WO2005042547A1 - Sterisch anspruchsvolle chelatphosphinitphosphitliganden, katalysator, umfassend wenigstens einen nickel (0) komplex stabilisiert durch diesen liganden sowie ein verfahren zur herstellung von nitrilen - Google Patents
Sterisch anspruchsvolle chelatphosphinitphosphitliganden, katalysator, umfassend wenigstens einen nickel (0) komplex stabilisiert durch diesen liganden sowie ein verfahren zur herstellung von nitrilen Download PDFInfo
- Publication number
- WO2005042547A1 WO2005042547A1 PCT/EP2004/012176 EP2004012176W WO2005042547A1 WO 2005042547 A1 WO2005042547 A1 WO 2005042547A1 EP 2004012176 W EP2004012176 W EP 2004012176W WO 2005042547 A1 WO2005042547 A1 WO 2005042547A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- catalyst
- transition metal
- pentenenitrile
- ligand
- phosphinite
- Prior art date
Links
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims description 56
- 239000003054 catalyst Substances 0.000 title claims description 48
- 239000003446 ligand Substances 0.000 title claims description 30
- 150000002825 nitriles Chemical class 0.000 title claims description 13
- 238000004519 manufacturing process Methods 0.000 title description 10
- 239000013522 chelant Substances 0.000 title description 8
- 239000000203 mixture Substances 0.000 claims abstract description 52
- -1 phosphinite phosphites Chemical class 0.000 claims abstract description 24
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 17
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 16
- 125000002947 alkylene group Chemical group 0.000 claims abstract description 16
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims abstract description 8
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims abstract description 7
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 claims description 79
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 48
- CFEYBLWMNFZOPB-UHFFFAOYSA-N Allylacetonitrile Natural products C=CCCC#N CFEYBLWMNFZOPB-UHFFFAOYSA-N 0.000 claims description 38
- 229910052723 transition metal Inorganic materials 0.000 claims description 34
- 150000003624 transition metals Chemical class 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 26
- UVKXJAUUKPDDNW-NSCUHMNNSA-N (e)-pent-3-enenitrile Chemical compound C\C=C\CC#N UVKXJAUUKPDDNW-NSCUHMNNSA-N 0.000 claims description 23
- 230000008569 process Effects 0.000 claims description 20
- 238000006317 isomerization reaction Methods 0.000 claims description 16
- 125000005538 phosphinite group Chemical group 0.000 claims description 14
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 claims description 14
- WBAXCOMEMKANRN-UHFFFAOYSA-N 2-methylbut-3-enenitrile Chemical compound C=CC(C)C#N WBAXCOMEMKANRN-UHFFFAOYSA-N 0.000 claims description 10
- 150000001875 compounds Chemical class 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 229910052759 nickel Inorganic materials 0.000 claims description 9
- 238000002360 preparation method Methods 0.000 claims description 9
- BTGRAWJCKBQKAO-UHFFFAOYSA-N adiponitrile Chemical compound N#CCCCCC#N BTGRAWJCKBQKAO-UHFFFAOYSA-N 0.000 claims description 8
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims description 3
- 125000004123 n-propyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])* 0.000 claims description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 30
- 238000005669 hydrocyanation reaction Methods 0.000 description 24
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 22
- 238000006243 chemical reaction Methods 0.000 description 18
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 16
- 229930195733 hydrocarbon Natural products 0.000 description 14
- 150000002430 hydrocarbons Chemical class 0.000 description 14
- 239000004912 1,5-cyclooctadiene Substances 0.000 description 13
- 239000004215 Carbon black (E152) Substances 0.000 description 13
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 13
- 229910052698 phosphorus Inorganic materials 0.000 description 12
- 239000011541 reaction mixture Substances 0.000 description 12
- 125000004437 phosphorous atom Chemical group 0.000 description 11
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 9
- 239000001257 hydrogen Substances 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 238000004587 chromatography analysis Methods 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 238000006467 substitution reaction Methods 0.000 description 6
- 239000012159 carrier gas Substances 0.000 description 5
- IQNYBCIGGNQJDL-UHFFFAOYSA-N (4-methylphenyl) dihydrogen phosphite Chemical compound CC1=CC=C(OP(O)O)C=C1 IQNYBCIGGNQJDL-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 150000001345 alkine derivatives Chemical class 0.000 description 4
- REJGOFYVRVIODZ-UHFFFAOYSA-N phosphanium;chloride Chemical compound P.Cl REJGOFYVRVIODZ-UHFFFAOYSA-N 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- ISBHMJZRKAFTGE-ONEGZZNKSA-N (e)-pent-2-enenitrile Chemical compound CC\C=C\C#N ISBHMJZRKAFTGE-ONEGZZNKSA-N 0.000 description 3
- FPPLREPCQJZDAQ-UHFFFAOYSA-N 2-methylpentanedinitrile Chemical compound N#CC(C)CCC#N FPPLREPCQJZDAQ-UHFFFAOYSA-N 0.000 description 3
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 3
- 150000001336 alkenes Chemical class 0.000 description 3
- 239000012300 argon atmosphere Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- GDLCVAIEPUCSCE-UHFFFAOYSA-N chloro-bis(2-methylphenoxy)phosphane Chemical compound CC1=CC=CC=C1OP(Cl)OC1=CC=CC=C1C GDLCVAIEPUCSCE-UHFFFAOYSA-N 0.000 description 3
- XGRJZXREYAXTGV-UHFFFAOYSA-N chlorodiphenylphosphine Chemical compound C=1C=CC=CC=1P(Cl)C1=CC=CC=C1 XGRJZXREYAXTGV-UHFFFAOYSA-N 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 238000005984 hydrogenation reaction Methods 0.000 description 3
- 150000002894 organic compounds Chemical class 0.000 description 3
- 239000002574 poison Substances 0.000 description 3
- 231100000614 poison Toxicity 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 125000001424 substituent group Chemical group 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- IHXNSHZBFXGOJM-HWKANZROSA-N (e)-2-methylbut-2-enenitrile Chemical compound C\C=C(/C)C#N IHXNSHZBFXGOJM-HWKANZROSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 239000010953 base metal Substances 0.000 description 2
