CN105859610A - Synthesis method of 2,2'-dipyridine by using supported bimetal nano catalyst - Google Patents
Synthesis method of 2,2'-dipyridine by using supported bimetal nano catalyst Download PDFInfo
- Publication number
- CN105859610A CN105859610A CN201610261790.8A CN201610261790A CN105859610A CN 105859610 A CN105859610 A CN 105859610A CN 201610261790 A CN201610261790 A CN 201610261790A CN 105859610 A CN105859610 A CN 105859610A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- pyridine
- bipyridyl
- autoclave
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- ROFVEXUMMXZLPA-UHFFFAOYSA-N Bipyridyl Chemical compound N1=CC=CC=C1C1=CC=CC=N1 ROFVEXUMMXZLPA-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 239000011943 nanocatalyst Substances 0.000 title claims abstract description 46
- 238000001308 synthesis method Methods 0.000 title abstract 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims abstract description 123
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 229910052751 metal Inorganic materials 0.000 claims abstract description 33
- 239000002184 metal Substances 0.000 claims abstract description 33
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229910052593 corundum Inorganic materials 0.000 claims abstract description 18
- 238000005859 coupling reaction Methods 0.000 claims abstract description 18
- 229910001845 yogo sapphire Inorganic materials 0.000 claims abstract description 18
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 11
- 229910052802 copper Inorganic materials 0.000 claims abstract description 10
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 8
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 6
- 229910052742 iron Inorganic materials 0.000 claims abstract description 3
- 150000002739 metals Chemical class 0.000 claims abstract description 3
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 3
- 239000003054 catalyst Substances 0.000 claims description 97
- 238000006243 chemical reaction Methods 0.000 claims description 47
- 239000000706 filtrate Substances 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 21
- 239000011541 reaction mixture Substances 0.000 claims description 21
- 230000004044 response Effects 0.000 claims description 21
- 239000007787 solid Substances 0.000 claims description 15
- 230000015572 biosynthetic process Effects 0.000 claims description 14
- 238000003786 synthesis reaction Methods 0.000 claims description 14
- 238000010189 synthetic method Methods 0.000 claims description 14
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 11
- 230000003197 catalytic effect Effects 0.000 claims description 8
- 239000000047 product Substances 0.000 claims description 5
- 238000006073 displacement reaction Methods 0.000 claims description 3
- 239000010970 precious metal Substances 0.000 claims description 3
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 2
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 125000000740 n-pentyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims description 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 38
- 238000004519 manufacturing process Methods 0.000 abstract description 18
- 230000008878 coupling Effects 0.000 abstract description 12
- 238000010168 coupling process Methods 0.000 abstract description 12
- 229910052763 palladium Inorganic materials 0.000 abstract description 12
- 239000000126 substance Substances 0.000 abstract description 6
- 239000003344 environmental pollutant Substances 0.000 abstract 1
- 231100000719 pollutant Toxicity 0.000 abstract 1
- 229910052703 rhodium Inorganic materials 0.000 abstract 1
- 229910052709 silver Inorganic materials 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 52
- 238000003756 stirring Methods 0.000 description 48
- 229910003158 γ-Al2O3 Inorganic materials 0.000 description 31
- 238000002360 preparation method Methods 0.000 description 30
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 29
- 229910052757 nitrogen Inorganic materials 0.000 description 27
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 26
- 239000001257 hydrogen Substances 0.000 description 26
- 229910052739 hydrogen Inorganic materials 0.000 description 26
- 238000006555 catalytic reaction Methods 0.000 description 24
- 238000005194 fractionation Methods 0.000 description 19
- 238000001514 detection method Methods 0.000 description 18
- 238000000227 grinding Methods 0.000 description 18
- 239000000203 mixture Substances 0.000 description 18
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 239000000243 solution Substances 0.000 description 17
- 238000011065 in-situ storage Methods 0.000 description 15
- 239000010949 copper Substances 0.000 description 13
- 239000008367 deionised water Substances 0.000 description 13
- 229910021641 deionized water Inorganic materials 0.000 description 13
- 239000008187 granular material Substances 0.000 description 13
- 235000011837 pasties Nutrition 0.000 description 13
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 11
- 229910002651 NO3 Inorganic materials 0.000 description 11
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 11
- 230000004913 activation Effects 0.000 description 11
- 239000002105 nanoparticle Substances 0.000 description 11
- 229910052799 carbon Inorganic materials 0.000 description 10
- 238000012545 processing Methods 0.000 description 10
- 229910002666 PdCl2 Inorganic materials 0.000 description 9
- YRKCREAYFQTBPV-UHFFFAOYSA-N acetylacetone Chemical compound CC(=O)CC(C)=O YRKCREAYFQTBPV-UHFFFAOYSA-N 0.000 description 8
- 229910045601 alloy Inorganic materials 0.000 description 8
- 239000000956 alloy Substances 0.000 description 8
- 229910021592 Copper(II) chloride Inorganic materials 0.000 description 7
- 229910018883 Pt—Cu Inorganic materials 0.000 description 7
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 7
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 7
- FKNQCJSGGFJEIZ-UHFFFAOYSA-N 4-methylpyridine Chemical compound CC1=CC=NC=C1 FKNQCJSGGFJEIZ-UHFFFAOYSA-N 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 6
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229910052594 sapphire Inorganic materials 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 229910002668 Pd-Cu Inorganic materials 0.000 description 4
- 229910018879 Pt—Pd Inorganic materials 0.000 description 4
- 229910000564 Raney nickel Inorganic materials 0.000 description 4
- 238000006887 Ullmann reaction Methods 0.000 description 4
- 238000000137 annealing Methods 0.000 description 4
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 4
- 229910052707 ruthenium Inorganic materials 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000004009 herbicide Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- -1 pyridine carbonyl Compound Chemical class 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- 238000007363 ring formation reaction Methods 0.000 description 3
- 229910006587 β-Al2O3 Inorganic materials 0.000 description 3
- ODIGIKRIUKFKHP-UHFFFAOYSA-N (n-propan-2-yloxycarbonylanilino) acetate Chemical compound CC(C)OC(=O)N(OC(C)=O)C1=CC=CC=C1 ODIGIKRIUKFKHP-UHFFFAOYSA-N 0.000 description 2
- AJKVQEKCUACUMD-UHFFFAOYSA-N 2-Acetylpyridine Chemical compound CC(=O)C1=CC=CC=N1 AJKVQEKCUACUMD-UHFFFAOYSA-N 0.000 description 2
- FNRMMDCDHWCQTH-UHFFFAOYSA-N 2-chloropyridine;3-chloropyridine;4-chloropyridine Chemical compound ClC1=CC=NC=C1.ClC1=CC=CN=C1.ClC1=CC=CC=N1 FNRMMDCDHWCQTH-UHFFFAOYSA-N 0.000 description 2
- KCDNYRPDKSGQCM-UHFFFAOYSA-N 4-[4-(3-chlorophenyl)-4-(pyrrolidine-1-carbonyl)piperidin-1-yl]-1-(4-fluorophenyl)butan-1-one Chemical compound C1=CC(F)=CC=C1C(=O)CCCN1CCC(C=2C=C(Cl)C=CC=2)(C(=O)N2CCCC2)CC1 KCDNYRPDKSGQCM-UHFFFAOYSA-N 0.000 description 2
- NBPGPQJFYXNFKN-UHFFFAOYSA-N 4-methyl-2-(4-methylpyridin-2-yl)pyridine Chemical group CC1=CC=NC(C=2N=CC=C(C)C=2)=C1 NBPGPQJFYXNFKN-UHFFFAOYSA-N 0.000 description 2
- 229910021580 Cobalt(II) chloride Inorganic materials 0.000 description 2
- 229910002482 Cu–Ni Inorganic materials 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 239000005630 Diquat Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910019029 PtCl4 Inorganic materials 0.000 description 2
- 229910002787 Ru-Ni Inorganic materials 0.000 description 2
- 229910002793 Ru–Ni Inorganic materials 0.000 description 2
- 125000004429 atom Chemical group 0.000 description 2
