CN112442087A - Preparation method and application of ionic phosphoramidite ligand - Google Patents
Preparation method and application of ionic phosphoramidite ligand Download PDFInfo
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- CN112442087A CN112442087A CN202011342977.3A CN202011342977A CN112442087A CN 112442087 A CN112442087 A CN 112442087A CN 202011342977 A CN202011342977 A CN 202011342977A CN 112442087 A CN112442087 A CN 112442087A
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- Prior art keywords
- phosphoramidite
- reaction
- ionic
- solvent
- ligand
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- 150000008300 phosphoramidites Chemical class 0.000 title claims abstract description 82
- 239000003446 ligand Substances 0.000 title claims abstract description 66
- 238000002360 preparation method Methods 0.000 title abstract description 14
- 238000006243 chemical reaction Methods 0.000 claims abstract description 61
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000000047 product Substances 0.000 claims abstract description 38
- 238000007037 hydroformylation reaction Methods 0.000 claims abstract description 23
- 239000002904 solvent Substances 0.000 claims abstract description 23
- 238000001914 filtration Methods 0.000 claims abstract description 21
- 239000000706 filtrate Substances 0.000 claims abstract description 17
- FAIAAWCVCHQXDN-UHFFFAOYSA-N phosphorus trichloride Chemical compound ClP(Cl)Cl FAIAAWCVCHQXDN-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 16
- 238000003756 stirring Methods 0.000 claims abstract description 5
- 238000005576 amination reaction Methods 0.000 claims abstract description 3
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 54
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 51
- 239000010948 rhodium Substances 0.000 claims description 25
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 24
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 18
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 230000003197 catalytic effect Effects 0.000 claims description 14
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 12
- 150000001336 alkenes Chemical class 0.000 claims description 11
- 239000007789 gas Substances 0.000 claims description 11
- 229910052703 rhodium Inorganic materials 0.000 claims description 11
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 11
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 10
- 239000002243 precursor Substances 0.000 claims description 10
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 8
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 7
- FSSPGSAQUIYDCN-UHFFFAOYSA-N 1,3-Propane sultone Chemical compound O=S1(=O)CCCO1 FSSPGSAQUIYDCN-UHFFFAOYSA-N 0.000 claims description 6
- VHYFNPMBLIVWCW-UHFFFAOYSA-N 4-Dimethylaminopyridine Chemical compound CN(C)C1=CC=NC=C1 VHYFNPMBLIVWCW-UHFFFAOYSA-N 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000003960 organic solvent Substances 0.000 claims description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N monobenzene Natural products C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 5
- VFWCMGCRMGJXDK-UHFFFAOYSA-N 1-chlorobutane Chemical compound CCCCCl VFWCMGCRMGJXDK-UHFFFAOYSA-N 0.000 claims description 4
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- JGFZNNIVVJXRND-UHFFFAOYSA-N N,N-Diisopropylethylamine (DIPEA) Chemical compound CCN(C(C)C)C(C)C JGFZNNIVVJXRND-UHFFFAOYSA-N 0.000 claims description 4
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- -1 methanesulfonic acid ester Chemical class 0.000 claims description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 4
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 4
- 150000008053 sultones Chemical class 0.000 claims description 4
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 4
- 239000002585 base Substances 0.000 claims description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 2
- VFLQQZCRHPIGJU-UHFFFAOYSA-N 1-(2-chloroethyl)piperidine;hydron;chloride Chemical compound Cl.ClCCN1CCCCC1 VFLQQZCRHPIGJU-UHFFFAOYSA-N 0.000 claims description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 2
- 229910019603 Rh2O3 Inorganic materials 0.000 claims description 2
- 150000008282 halocarbons Chemical class 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- 125000001967 indiganyl group Chemical group [H][In]([H])[*] 0.000 claims description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N methanesulfonic acid Substances CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 claims description 2
- 229940098779 methanesulfonic acid Drugs 0.000 claims description 2
- OIRDBPQYVWXNSJ-UHFFFAOYSA-N methyl trifluoromethansulfonate Chemical compound COS(=O)(=O)C(F)(F)F OIRDBPQYVWXNSJ-UHFFFAOYSA-N 0.000 claims description 2
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N pentanal Chemical compound CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 claims description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 2
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 239000008096 xylene Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 2
- POILWHVDKZOXJZ-ARJAWSKDSA-M (z)-4-oxopent-2-en-2-olate Chemical compound C\C([O-])=C\C(C)=O POILWHVDKZOXJZ-ARJAWSKDSA-M 0.000 claims 1