- KDKYADYSIPSCCQ-UHFFFAOYSA-N but-1-yne Chemical compound CCC#C KDKYADYSIPSCCQ-UHFFFAOYSA-N 0.000 description 2
- WFYPICNXBKQZGB-UHFFFAOYSA-N butenyne Chemical group C=CC#C WFYPICNXBKQZGB-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 150000001805 chlorine compounds Chemical class 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 239000002638 heterogeneous catalyst Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000005673 monoalkenes Chemical class 0.000 description 2
- 125000002560 nitrile group Chemical group 0.000 description 2
- UIUWNILCHFBLEQ-UHFFFAOYSA-N pent-3-enoic acid Chemical compound CC=CCC(O)=O UIUWNILCHFBLEQ-UHFFFAOYSA-N 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- XRBCRPZXSCBRTK-UHFFFAOYSA-N phosphonous acid Chemical class OPO XRBCRPZXSCBRTK-UHFFFAOYSA-N 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- 238000010626 work up procedure Methods 0.000 description 2
- DNZZPKYSGRTNGK-PQZOIKATSA-N (1z,4z)-cycloocta-1,4-diene Chemical compound C1C\C=C/C\C=C/C1 DNZZPKYSGRTNGK-PQZOIKATSA-N 0.000 description 1
- IHXNSHZBFXGOJM-HYXAFXHYSA-N (z)-2-methylbut-2-enenitrile Chemical compound C\C=C(\C)C#N IHXNSHZBFXGOJM-HYXAFXHYSA-N 0.000 description 1
- UVKXJAUUKPDDNW-IHWYPQMZSA-N (z)-pent-3-enenitrile Chemical compound C\C=C/CC#N UVKXJAUUKPDDNW-IHWYPQMZSA-N 0.000 description 1
- VYXHVRARDIDEHS-UHFFFAOYSA-N 1,5-cyclooctadiene Chemical compound C1CC=CCCC=C1 VYXHVRARDIDEHS-UHFFFAOYSA-N 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical class [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- 239000002841 Lewis acid Substances 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 101100425947 Mus musculus Tnfrsf13b gene Proteins 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- JHQYNYXQKSKNAK-UHFFFAOYSA-N OP(O)O.OP(O)O Chemical class OP(O)O.OP(O)O JHQYNYXQKSKNAK-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 125000005595 acetylacetonate group Chemical group 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- IYABWNGZIDDRAK-UHFFFAOYSA-N allene Chemical compound C=C=C IYABWNGZIDDRAK-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 150000003842 bromide salts Chemical class 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000021615 conjugation Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- XMDBKXFFPNRIQD-UHFFFAOYSA-N dichloro-(4-fluorophenyl)phosphane Chemical compound FC1=CC=C(P(Cl)Cl)C=C1 XMDBKXFFPNRIQD-UHFFFAOYSA-N 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical class O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- PXRDVIVDFIVDHI-UHFFFAOYSA-N diphenylphosphane;hydrochloride Chemical class [Cl-].C=1C=CC=CC=1[PH2+]C1=CC=CC=C1 PXRDVIVDFIVDHI-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000895 extractive distillation Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007172 homogeneous catalysis Methods 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 1
- 150000007517 lewis acids Chemical class 0.000 description 1
- 125000000040 m-tolyl group Chemical group [H]C1=C([H])C(*)=C([H])C(=C1[H])C([H])([H])[H] 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 1
- NLEUXPOVZGDKJI-UHFFFAOYSA-N nickel(2+);dicyanide Chemical compound [Ni+2].N#[C-].N#[C-] NLEUXPOVZGDKJI-UHFFFAOYSA-N 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- HVAMZGADVCBITI-UHFFFAOYSA-M pent-4-enoate Chemical compound [O-]C(=O)CCC=C HVAMZGADVCBITI-UHFFFAOYSA-M 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- AQSJGOWTSHOLKH-UHFFFAOYSA-N phosphite(3-) Chemical class [O-]P([O-])[O-] AQSJGOWTSHOLKH-UHFFFAOYSA-N 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 150000003018 phosphorus compounds Chemical class 0.000 description 1
- 229910000073 phosphorus hydride Inorganic materials 0.000 description 1
- MWWATHDPGQKSAR-UHFFFAOYSA-N propyne Chemical compound CC#C MWWATHDPGQKSAR-UHFFFAOYSA-N 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002683 reaction inhibitor Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 description 1
- 125000002914 sec-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- 238000004230 steam cracking Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 150000003623 transition metal compounds Chemical class 0.000 description 1
- BKHZQJRTFNFCTG-UHFFFAOYSA-N tris(2-methylphenyl) phosphite Chemical compound CC1=CC=CC=C1OP(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C BKHZQJRTFNFCTG-UHFFFAOYSA-N 0.000 description 1
- AZLGDNBTDKZORI-UHFFFAOYSA-N tris(3-methylphenyl) phosphite Chemical compound CC1=CC=CC(OP(OC=2C=C(C)C=CC=2)OC=2C=C(C)C=CC=2)=C1 AZLGDNBTDKZORI-UHFFFAOYSA-N 0.000 description 1
- FEVFLQDDNUQKRY-UHFFFAOYSA-N tris(4-methylphenyl) phosphite Chemical compound C1=CC(C)=CC=C1OP(OC=1C=CC(C)=CC=1)OC1=CC=C(C)C=C1 FEVFLQDDNUQKRY-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/06—Phosphorus compounds without P—C bonds
- C07F9/08—Esters of oxyacids of phosphorus
- C07F9/09—Esters of phosphoric acids
- C07F9/12—Esters of phosphoric acids with hydroxyaryl compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
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- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
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- C07F9/48—Phosphonous acids [RP(OH)2] including [RHP(=O)(OH)]; Thiophosphonous acids including [RP(SH)2], [RHP(=S)(SH)]; Derivatives thereof
- C07F9/4866—Phosphonous acids [RP(OH)2] including [RHP(=O)(OH)]; Thiophosphonous acids including [RP(SH)2], [RHP(=S)(SH)]; Derivatives thereof the ester moiety containing a substituent or structure which is considered as characteristic
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- B01J31/1875—Phosphinites (R2P(OR), their isomeric phosphine oxides (R3P=O) and RO-substitution derivatives thereof)
Definitions
- the present invention relates to new phosphinite phosphites, in particular chelate phosphinite phosphites, and a process for their preparation.