- 239000010953 base metal Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- MXZACTZQSGYANA-UHFFFAOYSA-N chembl545463 Chemical compound Cl.C1=CC(OC)=CC=C1C(N=C1)=CN2C1=NC(C)=C2O MXZACTZQSGYANA-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- DHCWLIOIJZJFJE-UHFFFAOYSA-L dichlororuthenium Chemical compound Cl[Ru]Cl DHCWLIOIJZJFJE-UHFFFAOYSA-L 0.000 description 2
- SZVJSHCCFOBDDC-UHFFFAOYSA-N ferrosoferric oxide Chemical compound O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 2
- 230000002363 herbicidal effect Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000005304 joining Methods 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- SHWZFQPXYGHRKT-FDGPNNRMSA-N (z)-4-hydroxypent-3-en-2-one;nickel Chemical compound [Ni].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O SHWZFQPXYGHRKT-FDGPNNRMSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- HGINCPLSRVDWNT-UHFFFAOYSA-N Acrolein Chemical compound C=CC=O HGINCPLSRVDWNT-UHFFFAOYSA-N 0.000 description 1
- YTGIXUBHJVYLRP-UHFFFAOYSA-N CO[Cu](OC)OC Chemical compound CO[Cu](OC)OC YTGIXUBHJVYLRP-UHFFFAOYSA-N 0.000 description 1
- 229910021582 Cobalt(II) fluoride Inorganic materials 0.000 description 1
- 229910021503 Cobalt(II) hydroxide Inorganic materials 0.000 description 1
- 229910002621 H2PtCl6 Inorganic materials 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- 229910000990 Ni alloy Inorganic materials 0.000 description 1
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 1
- 229910019032 PtCl2 Inorganic materials 0.000 description 1
- 229910019603 Rh2O3 Inorganic materials 0.000 description 1
- 229910021604 Rhodium(III) chloride Inorganic materials 0.000 description 1
- 229910019891 RuCl3 Inorganic materials 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000000729 antidote Substances 0.000 description 1
- 239000008346 aqueous phase Substances 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
- ZJRWDIJRKKXMNW-UHFFFAOYSA-N carbonic acid;cobalt Chemical compound [Co].OC(O)=O ZJRWDIJRKKXMNW-UHFFFAOYSA-N 0.000 description 1
- 150000001728 carbonyl compounds Chemical class 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 1
- 229910000001 cobalt(II) carbonate Inorganic materials 0.000 description 1
- SZKXDURZBIICCF-UHFFFAOYSA-N cobalt;pentane-2,4-dione Chemical compound [Co].CC(=O)CC(C)=O SZKXDURZBIICCF-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 208000012839 conversion disease Diseases 0.000 description 1
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(I) oxide Inorganic materials [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 1
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 description 1
- QNZRVYCYEMYQMD-UHFFFAOYSA-N copper;pentane-2,4-dione Chemical compound [Cu].CC(=O)CC(C)=O QNZRVYCYEMYQMD-UHFFFAOYSA-N 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- KRFJLUBVMFXRPN-UHFFFAOYSA-N cuprous oxide Chemical compound [O-2].[Cu+].[Cu+] KRFJLUBVMFXRPN-UHFFFAOYSA-N 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- WIWBLJMBLGWSIN-UHFFFAOYSA-L dichlorotris(triphenylphosphine)ruthenium(ii) Chemical compound [Cl-].[Cl-].[Ru+2].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 WIWBLJMBLGWSIN-UHFFFAOYSA-L 0.000 description 1
- WJJMNDUMQPNECX-UHFFFAOYSA-N dipicolinic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=N1 WJJMNDUMQPNECX-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000010411 electrocatalyst Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 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 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 235000021384 green leafy vegetables Nutrition 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(III) nitrate Inorganic materials [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- GEMHFKXPOCTAIP-UHFFFAOYSA-N n,n-dimethyl-n'-phenylcarbamimidoyl chloride Chemical compound CN(C)C(Cl)=NC1=CC=CC=C1 GEMHFKXPOCTAIP-UHFFFAOYSA-N 0.000 description 1
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 1
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 1
- 229910000008 nickel(II) carbonate Inorganic materials 0.000 description 1
- 229910021508 nickel(II) hydroxide Inorganic materials 0.000 description 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(II) nitrate Inorganic materials [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 1
- GNMQOUGYKPVJRR-UHFFFAOYSA-N nickel(III) oxide Inorganic materials [O-2].[O-2].[O-2].[Ni+3].[Ni+3] GNMQOUGYKPVJRR-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- PZFKDUMHDHEBLD-UHFFFAOYSA-N oxo(oxonickeliooxy)nickel Chemical compound O=[Ni]O[Ni]=O PZFKDUMHDHEBLD-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- RFLFDJSIZCCYIP-UHFFFAOYSA-L palladium(2+);sulfate Chemical compound [Pd+2].[O-]S([O-])(=O)=O RFLFDJSIZCCYIP-UHFFFAOYSA-L 0.000 description 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 1
- 229910000364 palladium(II) sulfate Inorganic materials 0.000 description 1
- YJVFFLUZDVXJQI-UHFFFAOYSA-L palladium(ii) acetate Chemical compound [Pd+2].CC([O-])=O.CC([O-])=O YJVFFLUZDVXJQI-UHFFFAOYSA-L 0.000 description 1
- JKDRQYIYVJVOPF-FDGPNNRMSA-L palladium(ii) acetylacetonate Chemical compound [Pd+2].C\C([O-])=C\C(C)=O.C\C([O-])=C\C(C)=O JKDRQYIYVJVOPF-FDGPNNRMSA-L 0.000 description 1
- FIKAKWIAUPDISJ-UHFFFAOYSA-L paraquat dichloride Chemical compound [Cl-].[Cl-].C1=C[N+](C)=CC=C1C1=CC=[N+](C)C=C1 FIKAKWIAUPDISJ-UHFFFAOYSA-L 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000003504 photosensitizing agent Substances 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- RDRCCJPEJDWSRJ-UHFFFAOYSA-N pyridine;1h-pyrrole Chemical compound C=1C=CNC=1.C1=CC=NC=C1 RDRCCJPEJDWSRJ-UHFFFAOYSA-N 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- SONJTKJMTWTJCT-UHFFFAOYSA-K rhodium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Rh+3] SONJTKJMTWTJCT-UHFFFAOYSA-K 0.000 description 1
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- FBEIPJNQGITEBL-UHFFFAOYSA-J tetrachloroplatinum Chemical compound Cl[Pt](Cl)(Cl)Cl FBEIPJNQGITEBL-UHFFFAOYSA-J 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
- C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
- C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D213/06—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom
- C07D213/22—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom containing two or more pyridine rings directly linked together, e.g. bipyridyl
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/60—Platinum group metals with zinc, cadmium or mercury
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/66—Silver or gold
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/72—Copper
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/80—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/892—Nickel and noble metals
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8926—Copper and noble metals
-
- B01J35/23—
-
- B01J35/393—
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0027—Powdering
- B01J37/0036—Grinding
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
- B01J37/18—Reducing with gases containing free hydrogen
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
- C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
- C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D213/06—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom
- C07D213/127—Preparation from compounds containing pyridine rings
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Abstract
The invention discloses a synthesis method of 2,2'-dipyridine by using a supported bimetal nano catalyst. The method is characterized in that the supported bimetal nano catalyst M1-M2@Al2O3 is utilized to catalyze the direct coupling reaction of pyridine so as to synthesize the 2,2'-dipyridine. The supported bimetal nano catalyst M1-M2@Al2O3 uses Al2O3 as a supporter and any two different metals M1 and M2 as active components, wherein M1 and M2 are respectively and independently selected from noble metals Pd, Pt, Ru, Au, Ag and Rh, or non-noble metals Ni, Cu, Fe, Zn and Co. By using the supported bimetal nano catalyst in direct coupling production of 2,2'-dipyridine from pyridine, the method has high production efficiency, conforms to the atom economy principle in chemical industry production, does not generate any pollutant which is harmful to the environment, and thus, is a green chemical-industry intermediate production technique.
