃,15℃下液体密度为1.44kg/L。六氟-1,3-丁二烯是新一代绿色干蚀刻气,具有优异的环境性能和工作性能,其在大气中的存在时间(ALT)仅为1.9天,GWP
100值为290。由于六氟-1,3-丁二烯具有较低的氟碳比,故表现出优良的蚀刻性能,用于含Cu和低K介电常数的整流线路板生产用的刻蚀,主要被用于关键尺寸的精密刻蚀(精度达100nm),有着比其他刻蚀气更好的选择性和深宽比。六氟-1,3-丁二烯作为生产高端芯片的必需材料之一,是新一代存储技术3D NAND闪存的关键蚀刻气。随着对高端芯片需求的不断增加,六氟-1,3-丁二烯的市场将日益增长。
Hexafluoro-1,3-butadiene, English name Hexafluoro-1,3-butadiene, HFBD for short, boiling point 5.5℃, freezing point -130℃, liquid density at 15℃ is 1.44kg/L. Hexafluoro-1,3-butadiene is a new generation of green dry etching gas, with excellent environmental performance and working performance, its existence time in the atmosphere (ALT) is only 1.9 days, and the GWP 100 value is 290. Because hexafluoro-1,3-butadiene has a low fluorine-to-carbon ratio, it exhibits excellent etching performance. It is used for the etching of rectifier circuit boards containing Cu and low K dielectric constant. It is mainly used For precision etching of critical dimensions (accuracy of 100nm), it has better selectivity and aspect ratio than other etching gases. As one of the necessary materials for the production of high-end chips, hexafluoro-1,3-butadiene is a key etching gas for the new generation of storage technology 3D NAND flash memory. As the demand for high-end chips continues to increase, the market for hexafluoro-1,3-butadiene will continue to grow.
现有技术中关于六氟-1,3-丁二烯的合成主要有以下报道:There are mainly the following reports on the synthesis of hexafluoro-1,3-butadiene in the prior art:
1)采用氯气和碘为原料的工艺1) Process using chlorine and iodine as raw materials
浙江博瑞电子专利CN106336342A公开了一种以氯气和碘为原料合成六氟-1,3-丁二烯的方法,该方法包括以下步骤:①氯气和碘反应合成氯化碘;②三氯氯乙烯与氯化碘反应得到1,2-二氯-1,1,2-三氟-2-碘乙烷(CF
2Cl-CFICl);③1,2-二氯-1,1,2-三氟-2-碘乙烷在催化剂存在下,进行分子间偶联反应,得到1,2,3,4-四氯-六氟丁烷(CF
2Cl-CFCl-CFCl-CF
2Cl);④1,2,3,4-四氯-六氟丁烷进行分子内脱卤得到六氟-1,3-丁二烯,反应方程式如下:
Zhejiang Borui Electronics Patent CN106336342A discloses a method for synthesizing hexafluoro-1,3-butadiene using chlorine and iodine as raw materials. The method includes the following steps: ①The reaction of chlorine and iodine to synthesize iodine chloride; ②Trichlorochloride The reaction of ethylene with iodine chloride gives 1,2-dichloro-1,1,2-trifluoro-2-iodoethane (CF 2 Cl-CFICl); ③1,2-dichloro-1,1,2-tri Fluoro-2-iodoethane undergoes intermolecular coupling reaction in the presence of a catalyst to obtain 1,2,3,4-tetrachloro-hexafluorobutane (CF 2 Cl-CFCl-CFCl-CF 2 Cl); ④1 ,2,3,4-Tetrachloro-hexafluorobutane undergoes intramolecular dehalogenation to obtain hexafluoro-1,3-butadiene. The reaction equation is as follows:
但该方法步骤较长,且用到昂贵的氯化碘,使得工艺原料成本较高。However, this method has longer steps and uses expensive iodine chloride, which makes the process raw material cost higher.
2)二聚工艺2) Dimerization process
俄罗斯专利RU0118462公开了以三氟氯乙烯为原料合成六氟-1,3-丁二烯的方法,所述方法包括:三氟氯乙烯在高温下发生二聚反应得到34%的1,2-二氯六氟环丁烷和27%的3,4-二氯六氟-1-丁烯,并通过高效精馏柱分离这两种产物,3,4-二氯六氟-1-丁烯直接锌粉脱氯得到目标产物六氟-1,3-丁二烯,反应方程式如下:Russian patent RU0118462 discloses a method for synthesizing hexafluoro-1,3-butadiene with chlorotrifluoroethylene as a raw material. The method includes: dimerization of chlorotrifluoroethylene at high temperature to obtain 34% of 1,2- Dichlorohexafluorocyclobutane and 27% of 3,4-dichlorohexafluoro-1-butene, and the two products, 3,4-dichlorohexafluoro-1-butene, are separated through a high-efficiency rectification column Direct zinc powder dechlorination to obtain the target product hexafluoro-1,3-butadiene, the reaction equation is as follows:
但该方法聚合反应需要高温高压条件,反应选择性仅有27%。However, the polymerization reaction of this method requires high temperature and high pressure conditions, and the reaction selectivity is only 27%.
3)锌试剂偶联工艺3) Zinc reagent coupling process
浙江蓝天环保专利CN105732301A公开了以三氟溴乙烯为原料,与锌粉反应合成三氟乙烯基锌试剂,然后在三价铁盐或二价铜盐的作用下,自偶联反应得到六氟-1,3-丁二烯的方法,反应方程式如下:Zhejiang Lantian Environmental Protection Patent CN105732301A discloses that trifluoroethylene bromide is used as raw material to react with zinc powder to synthesize trifluorovinyl zinc reagent, and then under the action of trivalent iron salt or divalent copper salt, the self-coupling reaction obtains hexafluoro- The 1,3-butadiene method, the reaction equation is as follows:
但该方法起始原料三氟溴乙烯来源存在问题。However, the source of the starting material of this method, bromotrifluoroethylene, has problems.