- the present invention furthermore relates to their use as ligands in transition metal complexes, new transition metal complexes and corresponding processes for their preparation.
- the present invention further relates to the use of the transition metal complexes as a catalyst and processes in the presence of such transition metal complexes as a catalyst.
- the object of the present object was therefore to provide suitable phosphinite phosphites as chelate phosphinite phosphites which enable the hydrocyanation of unsaturated organic compounds with high stability, high reactivity and high selectivity of the catalyst in a technically simple and economical manner.
- phosphinite phosphites I of the formula 1 or 2 or 3 or 4 or 5 or 6 were 35
- R1, R2, R4 are independently an alkyl or alkylene group with 1 to 8 carbon atoms, with the proviso that at least one of the groups R1, R2, R4 is not H,
- R5 to R22 are independently H, an alkyl or alkylene group having 1 to 8 carbon atoms,
- R3 is H, methyl or ethyl
- X is F, Cl or CF 3 if n is 1 or 2,
- X is H when n is 0.
- the radicals R1, R2, R4 are independently an alkyl or alkylene group having 1 to 8 carbon atoms, with the proviso that at least one of the groups R1, R2, R4 is not equal to H,
- R1 stands for hydrogen
- R2 can be hydrogen and R4 can be an alkyl or alkylene group with 1 to 8 carbon atoms or R2 can be an alkyl or alkylene group with 1 to 8 carbon atoms and R4 can be hydrogen or R2 and R4 independently of one another with an alkyl or alkylene group 1 to 8 carbon atoms.
- R1 represents an alkyl or alkylene group with 1 to 8 carbon atoms
- R2 and R4 can be hydrogen or R2 independently of R1 can be an alkyl or alkylene group with 1 to 8 carbon atoms and R4 can be hydrogen or R2 can be hydrogen and R4 independently of R1 an alkyl - or alkylene group having 1 to 8 carbon atoms or R2 and R4 independently of one another and independently of R1 are an alkyl or alkylene group with 1 to 8 carbon atoms.
- the alkyl or alkylene group having 1 to 8 carbon atoms is preferably an alkyl group having 1 to 8 carbon atoms, in particular 1 to 4 carbon atoms, advantageously selected from the group consisting of methyl, ethyl, n-propyl, i-propyl, n-butyl, s-butyl, i-butyl and t-butyl, in particular from the group consisting of methyl, ethyl, n-propyl, i-propyl and t-butyl, into consideration.
- R3 represents H or a methyl or an ethyl group.
- the phenyl groups connected to a phosphorus atom can be unsubstituted or can carry 1 or 2 substituents X independently of one another per phenyl group, so that the values 0, 1 or 2 result for n.
- the two phenyl groups connected to a phosphorus atom can be substituted identically or differently, the differences relating to both the number of substituents and the type of substituents in the case of a different substitution.
- the formulas 1, 2 and 3 comprise both the same and a different substitution of the phenyl groups connected to a phosphorus atom.
- X is F, Cl or CF 3 , preferably F or CF 3 .
- the two radicals X1 and X2 can independently represent F, Cl or CF 3 , that is to say F and F, F and Cl, F and CF 3 , Cl and Cl, Cl and CF 3 , CF 3 and CF. 3 , preferably F and F, CF 3 and CF 3 .
- n 1
- X a substitution in the m position to the phosphorus atom connected to the phenyl ring in a phenyl ring connected to a phosphorus atom is possible.
- n 1 and X equal to CF 3
- a substitution in the p-position to the phosphorus atom connected to the phenyl ring in a phenyl ring connected to a phosphorus atom can be considered.
- n 2 and X1 and X2 equal to F
- a substitution in the two m-positions to the phosphorus atom connected to the phenyl ring in a phenyl ring connected to a phosphorus atom is possible.
- n 2 and X1 and X2 equal to CF 3
- a substitution in the two m positions to the phosphorus atom connected to the phenyl ring in a phenyl ring connected to a phosphorus atom can be considered.
- Particularly preferred phosphinite phosphites are those of the following formulas Ia-Ij with the meanings of the groups R1, R2, R3 and R4, and R18 to R22, which are given in Table 1.
- radicals R1, R2, R3 and R4, and R18 to R22 have the following meanings:
- phosphinite phosphites are those of the following formulas Ik-Io.
- the presentation is efficient and economical from easily accessible starting materials.
- the diphenylphosphine chlorides used as the starting compound and their preparation are known per se, for example from: H. Schindibauer, Monthly Bulletin Chemistry, Volume 96, 1965, page 1936-1942.
- the process described there for the preparation of 4-fluorophenyldichlorophosphine can be used analogously to the preparation of the (Xn-phenyl) (Xn-phenyl) phosphine chlorides.