Description
One, technical field
The present invention relates to one 2, the synthetic method of 2 '-bipyridyl, be specifically related to load type double-metal nanocatalyst catalytic pyridine
Directly coupling synthesis 2, the method for 2 '-bipyridyl.
Two, background technology
2,2 '-bipyridyl, can be as part, photosensitizer, the indicator of detection metal ion as one of the isomer of bipyridyl
Deng;2, the important intermediate in 2 '-bipyridyl or organic chemical industry's production, such as the key intermediate produced as herbicide diquat dibromide.
The existing cheap herbicides paraquat being widely used due to its hypertoxicity, because of after person poultry poisoning without specially good effect antidote so that it is should
With being restricted.Diquat dibromide herbicide is as the best substitute kind of N,N'-dimethyl-.gamma..gamma.'-dipyridylium, and its primary raw material 2, the production of 2 '-bipyridyl determines
Its production cost.Therefore, high yield, low cost, good and oligosaprobic 2,2 ' the bipyridyl greens productions of safety are researched and developed
Technology, will have important application prospect and market value.
Report has multiple bipyridyl synthetic route both at home and abroad, mainly includes pyridine carbonyl based compound Cyclization method, haloperidid
Ullmann coupling synthetic method, raney ni catalysis pyridine direct oxidation coupling synthetic method and the catalysis method etc. of precious metals complex.
Bipyridyl synthetic method the earliest is to prepare with pyridine carbonyl based compound cyclization.Beschke in experiments it is found that pyridine carbonyl
Compound and alpha-beta-beta-unsaturated carbonyl compounds can be with Cyclization 2,2 '-bipyridyls under the effect of catalyst.Will at 440 DEG C
Mol ratio is the 2-acetylpyridine of 1:2:6, acrylic aldehyde and ammonia mixing, produces 2 under catalyst action, 2 '-bipyridyl,
On the basis of 2-acetylpyridine, conversion ratio is up to 69%.Although the method yield is higher, but reaction temperature is too high, instead
Should carry out under gas phase condition, there is production safety hidden danger;This reaction stability and catalytic efficiency are unstable;Secondly pyridine carbonyl
Compound is expensive, is relatively difficult to obtain, and therefore the method does not possess commercial production value.
Haloperidid Ullmann coupling synthesis 2,2 '-bipyridyl has had more ripe commercial Application.Its building-up process is:
It is converted into chloro-pyridine, then coupling synthesis 2,2 '-bipyridyl for raw material by chloro with pyridine.The technology of the method and technique are
Comparative maturity, but that route be synthesized is the longest for it, and production efficiency is relatively low;On pyridine ring, hydrogen atom is first former by halogen
Son replaces, and synthesizes 2, is taken off by halogen atom during 2 '-bipyridyl again.ICI company once applied the Ullmann coupling of raney ni catalysis
Synthesis 2,2 '-bipyridyl, under high pressure reacting by heating, but productivity is relatively low.Ullmann coupling method production process can cause very
Big pollution, product cost is of a relatively high, and the production requirement with atom economy and Modern Green chemical industry does not meets.
Pyridine direct coupling synthesis bipyridyl research and report existing long period under anhydrous raney ni catalysis.Gerald L.Goe exists
The nineties in last century once with raney ni catalysis pyridine direct coupling synthesis 2,2 '-bipyridyl, controlled reaction temperature and was 200-400 DEG C,
After optimal conditions catalytic efficiency reach 0.174g 2,2 '-bipyridyl/g Raney's nickel/hour.Owing to reaction temperature is the highest, Raney's nickel is very
Easily inactivation, but temperature too low-yield just declines.Although raney ni catalysis pyridine direct coupling synthesis bipyridyl synthetic route is short,
Production process is simple, but reaction conversion ratio is low, and the Raney's nickel catalyst of industrial production is generally held in aqueous phase system, and
The direct coupling reaction of its catalytic pyridine needs carrying out in anhydrous conditions, prepares and uses anhydrous Raney's nickel catalyst complex operation,
There is certain security risk.
Takashi Kawashima in 2007 etc. report on JACS Ru complex-catalyzed pyridine direct coupling synthesis 2,2 '-
Method (the Takashi Kawashima of bipyridyl;Toshiro Takao;Hiroharu Suzuki*.J.Am.Chem.Soc.
2007,129 (36), 11006-11007.), can reach 20% through condition optimizing conversion per pass.But metal combination in the method
Thing catalyst complex synthetic route, expensive;Ru composition catalyst used is homogeneous catalyst, reclaims complexity, work
Difficulty is reused big, so production application is worth limited in industry.
In sum, although bipyridyl has multiple synthetic route, but industrial still employing chloro-pyridine is by Uullman coupling
Reaction produces, and the essential contaminative of the method does not meets Modern Green chemical industry theory.Design and prepare new catalyst, be catalyzed pyrrole
Pyridine direct coupling synthesis 2,2 '-bipyridyl has the most wide application prospect.
Three, summary of the invention
The present invention is for avoiding the weak point existing for above-mentioned prior art, it is provided that a kind of with load type double-metal nanocatalyst
M1-M2@Al2O3Efficient catalytic pyridine is directly synthesized 2, the method for 2 '-bipyridyl, it is intended to reduces production cost, improve operation peace
Quan Xing, with applicable large-scale industrial production.
The present invention uses the 2 of load type double-metal nanocatalyst, the synthetic method of 2 '-bipyridyl, and its feature is: with support type
Bimetal nano catalyst M1-M2@Al2O3For catalyst, catalytic pyridine direct coupling reaction synthesis 2,2 '-bipyridyl, reaction
Shown in equation such as formula (1):
R in formula1、R2、R3、R4It is independently selected from H, methyl, ethyl, propyl group, butyl, amyl group or hexyl;
Above-mentioned synthetic method is to carry out as follows:
By M1-M2@Al2O3Join in autoclave, and add pyridine, use N2O in displacement autoclave2After,
Sealed reactor;It is heated to 100~600 DEG C, reacts 2~48h, stop heating and be down to room temperature, it is thus achieved that reaction mixture;
Gained reaction mixture carries out solid-liquid separation, and gained solid is catalyst, is recycled use;Gained filtrate is through subtracting
Pressure fractionating obtains unreacted pyridine and target product 2,2 '-bipyridyl.
