WO2008022233A1 - Extraction process using an ionic liquid - Google Patents
Extraction process using an ionic liquid Download PDFInfo
- Publication number
- WO2008022233A1 WO2008022233A1 PCT/US2007/076061 US2007076061W WO2008022233A1 WO 2008022233 A1 WO2008022233 A1 WO 2008022233A1 US 2007076061 W US2007076061 W US 2007076061W WO 2008022233 A1 WO2008022233 A1 WO 2008022233A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- cycloalkane
- separation
- ionic liquid
- cycloalkanone
- cycloalkanol
- Prior art date
Links
- 239000002608 ionic liquid Substances 0.000 title claims abstract description 116
- 238000000605 extraction Methods 0.000 title description 4
- 238000000926 separation method Methods 0.000 claims abstract description 115
- 239000000203 mixture Substances 0.000 claims abstract description 91
- 238000000034 method Methods 0.000 claims abstract description 71
- 230000008569 process Effects 0.000 claims abstract description 62
- 239000012454 non-polar solvent Substances 0.000 claims abstract description 60
- 150000002576 ketones Chemical class 0.000 claims abstract description 53
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 52
- 150000001924 cycloalkanes Chemical group 0.000 claims description 83
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexyloxide Natural products O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 claims description 51
- 238000009826 distribution Methods 0.000 claims description 28
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 claims description 26
- 238000007254 oxidation reaction Methods 0.000 claims description 20
- 230000003647 oxidation Effects 0.000 claims description 19
- 125000004432 carbon atom Chemical group C* 0.000 claims description 18
- -1 N-Methyl-N'-butylimidazolium tetrafluoroborate Chemical compound 0.000 claims description 16
- IQQRAVYLUAZUGX-UHFFFAOYSA-N 1-butyl-3-methylimidazolium Chemical compound CCCCN1C=C[N+](C)=C1 IQQRAVYLUAZUGX-UHFFFAOYSA-N 0.000 claims description 11
- 125000000217 alkyl group Chemical group 0.000 claims description 9
- 150000001450 anions Chemical class 0.000 claims description 9
- FGGJBCRKSVGDPO-UHFFFAOYSA-N hydroperoxycyclohexane Chemical compound OOC1CCCCC1 FGGJBCRKSVGDPO-UHFFFAOYSA-N 0.000 claims description 9
- HSLXOARVFIWOQF-UHFFFAOYSA-N bis(trifluoromethylsulfonyl)azanide;1-butyl-1-methylpyrrolidin-1-ium Chemical compound CCCC[N+]1(C)CCCC1.FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F HSLXOARVFIWOQF-UHFFFAOYSA-N 0.000 claims description 7
- 150000001768 cations Chemical class 0.000 claims description 7
- ITMCEJHCFYSIIV-UHFFFAOYSA-M triflate Chemical compound [O-]S(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-M 0.000 claims description 7
- SXVPOSFURRDKBO-UHFFFAOYSA-N Cyclododecanone Chemical group O=C1CCCCCCCCCCC1 SXVPOSFURRDKBO-UHFFFAOYSA-N 0.000 claims description 6
- RJMNDNYSRMKWON-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;2-methoxyethanesulfonate Chemical compound COCCS([O-])(=O)=O.CCCCN1C=C[N+](C)=C1 RJMNDNYSRMKWON-UHFFFAOYSA-M 0.000 claims description 5
- HBVMIVDRXXVSTN-UHFFFAOYSA-M 1-ethyl-3-methylimidazol-3-ium;2-methoxyethanesulfonate Chemical compound CCN1C=C[N+](C)=C1.COCCS([O-])(=O)=O HBVMIVDRXXVSTN-UHFFFAOYSA-M 0.000 claims description 5
- INDFXCHYORWHLQ-UHFFFAOYSA-N bis(trifluoromethylsulfonyl)azanide;1-butyl-3-methylimidazol-3-ium Chemical compound CCCCN1C=C[N+](C)=C1.FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F INDFXCHYORWHLQ-UHFFFAOYSA-N 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 5
- KYCQOKLOSUBEJK-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;bromide Chemical compound [Br-].CCCCN1C=C[N+](C)=C1 KYCQOKLOSUBEJK-UHFFFAOYSA-M 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- RWRDLPDLKQPQOW-UHFFFAOYSA-O Pyrrolidinium ion Chemical compound C1CC[NH2+]C1 RWRDLPDLKQPQOW-UHFFFAOYSA-O 0.000 claims description 4
- GNWJDYQCOZNHPC-UHFFFAOYSA-N bis(trifluoromethylsulfonyl)azanide;1-ethylpyridin-1-ium Chemical compound CC[N+]1=CC=CC=C1.FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F GNWJDYQCOZNHPC-UHFFFAOYSA-N 0.000 claims description 4
- 238000000354 decomposition reaction Methods 0.000 claims description 4
- RAXXELZNTBOGNW-UHFFFAOYSA-O Imidazolium Chemical compound C1=C[NH+]=CN1 RAXXELZNTBOGNW-UHFFFAOYSA-O 0.000 claims description 3
- 150000008051 alkyl sulfates Chemical class 0.000 claims description 3
- DDTBPAQBQHZRDW-UHFFFAOYSA-N cyclododecane Chemical group C1CCCCCCCCCCC1 DDTBPAQBQHZRDW-UHFFFAOYSA-N 0.000 claims description 3
- SFVWPXMPRCIVOK-UHFFFAOYSA-N cyclododecanol Chemical compound OC1CCCCCCCCCCC1 SFVWPXMPRCIVOK-UHFFFAOYSA-N 0.000 claims description 3
- XYFCBTPGUUZFHI-UHFFFAOYSA-O phosphonium Chemical compound [PH4+] XYFCBTPGUUZFHI-UHFFFAOYSA-O 0.000 claims description 3
- UGNONFHRNZDGBX-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;1,1-diethoxypropane-2-sulfonate Chemical compound CCCCN1C=C[N+](C)=C1.CCOC(OCC)C(C)S([O-])(=O)=O UGNONFHRNZDGBX-UHFFFAOYSA-M 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 claims description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 claims description 2
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910052796 boron Inorganic materials 0.000 claims description 2
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 claims description 2
- 150000004820 halides Chemical class 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 150000002367 halogens Chemical class 0.000 claims description 2
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 claims description 2
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 150000002739 metals Chemical class 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 229910052711 selenium Inorganic materials 0.000 claims description 2
- 239000011669 selenium Substances 0.000 claims description 2
- 229910052710 silicon Inorganic materials 0.000 claims description 2
- 239000010703 silicon Substances 0.000 claims description 2
- 229910052714 tellurium Inorganic materials 0.000 claims description 2
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 claims description 2
- BRYVPURDEAOXCY-UHFFFAOYSA-M 2-ethoxyethanesulfonate;1-ethyl-3-methylimidazol-3-ium Chemical compound CCN1C=C[N+](C)=C1.CCOCCS([O-])(=O)=O BRYVPURDEAOXCY-UHFFFAOYSA-M 0.000 claims 1
- OEYIOHPDSNJKLS-UHFFFAOYSA-N choline Chemical compound C[N+](C)(C)CCO OEYIOHPDSNJKLS-UHFFFAOYSA-N 0.000 claims 1
- 125000002243 cyclohexanonyl group Chemical group *C1(*)C(=O)C(*)(*)C(*)(*)C(*)(*)C1(*)* 0.000 claims 1
- 239000012071 phase Substances 0.000 description 51
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 29
- 239000007788 liquid Substances 0.000 description 27
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 14
- 150000001335 aliphatic alkanes Chemical class 0.000 description 12
- 239000007791 liquid phase Substances 0.000 description 12
- ZPVFWPFBNIEHGJ-UHFFFAOYSA-N 2-octanone Chemical compound CCCCCCC(C)=O ZPVFWPFBNIEHGJ-UHFFFAOYSA-N 0.000 description 10
- 238000002156 mixing Methods 0.000 description 9
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 125000001424 substituent group Chemical group 0.000 description 8
- 238000004821 distillation Methods 0.000 description 7
- 239000012074 organic phase Substances 0.000 description 7
- 238000011084 recovery Methods 0.000 description 7
- 239000002904 solvent Substances 0.000 description 7
- 238000000638 solvent extraction Methods 0.000 description 7
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 6
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 6
- 125000000753 cycloalkyl group Chemical group 0.000 description 6
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000000622 liquid--liquid extraction Methods 0.000 description 5
- ZXMGHDIOOHOAAE-UHFFFAOYSA-N 1,1,1-trifluoro-n-(trifluoromethylsulfonyl)methanesulfonamide Chemical compound FC(F)(F)S(=O)(=O)NS(=O)(=O)C(F)(F)F ZXMGHDIOOHOAAE-UHFFFAOYSA-N 0.000 description 4
- 125000002015 acyclic group Chemical group 0.000 description 4
- 239000008346 aqueous phase Substances 0.000 description 4
- XFXJXURAALDGSW-UHFFFAOYSA-N bis(trifluoromethylsulfonyl)azanide;2-hydroxyethyl(trimethyl)azanium Chemical compound C[N+](C)(C)CCO.FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F XFXJXURAALDGSW-UHFFFAOYSA-N 0.000 description 4
- 238000005191 phase separation Methods 0.000 description 4
- PYRYLYCORAEDGW-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;2-ethoxyethanesulfonate Chemical compound CCOCCS([O-])(=O)=O.CCCCN1C=C[N+](C)=C1 PYRYLYCORAEDGW-UHFFFAOYSA-M 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 235000011037 adipic acid Nutrition 0.000 description 3
- 239000001361 adipic acid Substances 0.000 description 3
- 125000004122 cyclic group Chemical group 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 125000005843 halogen group Chemical group 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- WXTXWUNHUKLSJD-UHFFFAOYSA-M 1-butyl-3-methylimidazol-3-ium;1-(1-methoxypropoxy)propane-1-sulfonate Chemical compound CCCCN1C=C[N+](C)=C1.CCC(OC)OC(CC)S([O-])(=O)=O WXTXWUNHUKLSJD-UHFFFAOYSA-M 0.000 description 2
- HLYLNDDPVBJRRG-UHFFFAOYSA-N 2-ethoxyethanesulfonic acid Chemical compound CCOCCS(O)(=O)=O HLYLNDDPVBJRRG-UHFFFAOYSA-N 0.000 description 2
- KBPHGUKTJKPERJ-UHFFFAOYSA-N 2-methoxyethanesulfonic acid Chemical compound COCCS(O)(=O)=O KBPHGUKTJKPERJ-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical class CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- CCIVGXIOQKPBKL-UHFFFAOYSA-M ethanesulfonate Chemical compound CCS([O-])(=O)=O CCIVGXIOQKPBKL-UHFFFAOYSA-M 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000007429 general method Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical class CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- BOENUIDIZIOASJ-UHFFFAOYSA-N 1,1-diethoxypropane-2-sulfonic acid Chemical compound CCOC(OCC)C(C)S(O)(=O)=O BOENUIDIZIOASJ-UHFFFAOYSA-N 0.000 description 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- NWKBDKPPNZZFRF-UHFFFAOYSA-N 1-(1-methoxyethoxy)ethanesulfonic acid Chemical compound COC(C)OC(C)S(O)(=O)=O NWKBDKPPNZZFRF-UHFFFAOYSA-N 0.000 description 1
- SGDLPOAAMXJFNX-UHFFFAOYSA-N 1-(1-methoxypropoxy)propane-1-sulfonic acid Chemical compound CCC(OC)OC(CC)S(O)(=O)=O SGDLPOAAMXJFNX-UHFFFAOYSA-N 0.000 description 1
- OIDIRWZVUWCCCO-UHFFFAOYSA-N 1-ethylpyridin-1-ium Chemical compound CC[N+]1=CC=CC=C1 OIDIRWZVUWCCCO-UHFFFAOYSA-N 0.000 description 1
- UAZWQYISMNDYAT-UHFFFAOYSA-N 2-(2-methoxyethoxy)ethanesulfonic acid Chemical compound COCCOCCS(O)(=O)=O UAZWQYISMNDYAT-UHFFFAOYSA-N 0.000 description 1
- GIDLTZLKUNAAFU-UHFFFAOYSA-N 3-(3-methoxypropoxy)propane-1-sulfonic acid Chemical compound COCCCOCCCS(O)(=O)=O GIDLTZLKUNAAFU-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- OPAGFYQFLVPPKG-UHFFFAOYSA-N C(C)OC(CS(=O)(=O)OC)OCC.C[N+]1=CN(C=C1)CCCC Chemical compound C(C)OC(CS(=O)(=O)OC)OCC.C[N+]1=CN(C=C1)CCCC OPAGFYQFLVPPKG-UHFFFAOYSA-N 0.000 description 1