- the optimal parameters for the production of the respective phenyl) - (Xn-phenyl) phosphine chlorides can easily be determined by a few simple preliminary tests.
- the phosphinite phosphites I can be used as ligands in transition metal complexes.
- Suitable transition metals are the metals of the 1st to 2nd and 6th to 8th subgroups of the periodic table, preferably the 8th subgroup of the periodic table, particularly preferably iron, cobalt and nickel, in particular nickel.
- nickel it can have different valences, such as 0, +1, +2, +3.
- Nickel (O) and nickel (+2), in particular nickel (O), are preferred.
- a chemical compound containing a transition metal or, preferably, a transition metal can be reacted with a phosphinite phosphite I, wherein a single phosphinite phosphite I or a mixture of several phosphinite phosphites I can be used as phosphinite phosphite I.
- the transition metal can be obtained from suitable chemical compounds before the reaction, for example by reduction with base metals such as zinc, from salts such as chlorides.
- a compound containing a transition metal is used to prepare the transition metal complexes, salts such as chlorides, bromides, acetylacetonates, sulfates, nitrates, for example nickel (II) chloride, or Ni (0) complex compounds, such as bis (1 , 5-cyclooctadiene) Ni (0).
- the valence of the transition metal in the complex can be with suitable oxidizing or reducing agents, for example base metals, such as zinc, or hydrogen in chemically bound form, such as sodium borohydride, or be changed in molecular form, or electrochemically.
- suitable oxidizing or reducing agents for example base metals, such as zinc, or hydrogen in chemically bound form, such as sodium borohydride, or be changed in molecular form, or electrochemically.
- reaction of a complex compound of Ni (0) with organic monophosphine, monophosphinite, monophosphonite or monophosphite units with a phosphinite phosphite I is suitable in accordance with the process described in German application 10136486.1.
- the molar ratio of transition metal to phosphinite phosphite I can be in the range between 1 and 6, preferably 2 to 5, in particular 2, 3 or 4.
- transition metal complexes can be free of ligands other than the phosphite-phosphites I.
- the transition metal complexes can contain further ligands, for example nitriles, such as acetonitrile, adiponitrile, 3-pentenenitrile, 4-pentenenitrile, 2-methyl-3-butenenitrile, olefins, such as butadiene, or phosphorus compounds, such as organic monophosphines , Monophosphinites, monophosphonites or monophosphites.
- nitriles such as acetonitrile, adiponitrile, 3-pentenenitrile, 4-pentenenitrile, 2-methyl-3-butenenitrile, olefins, such as butadiene, or phosphorus compounds, such as organic monophosphines , Monophosphinites, monophosphonites or monophosphites.
- transition metal complexes can in principle be prepared in such a manner as is described in the literature, for example in DE-OS-2237703, US-A-3,850,973, US-A-3,766,237 or US-A-3,903,120, for the production of transition metal complexes which Tri-o-tolyl-phosphite, Tri-m-tolyl-phosphite or Tri-p-tolyl-phosphite, is described by partially or completely replacing these phosphites with the phosphinite phosphites I according to the invention.
- the transition metal complexes according to the invention can be used as a catalyst, in particular as a homogeneous catalyst.
- transition metal complexes according to the invention as a catalyst in the addition of hydrocyanic acid to olefinic double bonds, in particular those which are conjugated to a further olefinic double bond, for example butadiene, to obtain a mixture comprising 2-methyl-3- butenenitrile and 3-pentenenitrile.
- Equally advantageous is the use as a catalyst in the addition of hydrocyanic acid to olefinic double bonds which are not associated with a further olefinic double bond, for example 3-pentenenitrile or 4-pentenenitrile or mixtures thereof, preferably 3-pentenenitrile, to give adiponitrile , or of 3-pentenoate or 4-pentenoate or mixtures thereof, preferably 3-pentenoate, to give 5-cyanovaleric acid ester.
- transition metal complexes according to the invention as a catalyst in the isomerization of organic nitriles, in particular those in which the nitrile group is not in conjugation with an olefinic double bond, for example of 2-methyl-3-butenenitrile to give 3-pentenenitrile, has likewise proven to be particularly advantageous , proven. Equally advantageous is the use as a catalyst in the isomerization of organic nitriles in which the nitrile group is conjugated to an olefinic double bond.
- Processes for the addition of hydrocyanic acid to an olefinic double bond or for the isomerization of organic nitriles can in principle be carried out in such a manner as is described, for example, in WO 99/13963 or WO 99/64155, in that the phosphonites described there are replaced by the phosphonites according to the invention Phosphinite phosphites I partially or completely replaced.
- a hydrocarbon mixture which has a 1,3-butadiene content of at least 10% by volume, preferably at least 25% by volume, in particular at least 40% by volume, is preferably used for the production of monoolefinic C 5 -mononitriles by the process according to the invention. -%, having. Pure butadiene or 1,3-butadiene-containing hydrocarbon mixtures can be used to prepare mixtures of monoolefinic C 5 -mononitriles which contain, for example, 3-pentenenitrile and 2-methyl-3-butenenitrile and which are suitable as intermediates for further processing to give adiponitrile deploy.
- Hydrocarbon mixtures containing 1,3-butadiene are available on an industrial scale. For example, when petroleum is worked up by steam cracking naphtha, a hydrocarbon mixture with a high total olefin content referred to as C 4 cut is obtained, with about 40% on 1,3-butadiene and the rest on monoolefins and polyunsaturated hydrocarbons and No alkanes. These streams always contain small amounts of generally up to 5% of alkynes, 1,2-dienes and vinyl acetylene.
- Pure 1,3-butadiene can e.g. B. be isolated by extractive distillation from commercially available hydrocarbon mixtures.
- those components which give rise to catalyst poisons in catalytic hydrocyanation are partially or completely removed from the hydrocarbon mixture.