4)元素氟氟化工艺4) Elemental fluorination process
索尔维专利WO2009087067A1公开了以三氯乙烯(TCE)和氟气为原料合成六氟-1,3-丁二烯的方法,该方法包括:①氟二聚反应:在AISI 316L反应器中,TCE与氦气稀释的氟气反应得到C
4H
2F
2Cl
6,TCE的转化率为22.9%,选择性为50%;②消去反应:在玻璃反应器中,C
4H
2F
2Cl
6与20%NaOH溶液反应得到四氯二氟丁二烯(CFCl=CCl-CCl=CFCl),反应收率为93%;③氟化反应:将四氯二氟丁二烯与氦气稀释的氟气反应得到四氯六氟丁烷(CF2Cl-CFCl-CFCl-CF2Cl,CFC-316),反应转化率为97.8%,选择性为64%;④脱卤反应:CFC-316在异丙醇溶剂中与锌粉反应得到六氟-1,3-丁二烯,收率96%,产品纯度99.5%。但该方法对设备要求较高,工艺安全风险大。
Solvay patent WO2009087067A1 discloses a method for synthesizing hexafluoro-1,3-butadiene using trichloroethylene (TCE) and fluorine gas as raw materials. The method includes: ① Fluorine dimerization reaction: In an AISI 316L reactor, TCE reacts with fluorine gas diluted with helium to obtain C 4 H 2 F 2 Cl 6 , the conversion rate of TCE is 22.9%, and the selectivity is 50%; ② Elimination reaction: In a glass reactor, C 4 H 2 F 2 Cl 6 React with 20% NaOH solution to obtain tetrachlorodifluorobutadiene (CFCl=CCl-CCl=CFCl), the reaction yield is 93%; ③Fluorination reaction: Dilute tetrachlorodifluorobutadiene with helium Fluorine gas reaction produces tetrachlorohexafluorobutane (CF2Cl-CFCl-CFCl-CF2Cl, CFC-316), the reaction conversion rate is 97.8%, the selectivity is 64%; ④Dehalogenation reaction: CFC-316 in isopropanol solvent The hexafluoro-1,3-butadiene is obtained by reacting with zinc powder with a yield of 96% and a product purity of 99.5%. However, this method has higher requirements for equipment and high process safety risks.
因此,仍有需求开发一种新的六氟-1,3-丁二烯合成工艺。Therefore, there is still a need to develop a new synthesis process of hexafluoro-1,3-butadiene.
发明内容Summary of the invention
为了解决上述技术问题,本发明提出了一种经调聚法制备六氟-1,3-丁二烯及其中间体的方法,该方法工艺简单、反应条件温和、三废量少、安全环保、适合工业化生产。In order to solve the above technical problems, the present invention proposes a method for preparing hexafluoro-1,3-butadiene and its intermediates by a telomerization method. The method has simple process, mild reaction conditions, small amount of three wastes, safety and environmental protection, Suitable for industrial production.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种六氟-1,3-丁二烯的制备方法,所述制备方法包括以下步骤:A preparation method of hexafluoro-1,3-butadiene, the preparation method comprising the following steps:
A1.在极性非质子溶剂中,在引发剂作用下,1,2-二溴-1-氯-1,2,2-三氟乙烷与三氟卤乙烯反应,反应液经提纯得到1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷(中间体A);所述三氟卤乙烯的结构式为:CF
2=CFX,其中X为Cl、Br或I;
A1. In a polar aprotic solvent, under the action of an initiator, 1,2-dibromo-1-chloro-1,2,2-trifluoroethane reacts with trifluoroethylene halide, and the reaction solution is purified to obtain 1 ,4-Dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane (Intermediate A); the structural formula of the trifluoroethylene halide is: CF 2 = CFX, where X is Cl, Br or I;
所述引发剂选自偶氮二异丁腈(AIBN)、过氧化二叔丁基(DTBP)、过氧化二苯甲酰(BPO)、过氧化二异丙苯(DCP)、叔丁基过氧化氢(TBHP)、过硫酸钾(KPS)、过硫酸铵(APS)中的至少一种;The initiator is selected from azobisisobutyronitrile (AIBN), di-tert-butyl peroxide (DTBP), dibenzoyl peroxide (BPO), dicumyl peroxide (DCP), tert-butyl peroxide At least one of hydrogen oxide (TBHP), potassium persulfate (KPS), and ammonium persulfate (APS);
A2. 1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷与锌粉经脱卤反应获得六氟-1,3-丁二烯。A2. 1,4-Dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane and zinc powder undergo dehalogenation reaction to obtain hexafluoro-1,3-butane Diene.
本发明中,不同的引发方式(如光引发或引发剂引发)对中间体A的合成具有较大的影响。虽然从反应机理而言,步骤A1可视为自由基反应,光引发和引发剂引发均可引发自由基反应。但本申请人发现,对A1步骤反应,引发剂的引发效果远优于光引发,甚至不同的引发剂种类,引发效果也不同。也即,引发剂的使用,可以提高中间体A的选择性。作为优选地,所述引发剂选自过氧化二叔丁基、过氧化二苯甲酰、叔丁基过氧化氢中的至少一种。更为优选地,所述引发剂为过氧化二苯甲酰或叔丁基过氧化氢。In the present invention, different initiation methods (such as photoinitiation or initiator initiation) have a greater impact on the synthesis of intermediate A. Although in terms of reaction mechanism, step A1 can be regarded as a free radical reaction, both photoinitiation and initiator initiation can initiate a free radical reaction. However, the applicant found that the initiation effect of the initiator is far better than that of photoinitiation for the reaction in step A1, and even different types of initiators have different initiation effects. That is, the use of initiators can increase the selectivity of intermediate A. Preferably, the initiator is selected from at least one of di-tert-butyl peroxide, dibenzoyl peroxide, and tert-butyl hydroperoxide. More preferably, the initiator is dibenzoyl peroxide or tert-butyl hydroperoxide.
