CN113788748A - Method for preparing straight-chain carbonyl compound by catalyzing unsaturated hydrocarbon with multidentate phosphine ligand modified palladium combined catalyst - Google Patents
Method for preparing straight-chain carbonyl compound by catalyzing unsaturated hydrocarbon with multidentate phosphine ligand modified palladium combined catalyst Download PDFInfo
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- CN113788748A CN113788748A CN202111081268.9A CN202111081268A CN113788748A CN 113788748 A CN113788748 A CN 113788748A CN 202111081268 A CN202111081268 A CN 202111081268A CN 113788748 A CN113788748 A CN 113788748A
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- Prior art keywords
- palladium
- phosphine ligand
- unsaturated hydrocarbon
- bis
- aryl
- Prior art date
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- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 title claims abstract description 98
- 239000003446 ligand Substances 0.000 title claims abstract description 58
- 229910000073 phosphorus hydride Inorganic materials 0.000 title claims abstract description 51
- 239000003054 catalyst Substances 0.000 title claims abstract description 36
- 229930195735 unsaturated hydrocarbon Natural products 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 33
- 150000001728 carbonyl compounds Chemical class 0.000 title claims abstract description 28
- 150000002940 palladium Chemical class 0.000 title claims description 4
- -1 phosphine ligand-modified palladium Chemical class 0.000 claims abstract description 40
- 238000006243 chemical reaction Methods 0.000 claims abstract description 37
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 30
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 30
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 30
- 238000005810 carbonylation reaction Methods 0.000 claims abstract description 28
- 150000002941 palladium compounds Chemical class 0.000 claims abstract description 18
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 13
- 239000012434 nucleophilic reagent Substances 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 13
- 239000002131 composite material Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 150000001408 amides Chemical class 0.000 claims abstract description 8
- 150000001733 carboxylic acid esters Chemical class 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 230000002378 acidificating effect Effects 0.000 claims abstract description 7
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 7
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 6
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 31
- 125000003118 aryl group Chemical group 0.000 claims description 24
- 230000006315 carbonylation Effects 0.000 claims description 21
- 125000001424 substituent group Chemical group 0.000 claims description 20
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 claims description 16
- 229910052763 palladium Inorganic materials 0.000 claims description 15
- 125000000217 alkyl group Chemical group 0.000 claims description 14
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 10
- 229910052736 halogen Inorganic materials 0.000 claims description 10
- 150000002367 halogens Chemical group 0.000 claims description 10
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 claims description 10
- 238000007789 sealing Methods 0.000 claims description 10
- 125000002023 trifluoromethyl group Chemical group FC(F)(F)* 0.000 claims description 10
- 238000001816 cooling Methods 0.000 claims description 9
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 9
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 9
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 8
- 238000005886 esterification reaction Methods 0.000 claims description 7
- 150000003141 primary amines Chemical class 0.000 claims description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 6
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 6
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 6
- 150000001336 alkenes Chemical group 0.000 claims description 6
- 125000003342 alkenyl group Chemical group 0.000 claims description 6
- 238000006473 carboxylation reaction Methods 0.000 claims description 6
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 claims description 6
- 238000007112 amidation reaction Methods 0.000 claims description 5
- CXNIUSPIQKWYAI-UHFFFAOYSA-N xantphos Chemical compound C=12OC3=C(P(C=4C=CC=CC=4)C=4C=CC=CC=4)C=CC=C3C(C)(C)C2=CC=CC=1P(C=1C=CC=CC=1)C1=CC=CC=C1 CXNIUSPIQKWYAI-UHFFFAOYSA-N 0.000 claims description 5