- the C 4 cut is preferably subjected to a catalytic partial hydrogenation before the addition of hydrogen cyanide.
- This partial hydrogenation takes place in the presence of a hydrogenation catalyst which is essentially capable of hydrogenating alkynes and 1,2-dienes selectively alongside other dienes and monoolefins.
- Suitable heterogeneous catalyst systems generally comprise a transition metal compound on an inert support.
- Suitable inorganic carriers are the oxides customary for this, in particular silicon and aluminum oxides, aluminosilicates, zeolites, carbides, nitrides etc. and mixtures thereof. Al 2 O 3 , SiO 2 and mixtures thereof are preferably used as carriers.
- the heterogeneous catalysts used are those described in US Pat. Nos. 4,587,369; US-A-4,704,492 and US-A-4,493,906, which are incorporated by reference in their entirety.
- Suitable copper-based catalyst systems are sold by Dow Chemical as KLP catalysts.
- the addition of hydrogen cyanide to 1,3-butadiene or a 1,3-butadiene-containing hydrocarbon mixture, e.g. B. a pretreated, partially hydrogenated C section can be carried out continuously, semi-continuously or discontinuously.
- the hydrogen cyanide is added continuously.
- Suitable reactors for the continuous reaction are known to the person skilled in the art and are described, for. B. in Ulimann's Encyclopedia of Industrial Chemistry, Vol. 1, 3rd Edition, 1951, pp. 743 ff.
- a stirred tank cascade or a tubular reactor is preferably used for the continuous variant of the process according to the invention.
- the hydrogen cyanide is added to 1,3-butadiene or a 1,3-butadiene-containing hydrocarbon mixture in a semi-continuous manner.
- the semi-continuous process includes:
- Suitable pressure-resistant reactors are known to the person skilled in the art and are described, for. B. in Ullmann's Encyclopedia of Industrial Chemistry, Vol. 1, 3rd Edition, 1951, pp. 769 ff.
- an autoclave is used for the method according to the invention, which can, if desired, be provided with a stirring device and an inner lining. The following should preferably be observed for the above steps:
- the pressure-resistant reactor Before the start of the reaction with the partially hydrogenated C 4 cut or butadiene, hydrogen cyanide, the pressure-resistant reactor is converted into a hydrocyanation catalyst and, if appropriate, one Filled with solvent.
- Suitable solvents are the aromatic hydrocarbons, such as toluene and xylene, or tetrahydrofuran mentioned above in the preparation of the catalysts according to the invention.
- the reaction of the mixture is generally carried out at elevated temperature and pressure.
- the reaction temperature is generally in a range from about 0 to 200 ° C., preferably about 50 to 150 ° C.
- the pressure is generally in a range from about 1 to 200 bar, preferably about 1 to 100 bar, in particular 1 to 50 bar, particularly preferably 1 to 20 bar.
- Hydrogen cyanide is fed in during the reaction in accordance with its consumption, the pressure in the autoclave remaining essentially constant.
- the reaction time is about 30 minutes to 5 hours.
- the reaction time can be followed by a post-reaction time of 0 minutes to about 5 hours, preferably about 1 hour to 3.5 hours, during which no more hydrogen cyanide is fed into the autoclave.
- the temperature is essentially kept constant at the previously set reaction temperature.
- the work-up is carried out according to conventional methods and includes the separation of the unreacted 1, 3-butadiene and the unreacted hydrogen cyanide, for. B. by washing or extracting and working up the remaining reaction mixture by distillation to separate the valuable products and recover the still active catalyst.
- the hydrogen cyanide is added batchwise to the 1,3-butadiene-containing hydrocarbon mixture. Essentially, the reaction conditions described for semi-continuous processes are observed, with no additional hydrogen cyanide being fed in in step b), but this being introduced completely.
- adiponitrile from a butadiene-containing mixture can be divided into three steps by adding 2 molar equivalents of hydrogen cyanide:
- the catalysts based on phosphinite ligands are advantageously also suitable for position and double bond isomerization in step 2 and / or the second addition of hydrogen cyanide in step 3.
- the catalysts used according to the invention not only show a high selectivity in relation to the monoaddition products obtained in the hydrocyanation of 1,3-butadiene-containing hydrocarbon mixtures, but they can also be mixed with an excess of hydrogen cyanide in the hydrocyanation without causing it noticeable deposition of inactive nickel (II) compounds, such as Nickel (ll) cyanide is coming.
- II inactive nickel
- the catalysts containing a phosphinite phosphite I are therefore not only suitable for continuous hydrocyanation processes in which an excess of hydrogen cyanide in the reaction mixture can generally be effectively avoided, but also for semi-continuous ones Processes and batch processes in which there is generally a large excess of hydrogen cyanide.
- the catalysts used according to the invention and the processes for hydrocyanation based on them generally have higher catalyst recycle rates and longer catalyst service lives than known processes. In addition to improved economy, this is also advantageous from an ecological point of view, since the nickel cyanide formed from the active catalyst with hydrogen cyanide is highly toxic and must be worked up or disposed of at high cost.
- the systems according to the invention are generally suitable for all common hydrocyanation processes.
- the hydrocyanation of unactivated olefins e.g. of styrene and 3-pentenenitrile.
- hydrocyanic acid to an olefinic double bond in the presence of a catalyst system according to the invention in particular the addition to butadiene, a butadiene or to 3-pentenenitrile, 4-pentenenitrile or mixtures of such pentenenitriles, or the isomerization of organic nitriles in the presence of a catalyst according to the invention
- Talysatorsystems in particular the isomerization of 2-methyl-3-butenenitrile to 3-pentenenitrile, can advantageously be carried out in the presence of one or more Lewis acids as promoters which influence the activity, selectivity or both of the catalyst system according to the invention.