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 1
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 1
- BDAGIHXWWSANSR-UHFFFAOYSA-M Formate Chemical compound [O-]C=O BDAGIHXWWSANSR-UHFFFAOYSA-M 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical class CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000001204 arachidyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- QWJNFFYFEKXZBF-UHFFFAOYSA-N cyanocyanamide Chemical compound N#CNC#N QWJNFFYFEKXZBF-UHFFFAOYSA-N 0.000 description 1
- 150000001923 cyclic compounds Chemical class 0.000 description 1
- 125000001995 cyclobutyl group Chemical group [H]C1([H])C([H])([H])C([H])(*)C1([H])[H] 0.000 description 1
- 125000000582 cycloheptyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 125000006547 cyclononyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C([H])([H])C1([H])[H] 0.000 description 1
- 125000000640 cyclooctyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C([H])([H])C1([H])[H] 0.000 description 1
- 125000001511 cyclopentyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C1([H])[H] 0.000 description 1
- 125000001559 cyclopropyl group Chemical group [H]C1([H])C([H])([H])C1([H])* 0.000 description 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 150000008040 ionic compounds Chemical class 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- QXDLXKIRMWCNGZ-UHFFFAOYSA-N methyl 2,2-diethoxyethanesulfonate Chemical compound CCOC(OCC)CS(=O)(=O)OC QXDLXKIRMWCNGZ-UHFFFAOYSA-N 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 125000001400 nonyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 125000002347 octyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 125000001147 pentyl group Chemical group C(CCCC)* 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 125000001889 triflyl group Chemical group FC(F)(F)S(*)(=O)=O 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
- C07C45/80—Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0492—Applications, solvents used
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B63/00—Purification; Separation; Stabilisation; Use of additives
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
- C07C29/86—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by liquid-liquid treatment
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/125—Monohydroxylic acyclic alcohols containing five to twenty-two carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/14—The ring being saturated
Definitions
- the present invention relates to the separation of alcohols and ketones in a mixture with a non-polar solvent, such as an alkane, using an ionic liquid.
- the invention particularly relates to the separation of cycloalkanols, cycloalkanones and cycloalkanes.
- the oxidation of cyclohexane and subsequent separation of a mixture of cyclohexanone and cyclohexanol from unreacted cyclohexane is a key step in the manufacture of both adipic acid and caprolactam.
- the primary industrial use of caprolactam is as a monomer in the production of nylon-6.
- Adipic acid is a monomer used in the production of nylon-6,6 amongst other applications.
- the oxidation of cyclohexane is carried out at a relatively low conversion of less than 10%.
- the primary oxidation products of cyclohexane are cyclohexane hydroperoxide, cyclohexanol and cyclohexanone.
- cyclohexyl hydroperoxide is then decomposed to cyclohexanol and cyclohexanone, either in the reactor or in a separate unit operation. This process as a whole can be described for the purposes of the present invention as the cyclohexane oxidation process.
- the desired final oxidation product after decomposition of cyclohexyl hydroperoxide is a mixture of primarily cyclohexanone and cyclohexanol.
- the mixture must then be separated from the unreacted cyclohexane whereby the unreacted cyclohexane can then typically be recycled to the oxidation reaction.
- caprolactam requires cyclohexanone as a starting material that is substantially free of cyclohexanol.
- this level of purity is achieved commercially through distillation, which again is an energy intensive process.
- Liquid-liquid or solvent separation also known as liquid-liquid or solvent extraction processes are well known in the art as processes for the separation of components of a mixture.
- Liquid-liquid separation is based on the transfer of component(s) from one liquid phase into another liquid phase and is used to separate component(s) selectively from a mixture.
- Mixing two immiscible liquids leads to a phase separation, and the formation of two liquid layers, also known as phases or fractions. The less dense liquid will form the upper layer, and the more dense liquid will form the lower layer.
- Liquid-liquid separation relies on the different relative solubilities of a component in two immiscible liquids.
- liquid- liquid separation utilises a water-based, or aqueous, phase and an organic phase (comprising an organic solvent) that is substantially immiscible in water.
- an organic phase comprising an organic solvent
- the aqueous phase and the organic phase are mixed with, for example, an aqueous solution of two separable components, if one of the separable components is more soluble in the organic phase it will be separated and become dissolved in the organic phase.
- Liquid- liquid separation can be a powerful technique provided suitable liquids are used.
- the traditional aqueous phase / organic phase separation would not be possible for the separation of a cycloalkanol and a cycloalkanone from a cycloalkane because all three of these components would dissolve more readily in the organic phase.
- Liquid-liquid extraction technology can also be carried out using two organic phases which are substantially immiscible with each other and in one of which the solubility of the component to be extracted is much greater than the other.
- a disadvantage of liquid-liquid extraction technology is that final recovery of the components extracted from the initial mixture can be complicated by the volatility of the extracting solvent. Typically final recovery of the components of interest is earned out by distillation, but often the extracting solvent is of comparable volatility to the desired product. Therefore, recovery of the component of interest can be very difficult, and process may also be energy intensive in terms of steam requirements. It is a feature of the present invention that such limitations are avoided by the use of Ionic Liquid(s) as the extracting solvent.
- Ionic Liquids are substantially non-volatile, they do not interfere with the recovery of the component of interest during final recovery. Recovery of said component may, therefore, be effected by simple flash recovery without the need for complicated separation technology with a corresponding reduction in energy (e.g., steam) requirements.
- caprolactam manufacture requires only cyclohexanone as a starting material.
- this separation is carried out by distillation wherein the separation of cyclohexanone from cyclohexanol requires significant energy and a high capital investment in the distillation column required.
- Liquid-liquid extraction technology is not conventionally used for the separation of cyclohexanone and cyclohexanol since, for this application, it is a requirement of the extraction solvent that it selectively removes one component only from the mixture.
- Conventional solvents which are suitable for use in a solvent extraction process will not selectively extract cyclohexanol from cyclohexanone.
- a distribution coefficient for a given separable component can be quoted as a measure of the extent to which a separable component is separated.
- the distribution coefficient is equal to the concentration of the separable component in the organic-based phase divided by the concentration of the separable component in the aqueous phase.
- the distribution coefficient can be a function of a number of different parameters e.g. temperature.
- the object of the present invention is to provide an improved method for the separation of an alcohol from a ketone in a mixture of these compounds in a non-polar solvent, and for the separation of an alcohol and/or a ketone from a non-polar solvent. It is a particular object of this invention to provide an improved method for the separation of a cycloalkanol from a cycloalkanone in a mixture of these compounds in a non-polar solvent (such as a cycloalkane), and for the separation of a cycloalkanol and/or a cycloalkanone from a non-polar solvent (such as a cycloalkane).
- a non-polar solvent such as a cycloalkane
- alcohol encompasses acyclic and cyclic aliphatic alcohols, and in one embodiment refers to an (alkyl-OH) group, and in an alternative embodiment to a (cycloalkyl-OH) group, i.e. a "cycloalkanol”.
- alkane refers to (alkyl-H) and the term “cycloalkane” refers to (cycloalkyl-H).
- alkyl refers to a straight-chain or branched-chain saturated monovalent hydrocarbon radical, and particularly one having from 1 to 20 carbon atoms.
- suitable alkyl groups include methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, nonyl, dodecyl and eicosyl.
- Said alkyl groups may be substituted by one or more halogen atoms, the same or different, but are preferably unsubstituted.
- cycloalkyl refers to a cyclic saturated monovalent hydrocarbon radical, having 3-20 carbon atoms.
- suitable cycloalkyl groups include cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, cyclononyl and cyclododecyl.
- the cycloalkyl groups contain from 5 to 12 carbon atoms.
- Said cycloalkyl groups may be substituted by one or more halogen atoms, the same or different, but are preferably unsubstituted.
- non-polar solvent refers to a compound which is immiscible with an ionic liquid.
- non-polar solvent refers to a solvent which has a dielectric constant of no more than 5, preferably no more than 3.0, more preferably no more than 2.5, measured at 20 0 C and atmospheric pressure according to ASTM D924-92.
- non-polar solvent refers to cyclic and acyclic aliphatic hydrocarbons, and particularly cyclic and acyclic saturated aliphatic hydrocarbons, i.e.
- alkanes and cycloalkanes such as pentanes, hexanes, heptanes, octanes and cyclohexane etc.
- Said non-polar aliphatic hydrocarbons may be substituted by one or more halogen atoms, the same or different, but are preferably unsubstituted.
- said alcohol contains a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the ketone and/or alkane present in the mixture to be separated
- said ketone has a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the alcohol and/or the alkane present in the mixture to be separated.