- GGRQQHADVSXBQN-FGSKAQBVSA-N carbon monoxide;(z)-4-hydroxypent-3-en-2-one;rhodium Chemical group [Rh].[O+]#[C-].[O+]#[C-].C\C(O)=C\C(C)=O GGRQQHADVSXBQN-FGSKAQBVSA-N 0.000 claims 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 claims 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 claims 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 150000005673 monoalkenes Chemical class 0.000 claims 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims 1
- BDDWSAASCFBVBK-UHFFFAOYSA-N rhodium;triphenylphosphane Chemical compound [Rh].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 BDDWSAASCFBVBK-UHFFFAOYSA-N 0.000 claims 1
- 230000002194 synthesizing effect Effects 0.000 abstract description 5
- 238000005956 quaternization reaction Methods 0.000 abstract description 4
- 230000007935 neutral effect Effects 0.000 abstract description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 30
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 19
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 16
- 229910052757 nitrogen Inorganic materials 0.000 description 15
- 239000013078 crystal Substances 0.000 description 14
- 238000001035 drying Methods 0.000 description 13
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 description 12
- 150000001299 aldehydes Chemical class 0.000 description 8
- 239000003054 catalyst Substances 0.000 description 8
- 238000005406 washing Methods 0.000 description 8
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- CUJRVFIICFDLGR-UHFFFAOYSA-N acetylacetonate Chemical compound CC(=O)[CH-]C(C)=O CUJRVFIICFDLGR-UHFFFAOYSA-N 0.000 description 6
- 238000004440 column chromatography Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 239000003480 eluent Substances 0.000 description 6
- 238000004817 gas chromatography Methods 0.000 description 6
- 229910000073 phosphorus hydride Inorganic materials 0.000 description 6
- 238000010992 reflux Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000012295 chemical reaction liquid Substances 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 5
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 description 4
- 230000002349 favourable effect Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- SIKJAQJRHWYJAI-UHFFFAOYSA-N Indole Chemical compound C1=CC=C2NC=CC2=C1 SIKJAQJRHWYJAI-UHFFFAOYSA-N 0.000 description 2
- KAESVJOAVNADME-UHFFFAOYSA-N Pyrrole Chemical compound C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 125000002883 imidazolyl group Chemical group 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000002390 rotary evaporation Methods 0.000 description 2
- 229910001495 sodium tetrafluoroborate Inorganic materials 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- DVWQNBIUTWDZMW-UHFFFAOYSA-N 1-naphthalen-1-ylnaphthalen-2-ol Chemical group C1=CC=C2C(C3=C4C=CC=CC4=CC=C3O)=CC=CC2=C1 DVWQNBIUTWDZMW-UHFFFAOYSA-N 0.000 description 1
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 1
- CCCUVHHPYBWVOW-UHFFFAOYSA-K [Na+].[Na+].[Na+].[O-]S(=O)(=O)c1ccccc1.[O-]S(=O)(=O)c1ccccc1.[O-]S(=O)(=O)c1ccccc1 Chemical compound [Na+].[Na+].[Na+].[O-]S(=O)(=O)c1ccccc1.[O-]S(=O)(=O)c1ccccc1.[O-]S(=O)(=O)c1ccccc1 CCCUVHHPYBWVOW-UHFFFAOYSA-K 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 150000004696 coordination complex Chemical class 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000007172 homogeneous catalysis Methods 0.000 description 1
- PZOUSPYUWWUPPK-UHFFFAOYSA-N indole Natural products CC1=CC=CC2=C1C=CN2 PZOUSPYUWWUPPK-UHFFFAOYSA-N 0.000 description 1
- RKJUIXBNRJVNHR-UHFFFAOYSA-N indolenine Natural products C1=CC=C2CC=NC2=C1 RKJUIXBNRJVNHR-UHFFFAOYSA-N 0.000 description 1
- 125000004433 nitrogen atom Chemical group N* 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- MYAJTCUQMQREFZ-UHFFFAOYSA-K tppts Chemical compound [Na+].[Na+].[Na+].[O-]S(=O)(=O)C1=CC=CC(P(C=2C=C(C=CC=2)S([O-])(=O)=O)C=2C=C(C=CC=2)S([O-])(=O)=O)=C1 MYAJTCUQMQREFZ-UHFFFAOYSA-K 0.000 description 1
- RIOQSEWOXXDEQQ-UHFFFAOYSA-N triphenylphosphine Substances C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 RIOQSEWOXXDEQQ-UHFFFAOYSA-N 0.000 description 1
- 231100000925 very toxic Toxicity 0.000 description 1
Classifications
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- 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
- C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
- C07F9/6564—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms
- C07F9/6571—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having phosphorus atoms, with or without nitrogen, oxygen, sulfur, selenium or tellurium atoms, as ring hetero atoms having phosphorus and oxygen atoms as the only ring hetero atoms
-
- 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
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1845—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
- B01J31/1865—Phosphonites (RP(OR)2), their isomeric phosphinates (R2(RO)P=O) and RO-substitution derivatives thereof
- B01J31/187—Amide derivatives thereof
-
- 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
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1845—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
- B01J31/1875—Phosphinites (R2P(OR), their isomeric phosphine oxides (R3P=O) and RO-substitution derivatives thereof)
- B01J31/188—Amide derivatives thereof
-
- 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
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/20—Carbonyls
-
- 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
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2213—At least two complexing oxygen atoms present in an at least bidentate or bridging ligand
-
- 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