进一步地,所述1,2-二溴-1-氯-1,2,2-三氟乙烷与引发剂的摩尔配比为1:0.01~1:0.1。作为优选,所述1,2-二溴-1-氯-1,2,2-三氟乙烷与引发剂的摩尔配比为1:0.03~1:0.06。Further, the molar ratio of the 1,2-dibromo-1-chloro-1,2,2-trifluoroethane to the initiator is 1:0.01 to 1:0.1. Preferably, the molar ratio of the 1,2-dibromo-1-chloro-1,2,2-trifluoroethane to the initiator is 1:0.03 to 1:0.06.
在本发明A1步骤的中间体制备过程中,非质子极性溶剂更有利于反应进行。作为优选,所述非质子极性溶剂选自四氢呋喃、1,4-二氧六环、乙腈、二乙二醇二甲醚、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺中的至少一种。更为优选地,所述极性非质子溶剂选自1,4-二氧六环、乙腈、二乙二醇二甲醚中的至少一种。In the preparation process of the intermediate in step A1 of the present invention, the aprotic polar solvent is more conducive to the progress of the reaction. Preferably, the aprotic polar solvent is selected from tetrahydrofuran, 1,4-dioxane, acetonitrile, diethylene glycol dimethyl ether, N,N-dimethylformamide, N,N-dimethyl At least one of acetamide. More preferably, the polar aprotic solvent is selected from at least one of 1,4-dioxane, acetonitrile, and diethylene glycol dimethyl ether.
在本发明A1步骤的中间体制备过程中,惰性气体气氛更有利于反应进行。作为优选,所述惰性气体选自氮气、氦气、氩气中的至少一种。In the preparation process of the intermediate in step A1 of the present invention, the inert gas atmosphere is more conducive to the progress of the reaction. Preferably, the inert gas is selected from at least one of nitrogen, helium, and argon.
在本发明A1步骤的中间体制备过程中,反应液的提纯采用常规的提纯方式即可,如常压精馏或减压精馏。In the preparation process of the intermediate in step A1 of the present invention, the purification of the reaction solution can be carried out by a conventional purification method, such as atmospheric distillation or vacuum distillation.
本发明A2步骤的六氟-1,3-丁二烯制备过程中,反应可以在无溶剂状态下进行。当然,在有机溶剂中反应效果更好。作为优选地,所述有机溶剂选自甲酸、乙酸、三氟乙酸、丙酸、二氯甲烷、氯仿、四氯化碳、二氯乙烷、1,1,1-三氯乙烷、异丙醇、叔丁醇、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、二甲基亚砜、N-甲基吡咯烷酮、六甲基磷酰胺中的至少一种。更为优选地,所述有机溶剂选自乙酸、N,N-二甲基甲酰胺或异丙醇中的至少一种。In the preparation process of hexafluoro-1,3-butadiene in step A2 of the present invention, the reaction can be carried out in a solvent-free state. Of course, the reaction effect is better in organic solvents. Preferably, the organic solvent is selected from formic acid, acetic acid, trifluoroacetic acid, propionic acid, dichloromethane, chloroform, carbon tetrachloride, dichloroethane, 1,1,1-trichloroethane, isopropyl At least one of alcohol, tert-butanol, N,N-dimethylformamide, N,N-dimethylacetamide, dimethylsulfoxide, N-methylpyrrolidone, and hexamethylphosphoramide. More preferably, the organic solvent is selected from at least one of acetic acid, N,N-dimethylformamide or isopropanol.
本发明A2步骤的六氟-1,3-丁二烯制备过程中,在催化剂存在下更有利于反应进行。作为优选,所述催化剂选自氯化锌(ZnCl
2)、溴化锌(ZnBr
2)或碘化锌(ZnI
2)、碘单质,1,2-二溴乙烷中的至少一种;中间体A与催化剂的摩尔配比为1:0.01~1:0.1。更为优选地,中间体A与催化剂的摩尔配比为1:0.03~1:0.06。
In the preparation process of hexafluoro-1,3-butadiene in step A2 of the present invention, the presence of a catalyst is more favorable for the reaction to proceed. Preferably, the catalyst is selected from at least one of zinc chloride (ZnCl 2 ), zinc bromide (ZnBr 2 ) or zinc iodide (ZnI 2 ), elemental iodine, and 1,2-dibromoethane; The molar ratio of body A to catalyst is 1:0.01 to 1:0.1. More preferably, the molar ratio of the intermediate A to the catalyst is 1:0.03 to 1:0.06.
本发明的六氟-1,3-丁二烯的制备方法,作为一种优选的方式,所述A1步骤的反应温度为60℃~200℃,保温反应1~12小时;所述A2步骤的反应温度为40℃~150℃,保温反应1~24小时。In the preparation method of hexafluoro-1,3-butadiene of the present invention, as a preferred mode, the reaction temperature in the A1 step is 60°C to 200°C, and the temperature is kept for 1 to 12 hours; The reaction temperature is 40°C to 150°C, and the reaction is kept for 1 to 24 hours.