- said cycloalkanol contains a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the cycloalkanone and/or cycloalkane present in the mixture to be separated
- said cycloalkanone has a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the cycloalkanol and/or the cycloalkane present in the mixture to be separated.
- the invention encompasses:
- said alcohol and said ketone may themselves have different numbers of carbon atoms to each other, but typically they will have the same number of carbon atoms.
- a method for the use of at least one ionic liquid for the separation of an alcohol and/or ketone from a non- polar solvent, or for the separation of an alcohol from a ketone in a mixture of these compounds in a non-polar solvent particularly when said alcohol is a cycloalkanol and said ketone is a cycloalkanone, and particularly when said alcohol is a cycloalkanol and said ketone is a cycloalkanone and said non-polar solvent is a cycloalkane.
- the cycloalkyl groups contain 6 carbon atoms, in which case the separation process described herein is particularly concerned with the separation of a cyclohexanol and/or a cyclohexanone from a cyclohexane, and with the separation of a cyclohexanol from a cyclohexanone and a cyclohexane.
- the cycloalkyl groups contain 12 carbon atoms, in which case the separation process described herein is particularly concerned with the separation of a cyclododecanol and/or a cyclododecanone from a cyclododecane, and with the separation of a cyclododecanol from a cyclododecanone and a cyclododecane.
- the mixture to be separated can therefore comprise, for instance, a cycloalkanol and a cycloalkane; or a cycloalkanone and a cycloalkane; or a cycloalkanol and a cycloalkanone and a cycloalkane.
- the process of the present invention involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a non-polar solvent phase, such as an organic hydrocarbon-based phase, that is substantially immiscible in the ionic liquid-based phase.
- a non-polar solvent phase such as an organic hydrocarbon-based phase
- substantially immiscible is intended to mean immiscible to the extent that two separate phases are formed.
- the process of the present invention thus relies upon the different relative solubility/solubilities of the component/components to be separated, i.e. the separable component(s), in the ionic liquid-based phase and the non-polar solvent phase.
- a separable component will partition itself between the ionic liquid-based phase and the non-polar solvent phase in such a way that more of the or each separable component will be dissolved in the ionic liquid-based phase.
- the ionic liquid(s) and the mixture comprising an alcohol and/or a ketone in a non-polar solvent is referred to herein as the "separation mixture”.
- the term "contacting" is intended to mean the bringing together of the ionic liquid(s) with said mixture comprising an alcohol and/or a ketone in a non-polar solvent to form the separation mixture.
- the ionic liquid(s) and said mixture comprising an alcohol and/or a ketone in a non-polar solvent can be contacted in a container (i.e., reaction vessel) that is suitable for said contact.
- the separation mixture is shaken, mixed or stirred vigorously for a period of time, hereinafter referred to as the contacting time, to allow thorough dispersion of the ionic liquid(s) throughout said mixture comprising an alcohol and/or a ketone in a non-polar solvent.
- the contacting time is too short, the ionic liquid(s) will not be fully dispersed throughout said mixture comprising an alcohol and/or a ketone in a non-polar solvent, and separation of the separable component(s) will be inefficient, i.e. only a small proportion of the separable component(s) present in the separation mixture will be separated.
- the contacting time of the separation mixture will increase the dispersion of the ionic liquid(s) and said mixture comprising an alcohol and/or a ketone in a non-polar solvent, and the efficiency of the separation will be increased, i.e. a larger proportion of the separable component(s) in the separation mixture will be separated.
- This increase of separation efficiency with contacting time will occur until a maximum possible proportion of the total volume of separable component(s) has been separated for the separation conditions used (e.g. type of ionic liquid, temperature etc) i.e. maximum separation has been obtained.
- the contacting time is preferably greater than 30 seconds, more preferably greater than 60 seconds and typically not greater than 5 minutes, although longer times periods may be used with satisfactory results.
- the separation mixture is allowed to settle for another period of time, hereinafter referred to as the "settling time".
- the separation mixture will separate into an ionic-liquid based phase and a non-polar solvent-based phase.
- the settling time should be long enough to allow the ionic liquid-based phase and the non-polar solvent-based phase to fully separate, at which point the system is described as being in equilibrium.
- the settling time is preferably longer than 1 minute, more preferably longer than 2 minutes and typically no longer than 10 minutes, although longer times periods may be used with satisfactory results.
- the mixture comprising an alcohol and/or a ketone in a non-polar solvent, and particularly at least one of a cycloalkanol and a cycloalkanone in a cycloalkane may be formed by an oxidation step preceding the separation process.
- the oxidation step may be, but is not limited to, oxidation with air alone or in the presence of a cobalt or other transition metal catalyst followed by decomposition of the resulting cyclohexyl hydroperoxide, either thermally or through other catalytic means.
- an oxidation step followed by a cyclohexyl hydroperoxide decomposition step followed by a separation, or contacting, step is defined as one oxidation and separation cycle.
- a plurality of oxidation and separation cycles can be carried out.
- a cycloalkane-based phase or fraction resulting from the separation may be recycled for further oxidation.
- the ionic liquid-based phase can be physically separated from the non-polar solvent-based phase.
- This physical separation can be earned out using any suitable apparatus
- the separable component(s) e.g. a cycloalkanol and/or a cycloalkanone, can be removed from the ionic liquid-based phase and said ionic liquid(s) can be recycled and re-used, for example, in a further separation step.
- Stage-wise operations typically involve a mixing step followed by a phase separation, or settling, step in devices generally known as mixer-settlers. Operations can be carried out in sequential batch fashion, in which case it is common for the same vessel to serve alternating functions of mixing and settling. Operations can also be carried out with continuous flow, for which the mixing and settling steps are usually, but not always performed in separate vessels. In continuous flow systems the necessary mixing time and settling time are obtained by proper sizing of equipment volume or holdup.
- Examples of commercial mixing equipment known to those skilled in the art includes in-line static mixers, jet mixers, injectors, orifices or mixing nozzles, valves, centrifugal pumps, agitated line mixers, packed tubes, mechanically agitated vessels, gas or vapor agitated vessels, and vessels with circulating flow loops.
- Examples of commercial settling equipment known to those skilled in the art includes gravity settlers, decanters, centrifugal cyclones, centrifuges, and settler auxiliaries such as coalescers, separating membranes, and electrical field devices (for electrically conducting emulsions or dispersions). Any type of mixer and settler can be combined to produce a stage. Stages can be arranged in a multi-stage cascade to achieve additional separation efficiency. Multi-stage arrangements can employ a variety of liquid flow schemes such as counter-current flow, co-current flow, cross-current flow, staged-flow, and so forth. Compact equipment consisting of alternative mixing and settling elements can be constructed.
- Continuous (differential) contacting equipment is usually arranged for multistage counter-current contact of insoluble liquids without repeated complete separation of the liquids from each other between stages. However it may also be arranged co- current or cross current. The liquids remain in continuous contact with each other throughout the equipment. Counter-current flow is maintained by differences in densities of the liquids in conjunction with gravity or centrifugal force.
- gravity-operated extractors such as spray towers, packed towers, or sieve tray towers
- gravity-operated extractors with mechanical agitation such as towers with rotating stirrers, rotary-disk contactors, Mixco (Oldshue-Rushton) multiple-mixer columns, Scheibel columns, Kuhni contactor columns, liquid pulsed towers, and reciprocating plate columns
- centrifugal extractors such as spray towers, packed towers, or sieve tray towers
- gravity-operated extractors with mechanical agitation such as towers with rotating stirrers, rotary-disk contactors, Mixco (Oldshue-Rushton) multiple-mixer columns, Scheibel columns, Kuhni contactor columns, liquid pulsed towers, and reciprocating plate columns
- centrifugal extractors such as spray towers, packed towers, or sieve tray towers
- gravity-operated extractors with mechanical agitation such as towers with rotating stirrers, rotary-
- the separation process of the present invention may form one or more separation steps in the manufacture of adipic acid or caprolactam.
- the separation steps of these processes have traditionally been performed by distillation.
- the separable component is a cycloalkanone which is separated from a cycloalkane.
- the ionic liquid(s) is contacted with a mixture of the cycloalkanone and the cycloalkane.
- the ionic liquid(s) and the mixture of the cycloalkanone and the cycloalkane is known as separation mixture (a).
- the process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase.
- the distribution coefficient of the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5 and preferably greater than 3.
- the separable component is a cycloalkanol which is separated from a cycloalkane.
- the ionic liquid(s) is contacted with a mixture of the cycloalkanol and the cycloalkane.
- the ionic liquid(s) and the mixture of the cycloalkanol and the cycloalkane is known as separation mixture (b).
- the process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase.
- the distribution coefficient of the cycloalkanol between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5 and preferably greater than 3.
- the separable component is a cycloalkanol which is separated from a mixture of a cycloalkanone and a cycloalkane.
- the ionic liquid(s) is contacted with a mixture of the cycloalkanol, the cycloalkanone and the cycloalkane.
- the ionic liquid(s) and the mixture of the cycloalkanol, the cycloalkanone and the cycloalkane is known as separation mixture (c).
- the process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid- based phase, and the other liquid phase is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase.
- the separation of a cycloalkanol from a cycloalkanone and a cycloalkane according to the process in this embodiment can be achieved when the distribution coefficient for the cycloalkanol between the ionic liquid- based phase and the cycloalkane- -based phase is greater than 1, and the distribution coefficient for the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is less than 1.
- This embodiment has application to the separation of cyclohexanol from cyclohexanone for caprolactam manufacture.
- the distribution coefficient of the cycloalkanol between the ionic liquid- based phase and the cycloalkane-based is greater than 1.5 and preferably greater than 3.
- the separable components are a mixture of a cycloalkanone and a cycloalkanol which are separated from a cycloalkane.
- the ionic liquid(s) is contacted with a mixture of the cycloalkanol, the cycloalkanone and the cycloalkane.
- the ionic liquid(s) and the mixture of the cycloalkanol, the cycloalkanone and the cycloalkane is known as separation mixture (d).
- the process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase.
- the distribution coefficient of the cycloalkanol and the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5 and preferably greater than 3.
- the mixtures to be separated may also contain materials other than the cycloalkanol, cycloalkanone and cycloalkane components.
- these other materials will either remain in the cycloalkane-based phase or be separated into the ionic liquid-based phase along with the separable component.
- cyclohexylhydroperoxide (CHHP) may be present in the separation mixture of cyclohexanol, cyclohexanone and cyclohexane. In these circumstances, CHHP would be separated with the cyclohexanol and/or cyclohexanone into the ionic liquid-based phase.
- ionic liquid(s) of the present invention may consist of a single ionic liquid or a mixture of two or more ionic liquids, i.e. a mixture of 2, 3, 4, 5, 6 etc different ionic liquids. Typically, one or two, and typically only one ionic liquid is used.