In above-mentioned synthetic method: M1-M2@Al2O3It is 1:1-10000, preferably 1:4-50 with the mass ratio of pyridine.
Reaction temperature is preferably 400 DEG C, and the response time is preferably 8h.
Described load type double-metal nanocatalyst M1-M2@Al2O3With Al2O3For carrier, with any two kinds of different metal M1
And M2For active component;Wherein M1And M2It is independently selected from precious metals pd, Pt, Ru, Au, Ag, Rh, or non-
Noble metal Ni, Cu, Fe, Zn, Co.Noble metal preferred Pd, Pt or Ru;Preferred Cu or Ni of base metal;
The carrier of catalyst can make the Al of various crystal formation2O3, such as α-Al2O3、β-Al2O3、γ-Al2O3With unformed Al2O3,
Preferably α-Al2O3、β-Al2O3、γ-Al2O3;
Described active component M1、M2The mol ratio of two kinds of metals is 1:0.01-100;It is total that described active component quality accounts for catalyst
The ratio of quality is 5-60%, preferably 30-50%;
Catalyst M in the present invention1-M2@Al2O3The noble metal active component of middle correspondence be the mineral acid by corresponding ion or
Acylate or metallo-organic compound etc. convert as precursor and obtain;Such as RuCl3·3H2O、
RuO2、(NH4)2RuCl6、[(C6H5)3P]3RuCl2, acetylacetone,2,4-pentanedione ruthenium, H2PtCl6·6H2O、PtCl4、PtCl3、
PtCl2、[Pt(NH3)4](NO3)2、(NH4)2PtCl6、Pt(NO3)2、(NH4)2PtCl4, acetylacetone,2,4-pentanedione platinum, Pd (NO3)2、Pd(OAc)2、
PdCl2、Pd(OH)2、PdSO4·2H2O、Pd(NH3)2Cl2、Pd(NH3)4Cl2, palladium acetylacetonate, (NH4)2PdCl4、Rh2O3、
RhCl3·3H2O、Rh(OAc)3、Rh(NO3)3Solution, Ru2(SO4)3Solution, (NH4)3RhCl6;Preferably its acetate and chlorine
Compound;
M in the present invention1-M2@Al2O3Base metal active component corresponding in catalyst is the mineral acid by corresponding ion
Or acylate or metallo-organic compound etc. convert as precursor and obtain;Such as Cu (NO3)2·3H2O、CuCl2·2H2O、
CuO、Cu2O、Cu(OAc)2、Cu2(OH)2CO3, acetylacetone copper, trimethoxy copper, C4H6O4Co、CoCO3、
CoCl2、CoSO4·7H2O、Co(OH)2、Co(NO3)2、CoF2、CoCl2(NH3)4, cobalt naphthenate, acetylacetone cobalt, FeCl3、
FeS、Fe2(C2O4)3·5H2O、Fe(NO3)3、Fe2O3、Fe3O4, ferrocene, trimethoxy ferrum, FeNH4(SO4)2·12H2O、
Ferric acetyl acetonade, NiCl2、C4H6NiO4·4H2O、Ni(OH)2、NiSO4、Ni2O3、NiCO3、Ni(OH)3、Ni(NO3)2、
Nickel acetylacetonate;Preferably its hydrochlorate, nitrate;
The preparation method of load type double-metal nanocatalyst of the present invention, can be nano-particle load method or original position load method.
The step of nano-particle load method is: buy commercially available or self-control alloy nanoparticle M1-M2, according to outside alloy nanoparticle
The kind of burden agent and character, select suitable solvent (such as deionized water, alcohol, ether, preferably water and alcohol), preparation uniformly and
The alloy nanoparticle dispersion soln of stable dispersion.Take appropriate above-mentioned solution according to required ratio, add certain mass mark
Carrier, and after being constantly uniformly mixed, be dried under the conditions of proper temperature and slough solvent, roasting under high temperature after grinding, also
Former, annealing, obtains load type double-metal nanometer alloy catalyst.
Load method is prepared the step of catalyst and is in situ: weigh precursor raw material according to the proportioning of active component, with water or the most molten
Agent dissolve, stirring, weigh carrier according still further to proportioning and join in above-mentioned solution, stirring a period of time to the most thick, with
After under the conditions of proper temperature be dried slough solvent, roasting under high temperature after grinding, reduce, annealing obtains this load type double-metal
Nanometer alloy catalyst.
Beneficial effects of the present invention is embodied in:
1, load type double-metal nanocatalyst is applied in the direct coupling production of pyridine 2 by the present invention, in 2 '-bipyridyl, produces effect
Rate is high, meets Chemical Manufacture Atom economic principle, does not produce environmentally harmful pollution, is that green chemical industry intermediate produces skill
Art.
2, in the synthetic method of the present invention, reclaiming pyridine through vacuum fractionation, the response rate reaches up to 90-98%, pyridine purity
98-99.5%, after distillation, pyridine can utilize with direct circulation;After catalyst reclaims simultaneously, as the case may be, directly repeat to make
With or simple dry regeneration and reuse, still keep higher catalysis activity and selectivity of product.
3, in the load type double-metal nanocatalyst of the present invention, double activated component can effectively regulate fracture and the C-C of c h bond
The coupling of key, thus improve the activity of catalyst;Use α-Al2O3、β-Al2O3With γ-Al2O3For carrier, specific surface area is big,
And the interaction between each active component is strong so that active component is stable on carrier, easily facilitates recovery and reuses.
Four, detailed description of the invention
By following example, the invention will be further described.
Embodiment 1: load method Pd@γ-Al in situ2O3The preparation of metal nano catalyst and catalytic reaction
(1) preparation of catalyst
Weigh 2.00g PdCl2Putting in container, add deionized water 20mL, stirring is to being completely dissolved;Weigh 4g γ-Al2O3
Joining in above-mentioned solution, stirring 4h becomes pasty state, is dried 12h at 75 DEG C, grinds uniformly, will grind after taking out above-mentioned solid
Granule after mill is (volume ratio of nitrogen and hydrogen is 1:1) 450 DEG C of activation processing 4h in nitrogen and hydrogen mixture atmosphere, i.e. obtain
5.03g load type metal nanocatalyst Pd@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 4g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 34.8g, and the response rate is 95%,
Content detection is 98.5%, obtains 2,2 '-bipyridyl 3.4g, yield 8.5%.
Embodiment 2: load method Cu@γ Al in situ2O3The preparation of metal nano catalyst and catalytic reaction
(1) preparation of catalyst
Weigh 5.34g CuCl2·2H2O puts in container, adds deionized water 20mL, and stirring is to being completely dissolved;Weigh 5g
γ-Al2O3Joining in above-mentioned solution, stirring 4h becomes pasty state, is dried 12h at 75 DEG C, grinds uniformly after taking out above-mentioned solid,
Granule (volume ratio of nitrogen and hydrogen is 1:1) 450 DEG C of activation processing 5h in nitrogen and hydrogen mixture atmosphere after grinding, to obtain final product
To 6.89g load type metal nanocatalyst Cu@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 4g step (1) prepared and 30g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 10h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate contains trace 2,2 '-bipyridyl after testing.Filtrate is through vacuum fractionation
Filtrate is reclaimed and is obtained pyridine 28.2g, and the response rate is 94%, and content detection is 97.5%, does not obtain 2,2 '-bipyridyl product.