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 4
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 claims description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 4
- 150000001345 alkine derivatives Chemical group 0.000 claims description 4
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims description 4
- 239000001099 ammonium carbonate Substances 0.000 claims description 4
- 235000019270 ammonium chloride Nutrition 0.000 claims description 4
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 4
- 150000001993 dienes Chemical class 0.000 claims description 4
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 4
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 4
- RIOQSEWOXXDEQQ-UHFFFAOYSA-N triphenylphosphine Chemical compound C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 RIOQSEWOXXDEQQ-UHFFFAOYSA-N 0.000 claims description 4
- HSWZLYXRAOXOLL-UHFFFAOYSA-N (6-diphenylphosphanyl-10h-phenoxazin-4-yl)-diphenylphosphane Chemical compound C=12OC(C(=CC=C3)P(C=4C=CC=CC=4)C=4C=CC=CC=4)=C3NC2=CC=CC=1P(C=1C=CC=CC=1)C1=CC=CC=C1 HSWZLYXRAOXOLL-UHFFFAOYSA-N 0.000 claims description 3
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 claims description 3
- YJVFFLUZDVXJQI-UHFFFAOYSA-L palladium(ii) acetate Chemical compound [Pd+2].CC([O-])=O.CC([O-])=O YJVFFLUZDVXJQI-UHFFFAOYSA-L 0.000 claims description 3
- CYPYTURSJDMMMP-WVCUSYJESA-N (1e,4e)-1,5-diphenylpenta-1,4-dien-3-one;palladium Chemical compound [Pd].[Pd].C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1.C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1.C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1 CYPYTURSJDMMMP-WVCUSYJESA-N 0.000 claims description 2
- UKSZBOKPHAQOMP-SVLSSHOZSA-N (1e,4e)-1,5-diphenylpenta-1,4-dien-3-one;palladium Chemical compound [Pd].C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1.C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1 UKSZBOKPHAQOMP-SVLSSHOZSA-N 0.000 claims description 2
- QFMZQPDHXULLKC-UHFFFAOYSA-N 1,2-bis(diphenylphosphino)ethane Chemical compound C=1C=CC=CC=1P(C=1C=CC=CC=1)CCP(C=1C=CC=CC=1)C1=CC=CC=C1 QFMZQPDHXULLKC-UHFFFAOYSA-N 0.000 claims description 2
- VYXHVRARDIDEHS-UHFFFAOYSA-N 1,5-cyclooctadiene Chemical compound C1CC=CCCC=C1 VYXHVRARDIDEHS-UHFFFAOYSA-N 0.000 claims description 2
- 239000004912 1,5-cyclooctadiene Substances 0.000 claims description 2
- JJRYTJCOOYOVOZ-UHFFFAOYSA-N 1-diphenylphosphanylbutan-2-yl(diphenyl)phosphane Chemical compound C=1C=CC=CC=1P(C=1C=CC=CC=1)C(CC)CP(C=1C=CC=CC=1)C1=CC=CC=C1 JJRYTJCOOYOVOZ-UHFFFAOYSA-N 0.000 claims description 2
- WGOBPPNNYVSJTE-UHFFFAOYSA-N 1-diphenylphosphanylpropan-2-yl(diphenyl)phosphane Chemical compound C=1C=CC=CC=1P(C=1C=CC=CC=1)C(C)CP(C=1C=CC=CC=1)C1=CC=CC=C1 WGOBPPNNYVSJTE-UHFFFAOYSA-N 0.000 claims description 2
- LDMOEFOXLIZJOW-UHFFFAOYSA-N 1-dodecanesulfonic acid Chemical compound CCCCCCCCCCCCS(O)(=O)=O LDMOEFOXLIZJOW-UHFFFAOYSA-N 0.000 claims description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 2
- CMWINYFJZCARON-UHFFFAOYSA-N 6-chloro-2-(4-iodophenyl)imidazo[1,2-b]pyridazine Chemical compound C=1N2N=C(Cl)C=CC2=NC=1C1=CC=C(I)C=C1 CMWINYFJZCARON-UHFFFAOYSA-N 0.000 claims description 2
- 235000011054 acetic acid Nutrition 0.000 claims description 2
- TWKVUTXHANJYGH-UHFFFAOYSA-L allyl palladium chloride Chemical compound Cl[Pd]CC=C.Cl[Pd]CC=C TWKVUTXHANJYGH-UHFFFAOYSA-L 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 2
- YNHIGQDRGKUECZ-UHFFFAOYSA-N dichloropalladium;triphenylphosphanium Chemical compound Cl[Pd]Cl.C1=CC=CC=C1[PH+](C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1[PH+](C=1C=CC=CC=1)C1=CC=CC=C1 YNHIGQDRGKUECZ-UHFFFAOYSA-N 0.000 claims description 2
- SFCNPIUDAIFHRD-UHFFFAOYSA-N ditert-butyl-[[2-(ditert-butylphosphanylmethyl)phenyl]methyl]phosphane Chemical compound CC(C)(C)P(C(C)(C)C)CC1=CC=CC=C1CP(C(C)(C)C)C(C)(C)C SFCNPIUDAIFHRD-UHFFFAOYSA-N 0.000 claims description 2
- KTWOOEGAPBSYNW-UHFFFAOYSA-N ferrocene Chemical compound [Fe+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 KTWOOEGAPBSYNW-UHFFFAOYSA-N 0.000 claims description 2
- 235000019253 formic acid Nutrition 0.000 claims description 2
- 239000002815 homogeneous catalyst Substances 0.000 claims description 2
- 235000011167 hydrochloric acid Nutrition 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 229940098779 methanesulfonic acid Drugs 0.000 claims description 2
- 235000006408 oxalic acid Nutrition 0.000 claims description 2
- PBDBXAQKXCXZCJ-UHFFFAOYSA-L palladium(2+);2,2,2-trifluoroacetate Chemical compound [Pd+2].[O-]C(=O)C(F)(F)F.[O-]C(=O)C(F)(F)F PBDBXAQKXCXZCJ-UHFFFAOYSA-L 0.000 claims description 2