- the ionic liquid(s) comprises a cation selected from one or more of 1- alkylpyridinium, alkyl- or poly-alkylpyridinium, phosphonium (PR 4 + ), alkyl- or polyalkylphosphonium, imidazolium, alkyl- or polyalkylimidazolium, ammonium (NR 4 + ), alkyl- or polyalkylammonium, alkyl- or polyalkylpyrazolium, alkyl- or polyalkylpyrrolidinium, alkyl or polyalkylazepinium, alkyloxonium or alkysulfonium.
- a cation selected from one or more of 1- alkylpyridinium, alkyl- or poly-alkylpyridinium, phosphonium (PR 4 + ), alkyl- or polyalkylphosphonium, imidazolium, alkyl- or polyalkylimidazolium, ammonium (NR 4 +
- Each R group of the phosphonium and ammonium cations may be separately selected from the group of substituents consisting of hydrogen, hydroxyl, alkyl, alkyl ethers, alkyl esters, alkyl amides, alkyl carboxylic acids, or sulfonate.
- the ionic liquid(s) comprises a cation selected from one or more of 1-alkylpyridinium, alkyl- or poly-alkylpyridinium, imidazolium, alkyl- or polyalkylimidazolium.
- the cations of each of the ionic liquids present in the mixture may be the same or different.
- the anion of the ionic liquid(s) is selected from one or more of a halide, preferably chloride, bromide or iodide, a nitrate, an alkylsulfate or alkyl polyalkoxysulfate, such as methanesulfonate, trifluoromethanesulfonate and hydrogensulfonate, anions based on nitrogen, phosphorous, boron, silicon, selenium, tellurium, halogens, and oxoanions of metals.
- a halide preferably chloride, bromide or iodide
- a nitrate such as methanesulfonate, trifluoromethanesulfonate and hydrogensulfonate
- anions based on nitrogen, phosphorous, boron, silicon, selenium, tellurium, halogens, and oxoanions of metals preferably one or more of a halide, preferably chlor
- Suitable anions include, but are not limited to bis(trifluoromethylsulfonyl)amide (NTf 2 " ), tetrafluoroborate (BF 4 " ), trifluoromethylsulfonyl (Tf), methoxyethylsulfonate, 2-methoxyethylsulfonate, ethoxyethylsulfonate, 2-ethoxyethylsulfonate, (methoxypropoxy)propylsulfonate, 1-(1- methoxypropoxy)-propylsulfonate, (methoxyethoxy)-ethylsulfonate, 1-(1- methoxyethoxy)-ethylsulfonate, methyl (diethoxy)ethylsulfonate, 1- methyl(diethoxy)ethylsulfonate, carboxylate, formate, acetate, dicyanimide and trifluoromethanesul
- the anion of the ionic liquid(s) is selected from one or more of an alkylsulfate or alkyl polyalkoxysulfate, bis(trifluoromethylsulfonyl)amide (NTf 2 " ) and tetrafluoroborate (BF 4 " ).
- the anion of each of the ionic liquids present in the mixture may be the same or different.
- the ionic liquid(s) will comprise at least one C 2 - C 6 alkyl group.
- the C 2 - C 6 alkyl group may be a substituent on either the anion or the cation of the ionic liquid(s). More preferably the C 2 - C 6 alkyl group is a substituent on the cation of the ionic liquid(s).
- the ionic liquid(s) consists of a single ionic liquid
- the single ionic liquid present preferably contains at least one C 2 - C 6 alkyl group substituent.
- the ionic liquid(s) consists of two or more ionic liquids
- at least one of the ionic liquids present contains at least one C 2 - C 6 alkyl group substituent
- more preferably two or more of the ionic liquids present contain at least one C 2 - C 6 alkyl group substituent, i.e. 2, 3, 4, 5 etc of the ionic liquids present contain at least one C 2 - C 6 alkyl group substituent.
- all the ionic liquids present in the at least on ionic liquid contain at least one C 2 - C 6 alkyl group substituent.
- the ionic liquid(s) of the present invention is preferably selected from the group consisting of N-ethylpyridinium bis(trifluoromethanesulfonyl)amide;
- N-Methyl-N'-butylimidazolium bromide N-Methyl-N'-butylimidazolium 2-ethoxyethylsulfonate;
- the ionic liquid(s) is N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide or N-Methyl-N'-butylimidazolium 1-(1- methoxypropoxy)-propylsulfonate.
- Ionic liquids most suitable for the separation of an alcohol from a non-polar solvent are:
- Ionic liquids most suitable for the separation of an alcohol from a mixture of a non-polar solvent and a ketone, particularly wherein said alcohol is a cycloalkanol
- Ionic liquids most suitable for the separation of a ketone from a non-polar solvent are: N-ethylpyridinium bis(trifluoromethanesulfonyl)amide;
- Ionic liquids most suitable for the separation of a mixture of an alcohol and a ketone from a non-polar solvent particularly when said alcohol is a cycloalkanol (and particularly cyclohexanol) and said ketone is a cycloalkanone (particularly cyclohexanone) and said non-polar solvent is a cycloalkane (particularly a cyclohexane) are:
- ionic liquid refers to an ionic compound which is liquid below 100 0 C.
- the term "distribution coefficient" referring to the liquid-liquid separation refers to the concentration of the separable component in the ionic liquid- based phase divided by the concentration of the separable component in the non-polar solvent-based phase. These concentrations are measured subsequent to settling, i.e. when the separation mixture has reached equilibrium subsequent to the vigorous shaking.
- the present invention is exemplified through separation of cyclohexanol and cyclohexanone from cyclohexane using a general method followed by calculation of the resulting distribution coefficient.
- equal volumes of cyclohexane and ionic liquid have been used.
- the volume of ionic liquid used would preferably be a small fraction of the volume of cyclohexane.
- the distribution coefficient is independent of volume, the data obtained for equivolume experiments will be relevant to industrial application in which the volumes of ionic liquid and cyclohexane may not be equivalent.
- the general method used for all the examples was as follows.
- Hnmr Hydrophilicity-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl-N-phenyl
- Table 1 details the results of the specific examples with comparisons to water and DMSO (dimethyl sulfoxide), where D is the distribution coefficient.
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Abstract
A process for the separation of an alcohol from a non-polar solvent; a ketone from a non-polar solvent; an alcohol from a mixture of a ketone and a non-polar solvent; or a mixture of an alcohol and a ketone from a non-polar solvent; said process comprising contacting at least one ionic liquid with a mixture comprising a non-polar solvent and at least one of an alcohol and a ketone.
Description
EXTRACTION PROCESS
CROSS-REFERENCE TO RELATED APPLICATIONS
This application claims benefit of priority from Provisional Application No.
60/838,957 filed August 18, 2006 and Provisional Application No. 60/901,053 filed February 12, 2007. This application hereby incorporates by reference Provisional Application No. 60/901,053 in its entirety.
FIELD OF THE INVENTION
The present invention relates to the separation of alcohols and ketones in a mixture with a non-polar solvent, such as an alkane, using an ionic liquid. The invention particularly relates to the separation of cycloalkanols, cycloalkanones and cycloalkanes.
BACKGROUND
The oxidation of cyclohexane and subsequent separation of a mixture of cyclohexanone and cyclohexanol from unreacted cyclohexane is a key step in the manufacture of both adipic acid and caprolactam. The primary industrial use of caprolactam is as a monomer in the production of nylon-6. Adipic acid is a monomer used in the production of nylon-6,6 amongst other applications.
Conventionally, the oxidation of cyclohexane is carried out at a relatively low conversion of less than 10%. The primary oxidation products of cyclohexane are cyclohexane hydroperoxide, cyclohexanol and cyclohexanone. In a typical commercial cyclohexane oxidation process cyclohexyl hydroperoxide is then decomposed to cyclohexanol and cyclohexanone, either in the reactor or in a separate unit operation. This process as a whole can be described for the purposes of the present invention as the cyclohexane oxidation process. The desired final oxidation product after decomposition of cyclohexyl hydroperoxide is a mixture of primarily cyclohexanone and cyclohexanol. The mixture must then be separated from the unreacted cyclohexane whereby the unreacted cyclohexane can then typically be recycled to the oxidation reaction. This
separation is commercially carried out by distillation, and since the great majority of the cyclohexane is recycled, it is this process step which accounts for a high proportion of process steam usage.
Therefore, there is a need for alternative separation technology that can reduce steam usage and, as a consequence, reduce the substantial energy cost associated with separation through distillation.
In addition, the process for manufacturing caprolactam requires cyclohexanone as a starting material that is substantially free of cyclohexanol. Currently, this level of purity is achieved commercially through distillation, which again is an energy intensive process.
Separation
Liquid-liquid or solvent separation (also known as liquid-liquid or solvent extraction) processes are well known in the art as processes for the separation of components of a mixture. Liquid-liquid separation is based on the transfer of component(s) from one liquid phase into another liquid phase and is used to separate component(s) selectively from a mixture. Mixing two immiscible liquids leads to a phase separation, and the formation of two liquid layers, also known as phases or fractions. The less dense liquid will form the upper layer, and the more dense liquid will form the lower layer. Liquid-liquid separation relies on the different relative solubilities of a component in two immiscible liquids. In particular, if the soluble component is allowed to mix freely with two immiscible liquids, it will partition between the two
liquid phases thus formed such that the component will generally be dissolved in one of the liquid phases to a greater extent than in the other liquid phase. Generally, liquid- liquid separation utilises a water-based, or aqueous, phase and an organic phase (comprising an organic solvent) that is substantially immiscible in water. In this instance, when the aqueous phase and the organic phase are mixed with, for example, an aqueous solution of two separable components, if one of the separable components is more soluble in the organic phase it will be separated and become dissolved in the organic phase. Assuming that the other separable component is more soluble in the aqueous phase, then the two separable components will have been separated. Liquid- liquid separation can be a powerful technique provided suitable liquids are used. The traditional aqueous phase / organic phase separation would not be possible for the separation of a cycloalkanol and a cycloalkanone from a cycloalkane because all three of these components would dissolve more readily in the organic phase.
Liquid-liquid extraction technology can also be carried out using two organic phases which are substantially immiscible with each other and in one of which the solubility of the component to be extracted is much greater than the other. A disadvantage of liquid-liquid extraction technology is that final recovery of the components extracted from the initial mixture can be complicated by the volatility of the extracting solvent. Typically final recovery of the components of interest is earned out by distillation, but often the extracting solvent is of comparable volatility to the desired product. Therefore, recovery of the component of interest can be very difficult, and process may also be energy intensive in terms of steam requirements. It is a feature of the present invention that such limitations are avoided by the use of Ionic Liquid(s) as the extracting solvent. Because Ionic Liquids are substantially non-volatile, they do not interfere with the recovery of the component of interest during final recovery. Recovery of said component may, therefore, be effected by simple flash recovery without the need for complicated separation technology with a corresponding reduction in energy (e.g., steam) requirements.