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
- C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
- C07C45/505—Asymmetric hydroformylation
-
- 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
- C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
- C07F9/645—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having two nitrogen atoms as the only ring hetero atoms
- C07F9/6503—Five-membered rings
- C07F9/6506—Five-membered rings having the nitrogen atoms in positions 1 and 3
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- 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
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
- B01J2231/32—Addition reactions to C=C or C-C triple bonds
- B01J2231/321—Hydroformylation, metalformylation, carbonylation or hydroaminomethylation
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0238—Complexes comprising multidentate ligands, i.e. more than 2 ionic or coordinative bonds from the central metal to the ligand, the latter having at least two donor atoms, e.g. N, O, S, P
- B01J2531/0241—Rigid ligands, e.g. extended sp2-carbon frameworks or geminal di- or trisubstitution
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/82—Metals of the platinum group
- B01J2531/822—Rhodium
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Abstract
Description
Technical Field
The invention relates to a preparation method and application of an ionic phosphoramidite ligand, and the catalyst has the advantages of simple synthesis process, unique physical and chemical properties, and higher industrial application prospect in hydroformylation and other reactions, and belongs to the technical field of metal organic and homogeneous catalysis.
Background
The hydroformylation reaction is also called oxo reaction, and is characterized in that under the action of a catalyst, olefin and synthesis gas (CO + H)2) Catalytic reaction process for generating aldehyde or alcohol. The yield of aldehydes and alcohols produced by hydroformylation reactions has exceeded 1000 million tons per year.
In the early hydroformylation, a Co metal complex is used as a catalyst, but the reaction condition is harsh, the product selectivity is poor, and the Co complex is very toxic (Angew. chem. int. Ed.,1994,33, 2144). With the progress of research, it was found that the catalytic activity of Rh metal complexes is much higher than that of Co metal complexes, and thus Rh metal complexes gradually become the main catalyst of hydroformylation reaction.
The ligand is an important factor influencing the catalytic activity of the transition metal catalyst, and the phosphine ligand becomes the ligand which is most researched and widely applied so far due to the structural diversity and unique effect of the phosphine ligand. Depending on the atom to which P is bonded, phosphine ligands can be further divided into three classes, organic phosphine ligands (P bonded to three carbon atoms), phosphite ligands (P bonded to one or more O atoms), and phosphoramidite ligands (P bonded to one or more N atoms). The phosphoramidite ligand has the advantages of simple synthesis, easy modification and unique effect, and compared with tertiary phosphine ligands and phosphite ligands, the phosphoramidite is a stronger pi electron acceptor, which is favorable for separating CO from a catalyst and is favorable for the reaction rate of hydroformylation, however, the research on the phosphoramidite ligand is less at present. Patent CN106000470A designs and synthesizes phosphoramidite ligands of binaphthol skeleton, and the phosphoramidite ligands are used for catalyzing the hydroformylation reaction of olefin, so that the conversion rate is higher, but the method needs larger ligand dosage which needs to reach 100 times of the mole number of rhodium. Patent CN102746338A designs and synthesizes bidentate phosphoramidite ligands with spiroketal frameworks, and the ligands are applied to hydroformylation of olefins, have better catalytic activity, but the cost of the ligand synthesis raw materials is higher, which is not beneficial to industrial application.
In addition, the design and use of the water-soluble ligand can realize the hydroformylation reaction of water and oil phases, and improve the separation and recovery efficiency of the catalyst. A breakthrough of the ligand is sulfonated aryl phosphine TPPTS (3, 3' -phosphinylidyne tris (benzenesulfonic acid) trisodium salt), however, the preparation process of the ligand is complex, the reaction conditions are harsh, and the existence of oxygen needs to be strictly eliminated, so that the development of a novel water-soluble ligand by a simple and efficient method is favorable for promoting the further development of hydroformylation reaction, and the ligand has a good industrial application prospect.
Although phosphoramidite ligands have been reported, most of the work is focused on pyrrole, indole and the like as modifying groups, and the synthesis method of the phosphoramidite ligands taking imidazole as a group is yet to be designed and optimized. In addition, the imidazole group can be subjected to quaternization modification so as to change the electronic effect, water solubility and other characteristics of the ligand, thereby regulating and controlling the catalytic effect of the transition metal catalyst and having the potential of realizing water-oil two-phase hydroformylation reaction.