- Inorganic and organic compounds in which the cation is selected from the group consisting of scandium, titanium, vanadium, chromium, manganese, iron, cobalt, copper, zinc, boron, aluminum, yttrium, zirconium, niobium, molybdenum are suitable as promoters , Cadmium, rhenium and tin.
- Examples include ZnBr 2 , Znl 2 , ZnCI 2 , ZnSO, CuCl z , CuCI, Cu (O 3 SCF 3 ) 2 , CoCI 2 , Col 2 , Fel 2 , FeCI 3 , FeCI 2 , FeCI 2 (THF) 2 , TiCI 4 (THF) 2 , TiCI 4 , TiCl 3 , CITi (O-iso-Pr) 3 , MnCI 2 , ScCI 3 , AICI 3 , (C 2 H 5 ) AICI 2 , (C 2 H 5 ) 2 AICI, (C 2 H 5 ) 3 AI 2 CI 3 ,
- Suitable promoters are further described in US 3,496,217, US 3,496,218 and US 4,774,353. These include metal salts such as ZnCl 2 , Col 2 and SnCl 2 , and organometallic compounds such as RAICI 2 , R 3 SnO 3 SCF 3 , and R 3 B, where R is an alkyl group or aryl group. No. 4,874,884 describes how synergistically effective combinations of promoters can be selected in order to increase the catalytic activity of the catalyst system.
- Preferred promoters include CdCl 2 , FeCI 2 , ZnCl 2 , B (C 6 H 5 ) 3 and (C 6 H 5 ) 3 SnZ, where Z is CF 3 SO 3 , CH 3 C 6 H 4 SO 3 or (C 6 H 5 ) 3 BCN stands.
- the molar ratio of promoter to nickel in the catalyst system can be between 1:16 to 50: 1.
- a further advantageous embodiment of the hydrocyanation can be found in US Pat. No. 5,693,843, the content of which is hereby incorporated by reference into the present invention, with the proviso that a system according to the invention or a mixture of such systems is used instead of the catalysts mentioned in this patent.
- a further advantageous embodiment of the hydrocyanation can be found in US 5,523,453, the content of which is hereby incorporated by reference into the present invention, with the proviso that a system according to the invention or a mixture of such systems is used instead of the catalysts mentioned in this patent.
- nickel (0) - (m / p-tolyl phosphite) stands for a mixture containing 2.35% by weight of Ni (0), 19% by weight of 3-pentenenitrile and 78.65% by weight of m / p -Tolyl phosphite with a m: p ratio of 2: 1.
- Ni (COD) 2 stands for Ni (0) -bis- (1,4-cyclooctadiene), 2M3BN for 2-methyl-3-butenenitrile, t2M2BN for trans-2-methyl-2-butenenitrile, c2M2BN for cis-2- Methyl-2-butenenitrile, t2PN for trans-2-pentenenitrile, 4PN for 4-pentenenitrile, t3PN for trans-3-pentenenitrile, c3PN for cis- 3-pentenenitrile, MGN for methylglutaronitrile, 3PN for the sum of t3PN and c3PN, BD for 1, 3-butadiene, HCN for hydrocyanic acid, ADN for adiponitrile and THF for tetrahydrofuran.
- Example 1-3 Hydrocyanation of BD to 2M3BN / 3PN with subsequent 2M3BN isomerization
- the HCN conversion to 2M3BN / 3PN was> 95% (GC weight percent, internal standard: ethylbenzene).
- the ratio 2M3BN / 3PN was 1.8 / 1.
- the entire batch is then heated to 115 ° C. for 60 minutes in order to isomerize 2M3BN directly to 3PN.
- Example 7 (0.38 mmol Ni (0))
- Example 8 (0.35 mmol Ni (0))
- Example 11 (0.37 mmol Ni (0))
- Example 12 (0.36 mmol Ni (0))
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Application Number | Priority Date | Filing Date | Title |
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EP04790949A EP1682559B1 (de) | 2003-10-30 | 2004-10-28 | Sterisch anspruchsvolle chelatphosphinitphosphitliganden, katalysator, umfassend wenigstens einen nickel(0)komplex stabilisiert durch diesen liganden sowie ein verfahren zur herstellung von nitrilen |
US10/577,138 US7521575B2 (en) | 2003-10-30 | 2004-10-28 | Sterically hindered chelate phosphinite-phosphite ligand, catalyst, comprising at least one nickel(0) complex stabilized by said ligand and method for production of nitriles |
MXPA06003939A MXPA06003939A (es) | 2003-10-30 | 2004-10-28 | Catalizador que comprende al menos un complejo de niquel (0) estabilizado con un ligando quelato de fosfinitfosfito afectado estericamente, asi como un procedimiento para preparar nitrilos. |
DE502004010604T DE502004010604D1 (de) | 2003-10-30 | 2004-10-28 | Sterisch anspruchsvolle chelatphosphinitphosphitlickel(0)komplex stabilisiert durch diesen liganden sowie ein verfahren zur herstellung von nitrilen |
AT04790949T ATE453652T1 (de) | 2003-10-30 | 2004-10-28 | Sterisch anspruchsvolle chelatphosphinitphosphitliganden, katalysator, umfassend wenigstens einen nickel(0)komplex stabilisiert durch diesen liganden sowie ein verfahren zur herstellung von nitrilen |
BRPI0416080-0A BRPI0416080A (pt) | 2003-10-30 | 2004-10-28 | composto, uso do mesmo, complexo de metal de transição, e, processos para preparar o mesmo, para adicionar ácido cianìdrico a uma dupla ligação olefìnica, e para isomerizar nitrilas orgánicas na presença de um catalisador, e, uso de complexos de metal de transição |