作为一种更为优选的方式,所述A1步骤的反应温度为80℃~160℃,保温 反应6~12小时;所述A2步骤的反应温度为60℃~90℃,保温反应3~6小时。As a more preferred way, the reaction temperature in the A1 step is 80°C to 160°C, and the temperature is kept for 6-12 hours; the reaction temperature in the A2 step is 60°C to 90°C, and the temperature is kept for 3 to 6 hours. .
本发明还提供一种1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷的制备方法,所述制备方法包括:The present invention also provides a preparation method of 1,4-dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane, the preparation method comprising:
在极性非质子溶剂中,在引发剂作用下,1,2-二溴-1-氯-1,2,2-三氟乙烷与三氟卤乙烯在惰性气体氛围中反应,反应液经精馏提纯得到1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷;所述三氟卤乙烯的结构式为:CF2=CFX,其中X为Cl、Br或I;In a polar aprotic solvent, under the action of an initiator, 1,2-dibromo-1-chloro-1,2,2-trifluoroethane reacts with trifluoroethylene halide in an inert gas atmosphere. 1,4-Dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane is obtained by distillation and purification; the structural formula of the trifluoroethylene halide is: CF2=CFX , Where X is Cl, Br or I;
所述引发剂选自偶氮二异丁腈(AIBN)、过氧化二叔丁基(DTBP)、过氧化二苯甲酰(BPO)、过氧化二异丙苯(DCP)、叔丁基过氧化氢(TBHP)、过硫酸钾(KPS)、过硫酸铵(APS)中的至少一种。The initiator is selected from azobisisobutyronitrile (AIBN), di-tert-butyl peroxide (DTBP), dibenzoyl peroxide (BPO), dicumyl peroxide (DCP), tert-butyl peroxide At least one of hydrogen oxide (TBHP), potassium persulfate (KPS), and ammonium persulfate (APS).
与现有技术相比,本发明具有的有益效果为:Compared with the prior art, the present invention has the following beneficial effects:
1.本发明采用1,2-二溴-1-氯-1,2,2-三氟乙烷与三氟卤乙烯的调聚反应制备六氟-1,3-丁二烯的中间体,工艺简单、反应条件温和、适合工业化生产。1. The present invention adopts the telomerization reaction of 1,2-dibromo-1-chloro-1,2,2-trifluoroethane and trifluoroethylene to prepare the intermediate of hexafluoro-1,3-butadiene, The process is simple, the reaction conditions are mild, and it is suitable for industrial production.
2.本发明采用自由基引发剂引发调聚反应,不仅可以控制自由基产生速率、调聚反应程度,相较于光引发而言,大大提高了中间体的选择性。2. The present invention uses a free radical initiator to initiate the telomerization reaction, which not only can control the rate of free radical generation and the degree of telomerization reaction, but also greatly improves the selectivity of the intermediate compared with photoinitiation.
下面结合具体实施例来对本发明进行进一步说明,但并不将本发明局限于这些具体实施方式。本领域技术人员应该认识到,本发明涵盖了权利要求书范围内所可能包括的所有备选方案、改进方案和等效方案。The present invention will be further described below in conjunction with specific examples, but the present invention is not limited to these specific embodiments. Those skilled in the art should realize that the present invention covers all alternatives, improvements and equivalents that may be included in the scope of the claims.
实施例1Example 1
本实施例提供一种六氟-1,3-丁二烯的制备方法,所述制备方法包括中间体制备步骤和六氟-1,3-丁二烯制备步骤,具体如下:This embodiment provides a method for preparing hexafluoro-1,3-butadiene. The preparation method includes an intermediate preparation step and a hexafluoro-1,3-butadiene preparation step, which are specifically as follows:
A1. 1,4-二溴-2,3-二氯-1,1,2,3,4,4-六氟丁烷的制备A1. Preparation of 1,4-dibromo-2,3-dichloro-1,1,2,3,4,4-hexafluorobutane
在500mL哈氏合金材质的可承压反应釜中加入乙腈150g、1,2-二溴-1-氯-1,2,2-三氟乙烷69.1g(0.25mol)、过氧化二苯甲酰1.8g(7.5mmol),用高纯 N
2吹扫10分钟,然后将34.8g(0.30mol)三氟氯乙烯从钢瓶灌入反应釜,机械搅拌下(300-500r/min)升温至80℃,反应釜压力升至0.5MPa左右,保温12小时,结束反应。
Add 150g of acetonitrile, 69.1g (0.25mol) of 1,2-dibromo-1-chloro-1,2,2-trifluoroethane, and diphenylmethyl peroxide into a 500mL Hastelloy pressure-bearing reactor 1.8g (7.5mmol) of acyl acid, purged with high-purity N 2 for 10 minutes, then pour 34.8g (0.30mol) of chlorotrifluoroethylene from a steel cylinder into the reactor, and heat up to 80 under mechanical stirring (300-500r/min) ℃, the pressure of the reactor was increased to about 0.5MPa, and the temperature was kept for 12 hours to complete the reaction.
反应液经GC-MS分析,并计算可知:原料1,2-二溴-1-氯-1,2,2-三氟乙烷的转化率为98.75%,中间体1,4-二溴-2,3-二氯-1,1,2,3,4,4-六氟丁烷选择性为59.09%。结果如表1所示。The reaction solution was analyzed by GC-MS, and calculations showed that the conversion rate of the raw material 1,2-dibromo-1-chloro-1,2,2-trifluoroethane was 98.75%, and the intermediate 1,4-dibromo- The selectivity of 2,3-dichloro-1,1,2,3,4,4-hexafluorobutane is 59.09%. The results are shown in Table 1.