The research on the phosphoramidite ligand is relatively limited compared with the synthesis application of the phosphite ligand, and the water-soluble phosphoramidite ligand is more rarely reported.
Disclosure of Invention
The technical problem to be solved by the invention is as follows: provides a series of ionic phosphoramidite ligands modified by imidazole groups, a method for efficiently synthesizing the ligands and application of the ligands in hydroformylation.
In order to solve the technical problems, the invention provides an ionic phosphoramidite ligand, which is characterized in that the structural general formula is as follows:
In the above formula, R1、R2Independently of one another is hydrogen, C1-C 6Alkyl or C1-C 6Alkoxy radical, R3Independently is C1-C18Alkyl or sultone.
The invention also provides the preparation method, which is characterized by comprising the following steps:
step 1): dissolving phosphorus trichloride and imidazole in a solvent, stirring for reaction, filtering, dissolving substituted biphenol in the solvent, dropwise adding the substituted biphenol into the filtrate for reaction, and purifying the obtained product to obtain monodentate phosphoramidite;
step 2): reacting monodentate phosphoramidite with a quaternizing agent in a solvent to obtain a product, and purifying the product to obtain an ionic monodentate phosphoramidite ligand shown in a formula I;
step 3): dissolving phosphorus trichloride and imidazole in a solvent, stirring for reaction under an alkaline condition, filtering, dissolving substituted biphenol in the solvent, dropwise adding the substituted biphenol into the filtrate for reaction, and purifying the obtained product to obtain the bidentate phosphoramidite.
Step 4): reacting the bidentate phosphoramidite with a quaternary amination reagent in a solvent to obtain a product, and purifying the product to obtain the ionic bidentate phosphoramidite ligand shown in the formula II.
The principle of the steps 1) and 2) is as follows:
the principles of the steps 3) and 4) are as follows:
preferably, the solvent is at least one of dichloromethane, tetrahydrofuran, chloroform, toluene, dimethyl sulfoxide, acetonitrile and deionized water; the purification means may be any post-treatment of the resulting product by various post-treatment methods conventionally used in the art. Methods of such post-processing include, but are not limited to: extraction, recrystallization, washing, drying, filtration, and the like.
Preferably, in the step 2) and 4), the quaternizing agent is at least one of halogenated hydrocarbon, a methanesulfonic acid ester derivative and a sultone derivative; the reaction temperature is 25-150 deg.C, and the reaction time is 0.5-48h, preferably 24 h.
More preferably, the quaternizing agent is at least one of n-butyl chloride, chloroethyl piperidine hydrochloride, methyl trifluoromethanesulfonate and 1, 3-propane sultone.
Preferably, the molar ratio of the phosphorus trichloride to the imidazole in the step 1) is 1:6-1:10, preferably 1: 7; the molar ratio of phosphorus trichloride to imidazole in the step 3) is 1: 2; the alkali adopted under the alkaline condition is organic alkali or inorganic alkali; the molar ratio of phosphorus trichloride to base is from 1:2 to 1:6, preferably 1: 3.
Preferably, the base used in the alkaline condition is at least one of triethylamine, pyridine, 4-dimethylaminopyridine, diisopropylethylamine and potassium carbonate, preferably any one or two of triethylamine and 4-dimethylaminopyridine.
Preferably, the reaction in step 1) and 3) is carried out at a temperature of 0-100 ℃, preferably 25 ℃ for 0.5-24h, preferably 1 h.
The invention also provides application of the ionic type phosphoramidite ligand in hydroformylation reaction, which is characterized in that a rhodium catalytic precursor, the ionic type phosphoramidite ligand and an organic solvent are added into a reaction kettle, olefin is added, then gas is filled, and the reaction kettle is heated for reaction.
Preferably, the rhodium catalytic precursor is rhodium acetylacetonate dicarbonyl, rhodium acetylacetonate triphenylphosphine carbonyl, rhodium triphenylphosphine hydride, Rh (OAc)3、Rh2O3、Rh4(CO)12And Rh6(CO)16At least one of; the organic solvent is at least one of benzene, toluene, xylene, valeraldehyde, dimethyl sulfoxide, dichloromethane, dichloroethane, acetonitrile, hexane, ethyl acetate, dioxane, tetrahydrofuran, methanol, ethanol, n-propanol, isopropanol and n-butanol; the olefin is C2-C18Preferably propylene, butene, octene, styrene; the molar ratio of the rhodium catalytic precursor to the ionic phosphoramidite ligand is 1: 1-1: 50, preferably in a molar ratio of rhodium catalytic precursor to monodentate phosphoramidite ligand of 1:10, the molar ratio of rhodium catalytic precursor to bidentate phosphoramidite ligand is 1: 5; the molar ratio of the rhodium catalytic precursor to the olefin is 1: 100-1: 10000; the volume ratio of the organic solvent to the olefin is 1: 1-20: 1; the gas is CO and H2In a molar ratio of 1:1, the pressure of the reaction kettle after being filled with gas is 2-8MPa, preferably 3-5 MPa.