- YNUJADNRNHJXDT-UHFFFAOYSA-N palladium;pentane-2,4-dione Chemical compound [Pd].CC(=O)CC(C)=O.CC(=O)CC(C)=O YNUJADNRNHJXDT-UHFFFAOYSA-N 0.000 claims description 2
- 235000011007 phosphoric acid Nutrition 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 2
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical compound OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 claims description 2
- FIQMHBFVRAXMOP-UHFFFAOYSA-N triphenylphosphane oxide Chemical compound C=1C=CC=CC=1P(C=1C=CC=CC=1)(=O)C1=CC=CC=C1 FIQMHBFVRAXMOP-UHFFFAOYSA-N 0.000 claims description 2
- 239000002671 adjuvant Substances 0.000 claims 1
- 150000002431 hydrogen Chemical group 0.000 claims 1
- 238000003786 synthesis reaction Methods 0.000 abstract description 6
- 230000015572 biosynthetic process Effects 0.000 abstract description 5
- 230000003197 catalytic effect Effects 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 4
- 238000005580 one pot reaction Methods 0.000 abstract description 3
- 230000002194 synthesizing effect Effects 0.000 abstract description 2
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 125000002924 primary amino group Chemical class [H]N([H])* 0.000 abstract 1
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 24
- UEXCJVNBTNXOEH-UHFFFAOYSA-N Ethynylbenzene Chemical group C#CC1=CC=CC=C1 UEXCJVNBTNXOEH-UHFFFAOYSA-N 0.000 description 16
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 4
- 230000032050 esterification Effects 0.000 description 4
- 239000002243 precursor Substances 0.000 description 4
- 230000021523 carboxylation Effects 0.000 description 3
- RPUSRLKKXPQSGP-UHFFFAOYSA-N methyl 3-phenylpropanoate Chemical compound COC(=O)CCC1=CC=CC=C1 RPUSRLKKXPQSGP-UHFFFAOYSA-N 0.000 description 3
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- 230000009435 amidation Effects 0.000 description 2
- 125000004429 atom Chemical group 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- KZPYGQFFRCFCPP-UHFFFAOYSA-N 1,1'-bis(diphenylphosphino)ferrocene Chemical compound [Fe+2].C1=CC=C[C-]1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=C[C-]1P(C=1C=CC=CC=1)C1=CC=CC=C1 KZPYGQFFRCFCPP-UHFFFAOYSA-N 0.000 description 1
- XGCDBGRZEKYHNV-UHFFFAOYSA-N 1,1-bis(diphenylphosphino)methane Chemical compound C=1C=CC=CC=1P(C=1C=CC=CC=1)CP(C=1C=CC=CC=1)C1=CC=CC=C1 XGCDBGRZEKYHNV-UHFFFAOYSA-N 0.000 description 1
- LVEYOSJUKRVCCF-UHFFFAOYSA-N 1,3-Bis(diphenylphosphino)propane Substances C=1C=CC=CC=1P(C=1C=CC=CC=1)CCCP(C=1C=CC=CC=1)C1=CC=CC=C1 LVEYOSJUKRVCCF-UHFFFAOYSA-N 0.000 description 1
- XMIIGOLPHOKFCH-UHFFFAOYSA-N 3-phenylpropionic acid Chemical compound OC(=O)CCC1=CC=CC=C1 XMIIGOLPHOKFCH-UHFFFAOYSA-N 0.000 description 1
- BCJVBDBJSMFBRW-UHFFFAOYSA-N 4-diphenylphosphanylbutyl(diphenyl)phosphane Chemical compound C=1C=CC=CC=1P(C=1C=CC=CC=1)CCCCP(C=1C=CC=CC=1)C1=CC=CC=C1 BCJVBDBJSMFBRW-UHFFFAOYSA-N 0.000 description 1
- 238000005684 Liebig rearrangement reaction Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 230000002862 amidating effect Effects 0.000 description 1
- 238000010697 carboxylic acid synthesis reaction Methods 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000007172 homogeneous catalysis Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- WBYWAXJHAXSJNI-UHFFFAOYSA-N methyl p-hydroxycinnamate Natural products OC(=O)C=CC1=CC=CC=C1 WBYWAXJHAXSJNI-UHFFFAOYSA-N 0.000 description 1
- TZHYFNJRLMHJCM-UHFFFAOYSA-N n-(3-phenylpropyl)aniline Chemical compound C=1C=CC=CC=1CCCNC1=CC=CC=C1 TZHYFNJRLMHJCM-UHFFFAOYSA-N 0.000 description 1
- 239000012038 nucleophile Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- WBYWAXJHAXSJNI-VOTSOKGWSA-N trans-cinnamic acid Chemical compound OC(=O)\C=C\C1=CC=CC=C1 WBYWAXJHAXSJNI-VOTSOKGWSA-N 0.000 description 1
- 150000003623 transition metal compounds Chemical class 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
- C07C51/14—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on a carbon-to-carbon unsaturated bond in organic 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
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0215—Sulfur-containing compounds
- B01J31/0225—Sulfur-containing compounds comprising sulfonic acid groups or the corresponding salts
-
- 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
- B01J31/24—Phosphines, i.e. phosphorus bonded to only carbon atoms, or to both carbon and hydrogen atoms, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, phosphole or anionic phospholide ligands