Embodiment 3: load method Pd-Ni@γ-Al in situ2O3The preparation of (Pd and Ni mol ratio is 2:1) bimetal nano catalyst
And catalytic reaction
(1) preparation of catalyst
Weigh 2.34g PdCl2With 1.92g Ni (NO3)2·6H2O puts in container, adds deionized water 30mL, and stirring is to complete
CL;Weigh 4g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, in taking-up
Grind uniformly after stating solid, granule (volume ratio of nitrogen and hydrogen is 1:1) 500 DEG C in nitrogen and hydrogen mixture atmosphere after grinding
Activation processing 5.5h, i.e. obtains 5.59g load type double-metal nanocatalyst Pd-Ni@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 5.0g step (1) prepared and 50g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 22.0g, and the response rate is 92%,
Content detection is 95.7%;Obtain 2,2 '-bipyridyl 25.9g, yield 52%.
Embodiment 4: load method Pd-Ni@γ-Al in situ2O3The preparation of (Pd and Ni mol ratio is 1:1) bimetal nano catalyst
And catalytic reaction:
(1) preparation of catalyst
Weigh 2.34g PdCl2With 3.84g Ni (NO3)2·6H2O puts in container, adds deionized water 30mL, and stirring is to complete
CL;Weigh 4g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, in taking-up
Grind uniformly after stating solid, granule (volume ratio of nitrogen and hydrogen is 1:1) 500 DEG C in nitrogen and hydrogen mixture atmosphere after grinding,
Activation processing 5.5h, i.e. obtains 5.94g load type double-metal nanocatalyst Pd-Ni@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 5.0g step (1) prepared and 50g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 34.1g, and the response rate is 94%,
Content detection is 96.6%;Obtain 2,2 '-bipyridyl 13.5g, yield 27%.
Embodiment 5: load method Pd-Cu@γ-Al in situ2O3The preparation of (Pd and Cu mol ratio is 3:1) bimetal nano catalyst
And catalytic reaction:
(1) preparation of catalyst
Weigh 2.50g PdCl2With 0.81g CuCl2·2H2O puts in container, adds deionized water 30mL, and stirring is to the most molten
Solve;Weigh 5g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, take out above-mentioned solid
Grind uniformly after body, granule (volume ratio of nitrogen and hydrogen is 1:1) the 480 DEG C of work in nitrogen and hydrogen mixture atmosphere after grinding
Change processes 4.5h, i.e. obtains 6.58g load type double-metal nanocatalyst Pd-Cu@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 5g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 9h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 25.2g, and the response rate is 92%,
Content detection is 96.1%;Obtain 2,2 '-bipyridyl 12.1g, yield 30%.
Embodiment 6: load method Pd-Cu@γ-Al in situ2O3The preparation of (Pd and Cu mol ratio is 1:1) bimetal nano catalyst
And catalytic reaction:
(1) preparation of catalyst
Weigh 2.50g PdCl2With 2.41g CuCl2·2H2O puts in container, adds deionized water 30mL, and stirring is to the most molten
Solve;Weigh 5g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, take out above-mentioned solid
Grind uniformly after body, granule (volume ratio of nitrogen and hydrogen is 1:1) the 480 DEG C of work in nitrogen and hydrogen mixture atmosphere after grinding
Change processes 4.5h, i.e. obtains 7.12g load type double-metal nanocatalyst Pd-Cu@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 5g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 9h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 29.6g, and the response rate is 95%,
Content detection is 97.2%;Obtain 2,2 '-bipyridyl 8.4g, yield 21%.
Embodiment 7: load method Ru-Cu@γ-Al in situ2O3The preparation of (Ru and Cu mol ratio is 1:1) bimetal nano catalyst
And catalytic reaction:
(1) preparation of catalyst
Weigh 3.69g RuCl2·3H2O and 3.05g CuCl2·2H2O puts in container, adds deionized water 25mL, and stirring is extremely
It is completely dissolved;Weigh 4.5g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, take
Grind uniformly after going out above-mentioned solid, the granule (volume ratio of nitrogen and hydrogen is 1:1) in nitrogen and hydrogen mixture atmosphere after grinding
Temperature is 500 DEG C, activation processing 4h, i.e. obtains 7.21g load type double-metal nanocatalyst Ru-Cu@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 5g step (1) prepared and 50g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 10h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 33.38g, and the response rate is 92
%, content detection is 96.7%;Obtain 2,2 '-bipyridyl 13.4g, yield 26.7%.
Embodiment 8: load method Pt-Cu@γ-Al in situ2O3The system of (Pt and Cu mol ratio is 1.5:1) bimetal nano catalyst
Standby and catalytic reaction:
(1) preparation of catalyst: weigh 2.66g chloroplatinic acid and 0.58g CuCl2·2H2O puts in container, adds deionization
Water 20mL, stirring is to being completely dissolved;Weigh 4g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C
Under be dried 12h, take out and grind after above-mentioned solid uniformly, the granule after grinding in nitrogen and hydrogen mixture atmosphere (nitrogen and hydrogen
Volume ratio is 1:1) 450 DEG C of activation processing 5h, i.e. obtain 5.08g load type double-metal nanocatalyst Pt-Cu@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized:
Catalyst 4.5g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 31.2g, and the response rate is 90%,
Content detection is 95.9%;Obtain 2,2 '-bipyridyl 4.68g, yield 11.7%.
Embodiment 9: load method Ru-Ni@γ-Al in situ2O3The system of (mol ratio of Ru and Ni is 2:1) bimetal nano catalyst
Standby and catalytic reaction:
(1) preparation of catalyst
Weigh 3.07g RuCl2·3H2O and 2.16g Ni (NO3)2·6H2O puts in container, adds deionized water 25mL, stirs
Mix to being completely dissolved;Weigh 5g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h,
Grind uniformly after taking out above-mentioned solid, the granule (volume ratio of nitrogen and hydrogen is 1:1) in nitrogen and hydrogen mixture atmosphere after grinding
550 DEG C of activation processing 5h, i.e. obtain 5.77g load type double-metal nanocatalyst Ru-Ni@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 6g step (1) prepared and 35g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 26.2g, and the response rate is 91%,
Content detection is 97.4%;Obtain 2,2 '-bipyridyl 5.34g, yield 15.3%.