反应液经减压精馏获得高纯中间体A。The reaction solution is subjected to vacuum distillation to obtain high-purity intermediate A.
A2.六氟-1,3-丁二烯的制备A2. Preparation of hexafluoro-1,3-butadiene
在装有磁力搅拌、温度计、冷凝器和滴液漏斗的500mL三口烧瓶中加入异丙醇150g,单质碘2.0g,锌粉130g(2.0mol)。冷凝器顶部通过气路与产品收集瓶相连,并将产品收集槽置于低温冷阱中(液氮冷却)。反应瓶升温至70℃,磁力搅拌下滴加1,4-二溴-2,3-二氯-1,1,2,3,4,4-六氟丁烷275g(纯度96%,0.7mol),并收集产品,约1h滴完。滴完后升温至80℃,保温3h,反应完成。在该冷阱中收集的产物经过GC-MS和核磁表征,为六氟-1,3-丁二烯,收得产品97.0g,纯度96.6%,收率86.0%。结果如表3所示。A 500 mL three-necked flask equipped with magnetic stirring, thermometer, condenser and dropping funnel was charged with 150 g of isopropanol, 2.0 g of elemental iodine, and 130 g (2.0 mol) of zinc powder. The top of the condenser is connected to the product collection bottle through a gas path, and the product collection tank is placed in a cryogenic cold trap (liquid nitrogen cooling). The reaction flask was heated to 70°C, and 1,4-dibromo-2,3-dichloro-1,1,2,3,4,4-hexafluorobutane 275g (purity 96%, 0.7mol) was added dropwise under magnetic stirring ), and collect the product, drip it in about 1h. After dripping, the temperature was raised to 80°C and kept for 3h, and the reaction was completed. The product collected in the cold trap was characterized by GC-MS and NMR, and it was hexafluoro-1,3-butadiene. The product obtained was 97.0 g with a purity of 96.6% and a yield of 86.0%. The results are shown in Table 3.
实施例2Example 2
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,改变引发剂种类,用1.1g(7.5mmol)过氧化二叔丁基代替实施例1中的过氧化二苯甲酰。反应结果如表1所示。During the preparation of the intermediate, the type of initiator was changed, and 1.1 g (7.5 mmol) of di-tert-butyl peroxide was used instead of dibenzoyl peroxide in Example 1. The results of the reaction are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,改变催化剂种类,用2.5g碘化锌代替实施例1中的单质碘,获得产品89.20g。结果如表3所示。During the preparation process of hexafluoro-1,3-butadiene, the type of catalyst was changed, and the elemental iodine in Example 1 was replaced with 2.5 g of zinc iodide to obtain 89.20 g of the product. The results are shown in Table 3.
实施例3Example 3
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,改变引发剂种类,用0.68g(7.5mmol)叔丁基过氧化氢代替实施例1中的过氧化二苯甲酰;反应结果如表1所示。During the preparation of the intermediate, the type of initiator was changed, and 0.68 g (7.5 mmol) of tert-butyl hydroperoxide was used instead of dibenzoyl peroxide in Example 1; the reaction results are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,改变催化剂种类,用1.5g 1,2-二溴乙烷代替实施例1中的单质碘,获得产品95.0g。结果如表3所示。In the preparation process of hexafluoro-1,3-butadiene, the type of catalyst was changed, and the elemental iodine in Example 1 was replaced with 1.5 g of 1,2-dibromoethane to obtain 95.0 g of the product. The results are shown in Table 3.
实施例4Example 4
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,反应温度由80℃降为60℃;反应结果如表1所示。During the preparation of the intermediate, the reaction temperature dropped from 80°C to 60°C; the reaction results are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,反应温度由70℃降为60℃,获得产品76.20g。结果如表3所示。During the preparation of hexafluoro-1,3-butadiene, the reaction temperature was reduced from 70°C to 60°C, and 76.20 g of the product was obtained. The results are shown in Table 3.
实施例5Example 5
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,反应温度由80℃升温为100℃。反应结果如表1所示。During the preparation of the intermediate, the reaction temperature increased from 80°C to 100°C. The results of the reaction are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,反应温度由70℃升温为90℃,获得产品101.3g。结果如表3所示。During the preparation process of hexafluoro-1,3-butadiene, the reaction temperature was increased from 70°C to 90°C to obtain 101.3 g of the product. The results are shown in Table 3.
实施例6Example 6
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,改变溶剂种类,用150g二乙二醇二甲醚代替实施例1中的乙腈。反应结果如表1所示。During the preparation of the intermediate, the type of solvent was changed, and 150 g of diethylene glycol dimethyl ether was used instead of acetonitrile in Example 1. The results of the reaction are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,改变溶剂种类,用150g N,N-二甲基乙酰胺代替实施例1中的异丙醇,获得产品80.50g。结果如表3所示。In the preparation process of hexafluoro-1,3-butadiene, the type of solvent was changed, and 150 g of N,N-dimethylacetamide was used instead of isopropanol in Example 1, to obtain 80.50 g of product. The results are shown in Table 3.
实施例7Example 7
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,改变物料配比,三氟氯乙烯用量由原来的34.8g(0.30mol)变为58.0g(0.50mol)。反应结果如表1所示。During the preparation of the intermediate, the material ratio was changed, and the amount of chlorotrifluoroethylene was changed from 34.8g (0.30mol) to 58.0g (0.50mol). The results of the reaction are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,改变物料配比,锌粉用量由原来的130g(2.0mol)变为91.0g(1.4mol)。获得产品68.4g。结果如表3所示。During the preparation of hexafluoro-1,3-butadiene, the material ratio was changed, and the amount of zinc powder was changed from 130g (2.0mol) to 91.0g (1.4mol). 68.4 g of product was obtained. The results are shown in Table 3.