- B01J31/2404—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring
- B01J31/2409—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring with more than one complexing phosphine-P atom
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/19—Catalysts containing parts with different compositions
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C231/00—Preparation of carboxylic acid amides
- C07C231/10—Preparation of carboxylic acid amides from compounds not provided for in groups C07C231/02 - C07C231/08
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/36—Preparation of carboxylic acid esters by reaction with carbon monoxide or formates
- C07C67/38—Preparation of carboxylic acid esters by reaction with carbon monoxide or formates by addition to an unsaturated carbon-to-carbon bond
-
- 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
-
- 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
- B01J2531/824—Palladium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention discloses a method for preparing a linear carbonyl compound by catalyzing unsaturated hydrocarbon with a multidentate phosphine ligand-modified palladium combined catalyst, wherein the linear carbonyl compound comprises carboxylic acid, carboxylic ester and amide; the composite catalyst consists of a divalent or zero-valent palladium compound, a multidentate phosphine ligand and an acidic auxiliary agent. Under the action of a combined catalyst, unsaturated hydrocarbon, carbon monoxide and a nucleophilic reagent are used as raw materials to carry out carbonylation reaction, so as to successfully prepare a straight-chain carbonyl compound; the nucleophilic reagent includes water, alcohol, organic primary amine or inorganic ammonia. The catalyst has the advantages of high catalytic activity, good selectivity of straight-chain carbonyl compounds, good stability and cyclic utilization. The invention is a homogeneous synthesis process by a one-pot method, has simple synthesis process and mild reaction conditions, provides a new technology for synthesizing important chemical straight-chain carbonyl compounds, and has good application and popularization prospects.
Description
Technical Field
The invention belongs to the chemical field of homogeneous catalysis and fine chemical synthesis, and relates to a method for preparing a linear carbonyl compound (comprising organic carboxylic acid, carboxylic ester or amide) by using unsaturated hydrocarbon, carbon monoxide and a nucleophilic reagent as raw materials through carbonylation under the action of a palladium combined catalyst modified by a multidentate phosphine ligand.
Background
Reppe, a German chemist, in the 40's of the 20 th century, first discovered a carboxylic acid synthesis reaction using carbonylation of acetylene, carbon monoxide and water (Reppe, W.; Vetter, H. Liebigs Ann. chem.1953,582,133) and generalized the nucleophile used in the reaction to alcohols (synthetic carboxylic esters) and organic primary amines (synthetic amides), wherein several carbonylation reactions such as BASF, Germany and Toyo Rayon (east Yang) have successfully been put into industrial use (US 3,501,518; US 3,455,989; US 3,437,676; DE OS 1,221,224; Acc. chem. Res.1969,2,144-151; chem. Rev.101(2001) 3435-. Since the carbonylation of unsaturated hydrocarbons (including carboxylation, carbonylation, esterification, and amidation) is 100 atom economical, methods for synthesizing carbonyl compounds (including carboxylic acids, carboxylic esters, and amides) based on this process have been attracting much attention so far (WO 96/19434, WO 01/10551 a1, WO 2004/014552A 1, WO 2005/079981 a1, WO 2007/020379 a1, WO 2008/023338 a1, GB 2529007 a, EP 3121186 a2, US 2017/0341067 Al CN 102531890 a, CN 111116415A, CN 107915630 a).
Unsaturated hydrocarbons (including terminal olefins, dienes or terminal alkynes) are cheap and easily-obtained bulk chemical raw materials, and the carbonylation reaction catalyzed by a phosphine ligand modified transition metal compound catalyst of the eighth subgroup is one of important ways for preparing carbonyl compounds with high added values. However, it is well known that for the carbonylation of terminal alkenes, dienes or alkynes, the products are mainly branched carbonyl compounds (Green Chemistry,2019,21, 5336-.
Disclosure of Invention
The invention aims to provide a method for preparing a linear carbonyl compound by catalyzing unsaturated hydrocarbon through carbonylation reaction by using a palladium combined catalyst modified by a multidentate phosphine ligand.