Embodiment 10: nano-particle load method Pd-Ni@γ-Al2O3(3:1) preparation of bimetal nano catalyst and catalytic reaction:
(1) preparation of catalyst
According to list of references [Feng, Li;Chong,Hanbao;Li,Peng;Xiang,Ji;Fu,Fangyu;Yang,Sha;Yu,
Hui;Sheng,Hongting;Zhu, Manzhou, Pd-Ni Alloy Nanoparticles as Effective Catalysts for
Miyaura-Heck Coupling Reactions.Journal of Physical Chemistry C(2015),119(21),
11511-11515.] prepare particle diameter about at the Pd-Ni alloy nanoparticle of 10nm (Pd and Ni mol ratio is 3:1) 5g, add
Enter water is made into the dispersion soln 20mL (Pd content 30%) of Pd-Ni.4g γ-Al is added in dispersion soln2O3Stirring 3h
Mix homogeneously.Mixed solution is put into vacuum drying oven is sloughed under room temperature solvent, roasting at 550 DEG C after grinding, reduction 4h,
Annealing obtains support type double nano alloy catalyst Pd-Ni@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 3g step (1) prepared and 30g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 15.7g, and the response rate is 93%,
Content detection is 96.3%;Obtain 2,2 '-bipyridyl 12.9g, yield 43.1%.
Embodiment 11: nano-particle load method Pt-Cu@γ-Al2O3(2:1) preparation of bimetal nano catalyst and catalytic reaction:
(1) preparation of catalyst
According to list of references [Lim, Taeho;Kim,Ok-Hee;Sung,Yung-Eun;Kim,Hyun-Jong;Lee,Ho-Nyun;
Cho,Yong-Hun;Kwon,Oh Joong.,Preparation of onion-like Pt-terminated Pt-Cu bimetallic
nano-sized electrocatalysts for oxygen reduction reaction in fuelcells.Journalof Power Sources
(2016) Pt-Cu alloy nanoparticle (Pd and Cu mol ratio the is 3:1) 5g of particle diameter about 6nm, 316,124-131.] is prepared,
It is added to the water the dispersion soln 20mL (Pt content 35%) being made into Pt-Cu.4g γ-Al is added in dispersion soln2O3Stirring 3h
Mix homogeneously.Mixed solution is put into vacuum drying oven is sloughed under room temperature solvent, roasting at 400 DEG C after grinding, reduction 5h,
Annealing obtains support type double nano alloy catalyst Pt-Cu@γ-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 3g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 10h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 30.2g, and the response rate is 94%,
Content detection is 95.9%.Obtain 2,2 '-bipyridyl 7.24g, yield 18.1%.
Embodiment 12: load method Pt-Pd@γ-Al in situ2O3The preparation of (Pt and Pd mol ratio is 1:1) bimetal nano catalyst
And catalytic reaction:
(1) preparation of catalyst
Weigh 2.66g chloroplatinic acid and 0.91g PdCl2Putting in container, add deionized water 20mL, stirring is to being completely dissolved;
Weigh 5g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, after taking out above-mentioned solid
Grinding uniformly, the granule after grinding is in nitrogen and hydrogen mixture atmosphere at (volume ratio of nitrogen and hydrogen is 1:1) 380 DEG C of activation
Reason 3.5h, i.e. obtains 6.41g load type double-metal nanocatalyst Pt-Pd@γ-Al2O3。
(2) catalytic pyridine direct coupling synthesis 2,2 '-bipyridyl
Catalyst 5g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate and return
Receiving catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 30.1g, and the response rate is 94%,
Content detection is 93.7%;Obtain 2,2 '-bipyridyl 7.32g, yield 18.3%.
Embodiment 13: load method Pt-Pd@γ-Al in situ2O3The system of (mol ratio of Pt and Pd is 2:1) bimetal nano catalyst
Standby and catalytic reaction:
(1) preparation of catalyst
Weigh 5.32g chloroplatinic acid and 0.91g PdCl2Putting in container, add deionized water 25mL, stirring is to being completely dissolved;
Weigh 5g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, after taking out above-mentioned solid
Grinding uniformly, granule (volume ratio of nitrogen and hydrogen the is 1:1) temperature in nitrogen and hydrogen mixture atmosphere after grinding is 380 DEG C,
Activation processing 3.5h, i.e. obtains 7.31g load type double-metal nanocatalyst Pt-Pd@γ-Al2O3。
(2) 2 are catalyzed and synthesized, 2 '-bipyridyl
Catalyst 5g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 28.3g, and the response rate is 93%,
Content detection is 95.9%;Obtain 2,2 '-bipyridyl 9.04g, yield 22.6%.
Embodiment 14: load method Cu-Ni@γ-Al in situ2O3The system of (mol ratio of Cu and Ni is 1:1) bimetal nano catalyst
Standby and catalytic reaction:
(1) preparation of catalyst
Weigh 3.21g CuCl2·3H2O and 5.45g Ni (NO3)2·6H2O puts in container, adds deionized water 25mL, stirs
Mix to being completely dissolved;Weigh 4g γ-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h,
Grind uniformly after taking out above-mentioned solid, the granule (volume ratio of nitrogen and hydrogen is 1:1) in nitrogen and hydrogen mixture atmosphere after grinding
600 DEG C of activation processing 7h, i.e. obtain 6.18g support type Cu-Ni@γ-Al2O3Metal nano catalyst.
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 3g step (1) prepared and 60g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and separate
And reclaiming catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 52.7g, and the response rate is 93%,
Content detection is 95.0%;Obtain 2,2 '-bipyridyl 3.48g, yield 5.8%.
Embodiment 15: load method Pd-Ni@α-Al in situ2O3The system of (mol ratio of Pd and Ni is 2:1) bimetal nano catalyst
Standby and catalytic reaction:
(1) preparation of catalyst
Weigh 2.34g PdCl2With 1.92g Ni (NO3)2·6H2O puts in container, adds deionized water 30mL, and stirring is to complete
CL;Weigh 4g α-Al2O3, join and above-mentioned solution stir 4h one-tenth pasty state, at 75 DEG C, be dried 12h, in taking-up
Grind uniformly after stating solid, granule (volume ratio of nitrogen and hydrogen is 1:1) 500 DEG C in nitrogen and hydrogen mixture atmosphere after grinding
Activation processing 5.5h, i.e. obtains 6.59g load type double-metal nanocatalyst Pd-Ni@α-Al2O3。
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 4g step (1) prepared and 40g pyridine add in autoclave, use N2Replace O therein2After,
Sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped after reaction 8h, to still temperature drop to room temperature,
Open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and be separated and recovered from urging
Agent, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 24.3g, and the response rate is 90%, content
It is detected as 94.8%;Obtain 2,2 '-bipyridyl 12.4g, yield 31.0%.
Embodiment 16: load method Pd-Ni@γ-Al in situ2O3The system of (mol ratio of Pd and Ni is 2:1) bimetal nano catalyst
Standby and catalytic reaction:
(1) preparation of catalyst is with embodiment 3
(2) catalysis 4-picoline synthesis 4,4 '-dimethyl-2,2 '-bipyridyl
Catalyst 5.0g step (1) prepared and 4-picoline 50g adds in autoclave, uses N2Displacement is wherein
O2After, sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Heating is stopped, to still after reaction 11h
Temperature drop, to room temperature, opens autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter
Being separated and recovered from catalyst, catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained 4-picoline 31.1g,
The response rate is 90%, and content detection is 96.1%.4,4 '-dimethyl-2,2 '-bipyridyl 14.8g, yield 29.6%.