Preferably, the heating reaction is carried out at a temperature of 80-180 ℃, preferably 90-120 ℃ for 0.5-10h, preferably 2 h.
The method provided by the invention can be used for conveniently synthesizing a series of neutral phosphoramidite ligands and efficiently synthesizing a series of ionic phosphoramidite ligands with different physicochemical properties by a quaternization method.
Compared with the prior art, the invention has the following advantages:
(1) the novel ionic phosphoramidite ligand provided by the invention has high pi electron accepting capacity and is favorable for the reaction rate of hydroformylation;
(2) the invention can change the characteristics of water solubility, oil solubility and the like of the obtained phosphoramidite ligand through simple quaternization, realizes the high-efficiency preparation and functional modification of the water-soluble phosphoramidite ligand, and has good application prospect in hydroformylation reaction.
Detailed Description
In order to make the invention more comprehensible, preferred embodiments are described in detail below.
Example 1
A preparation method of ionic monodentate phosphoramidite with a structural formula A and an application thereof in butene hydroformylation are disclosed:
dissolving 2.04g of imidazole in 50mL of ultra-dry dichloromethane under the protection of nitrogen, dropwise adding 0.43mL of phosphorus trichloride under ice bath, reacting for 30min, filtering, and protecting the filtrate with nitrogen. Dissolving 0.93g of diphenol in 10mL of ultra-dry dichloromethane, dropwise adding the solution into the filtrate, reacting at room temperature for 1h, filtering, spin-drying the solvent, and purifying the obtained product by column chromatography, wherein an eluent is ethyl acetate: n-hexane ═ 1:10, obtaining the monodentate phosphoramidite product. Under the protection of nitrogen, dissolving 1.41g of the obtained monodentate phosphoramidite in 20mL of toluene, adding 0.52mL of n-butyl chloride, heating to 110 ℃, refluxing for 12h, cooling, precipitating crystals, quickly filtering, washing the crystals with diethyl ether, dissolving the obtained crystals in deionized water, and adding NaBF40.55g is stirred at room temperature for 24 h. And (3) after the reaction is finished, removing water by rotary evaporation, extracting the product by using dichloromethane, drying the product by using anhydrous sodium sulfate, and then carrying out rotary drying to obtain the ionic phosphoramidite product A with the yield of 85%.
0.02mmol of Rh (acac) (CO)20.2mmol of phosphoramidite ligand A was charged into a 100mL reaction vessel, 40mL of a toluene solvent was added, followed by three-time replacement with a synthetic gas, 20mmol (1.72g) of n-butene was added, and the reaction was carried out at 120 ℃ with purging of the synthetic gas to 4 MPa. After 4h, the reaction kettle is cooled, the reaction liquid is washed out by toluene, an internal standard substance is added, and gas chromatography analysis is carried out, so that the n-butene conversion rate is 35%, the aldehyde selectivity is 91%, and the normal-iso ratio is 4.5.
Example 2
A preparation method of ionic monodentate phosphoramidite with a structural formula B and an application thereof in butene hydroformylation are disclosed:
dissolving 2.04g of imidazole in 50mL of ultra-dry dichloromethane under the protection of nitrogen, dropwise adding 0.43mL of phosphorus trichloride under ice bath, reacting for 30min, filtering, and protecting the filtrate with nitrogen. Dissolving 0.93g of diphenol in 10mL of ultra-dry dichloromethane, dropwise adding the solution into the filtrate, reacting at room temperature for 1h, filtering, spin-drying the solvent, and purifying the obtained product by column chromatography, wherein an eluent is ethyl acetate: n-hexane ═ 1:10, obtaining the monodentate phosphoramidite product. Under the protection of nitrogen, 1.41g of the obtained monodentate phosphoramidite is dissolved in 20mL of toluene, 0.61g of 1, 3-propane sultone is added, the temperature is raised to 110 ℃, reflux is carried out for 12h, crystals are separated out after cooling, the crystals are quickly filtered, washed by ether and dried to obtain the ionic phosphoramidite product B, and the yield is 79%.