For the manufacture of caprolactam from the oxidation of cyclohexane, it is further necessary to separate cyclohexanol from cyclohexanone, either directly from a mixture of the two or in the presence of cyclohexane. This is because caprolactam
manufacture requires only cyclohexanone as a starting material. Conventionally, this separation is carried out by distillation wherein the separation of cyclohexanone from cyclohexanol requires significant energy and a high capital investment in the distillation column required. Liquid-liquid extraction technology is not conventionally used for the separation of cyclohexanone and cyclohexanol since, for this application, it is a requirement of the extraction solvent that it selectively removes one component only from the mixture. Conventional solvents which are suitable for use in a solvent extraction process will not selectively extract cyclohexanol from cyclohexanone.
In liquid-liquid separation, a distribution coefficient for a given separable component can be quoted as a measure of the extent to which a separable component is separated. In traditional liquid-liquid separation, the distribution coefficient is equal to the concentration of the separable component in the organic-based phase divided by the concentration of the separable component in the aqueous phase. The distribution coefficient can be a function of a number of different parameters e.g. temperature.
SUMMARY OF THE INVENTION
The object of the present invention is to provide an improved method for the separation of an alcohol from a ketone in a mixture of these compounds in a non-polar solvent, and for the separation of an alcohol and/or a ketone from a non-polar solvent. It is a particular object of this invention to provide an improved method for the separation of a cycloalkanol from a cycloalkanone in a mixture of these compounds in a non-polar solvent (such as a cycloalkane), and for the separation of a cycloalkanol and/or a cycloalkanone from a non-polar solvent (such as a cycloalkane).
DETAILED DESCRIPTION OF THE INVENTION
According to the present invention, there is provided a process for the separation of an alcohol from a non-polar solvent; a ketone from a non-polar solvent; an alcohol from a mixture of a ketone and a non-polar solvent; or a mixture of an alcohol and a ketone from a non-polar solvent;
said process comprising contacting at least one ionic liquid with a mixture comprising a non-polar solvent and at least one of an alcohol and a ketone.
As used herein, the term "alcohol" encompasses acyclic and cyclic aliphatic alcohols, and in one embodiment refers to an (alkyl-OH) group, and in an alternative embodiment to a (cycloalkyl-OH) group, i.e. a "cycloalkanol".
As used herein, the term "ketone" encompasses acyclic and cyclic aliphatic ketones, and in one embodiment refers to an (alkyl-(C=O)-alkyl) group and in an alternative embodiment to a cyclic compound corresponding to a cycloalkane wherein a
(CH2) group is replaced with a (C=O) group, i.e. a "cycloalkanone".
As used herein, the term "alkane" refers to (alkyl-H) and the term "cycloalkane" refers to (cycloalkyl-H).
As used herein, the term "alkyl" refers to a straight-chain or branched-chain saturated monovalent hydrocarbon radical, and particularly one having from 1 to 20 carbon atoms. By way of non-limiting example, suitable alkyl groups include methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, nonyl, dodecyl and eicosyl. Said alkyl groups may be substituted by one or more halogen atoms, the same or different, but are preferably unsubstituted.
As used herein, the term "cycloalkyl" refers to a cyclic saturated monovalent hydrocarbon radical, having 3-20 carbon atoms. By way of non-limiting example, suitable cycloalkyl groups include cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, cyclononyl and cyclododecyl. Preferably, the cycloalkyl groups contain from 5 to 12 carbon atoms. Said cycloalkyl groups may be substituted by one or more halogen atoms, the same or different, but are preferably unsubstituted.
As used herein, the term "non-polar solvent" refers to a compound which is immiscible with an ionic liquid. In one embodiment, the term "non-polar solvent" refers to a solvent which has a dielectric constant of no more than 5, preferably no more than 3.0, more preferably no more than 2.5, measured at 200C and atmospheric pressure
according to ASTM D924-92. In a preferred embodiment, the term "non-polar solvent" refers to cyclic and acyclic aliphatic hydrocarbons, and particularly cyclic and acyclic saturated aliphatic hydrocarbons, i.e. alkanes and cycloalkanes, such as pentanes, hexanes, heptanes, octanes and cyclohexane etc. Said non-polar aliphatic hydrocarbons may be substituted by one or more halogen atoms, the same or different, but are preferably unsubstituted.
Thus, in one embodiment of the present invention, there is provided a process for the separation of: a cycloalkanol from a non-polar solvent; a cycloalkanone from a non-polar solvent; a cycloalkanol from a mixture of a cycloalkanone and a non-polar solvent; or a mixture of a cycloalkanol and a cycloalkanone from a non-polar solvent; said process comprising contacting at least one ionic liquid with a mixture comprising a non-polar solvent and at least one of a cycloalkanol and a cycloalkanone.
In a further embodiment of the present invention, there is provided a process for the separation of an alcohol from an alkane; a ketone from an alkane; an alcohol from a mixture of a ketone and an alkane; or a mixture of an alcohol and a ketone from an alkane; particularly wherein said alcohol and said ketone are acyclic, said process comprising contacting at least one ionic liquid with a mixture comprising an alkane and at least one of an alcohol and a ketone.
In this embodiment, said alcohol contains a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the ketone and/or alkane present in the mixture to be separated, and said ketone has a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the alcohol and/or the alkane present in the mixture to be separated.
In a particularly preferred embodiment of the present invention, there is provided a process for the separation of a cycloalkanol from a cycloalkane; a cycloalkanone from a cycloalkane; a cycloalkanol from a mixture of a cycloalkanone and a cycloalkane; or a mixture of a cycloalkanol and a cycloalkanone from a cycloalkane; said process comprising contacting at least one ionic liquid with a mixture comprising a cycloalkane and at least one of a cycloalkanol and a cycloalkanone.
In this embodiment, said cycloalkanol contains a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the cycloalkanone and/or cycloalkane present in the mixture to be separated, and said cycloalkanone has a number of carbon atoms which may be different to, but is preferably the same as, the number of carbon atoms in the cycloalkanol and/or the cycloalkane present in the mixture to be separated.
Thus, the invention encompasses:
(i) processes for the separation of an alcohol and/or a ketone from the corresponding aliphatic hydrocarbon, i.e. the alkane or cycloalkane having the corresponding number of carbon atoms, and for the separation of said alcohol from said corresponding ketone and aliphatic hydrocarbon;
(ii) processes for the separation of an alcohol and/or a ketone from an aliphatic hydrocarbon (e.g. an alkane or cycloalkane) which has a different number of carbon atoms, and for the separation of said alcohol from said ketone and aliphatic hydrocarbon; and
(iii) processes for the separation of an alcohol and/or a ketone from a non-polar solvent as defined herein, and for the separation of said alcohol from said corresponding ketone and non-polar solvent.
Moreover, in the processes described under (ii) and (iii) above, said alcohol and said ketone may themselves have different numbers of carbon atoms to each other, but typically they will have the same number of carbon atoms.
According to the present invention there is further provided a method for the use of at least one ionic liquid for the separation of an alcohol and/or ketone from a non- polar solvent, or for the separation of an alcohol from a ketone in a mixture of these compounds in a non-polar solvent, particularly when said alcohol is a cycloalkanol and said ketone is a cycloalkanone, and particularly when said alcohol is a cycloalkanol and said ketone is a cycloalkanone and said non-polar solvent is a cycloalkane.
In one embodiment, the cycloalkyl groups contain 6 carbon atoms, in which case the separation process described herein is particularly concerned with the separation of a cyclohexanol and/or a cyclohexanone from a cyclohexane, and with the separation of a cyclohexanol from a cyclohexanone and a cyclohexane.
In another embodiment, the cycloalkyl groups contain 12 carbon atoms, in which case the separation process described herein is particularly concerned with the separation of a cyclododecanol and/or a cyclododecanone from a cyclododecane, and with the separation of a cyclododecanol from a cyclododecanone and a cyclododecane.
Thus, the mixture to be separated can therefore comprise, for instance, a cycloalkanol and a cycloalkane; or a cycloalkanone and a cycloalkane; or a cycloalkanol and a cycloalkanone and a cycloalkane.
The process of the present invention involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a non-polar solvent phase, such as an organic hydrocarbon-based phase, that is substantially immiscible in the ionic liquid-based phase. As used herein, the term "substantially immiscible" is intended to mean immiscible to the extent that two separate phases are formed. The process of the present invention thus relies upon the different relative solubility/solubilities of the component/components to be separated, i.e. the separable component(s), in the ionic liquid-based phase and the non-polar solvent phase. In particular, a separable component will partition itself between the ionic liquid-based phase and the non-polar solvent phase in such a way that more of the or each separable component will be dissolved in the ionic liquid-based phase.
Once brought into contact, the ionic liquid(s) and the mixture comprising an alcohol and/or a ketone in a non-polar solvent (e.g. a cycloalkanol and/or a cycloalkanone in a cycloalkane) is referred to herein as the "separation mixture". As used herein, the term "contacting" is intended to mean the bringing together of the ionic liquid(s) with said mixture comprising an alcohol and/or a ketone in a non-polar solvent to form the separation mixture. The ionic liquid(s) and said mixture comprising an alcohol and/or a ketone in a non-polar solvent can be contacted in a container (i.e., reaction vessel) that is suitable for said contact.
Typically, the separation mixture is shaken, mixed or stirred vigorously for a period of time, hereinafter referred to as the contacting time, to allow thorough dispersion of the ionic liquid(s) throughout said mixture comprising an alcohol and/or a ketone in a non-polar solvent. It will be appreciated that if the contacting time is too short, the ionic liquid(s) will not be fully dispersed throughout said mixture comprising an alcohol and/or a ketone in a non-polar solvent, and separation of the separable component(s) will be inefficient, i.e. only a small proportion of the separable component(s) present in the separation mixture will be separated. Increasing the contacting time of the separation mixture will increase the dispersion of the ionic liquid(s) and said mixture comprising an alcohol and/or a ketone in a non-polar solvent, and the efficiency of the separation will be increased, i.e. a larger proportion of the separable component(s) in the separation mixture will be separated. This increase of separation efficiency with contacting time will occur until a maximum possible proportion of the total volume of separable component(s) has been separated for the separation conditions used (e.g. type of ionic liquid, temperature etc) i.e. maximum separation has been obtained. At this point, contacting the separation mixture for any longer would not provide any benefit to the separation of the separable component(s). Therefore, as used herein, the contacting time is preferably greater than 30 seconds, more preferably greater than 60 seconds and typically not greater than 5 minutes, although longer times periods may be used with satisfactory results.