CA002543673A CA2543673A1 (en) | 2003-10-30 | 2004-10-28 | Sterically hindered chelate phosphinite-phosphite ligand, catalyst, comprising at least one nickel(0) complex stabilized by said ligand and method for production of nitriles |
JP2006537184A JP4479925B2 (ja) | 2003-10-30 | 2004-10-28 | 立体規制ホスフィニット・ホスフィットキレート配位子で安定化された少なくとも1個のニッケル(0)錯体を含む触媒、およびニトリルの製造 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10350999.2 | 2003-10-30 | ||
DE10350999A DE10350999A1 (de) | 2003-10-30 | 2003-10-30 | Katalysator, umfassend wenigstens einen Nickel(O)Komplex stabilisiert durch einen sterisch anspruchsvollen Chelatphosphinitphosphitliganden, sowie ein Verfahren zur Herstellung von Nitrilen |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2005042547A1 true WO2005042547A1 (de) | 2005-05-12 |
Family
ID=34529999
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2004/012176 WO2005042547A1 (de) | 2003-10-30 | 2004-10-28 | Sterisch anspruchsvolle chelatphosphinitphosphitliganden, katalysator, umfassend wenigstens einen nickel (0) komplex stabilisiert durch diesen liganden sowie ein verfahren zur herstellung von nitrilen |
Country Status (12)
Country | Link |
---|---|
US (1) | US7521575B2 (de) |
EP (1) | EP1682559B1 (de) |
JP (1) | JP4479925B2 (de) |
KR (1) | KR20060107797A (de) |
CN (1) | CN100445292C (de) |
AR (1) | AR046817A1 (de) |
AT (1) | ATE453652T1 (de) |
BR (1) | BRPI0416080A (de) |
CA (1) | CA2543673A1 (de) |
DE (2) | DE10350999A1 (de) |
MX (1) | MXPA06003939A (de) |
WO (1) | WO2005042547A1 (de) |
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US7709674B2 (en) | 2006-07-14 | 2010-05-04 | Invista North America S.A R.L | Hydrocyanation process with reduced yield losses |
US7880028B2 (en) | 2006-07-14 | 2011-02-01 | Invista North America S.A R.L. | Process for making 3-pentenenitrile by hydrocyanation of butadiene |
US7897801B2 (en) | 2003-05-12 | 2011-03-01 | Invista North America S.A R.L. | Process for the preparation of dinitriles |
US7919646B2 (en) | 2006-07-14 | 2011-04-05 | Invista North America S.A R.L. | Hydrocyanation of 2-pentenenitrile |
US7973174B2 (en) | 2005-10-18 | 2011-07-05 | Invista North America S.A.R.L. | Process of making 3-aminopentanenitrile |
US7977502B2 (en) | 2008-01-15 | 2011-07-12 | Invista North America S.A R.L. | Process for making and refining 3-pentenenitrile, and for refining 2-methyl-3-butenenitrile |
US8088943B2 (en) | 2008-01-15 | 2012-01-03 | Invista North America S.A R.L. | Hydrocyanation of pentenenitriles |
US8101790B2 (en) | 2007-06-13 | 2012-01-24 | Invista North America S.A.R.L. | Process for improving adiponitrile quality |
US8178711B2 (en) | 2006-03-17 | 2012-05-15 | Invista North America S.A R.L. | Method for the purification of triorganophosphites by treatment with a basic additive |
US8247621B2 (en) | 2008-10-14 | 2012-08-21 | Invista North America S.A.R.L. | Process for making 2-secondary-alkyl-4,5-di-(normal-alkyl)phenols |
US8338636B2 (en) | 2009-08-07 | 2012-12-25 | Invista North America S.A R.L. | Hydrogenation and esterification to form diesters |
US8373001B2 (en) | 2003-02-10 | 2013-02-12 | Invista North America S.A R.L. | Method of producing dinitrile compounds |
DE102013211744A1 (de) | 2013-06-21 | 2014-12-24 | Evonik Industries Ag | Elektrochemisches Verfahren zur Herstellung von symmetrischen Biphenolen unter Verwendung einer Glaskohlenstoffanode |
DE102013211745A1 (de) | 2013-06-21 | 2014-12-24 | Evonik Industries Ag | Elektrochemisches Verfahren zur Herstellung von symmetrischen Biphenolen unter Verwendung von Essigsäure als Elektrolyt |
EP3064484A1 (de) | 2015-03-05 | 2016-09-07 | Evonik Degussa GmbH | Herstellung von 2,2'-biarylen in gegenwart von molybdän(v)-chlorid |
EP3095776A1 (de) | 2015-05-20 | 2016-11-23 | Evonik Degussa GmbH | Kupplung von einem Phenol und einem Aren unter Verwendung von Selendioxid |
EP3095775A1 (de) | 2015-05-20 | 2016-11-23 | Evonik Degussa GmbH | Verfahren zur herstellung von 2,2'-dihydroxy-3,3'-di-tert-butyl-5,5'-dimethoxy-1,1'-biphenol |
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DE102004004718A1 (de) | 2004-01-29 | 2005-08-18 | Basf Ag | Verfahren zur Hydrocyanierung |
US8906334B2 (en) | 2007-05-14 | 2014-12-09 | Invista North America S.A R.L. | High efficiency reactor and process |
JP2011515411A (ja) * | 2008-03-19 | 2011-05-19 | インビスタ テクノロジーズ エス エイ アール エル | シクロドデカトリエンの製造方法およびラウロラクトンの製造方法 |
FR2950349B1 (fr) * | 2009-09-18 | 2011-08-26 | Rhodia Operations | Composes organophosphores, systemes catalytiques comprenant ces composes et procede d'hydrocyanation utilisant ces systemes catalytiques |