The invention relates to a method for preparing a linear carbonyl compound by catalyzing unsaturated hydrocarbon with a palladium combined catalyst modified by a multidentate phosphine ligand, which is a process for generating the carbonyl compound (comprising organic carboxylic acid, carboxylic ester and amide) by using unsaturated hydrocarbon, carbon monoxide and a nucleophilic reagent (comprising water, alcohol, organic primary amine or inorganic ammonia (inorganic ammonia comprises ammonia gas, an ammonia substitute (such as ammonium bicarbonate or ammonium chloride) or ammonia water) as raw materials to carry out carbonylation reaction (comprising carbonylation carboxylation reaction, carbonylation esterification reaction and carbonylation amidation reaction) under the action of the combined catalyst of the palladium compound/the multidentate phosphine ligand/an acid assistant.
The specific technical scheme for realizing the purpose of the invention is as follows:
a multidentate phosphine ligand modified palladium composite catalyst is used for catalyzing unsaturated hydrocarbon to prepare straight-chain carbonyl compounds, and the method is characterized in that under the action of the composite catalyst, unsaturated hydrocarbon, carbon monoxide and nucleophilic reagent are used as raw materials to generate straight-chain carbonyl compounds through carbonylation reaction, and specifically comprises the following steps: sequentially adding a palladium compound, a polydentate phosphine ligand, an acidic assistant, unsaturated hydrocarbon and a nucleophilic reagent into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, sealing, filling carbon monoxide gas, keeping the pressure of 1.0-5.0MPa, reacting at 80-200 ℃ for 1-48 hours after ensuring the air tightness of the reaction kettle device, and cooling to room temperature after the reaction is finished, wherein the yield of the linear chain carbonyl compound is 50-90%; wherein the unsaturated hydrocarbon comprises a terminal olefin, internal olefin, diene, or terminal alkyne; the composite catalyst is a homogeneous catalyst, is a palladium composite catalyst modified by multidentate phosphine ligands, consists of palladium compounds, multidentate phosphine ligands and acidic auxiliary agents, and is expressed as a 'palladium compound/multidentate phosphine ligand/acidic auxiliary agent' composite catalyst, and the molar ratio of the multidentate phosphine ligands to the palladium compounds is 0.1-100: 1; the molar ratio of the acid auxiliary agent to the palladium compound is 0.1-1000: 1;
the nucleophilic reagent is water, alcohol, organic primary amine or inorganic ammonia;
the inorganic ammonia is ammonia gas, ammonium bicarbonate, ammonium chloride or ammonia water;
the polydentate phosphine ligand is one of or a combination of one of tridentate or tetradentate phosphine ligands of the following structures and a commercially available monodentate or bidentate phosphine ligand, the tridentate or tetradentate phosphine ligand having the following structural formula:
in the formula: r1Selected from alkyl, aryl, heterocyclic aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic acid group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; r is selected from hydrogen H, alkyl, cycloalkyl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; the value range of n is 0-2, and represents that the compound in the structural formula has carbon chains with different lengths; the value range of m is 1-4, and the compound in the structural formula has carbon chains with different lengths;
the molar ratio of the commercially available monodentate or bidentate phosphine ligand to the tridentate or tetradentate phosphine ligand is 0.1-50: 1;
the molar ratio of the unsaturated hydrocarbon to the palladium compound is 100-100000: 1;
the molar ratio of the nucleophilic reagent to the unsaturated hydrocarbon is 1-500: 1.
The commercially available monodentate or bidentate phosphine ligands include one or more combinations of triphenylphosphine, triphenylphosphine oxide, 1, 2-bis (diphenylphosphino) methane (dppm), 1, 2-bis (diphenylphosphino) ethane (dppe), 1, 2-bis (diphenylphosphino) propane (dppp), 1, 2-bis (diphenylphosphino) butane (dppb), 1 '-bis (diphenylphosphino) ferrocene (dppf), 4, 5-bis (diphenylphosphino) -9, 9-dimethylxanthene (xanthphos), 4, 6-bis (diphenylphosphino) -10H-phenoxazine (nixantpos), 1, 2-bis (di-t-butylphosphinomethyl) benzene, and 1,1' -bis (di-t-butylphosphinomethyl) ferrocene.
The palladium compound is one or more of palladium dichloride, bis (acetonitrile) palladium dichloride, palladium acetate, palladium trifluoroacetate, bis (triphenylphosphine) palladium dichloride, (1, 5-cyclooctadiene) palladium dichloride, allyl palladium chloride, tetratriphenylphosphine palladium, bis (acetylacetone) palladium, bis (dibenzylidene acetone) palladium and tris (dibenzylidene acetone) dipalladium.
The acid auxiliary agent is selected from one of formic acid, acetic acid, oxalic acid, phosphoric acid, hydrochloric acid, methanesulfonic acid, trifluoroacetic acid, trifluoromethanesulfonic acid, p-toluenesulfonic acid, dodecylsulfonic acid and aluminum trifluoromethanesulfonate.