Subsequent to the vigorous shaking, mixing or stirring, the separation mixture is allowed to settle for another period of time, hereinafter referred to as the "settling time". During the settling time the separation mixture will separate into an ionic-liquid based
phase and a non-polar solvent-based phase. The settling time should be long enough to allow the ionic liquid-based phase and the non-polar solvent-based phase to fully separate, at which point the system is described as being in equilibrium. The settling time is preferably longer than 1 minute, more preferably longer than 2 minutes and typically no longer than 10 minutes, although longer times periods may be used with satisfactory results.
The mixture comprising an alcohol and/or a ketone in a non-polar solvent, and particularly at least one of a cycloalkanol and a cycloalkanone in a cycloalkane, may be formed by an oxidation step preceding the separation process. For instance, in the case of the oxidation of a cycloalkane such as cyclohexane as described hereinabove, the oxidation step may be, but is not limited to, oxidation with air alone or in the presence of a cobalt or other transition metal catalyst followed by decomposition of the resulting cyclohexyl hydroperoxide, either thermally or through other catalytic means. For the puiposes of this invention, an oxidation step followed by a cyclohexyl hydroperoxide decomposition step followed by a separation, or contacting, step is defined as one oxidation and separation cycle. A plurality of oxidation and separation cycles can be carried out. In this instance, a cycloalkane-based phase or fraction resulting from the separation may be recycled for further oxidation.
In addition, following the separation step, the ionic liquid-based phase can be physically separated from the non-polar solvent-based phase. This physical separation can be earned out using any suitable apparatus Furthermore, the separable component(s), e.g. a cycloalkanol and/or a cycloalkanone, can be removed from the ionic liquid-based phase and said ionic liquid(s) can be recycled and re-used, for example, in a further separation step.
Commercial equipment for liquid-liquid extraction contacting and separation may be generally classified into two categories: stage-wise and continuous (differential) contacting. Stage-wise operations typically involve a mixing step followed by a phase separation, or settling, step in devices generally known as mixer-settlers. Operations can be carried out in sequential batch fashion, in which case it is common for the same vessel to serve alternating functions of mixing and settling. Operations can also be
carried out with continuous flow, for which the mixing and settling steps are usually, but not always performed in separate vessels. In continuous flow systems the necessary mixing time and settling time are obtained by proper sizing of equipment volume or holdup. Examples of commercial mixing equipment known to those skilled in the art includes in-line static mixers, jet mixers, injectors, orifices or mixing nozzles, valves, centrifugal pumps, agitated line mixers, packed tubes, mechanically agitated vessels, gas or vapor agitated vessels, and vessels with circulating flow loops. Examples of commercial settling equipment known to those skilled in the art includes gravity settlers, decanters, centrifugal cyclones, centrifuges, and settler auxiliaries such as coalescers, separating membranes, and electrical field devices (for electrically conducting emulsions or dispersions). Any type of mixer and settler can be combined to produce a stage. Stages can be arranged in a multi-stage cascade to achieve additional separation efficiency. Multi-stage arrangements can employ a variety of liquid flow schemes such as counter-current flow, co-current flow, cross-current flow, staged-flow, and so forth. Compact equipment consisting of alternative mixing and settling elements can be constructed.
Continuous (differential) contacting equipment is usually arranged for multistage counter-current contact of insoluble liquids without repeated complete separation of the liquids from each other between stages. However it may also be arranged co- current or cross current. The liquids remain in continuous contact with each other throughout the equipment. Counter-current flow is maintained by differences in densities of the liquids in conjunction with gravity or centrifugal force. Commercial equipment known to those skilled in the art includes gravity-operated extractors such as spray towers, packed towers, or sieve tray towers; gravity-operated extractors with mechanical agitation such as towers with rotating stirrers, rotary-disk contactors, Mixco (Oldshue-Rushton) multiple-mixer columns, Scheibel columns, Kuhni contactor columns, liquid pulsed towers, and reciprocating plate columns; and centrifugal extractors.
The separation process of the present invention may form one or more separation steps in the manufacture of adipic acid or caprolactam. The separation steps of these processes have traditionally been performed by distillation.
In embodiment (a) the separable component is a cycloalkanone which is separated from a cycloalkane. The ionic liquid(s) is contacted with a mixture of the cycloalkanone and the cycloalkane. In this embodiment, the ionic liquid(s) and the mixture of the cycloalkanone and the cycloalkane is known as separation mixture (a).
The process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase. In this embodiment, the distribution coefficient of the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5 and preferably greater than 3.
In embodiment (b), the separable component is a cycloalkanol which is separated from a cycloalkane. The ionic liquid(s) is contacted with a mixture of the cycloalkanol and the cycloalkane. In this embodiment, the ionic liquid(s) and the mixture of the cycloalkanol and the cycloalkane is known as separation mixture (b). The process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase. In this embodiment, the distribution coefficient of the cycloalkanol between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5 and preferably greater than 3.
In embodiment (c) the separable component is a cycloalkanol which is separated from a mixture of a cycloalkanone and a cycloalkane. The ionic liquid(s) is contacted with a mixture of the cycloalkanol, the cycloalkanone and the cycloalkane. In this embodiment, the ionic liquid(s) and the mixture of the cycloalkanol, the cycloalkanone and the cycloalkane is known as separation mixture (c). The process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid- based phase, and the other liquid phase is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase. The separation of a cycloalkanol from a cycloalkanone and a cycloalkane according to the process in this embodiment can be achieved when the distribution coefficient for the cycloalkanol between the ionic liquid- based phase and the cycloalkane- -based phase is greater than 1, and the distribution coefficient for the cycloalkanone between the ionic liquid-based phase and the
cycloalkane-based phase is less than 1. This embodiment has application to the separation of cyclohexanol from cyclohexanone for caprolactam manufacture. Tn this embodiment, the distribution coefficient of the cycloalkanol between the ionic liquid- based phase and the cycloalkane-based is greater than 1.5 and preferably greater than 3.
In embodiment (d) the separable components are a mixture of a cycloalkanone and a cycloalkanol which are separated from a cycloalkane. The ionic liquid(s) is contacted with a mixture of the cycloalkanol, the cycloalkanone and the cycloalkane. In this embodiment, the ionic liquid(s) and the mixture of the cycloalkanol, the cycloalkanone and the cycloalkane is known as separation mixture (d). The process of this embodiment involves a liquid-liquid separation wherein one of the liquid phases is an ionic liquid-based phase and the other is a cycloalkane-based phase that is substantially immiscible in the ionic liquid-based phase. In this embodiment, the distribution coefficient of the cycloalkanol and the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5 and preferably greater than 3.
In each of embodiments (a) to (d), the mixtures to be separated may also contain materials other than the cycloalkanol, cycloalkanone and cycloalkane components. Depending on the distribution coefficient of these other materials between the ionic liquid-based phase and the cycloalkane-based phase, these other materials will either remain in the cycloalkane-based phase or be separated into the ionic liquid-based phase along with the separable component. In particular, cyclohexylhydroperoxide (CHHP) may be present in the separation mixture of cyclohexanol, cyclohexanone and cyclohexane. In these circumstances, CHHP would be separated with the cyclohexanol and/or cyclohexanone into the ionic liquid-based phase.
It will be appreciated that the processes of embodiments (a) to (d) are also applicable to the generic cases in which the above references to a cycloalkanol, a cycloalkanone and a cyclohexane are respectively replaced with references to an alcohol, a ketone and a non-polar solvent.
The ionic liquid(s) of the present invention may consist of a single ionic liquid or a mixture of two or more ionic liquids, i.e. a mixture of 2, 3, 4, 5, 6 etc different ionic liquids. Typically, one or two, and typically only one ionic liquid is used.
Preferably the ionic liquid(s) comprises a cation selected from one or more of 1- alkylpyridinium, alkyl- or poly-alkylpyridinium, phosphonium (PR4 +), alkyl- or polyalkylphosphonium, imidazolium, alkyl- or polyalkylimidazolium, ammonium (NR4 +), alkyl- or polyalkylammonium, alkyl- or polyalkylpyrazolium, alkyl- or polyalkylpyrrolidinium, alkyl or polyalkylazepinium, alkyloxonium or alkysulfonium.
Each R group of the phosphonium and ammonium cations may be separately selected from the group of substituents consisting of hydrogen, hydroxyl, alkyl, alkyl ethers, alkyl esters, alkyl amides, alkyl carboxylic acids, or sulfonate.
More preferably the ionic liquid(s) comprises a cation selected from one or more of 1-alkylpyridinium, alkyl- or poly-alkylpyridinium, imidazolium, alkyl- or polyalkylimidazolium.
When a mixture of two or more ionic liquids is used, the cations of each of the ionic liquids present in the mixture may be the same or different.
Preferably the anion of the ionic liquid(s) is selected from one or more of a halide, preferably chloride, bromide or iodide, a nitrate, an alkylsulfate or alkyl polyalkoxysulfate, such as methanesulfonate, trifluoromethanesulfonate and hydrogensulfonate, anions based on nitrogen, phosphorous, boron, silicon, selenium, tellurium, halogens, and oxoanions of metals. Suitable anions include, but are not limited to bis(trifluoromethylsulfonyl)amide (NTf2 "), tetrafluoroborate (BF4 "), trifluoromethylsulfonyl (Tf), methoxyethylsulfonate, 2-methoxyethylsulfonate, ethoxyethylsulfonate, 2-ethoxyethylsulfonate, (methoxypropoxy)propylsulfonate, 1-(1- methoxypropoxy)-propylsulfonate, (methoxyethoxy)-ethylsulfonate, 1-(1- methoxyethoxy)-ethylsulfonate, methyl (diethoxy)ethylsulfonate, 1- methyl(diethoxy)ethylsulfonate, carboxylate, formate, acetate, dicyanimide and trifluoromethanesulfonate.
More preferably the anion of the ionic liquid(s) is selected from one or more of an alkylsulfate or alkyl polyalkoxysulfate, bis(trifluoromethylsulfonyl)amide (NTf2 ") and tetrafluoroborate (BF4 ").
When a mixture of two or more ionic liquids is used, the anion of each of the ionic liquids present in the mixture may be the same or different.
Preferably the ionic liquid(s) will comprise at least one C2 - C6 alkyl group. The C2 - C6 alkyl group may be a substituent on either the anion or the cation of the ionic liquid(s). More preferably the C2 - C6 alkyl group is a substituent on the cation of the ionic liquid(s). When the ionic liquid(s) consists of a single ionic liquid, the single ionic liquid present preferably contains at least one C2 - C6 alkyl group substituent. When the ionic liquid(s) consists of two or more ionic liquids, preferably at least one of the ionic liquids present contains at least one C2 - C6 alkyl group substituent, more preferably two or more of the ionic liquids present contain at least one C2 - C6 alkyl group substituent, i.e. 2, 3, 4, 5 etc of the ionic liquids present contain at least one C2 - C6 alkyl group substituent. Most preferably, all the ionic liquids present in the at least on ionic liquid contain at least one C2 - C6 alkyl group substituent.