实施例8Example 8
本实施例提供一种六氟-1,3-丁二烯的制备方法,所述制备方法包括中间体制备步骤和六氟-1,3-丁二烯制备步骤,具体如下:This embodiment provides a method for preparing hexafluoro-1,3-butadiene. The preparation method includes an intermediate preparation step and a hexafluoro-1,3-butadiene preparation step, which are specifically as follows:
A1. 1,2,4-三溴-3-氯-1,1,2,3,4,4-六氟丁烷的制备A1. Preparation of 1,2,4-tribromo-3-chloro-1,1,2,3,4,4-hexafluorobutane
在500mL哈氏合金材质的可承压反应釜中加入乙腈150g、1,2-二溴-1-氯-1,2,2-三氟乙烷69.1g(0.25mol)、过氧化二叔丁基1.1g(7.5mmol),用高纯N2吹扫10分钟,然后将48.3g(0.30mol)三氟溴乙烯从钢瓶灌入反应釜,机械搅拌下(300-500r/min)升温至100℃,反应釜压力升至0.6MPa左右,保温12小时,结束反应。Add 150g of acetonitrile, 69.1g (0.25mol) of 1,2-dibromo-1-chloro-1,2,2-trifluoroethane, and di-tert-butyl peroxide to a 500mL Hastelloy pressure-bearable reactor Base 1.1g (7.5mmol), purged with high-purity N2 for 10 minutes, then pour 48.3g (0.30mol) of bromotrifluoroethylene from a steel cylinder into the reaction kettle, and heat up to 100℃ under mechanical stirring (300-500r/min) , The pressure of the reactor is increased to about 0.6MPa, and the temperature is kept for 12 hours to complete the reaction.
反应液经GC-MS分析,并计算可知:原料1,2-二溴-1-氯-1,2,2-三氟乙烷的转化率为97.6%,中间体1,2,4-三溴-3-氯-1,1,2,3,4,4-六氟丁烷的选择性为73.9%。结果如表2所示。The reaction liquid was analyzed by GC-MS, and calculations showed that the conversion rate of the raw material 1,2-dibromo-1-chloro-1,2,2-trifluoroethane was 97.6%, and the intermediate 1,2,4-trifluoroethane The selectivity of bromo-3-chloro-1,1,2,3,4,4-hexafluorobutane is 73.9%. The results are shown in Table 2.
反应液经减压精馏获得高纯中间体A。The reaction solution is subjected to vacuum distillation to obtain high-purity intermediate A.
A2.六氟-1,3-丁二烯的制备A2. Preparation of hexafluoro-1,3-butadiene
在装有磁力搅拌、温度计、冷凝器和滴液漏斗的500mL三口烧瓶中加入乙酸150g,单质碘2.0g,锌粉130g(2.0mol)。冷凝器顶部通过气路与产品收集瓶相连,并将产品收集槽置于低温冷阱中(液氮冷却)。反应瓶升温至60℃,磁力搅拌下滴加1,2,4-三溴-3-氯-1,1,2,3,4,4-六氟丁烷312.3g(纯度98%,0.7mol),并收集产品,约2h滴完。滴完后升温至80℃,保温3h,反应完成。在该冷阱中收集的产物经过GC-MS和核磁表征,为六氟-1,3-丁二烯,收得产品78.20g,纯度97.5%,收率69.9%。结果如表3所示。In a 500 mL three-necked flask equipped with magnetic stirring, thermometer, condenser and dropping funnel, 150 g of acetic acid, 2.0 g of elemental iodine, and 130 g (2.0 mol) of zinc powder were added. The top of the condenser is connected to the product collection bottle through a gas path, and the product collection tank is placed in a cryogenic cold trap (liquid nitrogen cooling). The reaction flask was heated to 60°C, and 312.3g of 1,2,4-tribromo-3-chloro-1,1,2,3,4,4-hexafluorobutane (purity 98%, 0.7mol) was added dropwise under magnetic stirring ), and collect the product, drip it in about 2h. After dripping, the temperature was raised to 80°C and kept for 3h, and the reaction was completed. The product collected in the cold trap was characterized by GC-MS and NMR, and it was hexafluoro-1,3-butadiene. The obtained product was 78.20 g with a purity of 97.5% and a yield of 69.9%. The results are shown in Table 3.
实施例9Example 9
本实施例的操作同实施例8,区别仅在于:The operation of this embodiment is the same as that of Embodiment 8. The only difference is:
在中间体制备过程中,改变溶剂种类,用150g二乙二醇二甲醚代替实施例7中的乙腈。反应结果如表2所示。During the preparation of the intermediate, the type of solvent was changed, and the acetonitrile in Example 7 was replaced with 150 g of diethylene glycol dimethyl ether. The results of the reaction are shown in Table 2.
在六氟-1,3-丁二烯制备过程中,改变溶剂种类,用150g N,N-二甲基乙酰 胺代替实施例7中的乙酸,获得产品82.50g。结果如表3所示。In the process of preparing hexafluoro-1,3-butadiene, the type of solvent was changed, and 150 g of N,N-dimethylacetamide was used instead of acetic acid in Example 7 to obtain 82.50 g of product. The results are shown in Table 3.
实施例10Example 10
本实施例的操作同实施例8,区别仅在于:The operation of this embodiment is the same as that of Embodiment 8. The only difference is:
在中间体制备过程中,反应温度由100℃升温为160℃。反应结果如表2所示。During the preparation of the intermediate, the reaction temperature increased from 100°C to 160°C. The results of the reaction are shown in Table 2.