Under the action of a palladium combined catalyst modified by a multidentate phosphine ligand, when unsaturated hydrocarbon, carbon monoxide and water are used as raw materials to carry out carbonylation and carboxylation reaction to prepare straight-chain carboxylic acid, the method comprises the following specific processes:
in the formula: r2Selected from H, alkyl, alkenyl, heterocyclic aryl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro.
Under the action of a palladium combined catalyst modified by a multidentate phosphine ligand, when unsaturated hydrocarbon, carbon monoxide and alcohol are used as raw materials to carry out carbonylation esterification reaction to prepare straight-chain organic carboxylic ester, the method comprises the following specific processes:
in the formula: r2Selected from H, alkyl, alkenyl, heterocyclic aryl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; r3Selected from alkyl or aryl.
Under the action of a palladium combined catalyst modified by a multidentate phosphine ligand, when unsaturated hydrocarbon, carbon monoxide and organic primary amine or inorganic ammonia are used as raw materials to carry out carbonylation and amidation reaction to prepare linear-chain amide, the method comprises the following specific processes:
in the formula: r2Selected from H, alkyl, alkenyl, heterocyclic aryl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; r4And R5Selected from H, alkyl or aryl.
The unsaturated hydrocarbon according to the invention is preferably an arylacetylene or an arylethylene.
The invention provides a green synthesis method for preparing a linear chain carbonyl compound (comprising organic carboxylic acid, carboxylic ester or amide) by a carbonylation one-pot method by taking unsaturated hydrocarbon, carbon monoxide and a nucleophilic reagent (comprising water, alcohol, organic primary amine or inorganic ammonia (the inorganic ammonia comprises ammonia gas, ammonia substitute (such as ammonium bicarbonate or ammonium chloride) or ammonia water) as raw materials under the action of a palladium combined catalyst modified by a multidentate phosphine ligand, and the green synthesis method has the following advantages:
(1) the synthesis process has 100% atom economy and no waste discharge.
(2) The palladium combined catalyst modified by the multidentate phosphine ligand has high activity, high chemical and regional selectivity, good stability and long service life.
(3) The reaction process for preparing the straight-chain carbonyl compound is a one-pot homogeneous synthesis process, the synthesis process is simple, and the reaction conditions are mild.
Detailed Description
The present invention is described in more detail in connection with the following examples. However, these examples are only illustrative of the present invention and do not limit the present invention in any way. The reagents mentioned in the examples are all conventional commercial products.
Examples 1 to 14
(1) Reaction result of carbonylation and carboxylation of styrene to prepare phenylpropionic acid by different palladium compounds and phosphine ligands
The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added 0.01mmol of a palladium compound, 0.012mmol of a multidentate phosphine ligand, 0.05mmol of p-toluenesulfonic acid, 20mmol of styrene, 5mL of water, and N-methylpyrrolidone solvent (NMP40mL) in that order. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas, pressurizing to 3.0MPa, reacting for 4 hours in a constant-temperature heating jacket at 120 ℃, cooling to room temperature, and slowly releasing pressure. The conversion of styrene and the selectivity and yield of the product were calculated by GC-MS.
Examples 15 to 24
(2) Reaction result of carbonylation and carboxylation of phenylacetylene to prepare phenylacrylic acid by using different palladium compounds and phosphine ligands
The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added 0.01mmol of the procatalyst, 0.012mmol of the ligand, 0.05mmol of p-toluenesulfonic acid, 20mmol of phenylacetylene, 5mL of water, and N-methylpyrrolidone (NMP40mL) in that order. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas, pressurizing to 3.0MPa, reacting for 4 hours in a constant-temperature heating jacket at 120 ℃, cooling to room temperature, and slowly releasing pressure. The conversion of phenylacetylene and the selectivity and yield of the product were calculated by GC-MS.
Examples 25 to 34
(3) Reaction result of carbonylation esterification of styrene to prepare methyl phenylpropionate by using different catalytic precursors and different ligands
The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added 0.01mmol of the procatalyst, 0.012mmol of the ligand, 0.05mmol of p-toluenesulfonic acid, 20mmol of styrene, 20mL of methanol, and 40mL of THF in that order. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas, pressurizing to 3.0MPa, reacting for 4 hours in a constant-temperature heating jacket at 140 ℃, cooling to room temperature, and slowly releasing pressure.
The conversion of styrene and the selectivity and yield of the product were calculated by GC-MS.
Examples 35 to 44
(4) Reaction result for preparing beta-methyl phenylacrylate by carbonylation and esterification of phenylacetylene with different catalytic precursors and different ligands
The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added 0.01mmol of the procatalyst, 0.012mmol of the ligand, 0.05mmol of p-toluenesulfonic acid, 20mmol of phenylacetylene, 20mL of methanol, and 40mL of THF in that order. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas, pressurizing to 3.0MPa, reacting for 4 hours in a constant-temperature heating jacket at 140 ℃, cooling to room temperature, and slowly releasing pressure.