The ionic liquid(s) of the present invention is preferably selected from the group consisting of N-ethylpyridinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium tetrafluoroborate;
N-Methyl-N'-butylimidazolium bis(trifluoromethanesulfonyl)amide; trimethyl-(2-hydroxyethyl)ammonium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-ethylimidazolium 2-methoxyethylsulfonate;
N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium 2-methoxyethylsulfonate;
N-Methyl-N'-butylimidazolium bromide; N-Methyl-N'-butylimidazolium 2-ethoxyethylsulfonate;
N-Methyl-N'-butylimidazolium 1 -( 1 -methoxypropoxy)-propylsulfonate;
N-Methyl-N'-butylimidazolium l-(l-methoxyethoxy)-ethylsulfonate;
N-Methyl-N'-butylimidazolium l-methyl(diethoxy)ethylsulfonate; or N-Methyl-N-(butyl-4-sulfonic acid)pyiτolidinium trifluoromethanesulfonate or mixtures thereof.
Most preferably the ionic liquid(s) is N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide or N-Methyl-N'-butylimidazolium 1-(1- methoxypropoxy)-propylsulfonate.
Ionic liquids most suitable for the separation of an alcohol from a non-polar solvent, particularly when said alcohol is a cycloalkanol (and particularly a cyclohexanol) and said non-polar solvent is a cycloalkane (particularly a cyclohexane) are:
N-ethylpyridinium bis(trifluorornethanesulfonyl)amide; N-Methyl-N'-butylimidazolium tetrafluoroborate;
N-Methyl-N'-butylimidazolium bis(trifluoromethanesulfonyl)amide; trimethyl-(2-hydroxyethyl)ammonium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-ethylimidazolium 2-methoxyethylsulfonate;
N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide; N-Methyl-N'-butylimidazolium 2-methoxyethylsulfonate;
N-Methyl-N'-butylimidazolium bromide;
N-Methyl-N'-butylimidazolium 2-ethoxyethylsulfonate;
N-Methyl-N'-butylimidazolium l-(l-methoxypropoxy)-propylsulfonate;
N-Methyl-N'-butylimidazolium l-(l-methoxyethoxy)-ethylsulfonate; N-Methyl-N'-butylimidazolium l-methyl(diethoxy)ethylsulfonate; or
N-Methyl-N-(butyl-4-sulfonic acid)pyrrolidinium trifluoromethanesulfonate, or mixtures thereof.
Ionic liquids most suitable for the separation of an alcohol from a mixture of a non-polar solvent and a ketone, particularly wherein said alcohol is a cycloalkanol
(particularly a cyclohexanol) and said ketone is a cycloalkanone (particularly a cyclohexanone) and said non-polar solvent is a cycloalkane (particularly a cyclohexane) are:
N-Methyl-N'-butylimidazolium bromide;
N-Methyl-N'-butylimidazolium l-(l -methoxyethoxy)-ethylsulfonate; or N-Methyl-N'-butylimidazolium 2-ethoxyethylsulfonate, or mixtures thereof.
Ionic liquids most suitable for the separation of a ketone from a non-polar solvent, particularly wherein said ketone is a cycloalkanone (particularly a cyclohexanone) and said non-polar solvent is a cycloalkane (particularly a cyclohexane) are: N-ethylpyridinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium tetrafluoroborate;
N-Methyl-N'-butylimidazolium bis(trifluoromethanesulfonyl)amide; trimethyl-(2-hydroxyethyl)ammonium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-ethylimidazolium 2-methoxyethylsulfonate; N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium 2-methoxyethylsulfonate;
N-Methyl-N'-butylimidazolium l-(l-methoxypropoxy)-propylsulfonate;
N-Methyl-N'-butylimidazolium 1 -methyl(diethoxy)ethylsulfonate; or
N-Meth yl -N- (butyl -4-sulfonic acid)pyrrolidinium trifluoromethanesulfonate, or mixtures thereof.
Ionic liquids most suitable for the separation of a mixture of an alcohol and a ketone from a non-polar solvent, particularly when said alcohol is a cycloalkanol (and particularly cyclohexanol) and said ketone is a cycloalkanone (particularly cyclohexanone) and said non-polar solvent is a cycloalkane (particularly a cyclohexane) are:
N-ethylpyridinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium tetrafluoroborate;
N-Methyl-N'-butylimidazolium bis(trifluoromethanesulfonyl)amide; trimethyl-(2-hydroxyethyl)ammonium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-ethylimidazolium 2-methoxyethylsulfonate;
N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium 2-methoxyethylsulfonate; N-Methyl-N'-butylimidazolium l-(l-methoxypropoxy)-propylsulfonate; N-Methyl-N'-butylimidazolium 1 -methyl (diethoxy)ethylsulfonate; or N-Methyl-N-(butyl-4-sulfonic acid)pyrrolidinium trifluororaethanesulfonate or mixtures thereof.
As used herein, the term "ionic liquid" refers to an ionic compound which is liquid below 1000C.
As used herein, the term "distribution coefficient" referring to the liquid-liquid separation refers to the concentration of the separable component in the ionic liquid- based phase divided by the concentration of the separable component in the non-polar solvent-based phase. These concentrations are measured subsequent to settling, i.e. when the separation mixture has reached equilibrium subsequent to the vigorous shaking.
The invention is further illustrated by the following examples. It will be appreciated that the examples are for illustrative purposes only and are not intended to limit the invention as described above. Modification of detail may be made without departing from the scope of the invention.
Examples
(i) Cyclohexanol/Cyclohexanone/Cyclohexane
The present invention is exemplified through separation of cyclohexanol and cyclohexanone from cyclohexane using a general method followed by calculation of the resulting distribution coefficient. To simplify these examples, equal volumes of cyclohexane and ionic liquid have been used. However, it should be noted that in practice the volume of ionic liquid used would preferably be a small fraction of the volume of cyclohexane. It should also be noted that since the distribution coefficient is independent of volume, the data obtained for equivolume experiments will be relevant to industrial application in which the volumes of ionic liquid and cyclohexane may not be equivalent. The general method used for all the examples was as follows.
Stock solution; 250mg cyclohexanol (Molecular Weight = lOOgmol"1) and 250mg cyclohexanone (Molecular Weight = θδgmor1) in 1Og of cyclohexane (Molecular Weight = 84gmor1).
Method: add ImL (0.8g) of stock solution (20mg each of cyclohexanol and cyclohexanone) to ImL of ionic liquid and shake vigorously. After settling time and complete phase separation, 3 drops of the top layer were added to a vial and filled with ethylene chloride. Gas chromatography analysis was used to provide the number of moles of the separable component in each liquid phase. The distribution coefficient for the separation was then calculated.
In addition, Hnmr (Hydrogen Nuclear Magnetic Resonance) was carried out on each layer. In all cases the cyclohexane- or cyclohexanone layer contained less than 5 mole % of ionic liquid, in most cases the amount of ionic liquid in the cyclohexane- based layer was undetectable.
Table 1 details the results of the specific examples with comparisons to water and DMSO (dimethyl sulfoxide), where D is the distribution coefficient.
Table 1
The difference in the distribution coefficients for cyclohexanol and cyclohexanone in these ionic liquids show the efficiency of separation of cyclohexanol. Thus, these ionic liquids are effective for the separation of cyclohexanol from cyclohexane, and for the separation of cyclohexanol from a mixture of cyclohexanone and cyclohexane.
(HjOoctanol/Octanone/Octane
A corresponding set of experiments was conducted to study the extraction of octanol and 2-octanone from octane using ionic liquids. The results are presented in
Table 2 below, in which the IL/Octane distribution coefficient is calculated as the concentration of substrate in IL divided by the concentration of substrate in octane.
Table 2
The difference in the distribution coefficients for octanol and 2-octanone in these ionic liquids demonstrate the separability of octanol and/or 2-octanone from octane (Example 15) and octanol from a mixture of 2-octanone and octane (Examples 16 to 18).
Claims
1. A process for the separation of an alcohol from a non-polar solvent; a ketone from a non-polar solvent; an alcohol from a mixture of a ketone and a non-polar solvent; or a mixture of an alcohol and a ketone from a non-polar solvent; said process comprising contacting at least one ionic liquid with a mixture comprising a non-polar solvent and at least one of an alcohol and a ketone.
2. The process according to claim 1 wherein said alcohol is a cycloalkanol, said ketone is a cycloalkanone, and said non-polar solvent is a cycloalkane.
3. The process according to claim 2 for the separation of a cycloalkanone from a cycloalkane
4. The process according to claim 2 for the separation of a cycloalkanol from a mixture of cycloalkanone and cycloalkane
5. The process according to claim 2 for the separation of a mixture of a cycloalkanone and a cycloalkanol from a cycloalkane.
6. The process according to claim 2 for the separation of a cycloalkanol or a cycloalkanone or a mixture thereof from a cycloalkane or the separation of a cycloalkanol from a cycloalkanone and a cycloalkane, wherein on contacting said at least one ionic liquid with the mixture comprising at least one of a cycloalkanol and a cycloalkanone in a cycloalkane, two separate phases are formed wherein the first phase is ionic liquid-based and the second phase is cycloalkane-based.
7. The process according to claim 6 for the separation of a cycloalkanol from a cycloalkanone and a cycloalkane, wherein the two separate phases are allowed to reach equilibrium and wherein at equilibrium the distribution coefficient of the
cycloalkanol between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5.
8. The process according to claim 7 for the separation of a cycloalkanol from a cycloalkanone and a cycloalkane, wherein said distribution coefficient is greater than
3.
9. The process according to claim 6 for the separation of a cycloalkanol from a cycloalkanone and a cycloalkane, wherein the two separate phases are allowed to reach equilibrium and wherein at equilibrium the distribution coefficient for the cycloalkanol between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1, and the distribution coefficient for the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is less than 1.
10. The process according to claim 6 for the separation of a cycloalkanol from a cycloalkane, wherein the two separate phases are allowed to reach equilibrium and wherein at equilibrium the distribution coefficient of the cycloalkanol between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5.
11. The process according to claim 10 for the separation of a cycloalkanol from a cycloalkane, wherein said distribution coefficient is greater than 3.
12. The process according to claim 6 for the separation of a cycloalkanone from a cycloalkane, wherein the two separate phases are allowed to reach equilibrium and wherein at equilibrium the distribution coefficient of the cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5.
13. The process according to claim 12 for the separation of a cycloalkanone from a cycloalkane, wherein said distribution coefficient is greater than 3.