在六氟-1,3-丁二烯制备过程中,改变催化剂种类,用2.5g碘化锌代替实施例7中的单质碘,获得产品72.2g。结果如表3所示。In the process of preparing hexafluoro-1,3-butadiene, the type of catalyst was changed, 2.5 g of zinc iodide was used instead of elemental iodine in Example 7, to obtain 72.2 g of product. The results are shown in Table 3.
实施例11Example 11
本实施例的操作同实施例8,区别仅在于:The operation of this embodiment is the same as that of Embodiment 8. The only difference is:
在中间体制备过程中,改变物料配比,三氟溴乙烯用量由原来的48.3g(0.30mol)变为40.3g(0.25mol)。反应结果如表2所示。During the preparation of the intermediate, the material ratio was changed, and the amount of bromotrifluoroethylene was changed from 48.3g (0.30mol) to 40.3g (0.25mol). The results of the reaction are shown in Table 2.
在六氟-1,3-丁二烯制备过程中,增加催化剂碘单质用量,由原来的2.0g增加至4.0g,获得产品74.5g。结果如表3所示。In the preparation process of hexafluoro-1,3-butadiene, the amount of iodine element of the catalyst was increased from the original 2.0g to 4.0g to obtain 74.5g of the product. The results are shown in Table 3.
对比例1Comparative example 1
本实施例的操作同实施例1,区别仅在于:The operation of this embodiment is the same as that of Embodiment 1, the only difference is:
在中间体制备过程中,不加入引发剂过氧化二苯甲酰。反应结果如表1所示。During the preparation of the intermediate, the initiator dibenzoyl peroxide is not added. The results of the reaction are shown in Table 1.
在六氟-1,3-丁二烯制备过程中,不加入催化剂单质碘,获得产品78.50g。结果如表3所示。During the preparation process of hexafluoro-1,3-butadiene, without adding catalyst elemental iodine, 78.50 g of the product was obtained. The results are shown in Table 3.
对比例2Comparative example 2
在带有夹套冷阱的玻璃光反应装置中,加入1,2-二溴-1-氯-1,2,2-三氟乙烷276.3g(1.0mol),插入400W紫外高压汞灯。开启低温循环(0℃),打开高压汞灯,将三氟氯乙烯缓慢通入(50mL/min),共通入139.2g(1.2mol),约10小时通完。通完后关闭高压汞灯和低温循环,反应液经GC-MS分析,并计算可知:原料1,2-二溴-1-氯-1,2,2-三氟乙烷的转化率为54.5%,中间体1,4-二溴-2,3-二氯-1,1,2,3,4,4-六氟丁烷的选择性为38.2%。结果如表1所示。Add 276.3g (1.0mol) of 1,2-dibromo-1-chloro-1,2,2-trifluoroethane into a glass photoreactor with a jacket cold trap, and insert a 400W ultraviolet high-pressure mercury lamp. Turn on the low-temperature cycle (0°C), turn on the high-pressure mercury lamp, and slowly feed chlorotrifluoroethylene (50 mL/min), a total of 139.2 g (1.2 mol), and complete the flow in about 10 hours. Turn off the high-pressure mercury lamp and low-temperature circulation after the passage, the reaction liquid is analyzed by GC-MS, and calculations show that the conversion rate of the raw material 1,2-dibromo-1-chloro-1,2,2-trifluoroethane is 54.5 %, the selectivity of intermediate 1,4-dibromo-2,3-dichloro-1,1,2,3,4,4-hexafluorobutane is 38.2%. The results are shown in Table 1.
表1以三氟氯乙烯为原料,调聚反应结果Table 1 The result of telomerization reaction with chlorotrifluoroethylene as raw material
备注:a.组分中除去溶剂峰和三氟氯乙烯;Remarks: a. Remove the solvent peak and chlorotrifluoroethylene from the components;
b.各物料色谱含量与实际含量未校正。b. The chromatographic content and actual content of each material are not corrected.
表2以三氟溴乙烯为原料,调聚反应结果表Table 2 The result of telomerization reaction with bromotrifluoroethylene as raw material
备注:a.组分中除去溶剂峰和三氟溴乙烯峰;Remarks: a. Remove the solvent peak and bromotrifluoroethylene peak from the components;
b.各物料色谱含量与实际含量未校正。b. The chromatographic content and actual content of each material are not corrected.
表3脱卤反应结果表Table 3 Dehalogenation reaction result table
Claims (10)
- 一种六氟-1,3-丁二烯的制备方法,其特征在于:所述制备方法包括以下步骤:A preparation method of hexafluoro-1,3-butadiene, characterized in that: the preparation method comprises the following steps:A1.在极性非质子溶剂中,在引发剂作用下,1,2-二溴-1-氯-1,2,2-三氟乙烷与三氟卤乙烯反应,反应液经提纯得到1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷;所述三氟卤乙烯的结构式为:CF 2=CFX,其中X为Cl、Br或I; A1. In a polar aprotic solvent, under the action of an initiator, 1,2-dibromo-1-chloro-1,2,2-trifluoroethane reacts with trifluoroethylene halide, and the reaction solution is purified to obtain 1 ,4-Dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane; the structural formula of the trifluoroethylene halide is: CF 2 =CFX, where X is Cl, Br or I;所述引发剂选自偶氮二异丁腈、过氧化二叔丁基、过氧化二苯甲酰、过氧化二异丙苯、叔丁基过氧化氢、过硫酸钾、过硫酸铵中的至少一种;The initiator is selected from the group consisting of azobisisobutyronitrile, di-tert-butyl peroxide, dibenzoyl peroxide, dicumyl peroxide, tert-butyl hydroperoxide, potassium persulfate, and ammonium persulfate At least oneA2.1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷与锌粉经脱卤反应获得六氟-1,3-丁二烯。A2.1,4-Dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane and zinc powder undergo dehalogenation reaction to obtain hexafluoro-1,3-butane Diene.