The conversion of phenylacetylene and the selectivity and yield of the product were calculated by GC-MS.
Examples 45 to 55
(5) Reaction result of preparing N-phenyl phenylpropylamide by amidating styrene with different catalytic precursors and different ligands
The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added 0.01mmol of the procatalyst, 0.012mmol of the ligand, 0.05mmol of p-toluenesulfonic acid, 20mmol of styrene, 24mmol of aniline, and 40mL of THF in that order. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas, pressurizing to 3.0MPa, reacting for 10 hours in a constant-temperature heating jacket at 140 ℃, cooling to room temperature, and slowly releasing pressure.
The conversion of styrene and the selectivity and yield of the product were calculated by GC-MS.
Examples 55 to 65
(6) Reaction result for preparing N-phenyl benzene acrylamide by carbonylation and amidation of p-phenylacetylene with different catalytic precursors and different ligands
The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added 0.01mmol of the procatalyst, 0.012mmol of the ligand, 0.05mmol of p-toluenesulfonic acid, 20mmol of phenylacetylene, 24mmol of aniline, and 40mL of THF in that order. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas, pressurizing to 3.0MPa, reacting for 10h at 140 ℃ in a constant-temperature heating jacket, cooling to room temperature, and slowly releasing pressure.
The conversion of phenylacetylene and the selectivity and yield of the product were calculated by GC-MS.
Example 65
And combining the service life investigation results of the catalyst.
“Pd(OAc)2/L6/MeSO3The H/Nixantphos combined catalyst can be recycled for 10 times in the reaction process of preparing methyl phenylpropionate by carbonylation and esterification of styrene and still maintain good performanceGood activity and stability. The tetradentate phosphine ligand L6 was used in combination with the bidentate phosphine ligand Nixantphos (Nixantphos is 4, 6-bis (diphenylphosphino) -10H-phenoxazine, a commercially available bidentate phosphine ligand) in a 2:1 molar ratio to L6. The specific experimental steps are as follows: to a 200mL polytetrafluoroethylene liner were added, in order, 0.01mmol Pd (OAc)20.012mmol of ligand L6, 0.024mmol of Nixantphos ligand, and MeSO30.2mmol of H, 20mmol of styrene and 50mL of methanol. And (3) placing the lining in a high-pressure reaction kettle, sealing, checking the air tightness of the device, and replacing air in the reaction kettle with carbon monoxide. Then introducing carbon monoxide gas and pressurizing to 3.0MPa, reacting for 4h at 140 ℃ in a constant-temperature heating jacket, cooling to room temperature, slowly decompressing, then adding 20mmol of styrene again, sealing, then injecting 3.0MPa carbon monoxide gas again, and reacting for 4h at 140 ℃. After repeating the above experimental procedure 9 times, the yield of the product methyl phenylpropionate was calculated by GC-MS.
Claims (7)
1. A multidentate phosphine ligand modified palladium composite catalyst is used for catalyzing unsaturated hydrocarbon to prepare a linear carbonyl compound, and is characterized in that under the action of the composite catalyst, unsaturated hydrocarbon, carbon monoxide and a nucleophilic reagent are used as raw materials to generate the linear carbonyl compound through carbonylation reaction, and the method specifically comprises the following steps: sequentially adding a palladium compound, a polydentate phosphine ligand, an acidic assistant, unsaturated hydrocarbon and a nucleophilic reagent into a stainless steel high-pressure reaction kettle with a polytetrafluoroethylene lining, sealing, filling carbon monoxide gas, keeping the pressure of 1.0-5.0MPa, reacting at 80-200 ℃ for 1-48 hours after ensuring the air tightness of the reaction kettle device, and cooling to room temperature after the reaction is finished, wherein the yield of the linear chain carbonyl compound is 50-90%; wherein the unsaturated hydrocarbon comprises a terminal olefin, internal olefin, diene, or terminal alkyne; the composite catalyst is a homogeneous catalyst, is a palladium composite catalyst modified by a multidentate phosphine ligand, and consists of a palladium compound, the multidentate phosphine ligand and an acidic auxiliary agent, wherein the molar ratio of the multidentate phosphine ligand to the palladium compound is 0.1-100: 1; the molar ratio of the acid auxiliary agent to the palladium compound is 0.1-1000: 1;
the nucleophilic reagent is water, alcohol, organic primary amine or inorganic ammonia;
the inorganic ammonia is ammonia gas, ammonium bicarbonate, ammonium chloride or ammonia water;
the polydentate phosphine ligand is one of or a combination of one of tridentate or tetradentate phosphine ligands of the following structures and a commercially available monodentate or bidentate phosphine ligand, the tridentate or tetradentate phosphine ligand having the following structural formula:
in the formula: r1Selected from alkyl, aryl, heterocyclic aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic acid group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; r is selected from hydrogen H, alkyl, cycloalkyl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; the value range of n is 0-2, and represents that the compound in the structural formula has carbon chains with different lengths; the value range of m is 1-4, and the compound in the structural formula has carbon chains with different lengths;
the molar ratio of the commercially available monodentate or bidentate phosphine ligand to the tridentate or tetradentate phosphine ligand is 0.1-50: 1;
the molar ratio of the unsaturated hydrocarbon to the palladium compound is 100-100000: 1;
the molar ratio of the nucleophilic reagent to the unsaturated hydrocarbon is 1-500: 1.