0.02mmol of Rh (acac) (CO)20.2mmol of phosphoramidite ligand B was charged into a 100mL reaction vessel, 40mL of a toluene solvent was added, followed by three-time replacement with a synthetic gas, 20mmol (1.72g) of n-butene was added, and the reaction was carried out at 120 ℃ with purging of the synthetic gas to 4 MPa. After 4h, the reaction kettle is cooled, the reaction liquid is washed out by toluene, an internal standard substance is added, and gas chromatography analysis is carried out, so that the n-butene conversion rate is 70%, the aldehyde selectivity is 94%, and the n-iso ratio is 5.4.
Example 3
A preparation method of ionic monodentate phosphoramidite with a structural formula of C and an application thereof in butene hydroformylation are disclosed:
dissolving 2.04g of imidazole in 50mL of ultra-dry dichloromethane under the protection of nitrogen, dropwise adding 0.43mL of phosphorus trichloride under ice bath, reacting for 30min, filtering, and protecting the filtrate with nitrogen. Dissolving 2.05g of 3,3 ' -5,5 ' -tetra-tert-butyl-2, 2 ' -biphenol in 10mL of ultra-dry dichloromethane, dropwise adding the solution into the filtrate, reacting at room temperature for 1h, filtering, spin-drying the solvent, and purifying the obtained product by column chromatography, wherein the eluent is ethyl acetate: n-hexane ═ 1:10, obtaining the monodentate phosphoramidite product. Under the protection of nitrogen, 2.53g of the obtained monodentate phosphoramidite is dissolved in 20mL of toluene, 0.61g of 1, 3-propane sultone is added, the temperature is raised to 110 ℃, reflux is carried out for 12h, crystals are separated out after cooling, the crystals are quickly filtered, washed by ether and dried to obtain the ionic phosphoramidite product C, and the yield is 75%.
0.02mmol of Rh (acac) (CO)20.1mmol of phosphoramidite ligand C was charged into a 100mL reaction vessel, 40mL of a toluene solvent was added, followed by three-time replacement with syngas, 20mmol (1.72g) of n-butene was added, and syngas was purged to 4MPa to conduct a reaction at 120 ℃. After 4h, the reaction kettle is cooled, toluene is used for washing out reaction liquid, an internal standard substance is added, and gas chromatography analysis is carried out, so that the n-butene conversion rate is 80%, the aldehyde selectivity is 94%, and the normal-iso ratio is 6.
Example 4
Preparation method of bidentate phosphoramidite with structural formula D and application of bidentate phosphoramidite in butene hydroformylation reaction
Dissolving 2.04g of imidazole and 1.39mL of triethylamine in 50mL of ultra-dry dichloromethane under the protection of nitrogen, dropwise adding 1.29mL of phosphorus trichloride under ice bath, reacting for 30min, filtering, and protecting the filtrate with nitrogen. Dissolving 0.93g of diphenol in 10mL of ultra-dry dichloromethane, dropwise adding the solution into the filtrate, reacting at room temperature for 1h, filtering, spin-drying the solvent, and purifying the obtained product by column chromatography, wherein an eluent is ethyl acetate: n-hexane ═ 1:6, obtaining the bidentate phosphoramidite product. Dissolving 2.57g of the obtained bidentate phosphoramidite in 40mL of toluene, adding 0.52mL of n-butyl chloride, heating to 110 ℃, refluxing for 12h, cooling, precipitating crystals, rapidly performing suction filtration, washing the crystals with diethyl ether, dissolving the obtained crystals in deionized water, and adding NaBF42.20g are stirred at room temperature for 24 h. And (3) after the reaction is finished, removing water by rotary evaporation, extracting the product by using dichloromethane, drying the product by using anhydrous sodium sulfate, and then carrying out rotary drying to obtain the ionic phosphoramidite product D with the yield of 74%.
0.02mmol of Rh (acac) (CO)20.1mmol of phosphoramidite ligand D, into a 100mL reaction vessel, 40mL of toluene solvent was added, followed by three times of replacement with syngas, 20mmol of n-butene was added, and syngas was purged to 4MPa to conduct the reaction at 120 ℃. After 4h, the reaction is finished, the reaction kettle is cooled, toluene is used for washing out reaction liquid, an internal standard substance is added, and gas chromatography analysis is carried out, so that the n-butene conversion rate is 90%, the aldehyde selectivity is 97%, and the normal-iso ratio is 11.