- 根据权利要求1所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述1,2-二溴-1-氯-1,2,2-三氟乙烷与引发剂的摩尔配比为1:0.01~1:0.1。The method for preparing hexafluoro-1,3-butadiene according to claim 1, characterized in that: the 1,2-dibromo-1-chloro-1,2,2-trifluoroethane and the initiator The molar ratio of the agent is 1:0.01 to 1:0.1.
- 根据权利要求1所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述A1步骤在惰性气体氛围中反应,惰性气体选自氮气、氦气、氩气中的至少一种。The method for preparing hexafluoro-1,3-butadiene according to claim 1, wherein the A1 step is reacted in an inert gas atmosphere, and the inert gas is selected from at least nitrogen, helium, and argon. A sort of.
- 根据权利要求3所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述极性非质子溶剂选自四氢呋喃、1,4-二氧六环、乙腈、二乙二醇二甲醚、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺中的至少一种。The method for preparing hexafluoro-1,3-butadiene according to claim 3, wherein the polar aprotic solvent is selected from tetrahydrofuran, 1,4-dioxane, acetonitrile, diethylenediene At least one of dimethyl ether, N,N-dimethylformamide, and N,N-dimethylacetamide.
- 根据权利要求1所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述A2步骤在催化剂存在下反应,所述催化剂选自溴化锌、碘化锌或碘单质中的至少一种。The method for preparing hexafluoro-1,3-butadiene according to claim 1, wherein the step A2 is reacted in the presence of a catalyst, and the catalyst is selected from zinc bromide, zinc iodide or iodine. At least one of them.
- 根据权利要求5所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷与催化剂的摩尔配比为1:0.01~1:0.1。The method for preparing hexafluoro-1,3-butadiene according to claim 5, wherein the 1,4-dibromo-2-chloro-3-halo-1,1,2,3 The molar ratio of 4,4-hexafluorobutane to catalyst is 1:0.01 to 1:0.1.
- 根据权利要求1所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述A2步骤在有机溶剂中反应,所述有机溶剂选自甲酸、乙酸、三氟乙酸、丙酸、二氯甲烷、氯仿、四氯化碳、二氯乙烷、1,1,1-三氯乙烷、异丙醇、叔丁醇、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、二甲基亚砜、N-甲基吡咯烷酮或六甲基磷酰 胺中的至少一种。The method for preparing hexafluoro-1,3-butadiene according to claim 1, wherein the step A2 is reacted in an organic solvent, and the organic solvent is selected from the group consisting of formic acid, acetic acid, trifluoroacetic acid, propylene Acid, dichloromethane, chloroform, carbon tetrachloride, dichloroethane, 1,1,1-trichloroethane, isopropanol, tert-butanol, N,N-dimethylformamide, N,N -At least one of dimethylacetamide, dimethylsulfoxide, N-methylpyrrolidone or hexamethylphosphoramide.
- 根据权利要求1所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述A1步骤的反应温度为60℃~200℃,保温反应1~12小时;所述A2步骤的反应温度为40℃~150℃,保温反应1~24小时。The method for preparing hexafluoro-1,3-butadiene according to claim 1, wherein the reaction temperature in the A1 step is 60°C to 200°C, and the temperature is kept for 1 to 12 hours; the A2 step The reaction temperature is 40°C to 150°C, and the temperature is kept for 1 to 24 hours.
- 根据权利要求8所述的六氟-1,3-丁二烯的制备方法,其特征在于:所述A1步骤的反应温度为80℃~160℃,保温反应6~12小时;所述A2步骤的反应温度为60℃~90℃,保温反应3~6小时。The method for preparing hexafluoro-1,3-butadiene according to claim 8, wherein the reaction temperature in the A1 step is 80°C to 160°C, and the temperature is kept for 6 to 12 hours; the A2 step The reaction temperature is 60°C to 90°C, and the reaction is kept warm for 3 to 6 hours.
- 一种1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷的制备方法,其特征在于:所述制备方法包括:A preparation method of 1,4-dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane, characterized in that: the preparation method comprises:在极性非质子溶剂中,在引发剂作用下,1,2-二溴-1-氯-1,2,2-三氟乙烷与三氟卤乙烯在惰性气体氛围中反应,反应液经精馏提纯得到1,4-二溴-2-氯-3-卤代-1,1,2,3,4,4-六氟丁烷;所述三氟卤乙烯的结构式为:CF 2=CFX,其中X为Cl、Br或I; In a polar aprotic solvent, under the action of an initiator, 1,2-dibromo-1-chloro-1,2,2-trifluoroethane reacts with trifluoroethylene halide in an inert gas atmosphere. 1,4-Dibromo-2-chloro-3-halo-1,1,2,3,4,4-hexafluorobutane is obtained by distillation and purification; the structural formula of the trifluoroethylene halide is: CF 2 = CFX, where X is Cl, Br or I;所述引发剂选自偶氮二异丁腈、过氧化二叔丁基、过氧化二苯甲酰、过氧化二异丙苯、叔丁基过氧化氢、过硫酸钾、过硫酸铵中的至少一种。The initiator is selected from the group consisting of azobisisobutyronitrile, di-tert-butyl peroxide, dibenzoyl peroxide, dicumyl peroxide, tert-butyl hydroperoxide, potassium persulfate, and ammonium persulfate At least one.
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