2. The method for preparing linear carbonyl compounds from unsaturated hydrocarbons catalyzed by the multidentate phosphine ligand-modified palladium combination catalyst as claimed in claim 1, characterized in that the commercially available monodentate or bidentate phosphine ligand comprises one or more combinations of triphenylphosphine, triphenylphosphine oxide, 1, 2-bis (diphenylphosphino) methane, 1, 2-bis (diphenylphosphino) ethane, 1, 2-bis (diphenylphosphino) propane, 1, 2-bis (diphenylphosphino) butane, 1 '-bis (diphenylphosphino) ferrocene, 4, 5-bis (diphenylphosphino) -9, 9-dimethylxanthene, 4, 6-bis (diphenylphosphino) -10H-phenoxazine, 1, 2-bis (di-tert-butylphosphinomethyl) benzene, and 1,1' -bis (di-tert-butylphosphinomethyl) ferrocene.
3. The method for preparing a linear carbonyl compound from an unsaturated hydrocarbon catalyzed by a polydentate phosphine ligand-modified palladium combination catalyst according to claim 1, wherein the palladium compound is selected from the group consisting of palladium dichloride, bis (acetonitrile) palladium dichloride, palladium acetate, palladium trifluoroacetate, bis (triphenylphosphine) palladium dichloride, (1, 5-cyclooctadiene) palladium dichloride, allylpalladium chloride, tetratriphenylphosphine palladium, bis (acetylacetone) palladium, bis (dibenzylideneacetone) palladium, and tris (dibenzylideneacetone) dipalladium.
4. The method for preparing linear carbonyl compounds from unsaturated hydrocarbons catalyzed by the multidentate phosphine ligand-modified palladium composite catalyst according to claim 1, wherein the acidic adjuvant is selected from the group consisting of formic acid, acetic acid, oxalic acid, phosphoric acid, hydrochloric acid, methanesulfonic acid, trifluoroacetic acid, trifluoromethanesulfonic acid, p-toluenesulfonic acid, dodecylsulfonic acid, and aluminum trifluoromethanesulfonate.
5. The method for preparing the linear carbonyl compound by catalyzing unsaturated hydrocarbon with the palladium combination catalyst modified by the multi-dentate phosphine ligand as the claim 1, is characterized in that under the action of the combination catalyst, when unsaturated hydrocarbon, carbon monoxide and water are used as raw materials to carry out carbonylation and carboxylation reaction to prepare linear carboxylic acid, the specific process is as follows:
in the formula: r2Selected from H, alkyl, alkenyl, heterocyclic aryl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro.
6. The method for preparing the linear carbonyl compound by catalyzing unsaturated hydrocarbon with the palladium combination catalyst modified by the multi-dentate phosphine ligand as the claim 1, is characterized in that under the action of the combination catalyst, when unsaturated hydrocarbon, carbon monoxide and alcohol are used as raw materials to carry out carbonylation and esterification reaction to prepare linear organic carboxylic ester, the specific process is as follows:
in the formula: r2Selected from H, alkyl, alkenyl, heterocyclic aryl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; r3Selected from alkyl or aryl.
7. The method for preparing the linear carbonyl compound by catalyzing unsaturated hydrocarbon with the palladium combination catalyst modified by the multi-dentate phosphine ligand as the claim 1, is characterized in that under the action of the combination catalyst, when unsaturated hydrocarbon, carbon monoxide and organic primary amine or inorganic ammonia are used as raw materials to carry out carbonylation and amidation reaction to prepare linear amide, the specific process is as follows:
in the formula: r2Selected from H, alkyl, alkenyl, heterocyclic aryl, aryl or aryl containing substituent, wherein the substituent is halogen, sulfonic group, carboxyl, amino, hydroxyl, trifluoromethyl or nitro; r4And R5Selected from H, alkyl or aryl.
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CN115819753A (en) * | 2022-11-02 | 2023-03-21 | 黄河三角洲京博化工研究院有限公司 | Polyketone polymerization method |
CN115819753B (en) * | 2022-11-02 | 2024-03-29 | 黄河三角洲京博化工研究院有限公司 | Polymerization method of polyketone |
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