Example 5
A preparation method of ionic bidentate phosphoramidite with a structural formula of E and an application thereof in butene hydroformylation reaction are disclosed:
dissolving 2.04g of imidazole and 1.39mL of triethylamine in 50mL of ultra-dry dichloromethane under the protection of nitrogen, dropwise adding 1.29mL of phosphorus trichloride under ice bath, reacting for 30min, filtering, and protecting the filtrate with nitrogen. Dissolving 0.93g of diphenol in 10mL of ultra-dry dichloromethane, dropwise adding the solution into the filtrate, reacting at room temperature for 1h, filtering, spin-drying the solvent, and purifying the obtained product by column chromatography, wherein an eluent is ethyl acetate: n-hexane ═ 1:6, obtaining the bidentate phosphoramidite product. Dissolving 2.57g of the obtained bidentate phosphoramidite in 40mL of toluene, refluxing 0.61g of 1, 3-propane sultone at 110 ℃ for 12h, cooling, separating out crystals, quickly filtering, washing the crystals with diethyl ether, and drying to obtain the ionic phosphoramidite product E with the yield of 70%.
0.02mmol of Rh (acac) (CO)20.1mmol of phosphoramidite ligand E, into a 100mL reaction vessel, 40mL of toluene solvent was added, followed by three times of replacement with syngas, 20mmol of n-butene was added, and syngas was purged to 4MPa to conduct the reaction at 120 ℃. After 4h, the reaction is finished, and the reaction kettle is cooledThe reaction solution was washed out with toluene, and an internal standard was added to conduct gas chromatography, whereby the n-butene conversion was 84%, the aldehyde selectivity was 95%, and the n-iso ratio was 10.
Example 6
A preparation method of ionic bidentate phosphoramidite with a structural formula of F and an application thereof in butene hydroformylation reaction are disclosed:
dissolving 2.04g of imidazole and 1.39mL of triethylamine in 50mL of ultra-dry dichloromethane under the protection of nitrogen, dropwise adding 1.29mL of phosphorus trichloride under ice bath, reacting for 30min, filtering, and protecting the filtrate with nitrogen. Dissolving 2.05g of 3,3 ' -5,5 ' -tetra-tert-butyl-2, 2 ' -biphenol in 10mL of ultra-dry dichloromethane, dropwise adding the solution into the filtrate, reacting at room temperature for 1h, filtering, spin-drying the solvent, and purifying the obtained product by column chromatography, wherein the eluent is ethyl acetate: n-hexane ═ 1:6, obtaining the bidentate phosphoramidite product. Dissolving 3.69g of the obtained bidentate phosphoramidite in 40mL of toluene, refluxing 0.61g of 1, 3-propane sultone at 110 ℃ for 12h, cooling, separating out crystals, quickly filtering, washing the crystals with diethyl ether, and drying to obtain the ionic phosphoramidite product F with the yield of 65%.
0.02mmol of Rh (acac) (CO)20.1mmol of phosphoramidite ligand F, into a 100mL reaction vessel, 40mL of toluene solvent was added, followed by three times of replacement with syngas, 20mmol of n-butene was added, and syngas was purged to 4MPa to conduct the reaction at 120 ℃. After 4h, the reaction is finished, the reaction kettle is cooled, toluene is used for washing out reaction liquid, an internal standard substance is added, and gas chromatography analysis is carried out, so that the n-butene conversion rate is 95%, the aldehyde selectivity is 99%, and the normal-iso ratio is 15.
Claims (11)
2. The process for preparing ionic phosphoramidite ligands according to claim 1, comprising the steps of:
step 1): dissolving phosphorus trichloride and imidazole in a solvent, stirring for reaction, filtering, dissolving substituted biphenol in the solvent, dropwise adding the substituted biphenol into the filtrate for reaction, and purifying the obtained product to obtain monodentate phosphoramidite;
step 2): reacting monodentate phosphoramidite with a quaternizing agent in a solvent to obtain a product, and purifying the product to obtain an ionic monodentate phosphoramidite ligand shown in a formula I;
step 3): dissolving phosphorus trichloride and imidazole in a solvent, stirring for reaction under an alkaline condition, filtering, dissolving substituted biphenol in the solvent, dropwise adding the substituted biphenol into the filtrate for reaction, and purifying the obtained product to obtain the bidentate phosphoramidite.
Step 4): reacting the bidentate phosphoramidite with a quaternary amination reagent in a solvent to obtain a product, and purifying the product to obtain the ionic bidentate phosphoramidite ligand shown in the formula II.
3. The method of claim 2, wherein the solvent is at least one of dichloromethane, tetrahydrofuran, chloroform, toluene, dimethylsulfoxide, acetonitrile, and deionized water.
4. The method of claim 2, wherein in the steps 2) and 4), the quaternizing agent is at least one of a halogenated hydrocarbon, a methanesulfonic acid ester derivative and a sultone derivative; the reaction temperature is 25-150 ℃ and the reaction time is 0.5-48 h.
5. The method of claim 4, wherein the quaternizing agent is at least one of n-butyl chloride, chloroethyl piperidine hydrochloride, methyl trifluoromethanesulfonate, and 1, 3-propane sultone.