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CN104662029A (zh) * | 2012-06-01 | 2015-05-27 | 因温斯特技术公司 | 稳定的氢氰化配体组合物 |
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2003
- 2003-10-30 DE DE10350999A patent/DE10350999A1/de not_active Withdrawn
-
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- 2004-10-27 AR ARP040103907A patent/AR046817A1/es unknown
- 2004-10-28 US US10/577,138 patent/US7521575B2/en not_active Expired - Fee Related
- 2004-10-28 DE DE502004010604T patent/DE502004010604D1/de active Active
- 2004-10-28 CN CNB200480032095XA patent/CN100445292C/zh not_active Expired - Fee Related
- 2004-10-28 CA CA002543673A patent/CA2543673A1/en not_active Abandoned
- 2004-10-28 EP EP04790949A patent/EP1682559B1/de not_active Not-in-force
- 2004-10-28 BR BRPI0416080-0A patent/BRPI0416080A/pt not_active IP Right Cessation
- 2004-10-28 MX MXPA06003939A patent/MXPA06003939A/es unknown
- 2004-10-28 AT AT04790949T patent/ATE453652T1/de not_active IP Right Cessation
- 2004-10-28 WO PCT/EP2004/012176 patent/WO2005042547A1/de active Application Filing
- 2004-10-28 JP JP2006537184A patent/JP4479925B2/ja active Active
- 2004-10-28 KR KR1020067010455A patent/KR20060107797A/ko not_active Application Discontinuation
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US5693843A (en) * | 1995-12-22 | 1997-12-02 | E. I. Du Pont De Nemours And Company | Process for hydrocyanation of diolefins and isomerization of nonconjugated 2 alkyl-3-monoalkenenitriles |
Cited By (18)
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US8373001B2 (en) | 2003-02-10 | 2013-02-12 | Invista North America S.A R.L. | Method of producing dinitrile compounds |
US7897801B2 (en) | 2003-05-12 | 2011-03-01 | Invista North America S.A R.L. | Process for the preparation of dinitriles |
US7973174B2 (en) | 2005-10-18 | 2011-07-05 | Invista North America S.A.R.L. | Process of making 3-aminopentanenitrile |
US8178711B2 (en) | 2006-03-17 | 2012-05-15 | Invista North America S.A R.L. | Method for the purification of triorganophosphites by treatment with a basic additive |
US7880028B2 (en) | 2006-07-14 | 2011-02-01 | Invista North America S.A R.L. | Process for making 3-pentenenitrile by hydrocyanation of butadiene |
US7709674B2 (en) | 2006-07-14 | 2010-05-04 | Invista North America S.A R.L | Hydrocyanation process with reduced yield losses |
US7919646B2 (en) | 2006-07-14 | 2011-04-05 | Invista North America S.A R.L. | Hydrocyanation of 2-pentenenitrile |
US8101790B2 (en) | 2007-06-13 | 2012-01-24 | Invista North America S.A.R.L. | Process for improving adiponitrile quality |
US7977502B2 (en) | 2008-01-15 | 2011-07-12 | Invista North America S.A R.L. | Process for making and refining 3-pentenenitrile, and for refining 2-methyl-3-butenenitrile |
US8088943B2 (en) | 2008-01-15 | 2012-01-03 | Invista North America S.A R.L. | Hydrocyanation of pentenenitriles |
US8247621B2 (en) | 2008-10-14 | 2012-08-21 | Invista North America S.A.R.L. | Process for making 2-secondary-alkyl-4,5-di-(normal-alkyl)phenols |
US8338636B2 (en) | 2009-08-07 | 2012-12-25 | Invista North America S.A R.L. | Hydrogenation and esterification to form diesters |
DE102013211744A1 (de) | 2013-06-21 | 2014-12-24 | Evonik Industries Ag | Elektrochemisches Verfahren zur Herstellung von symmetrischen Biphenolen unter Verwendung einer Glaskohlenstoffanode |
DE102013211745A1 (de) | 2013-06-21 | 2014-12-24 | Evonik Industries Ag | Elektrochemisches Verfahren zur Herstellung von symmetrischen Biphenolen unter Verwendung von Essigsäure als Elektrolyt |
EP3064484A1 (de) | 2015-03-05 | 2016-09-07 | Evonik Degussa GmbH | Herstellung von 2,2'-biarylen in gegenwart von molybdän(v)-chlorid |
EP3095776A1 (de) | 2015-05-20 | 2016-11-23 | Evonik Degussa GmbH | Kupplung von einem Phenol und einem Aren unter Verwendung von Selendioxid |
EP3095775A1 (de) | 2015-05-20 | 2016-11-23 | Evonik Degussa GmbH | Verfahren zur herstellung von 2,2'-dihydroxy-3,3'-di-tert-butyl-5,5'-dimethoxy-1,1'-biphenol |
US9771311B2 (en) | 2015-05-20 | 2017-09-26 | Evonik Degussa Gmbh | Coupling a phenol and an arene using selenium dioxide |
Also Published As
Publication number | Publication date |
---|---|
MXPA06003939A (es) | 2006-07-03 |
DE502004010604D1 (de) | 2010-02-11 |
KR20060107797A (ko) | 2006-10-16 |
EP1682559A1 (de) | 2006-07-26 |
CA2543673A1 (en) | 2005-05-12 |
JP2007509886A (ja) | 2007-04-19 |
CN100445292C (zh) | 2008-12-24 |
CN1875025A (zh) | 2006-12-06 |
DE10350999A1 (de) | 2005-06-02 |
JP4479925B2 (ja) | 2010-06-09 |
US20070060766A1 (en) | 2007-03-15 |
AR046817A1 (es) | 2005-12-28 |
EP1682559B1 (de) | 2009-12-30 |
BRPI0416080A (pt) | 2007-01-02 |
US7521575B2 (en) | 2009-04-21 |
ATE453652T1 (de) | 2010-01-15 |
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