Embodiment 17, pyridine the synthesis 2,2 '-bipyridyl reclaimed
(1) preparation of catalyst is with embodiment 3;
(2) 2,2 '-bipyridyl is catalyzed and synthesized
Catalyst 2.5g step (1) prepared and the pyridine 20g (content >=98.0%) of recovery adds in autoclave,
Use N2Replace O therein2After, sealed reactor;Unlatching autoclave stirs, and is heated to still temperature 400 DEG C;Stop after reaction 8h
Only heating, to still temperature drop to room temperature, opens autoclave valve, the H that safety dumping reaction generates2.Reaction is taken out from autoclave
Mixed liquor, filters and is separated and recovered from catalyst, and catalyst can utilize by direct circulation.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 9.05
G, the response rate is 91%, and content detection is 94.6%;Obtain 2,2 '-bipyridyl 10.02g, yield 50.1%.
Embodiment 18, recovery catalyst performance research
(1) catalyst is the catalyst that embodiment 3 reclaims
(2) 2,2 '-bipyridyl is catalyzed and synthesized
The catalyst 3g that will reclaim in pyridine 30g and embodiment 3, adds in autoclave, uses N2Replace O therein2
After, sealed reactor;Unlatching autoclave stirs, and is heated to still temperature to 400 DEG C;Heating is stopped, to still temperature drop after reaction 8h
Low to room temperature, open autoclave valve, the H that safety dumping reaction generates2.From autoclave, take out reaction mixture, filter and divide
From and reclaim catalyst, catalyst can direct circulation utilize.Filtrate is reclaimed through vacuum fractionation and is obtained pyridine 13.9g, and the response rate is
92%, content detection is 95.8%;Obtain 2,2 '-bipyridyl 14.55g, yield 48.2%.
Claims (5)
1. use the 2 of load type double-metal nanocatalyst, the synthetic method of 2 '-bipyridyl, it is characterised in that: double with support type
Metal nano catalyst M1-M2@Al2O3For catalyst, catalytic pyridine direct coupling reaction synthesis 2,2 '-bipyridyl, reaction side
Shown in formula such as formula (1):
R in formula1、R2、R3、R4It is independently selected from H, methyl, ethyl, propyl group, butyl, amyl group or hexyl;
Described load type double-metal nanocatalyst M1-M2@Al2O3It is with Al2O3For carrier, with any two kinds of different metals
M1And M2Catalyst for active component;Wherein M1And M2Be independently selected from precious metals pd, Pt, Ru, Au, Ag,
Rh, or non-noble metal Ni, Cu, Fe, Zn, Co.
Synthetic method the most according to claim 1, it is characterised in that be to carry out as follows:
By M1-M2@Al2O3Join in autoclave, and add pyridine, use N2O in displacement autoclave2After,
Sealed reactor;It is heated to 100~600 DEG C, reacts 2~48h, stop heating and be down to room temperature, it is thus achieved that reaction mixture;
Carrying out gained reaction mixture filtering and separate, gained solid is catalyst, is recycled use;Gained filtrate is through subtracting
Pressure fractionating obtains unreacted pyridine and target product 2,2 '-bipyridyl.
Synthetic method the most according to claim 2, it is characterised in that: M1-M2@Al2O3It is 1 with the mass ratio of pyridine:
1-10000。
Synthetic method the most according to claim 3, it is characterised in that: M1-M2@Al2O3It is 1:4 with the mass ratio of pyridine
-50。
Synthetic method the most according to claim 2, it is characterised in that: reaction temperature is 400 DEG C, and the response time is 8h.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610261790.8A CN105859610B (en) | 2016-04-22 | 2016-04-22 | Using the synthetic method of 2,2 '-bipyridyls of load type double-metal nanocatalyst |
PCT/CN2016/086353 WO2017181514A1 (en) | 2016-04-22 | 2016-06-20 | Synthesis method for 2,2'-dipyridine using supported bimetal nano catalyst |
BE2016/5630A BE1023807B1 (en) | 2016-04-22 | 2016-08-09 | Synthesis of 2, 2'-bipyridyl using supported bimetal nanoparticle catalyst |
CH00511/17A CH712355B1 (en) | 2016-04-22 | 2017-04-16 | Synthesis of 2,2'-bipyridyl using supported metal and bimetallic nanoparticle catalysts. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610261790.8A CN105859610B (en) | 2016-04-22 | 2016-04-22 | Using the synthetic method of 2,2 '-bipyridyls of load type double-metal nanocatalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105859610A true CN105859610A (en) | 2016-08-17 |
CN105859610B CN105859610B (en) | 2019-04-05 |
Family
ID=56629022
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610261790.8A Active CN105859610B (en) | 2016-04-22 | 2016-04-22 | Using the synthetic method of 2,2 '-bipyridyls of load type double-metal nanocatalyst |
Country Status (4)
Country | Link |
---|---|
CN (1) | CN105859610B (en) |
BE (1) | BE1023807B1 (en) |
CH (1) | CH712355B1 (en) |
WO (1) | WO2017181514A1 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107935919A (en) * | 2017-11-17 | 2018-04-20 | 南京红太阳生物化学有限责任公司 | A kind of preparation method of 2,2 ' bipyridyls and its derivative |
CN108484486A (en) * | 2018-05-23 | 2018-09-04 | 安徽国星生物化学有限公司 | A kind of process for purification of bipy 2,2' bipyridyl |
CN110586102A (en) * | 2019-08-21 | 2019-12-20 | 中山大学 | Preparation method of heteroatom-like catalyst |
CN110801841A (en) * | 2019-11-27 | 2020-02-18 | 中国科学院大连化学物理研究所 | Catalyst for preparing 2, 2' -bipyridine by coupling synthesis of pyridine and preparation method and application thereof |
CN114014799A (en) * | 2021-12-08 | 2022-02-08 | 安徽国星生物化学有限公司 | Production process of 2, 2-bipyridine |
CN115245841A (en) * | 2022-08-22 | 2022-10-28 | 山东明化新材料有限公司 | Application of nickel-cobalt metal framework catalyst in preparation of 2,2' -bipyridyl |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3173920A (en) * | 1962-07-03 | 1965-03-16 | Ici Ltd | Process for preparing 2:2'-dipyridyls |
CN1736604A (en) * | 2005-07-27 | 2006-02-22 | 北京化工大学 | Egg shell type metal catalyst, its preparing process and application method |
CN1931841A (en) * | 2006-10-11 | 2007-03-21 | 哈尔滨工业大学 | Synthesis process of 4,4'-dimethyl-2,2'-bipyridine |
CN101219988A (en) * | 2008-01-16 | 2008-07-16 | 清华大学 | Synthesis of 4,4'disubstituted-2,2'-dipyridine |
CN103041826A (en) * | 2013-01-14 | 2013-04-17 | 中国科学院福建物质结构研究所 | Bimetal nanometer catalyst as well as preparation and application method thereof |
CN105461620A (en) * | 2015-11-23 | 2016-04-06 | 安徽千和新材料科技发展有限公司 | Raney nickel catalytic preparation method of 2,2'-bipyridine |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1377213A (en) * | 1971-05-03 | 1974-12-11 | Ici Ltd | Preparation of 2,2-bipyridyls |
-
2016
- 2016-04-22 CN CN201610261790.8A patent/CN105859610B/en active Active