6. The method for preparing ionic phosphoramidite ligands according to claim 2, wherein the molar ratio of phosphorus trichloride to imidazole in step 1) is from 1:6 to 1: 10; the molar ratio of phosphorus trichloride to imidazole in the step 3) is 1: 2; the alkali adopted under the alkaline condition is organic alkali or inorganic alkali; the molar ratio of the phosphorus trichloride to the alkali is 1:2-1: 6.
7. The method of claim 6, wherein the basic conditions are performed using at least one base selected from the group consisting of triethylamine, pyridine, 4-dimethylaminopyridine, diisopropylethylamine, and potassium carbonate.
8. The process for preparing ionic phosphoramidite ligands according to claim 2, wherein the reaction in steps 1) and 3) is carried out at a temperature of 0 to 100 ℃ for a time of 0.5 to 24 hours.
9. The use of the ionic phosphoramidite ligand of claim 1 in hydroformylation reactions, wherein the rhodium catalytic precursor, the ionic phosphoramidite ligand and an organic solvent are added into a reaction vessel, an olefin is added, then a gas is introduced, and the reaction vessel is heated for reaction.
10. The use of claim 9 wherein the rhodium catalytic precursor is rhodium dicarbonyl acetylacetonate, rhodium triphenylphosphine carbonyl acetylacetonate, rhodium triphenylphosphine hydride, Rh (OAc)3、Rh2O3、Rh4(CO)12And Rh6(CO)16At least one of; the organic solvent is benzene, toluene, xylene, valeraldehyde, dimethyl sulfoxide or dimethyl sulfoxideAt least one of methyl chloride, dichloroethane, acetonitrile, hexane, ethyl acetate, dioxane, tetrahydrofuran, methanol, ethanol, n-propanol, isopropanol, and n-butanol; the olefin is C2-C18A monoolefin of (a); the molar ratio of the rhodium catalytic precursor to the ionic phosphoramidite ligand is 1: 1-1: 50; the molar ratio of the rhodium catalytic precursor to the olefin is 1: 100-1: 10000; the volume ratio of the organic solvent to the olefin is 1: 1-20: 1; the gas is CO and H2In a molar ratio of 1:1, the pressure of the reaction kettle filled with gas is 2-8 MPa.
11. The use according to claim 9, wherein the heating reaction is carried out at a temperature of 80 to 180 ℃ for a time of 0.5 to 10 hours.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114456041A (en) * | 2022-02-21 | 2022-05-10 | 广东仁康达材料科技有限公司 | Preparation method of isomeric tridecanol |
CN114835905A (en) * | 2022-06-01 | 2022-08-02 | 常州巨德新材料有限公司 | Polyphosphazene amide metal complex catalyst for catalytic polymerization and preparation method thereof |
CN115739184A (en) * | 2022-09-27 | 2023-03-07 | 成都欣华源科技有限责任公司 | Diisobutylene hydroformylation catalyst composition and application thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108525704A (en) * | 2018-04-25 | 2018-09-14 | 四川大学 | Catalyst and its preparation method and application for hydroformylation of olefin |
-
2020
- 2020-11-26 CN CN202011342977.3A patent/CN112442087A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108525704A (en) * | 2018-04-25 | 2018-09-14 | 四川大学 | Catalyst and its preparation method and application for hydroformylation of olefin |
Non-Patent Citations (3)
Title |
---|
ARMIN·BORNER 等 著: "《氢甲酰化反应的原理、过程和工业应用 上》", 30 November 2018, 华东理工大学出版社, pages: 83 * |
LAURENT LEFORT: "Rapid Identification of a Scalable Catalyst for the Asymmetric Hydrogenation of a Sterically Demanding Aryl Enamide", 《ORGANIC PROCESS RESEARCH & DEVELOPMENT》, vol. 14, no. 3, 31 December 2010 (2010-12-31), pages 568 - 573, XP055134224, DOI: 10.1021/op100011y * |
VARINIA BERNALES: "Rhodium catalyzed hydroformylation of olefins", 《JOURNAL OF COMPUTATIONAL CHEMISTRY》, vol. 40, no. 2, 31 December 2019 (2019-12-31), pages 342 - 348 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114456041A (en) * | 2022-02-21 | 2022-05-10 | 广东仁康达材料科技有限公司 | Preparation method of isomeric tridecanol |
CN114835905A (en) * | 2022-06-01 | 2022-08-02 | 常州巨德新材料有限公司 | Polyphosphazene amide metal complex catalyst for catalytic polymerization and preparation method thereof |
CN115739184A (en) * | 2022-09-27 | 2023-03-07 | 成都欣华源科技有限责任公司 | Diisobutylene hydroformylation catalyst composition and application thereof |
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