14. The process according to claim 6 for the separation of a mixture of a cycloalkanone and a cycloalkanol from a cycloalkane, wherein the two phase system is allowed to reach equilibrium and wherein at equilibrium the distribution coefficient of the
cycloalkanone between the ionic liquid-based phase and the cycloalkane-based phase is greater than 1.5.
15. The process according to claim 14 for the separation of a cycloalkanone and a cycloalkanol from a cycloalkane, wherein said distribution coefficient is greater than
3.
16. The process according to any of claims 2 to 15, wherein each of said cycloalkanol, cycloalkanone and said cycloalkane contain 3-20 carbon atoms.
17. The process according to any of claims 2 to 16, wherein the cycloalkanol is cyclohexanol, the cycloalkanone is cyclohexanone and the cycloalkane is cyclohexane.
18. The process according to any of claims 2 to 16, wherein the cycloalkanol is cyclododecanol, the cycloalkanone is cyclododecanone and the cycloalkane is cyclododecane.
19. The process according to any of claims 2 to 18, further comprising, prior to said contacting step, the step of oxidation of a cycloalkane followed by a cyclohexyl hydroperoxide decomposition step followed by said contacting step defining one oxidation and separation cycle.
20. The process according to claim 19, comprising a plurality of oxidation and separation cycles, wherein the cycloalkane-based phase or fraction which results from said separation is recycled for oxidation.
21. The process according to claim 20, wherein subsequent to equilibrium being reached, the at least one ionic liquid-based phase is physically separated from the cycloalkane-based phase, and the cycloalkanol and/or cycloalkanone is removed from said at least one ionic liquid and said at least one ionic liquid is recycled.
22. The process according to any preceding claim, wherein said at least one ionic liquid consists of a mixture of two or more ionic liquids.
23. The process according to any preceding claim, wherein the cation of said at least one ionic liquid is selected from one or more of: 1-alkylpyridinium, alkyl- or poly- alkylpyridinium, phosphonium, alkyl- or polyalkylphosphonium, imidazolium, alkyl- or polyalkylimidazolium, ammonium, alkyl- or polyalkylammonium, alkyl- or polyalkylpyrazolium, alkyl- or polyalkylpyrrolidinium, alkyl- or polyalkylazepinium, alkyloxonium or alkysulfonium.
24. The process according to any preceding claim, wherein the anion of said at least one ionic liquid is selected from one or more of a halide (chloride, bromide or iodide) or a nitrate, an alkylsulfate or alkyl polyalkoxysulfate, such as methanesulfonate, trifluoromethanesulfonate and hydrogensulfonate, anions based on nitrogen, phosphorous, boron, silicon, selenium, tellurium, halogens, and oxoanions of metals.
25. The process according to any preceding claim, wherein at least one ionic liquid of said at least one ionic liquid comprises at least one C2 - C6 alkyl group, wherein the alkyl group may be present on the anion or the cation of said at least one ionic liquid.
26. The process according to any preceding claim, wherein said at least one ionic liquid is:
N-ethylpyridinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium tetrafluoroborate; N-Methyl-N'-butylimidazolium bis(trifluoromethanesulfonyl)amide; trimethyl-(2-hydroxyethyl)ammonium bis(trifluoromethanesulfonyl)arnide;
N-Methyl-N'-ethylimidazolium 2-methoxyethylsulfonate;
N-butyl-N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide;
N-Methyl-N'-butylimidazolium 2-methoxyethylsulfonate; N-Methyl-N'-butylimidazolium bromide;
N-Methyl-N'-ethylimidazolium 2-ethoxyethylsulfonate;
N-Methyl-N'-butylimidazolium l-(l-methoxypropoxy)-propylsulfonate;
N-Methyl-N'-butylimidazolium l-(l-methoxyethoxy)-ethylsulfonate;
N-Methyl-N'-butylimidazolium 1 -methyl(diethoxy)ethylsulfonate; or N-Methyl-N-(butyl-4-sulfonic acid)pyrrolidinium trifluoromethanesulfonate, or mixtures thereof.
27. The process according to claim 26, wherein said at least one ionic liquid is N-butyl-
N-methylpyrrolidinium bis(trifluoromethanesulfonyl)amide.
28. The process according to claim 26, wherein said at least one ionic liquid is N- Methyl-N'-butylimidazolium l-(l-methoxypropoxy)-propylsulfonate.
29. A method for the use of at least one ionic liquid for the separation of an alcohol and/or ketone from a non-polar solvent, or for the separation of an alcohol from a ketone in a mixture of these compounds in a non-polar solvent.
30. The method according to claim 29 wherein said alcohol is a cycloalkanol and said ketone is a cycloalkanone.
31. The method according to claim 29 wherein said alcohol is a cycloalkanol and said ketone is a cycloalkanone and said non-polar solvent is a cycloalkane.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009525697A JP5350244B2 (en) | 2006-08-18 | 2007-08-16 | Extraction method using ionic liquid |
| EP07814141A EP2051788A1 (en) | 2006-08-18 | 2007-08-16 | Extraction process using an ionic liquid |
| KR1020147029293A KR101474209B1 (en) | 2006-08-18 | 2007-08-16 | Extraction process using an ionic liquid |
| CN200780030553XA CN101505844B (en) | 2006-08-18 | 2007-08-16 | Extraction process |
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| US83895706P | 2006-08-18 | 2006-08-18 | |
| US60/838,957 | 2006-08-18 | ||
| US90105307P | 2007-02-12 | 2007-02-12 | |
| US60/901,053 | 2007-02-12 |
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| EP (1) | EP2051788A1 (en) |
| JP (1) | JP5350244B2 (en) |
| KR (2) | KR20090057389A (en) |
| CN (1) | CN101505844B (en) |
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| WO (1) | WO2008022233A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010520896A (en) * | 2007-03-12 | 2010-06-17 | 中国科学院過程工程研究所 | Method of absorbing methyl acrolein with ionic liquid |
| RU2492161C2 (en) * | 2008-05-26 | 2013-09-10 | Мерк Патент Гмбх | Use of ionic liquids with tetracyanoborate anions as solvent for extraction of alcohols from aqueous solutions |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103274568B (en) * | 2013-05-30 | 2014-08-20 | 湖南百利工程科技股份有限公司 | Method for treating ketone-containing wastewater in cyclohexanone ammoximation device by employing extraction method |
| CN113004113A (en) * | 2021-03-01 | 2021-06-22 | 广东工业大学 | Method for separating cyclohexane and KA oil by taking ionic liquid as extracting agent |
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| WO2003037835A2 (en) * | 2001-11-02 | 2003-05-08 | Solvent Innovation Gmbh | Method for eliminating polarizable impurities from hydrocarbons with ionic liquids |
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| GB2427192A (en) * | 2005-06-17 | 2006-12-20 | Johnson Matthey Plc | A process for the oxidation of an alkyl-group containing substrate in the presence of an ionic liquid |
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|---|---|---|---|---|
| CN1274382C (en) * | 2001-03-20 | 2006-09-13 | 巴斯福股份公司 | Ionic liquids as selective additives for separation of close-boiling or azeotropic mixtures |
| US6703529B1 (en) * | 2002-09-12 | 2004-03-09 | E. I. Du Pont De Nemours And Company | Process for oxidation of cyclohexane |
| DE102005027172A1 (en) * | 2005-06-13 | 2006-12-14 | Merck Patent Gmbh | Extraction of proteins, protein fragments or peptides from biological samples comprises using an ionic liquid as the extractant |
-
2007
- 2007-08-16 EP EP07814141A patent/EP2051788A1/en not_active Withdrawn
- 2007-08-16 KR KR1020097005451A patent/KR20090057389A/en not_active Application Discontinuation
- 2007-08-16 WO PCT/US2007/076061 patent/WO2008022233A1/en active Application Filing
- 2007-08-16 JP JP2009525697A patent/JP5350244B2/en not_active Expired - Fee Related
- 2007-08-16 CN CN200780030553XA patent/CN101505844B/en not_active Expired - Fee Related
- 2007-08-16 KR KR1020147029293A patent/KR101474209B1/en not_active IP Right Cessation
- 2007-08-17 TW TW096130580A patent/TW200815339A/en unknown
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| WO2000015594A1 (en) * | 1998-09-10 | 2000-03-23 | Exxon Chemical Patents Inc. | Process for making aromatic aldehydes using ionic liquids |
| WO2003037835A2 (en) * | 2001-11-02 | 2003-05-08 | Solvent Innovation Gmbh | Method for eliminating polarizable impurities from hydrocarbons with ionic liquids |
| WO2003070667A1 (en) * | 2002-02-19 | 2003-08-28 | Oxeno Olefinchemie Gmbh | Method for separating substances by extraction or by washing them with ionic liquids |
| WO2005019137A1 (en) * | 2003-07-21 | 2005-03-03 | Basf Aktiengesellschaft | Method for extracting impurities using ionic liquids |
| US20050187421A1 (en) * | 2004-02-13 | 2005-08-25 | Renaud Cadours | Method for extracting an antihydrate contained in condensed hydrocarbons |
| WO2006009266A1 (en) * | 2004-07-20 | 2006-01-26 | Sumitomo Chemical Company, Limited | Process for producing oxygenic compound |
| EP1797953A1 (en) * | 2004-07-20 | 2007-06-20 | Sumitomo Chemical Company, Limited | Process for producing oxygenic compound |
| US20060070919A1 (en) * | 2004-09-10 | 2006-04-06 | Christophe Vallee | Process for separating oxygen-containing compounds contained in a hydrocarbon feed, employing an ionic liquid |
| GB2427192A (en) * | 2005-06-17 | 2006-12-20 | Johnson Matthey Plc | A process for the oxidation of an alkyl-group containing substrate in the presence of an ionic liquid |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2010520896A (en) * | 2007-03-12 | 2010-06-17 | 中国科学院過程工程研究所 | Method of absorbing methyl acrolein with ionic liquid |
| RU2492161C2 (en) * | 2008-05-26 | 2013-09-10 | Мерк Патент Гмбх | Use of ionic liquids with tetracyanoborate anions as solvent for extraction of alcohols from aqueous solutions |
Also Published As
| Publication number | Publication date |
|---|---|
| KR101474209B1 (en) | 2014-12-17 |
| KR20090057389A (en) | 2009-06-05 |
| JP2010501582A (en) | 2010-01-21 |
| TW200815339A (en) | 2008-04-01 |
| EP2051788A1 (en) | 2009-04-29 |
| CN101505844B (en) | 2012-07-11 |
| CN101505844A (en) | 2009-08-12 |
| KR20140130241A (en) | 2014-11-07 |
| JP5350244B2 (en) | 2013-11-27 |
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