- 2016-06-20 WO PCT/CN2016/086353 patent/WO2017181514A1/en active Application Filing
- 2016-08-09 BE BE2016/5630A patent/BE1023807B1/en active IP Right Grant
-
2017
- 2017-04-16 CH CH00511/17A patent/CH712355B1/en unknown
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3173920A (en) * | 1962-07-03 | 1965-03-16 | Ici Ltd | Process for preparing 2:2'-dipyridyls |
CN1736604A (en) * | 2005-07-27 | 2006-02-22 | 北京化工大学 | Egg shell type metal catalyst, its preparing process and application method |
CN1931841A (en) * | 2006-10-11 | 2007-03-21 | 哈尔滨工业大学 | Synthesis process of 4,4'-dimethyl-2,2'-bipyridine |
CN101219988A (en) * | 2008-01-16 | 2008-07-16 | 清华大学 | Synthesis of 4,4'disubstituted-2,2'-dipyridine |
CN103041826A (en) * | 2013-01-14 | 2013-04-17 | 中国科学院福建物质结构研究所 | Bimetal nanometer catalyst as well as preparation and application method thereof |
CN105461620A (en) * | 2015-11-23 | 2016-04-06 | 安徽千和新材料科技发展有限公司 | Raney nickel catalytic preparation method of 2,2'-bipyridine |
Non-Patent Citations (2)
Title |
---|
JUSTIN J.D. ET AL.: "The influence of ZnO, CeO2 and ZrO2 on nanoparticle-oxide-supported palladium oxide catalysts for the oxidative coupling of 4-methylpyridine", 《JOURNAL OF MOLECULAR CATALYSIS A: CHEMICAL》 * |
LI FENG ET AL.: "Pd-Ni Alloy Nanoparticles as Effective Catalysts for Miyaura-Heck Coupling Reactions", 《THE JOURNAL OF PHYSICAL CHEMISTRY C》 * |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2583216A (en) * | 2017-11-17 | 2020-10-21 | Nanjing Redsun Biochemistry Co Ltd | Method for preparing 2,2'-dipyridine and derivatives thereof |
US11014886B2 (en) | 2017-11-17 | 2021-05-25 | Nanjing Redsun Biochemistry Co., Ltd. | Method for preparing 2,2′-dipyridine and derivatives thereof |
WO2019095613A1 (en) * | 2017-11-17 | 2019-05-23 | 南京红太阳生物化学有限责任公司 | Method for preparing 2,2'-dipyridine and derivatives thereof |
CN107935919B (en) * | 2017-11-17 | 2019-09-03 | 南京红太阳生物化学有限责任公司 | The preparation method of 2,2 '-bipyridyls of one kind and its derivative |
GB2583216B (en) * | 2017-11-17 | 2022-08-10 | Nanjing Redsun Biochemistry Co Ltd | Method for preparing 2,2'-dipyridine and derivatives thereof |
CN107935919A (en) * | 2017-11-17 | 2018-04-20 | 南京红太阳生物化学有限责任公司 | A kind of preparation method of 2,2 ' bipyridyls and its derivative |
CN108484486A (en) * | 2018-05-23 | 2018-09-04 | 安徽国星生物化学有限公司 | A kind of process for purification of bipy 2,2' bipyridyl |
CN108484486B (en) * | 2018-05-23 | 2021-04-27 | 安徽国星生物化学有限公司 | Refining method of 2, 2' -bipyridine |
CN110586102A (en) * | 2019-08-21 | 2019-12-20 | 中山大学 | Preparation method of heteroatom-like catalyst |
CN110586102B (en) * | 2019-08-21 | 2022-09-27 | 中山大学 | Preparation method of heteroatom-like catalyst |
CN110801841A (en) * | 2019-11-27 | 2020-02-18 | 中国科学院大连化学物理研究所 | Catalyst for preparing 2, 2' -bipyridine by coupling synthesis of pyridine and preparation method and application thereof |
CN114014799A (en) * | 2021-12-08 | 2022-02-08 | 安徽国星生物化学有限公司 | Production process of 2, 2-bipyridine |
CN115245841A (en) * | 2022-08-22 | 2022-10-28 | 山东明化新材料有限公司 | Application of nickel-cobalt metal framework catalyst in preparation of 2,2' -bipyridyl |
CN115245841B (en) * | 2022-08-22 | 2024-01-26 | 山东明化新材料有限公司 | Application of nickel-cobalt metal framework catalyst in preparation of 2,2' -bipyridine |
Also Published As
Publication number | Publication date |
---|---|
CH712355A2 (en) | 2017-10-31 |
CN105859610B (en) | 2019-04-05 |
WO2017181514A1 (en) | 2017-10-26 |
CH712355B1 (en) | 2018-03-29 |
BE1023807B1 (en) | 2017-07-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105859610B (en) | Using the synthetic method of 2,2 '-bipyridyls of load type double-metal nanocatalyst | |
CN113019414B (en) | Hydrogenation catalyst, preparation method and application thereof | |
Pietrowski | Recent developments in heterogeneous selective hydrogenation of halogenated nitroaromatic compounds to halogenated anilines | |
US9944587B2 (en) | Process for vapor-phase methanol carbonylation to methyl formate, a catalyst used in the process and a method for preparing the catalyst | |
US7947191B2 (en) | Composite material composed of nanoparticles of transition metal and magnetic ferric oxide, a methode of preparing the same, and uses of the same | |
CN102091625B (en) | Nickel-based catalyst prepared through solid-phase thermal dispersion and preparation method thereof | |
CN101195579A (en) | Method for synthesizing chloro-aniline by chloronitrobenzene selective hydrogenation in alcohol-water system | |
CN102489315A (en) | Ruthenium catalyst, preparation method and application in synthesizing tetrahydrofurfuryl alcohol | |
Formenti et al. | A State‐of‐the‐Art Heterogeneous Catalyst for Efficient and General Nitrile Hydrogenation | |
CN101966460B (en) | Supported catalyst for synthesis of dimethyl carbonate, preparation method and using method thereof | |
CN110961110A (en) | Catalyst and application thereof in hydrodechlorination of 2,3, 6-trichloropyridine | |
CN105153058A (en) | Synthetic method of benzotriazoles compound | |
CN104974016A (en) | Method for preparing cinnamyl alcohol through cinnamaldehyde hydrogenation | |
Yang | Partial reductions of carboxylic acids and their derivatives to aldehydes | |
CN106111129B (en) | Photochemical catalyst and preparation method thereof for simultaneous hydrogen production and selective oxidation ethyl alcohol | |
CN106732725B (en) | The preparation and its application of the carbon-based transition-metal catalyst of MgO-Supported N doping | |
CN102249886A (en) | Method for preparing beta-methyl naphthoquinone through catalytic oxidation of beta-methylnaphthalene by MCM-41 molecular sieve with iron-containing framework | |
CN110256230A (en) | Efficient catalytic glycerol prepares catalyst of glyceric acid and preparation method thereof under the conditions of a kind of alkali-free | |
CN106512993B (en) | Palladium-ruthenium bimetal nano catalyst preparation and plus hydrogen application | |
JPS62130208A (en) | Production of finely divided metal powder | |
CN109400452A (en) | A kind of method that furan derivatives acid catalysis adds hydrogen 3- acetylpropyl alcohol and 1,4- pentanediol | |
CN104399537B (en) | A kind of reactive means with highly active catalytic performance | |
Zhang et al. | Acidic bimetallic LaCo-MOF materials showing synergistic catalytic effect on the air epoxidation of cyclooctene | |
CN114192162A (en) | Dimethyl benzyl alcohol hydrogenolysis catalyst and preparation method and application thereof | |
CN103785381B (en) | A kind of method for preparing low-load amount noble metal catalyst |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |