CN111196763A - Catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile and preparation method thereof - Google Patents
Catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile and preparation method thereof Download PDFInfo
- Publication number
- CN111196763A CN111196763A CN201811372092.0A CN201811372092A CN111196763A CN 111196763 A CN111196763 A CN 111196763A CN 201811372092 A CN201811372092 A CN 201811372092A CN 111196763 A CN111196763 A CN 111196763A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- auxiliary agent
- active metal
- hydroxypropionitrile
- carrier
- 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
- 239000003054 catalyst Substances 0.000 title claims abstract description 111
- WSGYTJNNHPZFKR-UHFFFAOYSA-N 3-hydroxypropanenitrile Chemical compound OCCC#N WSGYTJNNHPZFKR-UHFFFAOYSA-N 0.000 title claims abstract description 46
- WUGQZFFCHPXWKQ-UHFFFAOYSA-N Propanolamine Chemical compound NCCCO WUGQZFFCHPXWKQ-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 238000002360 preparation method Methods 0.000 title description 6
- 229910052751 metal Inorganic materials 0.000 claims abstract description 30
- 239000002184 metal Substances 0.000 claims abstract description 26
- 229910052802 copper Inorganic materials 0.000 claims abstract description 13
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 12
- 239000011148 porous material Substances 0.000 claims abstract description 11
- 239000012752 auxiliary agent Substances 0.000 claims description 40
- 238000000034 method Methods 0.000 claims description 31
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 30
- 238000006243 chemical reaction Methods 0.000 claims description 27
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 26
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 26
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 22
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 21
- 229910052593 corundum Inorganic materials 0.000 claims description 21
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 21
- 229910052681 coesite Inorganic materials 0.000 claims description 20
- 239000010949 copper Substances 0.000 claims description 20
- 229910052906 cristobalite Inorganic materials 0.000 claims description 20
- 239000000377 silicon dioxide Substances 0.000 claims description 20
- 229910052682 stishovite Inorganic materials 0.000 claims description 20
- 229910052905 tridymite Inorganic materials 0.000 claims description 20
- 150000003839 salts Chemical class 0.000 claims description 16
- 239000001257 hydrogen Substances 0.000 claims description 15
- 229910052739 hydrogen Inorganic materials 0.000 claims description 15
- 229910021529 ammonia Inorganic materials 0.000 claims description 14
- 238000005470 impregnation Methods 0.000 claims description 14
- 229910052748 manganese Inorganic materials 0.000 claims description 14
- 238000001556 precipitation Methods 0.000 claims description 12
- 229910052788 barium Inorganic materials 0.000 claims description 11
- 230000004913 activation Effects 0.000 claims description 10
- 239000012298 atmosphere Substances 0.000 claims description 9
- 238000005984 hydrogenation reaction Methods 0.000 claims description 8
- 230000009467 reduction Effects 0.000 claims description 8
- 239000000725 suspension Substances 0.000 claims description 8
- 229910052804 chromium Inorganic materials 0.000 claims description 6
- 229910052746 lanthanum Inorganic materials 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 229910052721 tungsten Inorganic materials 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 5
- 229910052749 magnesium Inorganic materials 0.000 claims description 5
- 229910052750 molybdenum Inorganic materials 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- 239000012716 precipitator Substances 0.000 claims description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 3
- MQRWBMAEBQOWAF-UHFFFAOYSA-N acetic acid;nickel Chemical compound [Ni].CC(O)=O.CC(O)=O MQRWBMAEBQOWAF-UHFFFAOYSA-N 0.000 claims description 3
- 150000001412 amines Chemical class 0.000 claims description 3
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims description 3
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims description 3
- 229910000365 copper sulfate Inorganic materials 0.000 claims description 3
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 claims description 3
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 3
- 229940078494 nickel acetate Drugs 0.000 claims description 3
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 claims description 3
- HRLYFPKUYKFYJE-UHFFFAOYSA-N tetraoxorhenate(2-) Chemical compound [O-][Re]([O-])(=O)=O HRLYFPKUYKFYJE-UHFFFAOYSA-N 0.000 claims description 3
- UPPLJLAHMKABPR-UHFFFAOYSA-H 2-hydroxypropane-1,2,3-tricarboxylate;nickel(2+) Chemical compound [Ni+2].[Ni+2].[Ni+2].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O.[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O UPPLJLAHMKABPR-UHFFFAOYSA-H 0.000 claims description 2
- QSHYGLAZPRJAEZ-UHFFFAOYSA-N 4-(chloromethyl)-2-(2-methylphenyl)-1,3-thiazole Chemical compound CC1=CC=CC=C1C1=NC(CCl)=CS1 QSHYGLAZPRJAEZ-UHFFFAOYSA-N 0.000 claims description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 2
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- XZQYTGKSBZGQMO-UHFFFAOYSA-I Rhenium(V) chloride Inorganic materials Cl[Re](Cl)(Cl)(Cl)Cl XZQYTGKSBZGQMO-UHFFFAOYSA-I 0.000 claims description 2
- 239000004327 boric acid Substances 0.000 claims description 2
- 125000005619 boric acid group Chemical group 0.000 claims description 2
- 229910021446 cobalt carbonate Inorganic materials 0.000 claims description 2
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 2
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 claims description 2
- ZOTKGJBKKKVBJZ-UHFFFAOYSA-L cobalt(2+);carbonate Chemical compound [Co+2].[O-]C([O-])=O ZOTKGJBKKKVBJZ-UHFFFAOYSA-L 0.000 claims description 2
- 229940116318 copper carbonate Drugs 0.000 claims description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 claims description 2
- GEZOTWYUIKXWOA-UHFFFAOYSA-L copper;carbonate Chemical compound [Cu+2].[O-]C([O-])=O GEZOTWYUIKXWOA-UHFFFAOYSA-L 0.000 claims description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 claims description 2
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 claims description 2
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 claims description 2
- 230000001376 precipitating effect Effects 0.000 claims description 2
- 238000002791 soaking Methods 0.000 claims description 2
- UXMRNSHDSCDMLG-UHFFFAOYSA-J tetrachlororhenium Chemical compound Cl[Re](Cl)(Cl)Cl UXMRNSHDSCDMLG-UHFFFAOYSA-J 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 2
- 229910000361 cobalt sulfate Inorganic materials 0.000 claims 1
- 229940044175 cobalt sulfate Drugs 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- 238000001035 drying Methods 0.000 description 16
- 239000002243 precursor Substances 0.000 description 15
- 239000007864 aqueous solution Substances 0.000 description 13
- 239000007788 liquid Substances 0.000 description 13
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 12
- 238000005303 weighing Methods 0.000 description 11
- 239000000047 product Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 229910052723 transition metal Inorganic materials 0.000 description 7
- 150000003624 transition metals Chemical class 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000006227 byproduct Substances 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000001914 filtration Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- SNPLKNRPJHDVJA-ZETCQYMHSA-N D-panthenol Chemical compound OCC(C)(C)[C@@H](O)C(=O)NCCCO SNPLKNRPJHDVJA-ZETCQYMHSA-N 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000002537 cosmetic Substances 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 4
- WGYKZJWCGVVSQN-UHFFFAOYSA-N propylamine Chemical compound CCCN WGYKZJWCGVVSQN-UHFFFAOYSA-N 0.000 description 4
- 229910052702 rhenium Inorganic materials 0.000 description 4
- 230000002194 synthesizing effect Effects 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 229940101267 panthenol Drugs 0.000 description 3
- 235000020957 pantothenol Nutrition 0.000 description 3
- 239000011619 pantothenol Substances 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- ZPVDPMMNPWSWMD-UHFFFAOYSA-N 3-(1-aminopropan-2-ylamino)propan-1-ol Chemical compound NCC(C)NCCCO ZPVDPMMNPWSWMD-UHFFFAOYSA-N 0.000 description 2
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910019891 RuCl3 Inorganic materials 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 239000001099 ammonium carbonate Substances 0.000 description 2
- 235000012501 ammonium carbonate Nutrition 0.000 description 2
- -1 ammonium halide Chemical class 0.000 description 2
- 239000000908 ammonium hydroxide Substances 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000012018 catalyst precursor Substances 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 150000007529 inorganic bases Chemical class 0.000 description 2
- GKQPCPXONLDCMU-CCEZHUSRSA-N lacidipine Chemical compound CCOC(=O)C1=C(C)NC(C)=C(C(=O)OCC)C1C1=CC=CC=C1\C=C\C(=O)OC(C)(C)C GKQPCPXONLDCMU-CCEZHUSRSA-N 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 229910052755 nonmetal Inorganic materials 0.000 description 2
- 238000000643 oven drying Methods 0.000 description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 description 2
- AOHJOMMDDJHIJH-UHFFFAOYSA-N propylenediamine Chemical compound CC(N)CN AOHJOMMDDJHIJH-UHFFFAOYSA-N 0.000 description 2
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 description 2
- 150000003335 secondary amines Chemical class 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- CMSMOCZEIVJLDB-UHFFFAOYSA-N Cyclophosphamide Chemical compound ClCCN(CCCl)P1(=O)NCCCO1 CMSMOCZEIVJLDB-UHFFFAOYSA-N 0.000 description 1
- 235000004866 D-panthenol Nutrition 0.000 description 1
- 239000011703 D-panthenol Substances 0.000 description 1
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 1
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 1
- 229910020350 Na2WO4 Inorganic materials 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000002246 antineoplastic agent Substances 0.000 description 1
- 229940041181 antineoplastic drug Drugs 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- AGSPXMVUFBBBMO-UHFFFAOYSA-O beta-ammoniopropionitrile Chemical compound [NH3+]CCC#N AGSPXMVUFBBBMO-UHFFFAOYSA-O 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229960004397 cyclophosphamide Drugs 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- SNPLKNRPJHDVJA-UHFFFAOYSA-N dl-panthenol Chemical compound OCC(C)(C)C(O)C(=O)NCCCO SNPLKNRPJHDVJA-UHFFFAOYSA-N 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- WOFDVDFSGLBFAC-UHFFFAOYSA-N lactonitrile Chemical compound CC(O)C#N WOFDVDFSGLBFAC-UHFFFAOYSA-N 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 239000002674 ointment Substances 0.000 description 1
- 150000002948 pantothenic acids Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 150000003141 primary amines Chemical class 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- XMVONEAAOPAGAO-UHFFFAOYSA-N sodium tungstate Chemical compound [Na+].[Na+].[O-][W]([O-])(=O)=O XMVONEAAOPAGAO-UHFFFAOYSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- GSQBIOQCECCMOQ-UHFFFAOYSA-N β-alanine ethyl ester Chemical compound CCOC(=O)CCN GSQBIOQCECCMOQ-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- B01J23/84—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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/889—Manganese, technetium or rhenium
- B01J23/8896—Rhenium
-
- B01J35/615—
-
- B01J35/633—
-
- B01J35/635—
-
- 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
- B01J37/03—Precipitation; Co-precipitation
-
- 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
- B01J37/08—Heat treatment
- B01J37/082—Decomposition and pyrolysis
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C213/00—Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
- C07C213/02—Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups
Abstract
The application discloses a catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile, which is characterized by comprising an active component and a carrier; the active component comprises an active metal element; the active component comprises an active metal element; the active metal elements include M and Re; m is at least one selected from Ni, Co and Cu; m accounts for 5.0-50.0% of the weight of the catalyst; re accounts for 0.1-15.0% of the weight of the catalyst; the carrier is selected from at least one of inorganic porous materials. The catalyst has high catalytic activity and selectivity.
Description
Technical Field
The application relates to a catalyst for synthesizing 3-aminopropanol, in particular to a catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile under the ammonia-contacting condition, belonging to the field of catalysis.
Background
3-aminopropanol is an important chemical raw material and a fine chemical intermediate, and has wide application in the fields of medicines, pesticides, dyes, surfactants, daily cosmetics and the like; as a common drug intermediate, can be used for synthesizing anti-cancer drugs such as cyclophosphamide, cardiotrophin and the like, and can also be used for synthesizing DL-panthenol (provitamin B5); the method can also be used for producing panthenol and pantothenic acid derivatives used as ointment components in daily cosmetics, and in recent years, due to the improvement of living standard of people, the application of the panthenol in daily chemical products is continuously improved, especially the application of the panthenol in hair care products and cosmetics is more and more extensive, so that the market demand of 3-aminopropanol is greatly driven.
The conventional method for producing 3-aminopropanol at present is obtained by catalytic hydrogenation of 3-hydroxypropionitrile, and 3-hydroxypropionitrile, Raney Ni, ethanol and ammonia are added into an autoclave for reaction, so that the selectivity of the obtained 3-aminopropanol is 95 percent, and the yield is 60 percent. In addition, 3-aminopropanol can also be synthesized by other routes: synthesizing ketoxime by using methyl isobutyl ketone or cyclohexanone as a raw material, further condensing with acrylonitrile, and preparing 3-aminopropanol by catalytic hydrocracking; 3-aminopropionic acid ethyl ester and 2-cyanoethanol are used as raw materials to synthesize the 3-aminopropanol. However, compared with the 3-hydroxypropionitrile hydrogenation route, other methods have the defects of high raw material cost, complex process, low product yield and the like.
German patent DE573983 reports the purification of hydrogenation products of 3-hydroxypropionitrile by fractional distillation using hydrogenation catalysts synthesized from transition metals of groups 8, 9 and 10. Swiss patent CH244837 reports a catalytic hydrogenation process of nitriles, the hydrogenation reaction is carried out in liquid ammonia, and the patent reports that the liquid ammonia can inhibit byproducts and improve the selectivity of primary amine. German patent DE2655794 reports a process for the hydrogenation of 3-aminopropanol from 3-hydroxypropionitrile, the reaction being carried out in the presence of a hydrogenation catalyst, hydrogen and ammonia, the addition of which makes it possible to suppress the formation of secondary amines and to increase the selectivity of 3-aminopropanol. Japanese patents JP2002201164 and JP05163213 adopt Raney cobalt catalyst to catalyze and hydrogenate 3-hydroxypropionitrile in the presence of ammonia, inhibit the generation of secondary amine and tertiary amine, and improve the yield of 3-aminopropanol. Japanese patent JP59210258 reports that in the preparation of 3-aminopropanol by catalytic hydrogenation of hydroxypropionitrile as a raw material, the catalyst selectivity is low, the number of byproducts is large, and the yield of the 3-aminopropanol is only 70%. In Chinese patent CN103261148A disclosed by BASF corporation, cobalt-based catalyst and P, Mn or alkaline earth metal as auxiliary are adopted to perform catalytic hydrogenation reaction of 3-hydroxypropionitrile in a fixed bed reactor, and the reaction product is subjected to multi-stage distillation to obtain high-purity 3-aminopropionitrile, so as to meet the quality standard of cosmetics and pharmaceutical industry.
The existing catalyst is used for preparing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile, and has the problems of poor catalyst activity, low 3-aminopropanol yield, high byproduct selectivity and the like.
Disclosure of Invention
According to one aspect of the application, a catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile is provided, and the catalyst has high catalytic activity and high selectivity to 3-aminopropanol.
The catalyst provided by the application comprises three parts of an active component, an auxiliary agent and a carrier: the active component is M-Re bimetal, wherein M is one or more than two of transition metals Ni, Co or Cu, and is preferably metal Ni.
The auxiliary agent is one or more of nonmetal, metal or metal oxide of one or more of Fe, Cr, W, Ru, B, Mg, Ba, Mn, La and Mo, and preferably one or more of the auxiliary agents Ru, B, Mn or Ba.
The carrier is porous material Al2O3、SiO2Or Al2O3-SiO2One or more than two of them.
The weight of the active component M accounts for 5.0-50.0% of the weight of the catalyst, preferably 10.0-25.0%; the weight of Re accounts for 0.1-15.0% of the weight of the catalyst, preferably 1.0-5.0%; the weight of the auxiliary agent accounts for 0.2-10.0% of the weight of the catalyst, preferably 1.0-5.0%; the specific surface area of the porous carrier is 50-600 m2A concentration of 200 to 500m is preferred2(ii)/g; the porous carrier has a pore volume of 0.2 to 1.5ml/g, preferably 0.4 to 1.0 ml/g.
The catalyst is characterized by comprising an active component and a carrier;
the active component comprises an active metal element; the active metal elements include M and Re; m is at least one selected from Ni, Co and Cu; m accounts for 5.0-50.0% of the weight of the catalyst; re accounts for 0.1-15.0% of the weight of the catalyst;
the carrier is selected from at least one of inorganic porous materials.
Optionally, the weight percentage of the active metal element M in the catalyst is 10.0-25.0%
Re accounts for 1.0-5.0% of the weight of the catalyst.
Optionally, the catalyst further comprises an auxiliary agent;
the auxiliary agent comprises an auxiliary agent element, and the auxiliary agent element comprises at least one of Fe, Cr, W, Ru, B, Mg, Ba, Mn, La and Mo;
the auxiliary agent comprises an oxide of the auxiliary agent element;
the weight percentage of the auxiliary agent in the catalyst is 0.2-10.0%.
Optionally, the weight percentage of the auxiliary agent in the catalyst is 1.0-5.0%;
wherein, the weight percentage of the auxiliary agent is calculated by the weight percentage of the auxiliary agent element.
Optionally, the auxiliary element is at least one selected from Ru, B, Mn, Ba.
Optionally, the upper limit of the weight percent content of M in the catalyst is selected from 6.0%, 7.0%, 8.0%, 9.0%, 10.0%, 15.0%, 20.0%, 25.0%, 30.0%, 35.0%, 40.0%, 45.0%, or 50%; the lower limit is selected from 5.0%, 6.0%, 7.0%, 8.0%, 9.0%, 10.0%, 15.0%, 20.0%, 25.0%, 30.0%, 35.0%, 40.0%, 45.0%, 50%.
Alternatively, the upper limit of the weight percent content of Re in the catalyst is selected from 0.5%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%, 4%, 4.5%, 5%, 8%, 10%, 12%, or 15%; the lower limit is selected from 0.1%, 0.5%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%, 4%, 4.5%, 5%, 8%, 10% or 12%.
Optionally, the upper limit of the weight percent of promoter in the catalyst is selected from 0.5%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%, 4%, 4.5%, 5%, 8%, or 10%; the lower limit is selected from 0.2%, 0.5%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%, 4%, 4.5%, 5% or 8%.
Optionally, the specific surface area of the carrier is 50-600 m2The pore volume is 0.2-1.5 ml/g.
Optionally, the specific surface area of the carrier is 200-500 m2The pore volume is 0.4-1.0 ml/g.
Optionally, the support is selected from porous Al2O3Porous SiO2Porous Al2O3-SiO2At least one of (1).
Optionally, the support is selected from Al2O3、SiO2、Al2O3-SiO2。
Optionally, the support is selected from porous inorganic oxides.
Optionally, the specific surface area of the carrier is 50-600 m2The pore volume is 0.2-1.5 ml/g.
Optionally, the metal element M includes at least one of Ni, Co, and Cu.
Optionally, the active component is metal Ni, metal Re; the active component accounts for 10.0-25.0% of the weight of the catalyst; re accounts for 1.0-5.0% of the weight of the catalyst; the auxiliary agent comprises at least one of Ru, B, Mn and Ba elements; the auxiliary agent accounts for 1.0-5.0% of the weight of the catalyst; the specific surface area of the carrier is 200-500 m2The pore volume is 0.4 to 1.0 ml/g.
According to another aspect of the present application, a preparation method of the catalyst is provided, which is simple and feasible and is suitable for industrial production.
The preparation method of the catalyst is characterized in that the catalyst adopts an impregnation method and/or a precipitation method to load the active component and the auxiliary agent on the carrier.
Optionally, the impregnation method comprises the steps of:
and (3) soaking the carrier in an aqueous solution containing an active component precursor and an auxiliary agent precursor, naturally airing, and roasting I to obtain the catalyst.
Optionally, the roasting I temperature is 300-700 ℃, the heating rate is 0.5-20.0 ℃/min, and the roasting I time is 0.5-10.0 h.
Optionally, the precipitation method comprises the steps of:
adding an active component precursor and an auxiliary agent precursor into a suspension containing a carrier, adding a precipitator, and aging, washing, filtering, drying and roasting II to obtain the catalyst.
Optionally, the temperature of the roasting II is 300-700 ℃, the heating rate is 0.5-20.0 ℃/min, and the time of the roasting II is 0.5-10.0 h.
Optionally, the active component precursor comprises soluble salts of Ni, Co, Cu and Re.
Optionally, the promoter precursor comprises a soluble precursor of B.
Specifically, the active component M-Re (M is one or more than two of transition metals Ni, Co or Cu) bimetal.
The soluble salt of Ni may be nickel nitrate, nickel acetate, nickel chloride, nickel sulfate or nickel citrate, preferably nickel nitrate or nickel acetate.
The soluble salt of Co used may be cobalt chloride, cobalt nitrate, cobalt carbonate or cobalt sulphate, with cobalt nitrate being preferred.
The soluble salt of Cu used may be copper nitrate, copper chloride, copper carbonate or copper sulfate, preferably copper nitrate, copper sulfate.
The soluble salt of Re used is ammonium rhenate, perrhenic acid or rhenium chloride, preferably ammonium rhenate; the soluble salt of the metal auxiliary agent is nitrate or chloride.
The nonmetal auxiliary agent B is boric acid.
Alternatively, the preparation method of the catalyst can adopt one or a combination of an impregnation method and a precipitation method to load the active component and the auxiliary agent on the carrier.
In a preferred embodiment, the catalyst precursor is supported on the support material by impregnation.
Alternatively, in the impregnation embodiment, the active ingredient and the adjunct may be supported on the carrier by co-impregnation or stepwise impregnation.
Alternatively, the impregnation method may include the steps of: preparing an aqueous solution containing an active component M-Re (M is one or more than two of transition metals of Ni, Co and Cu) and an auxiliary agent, wherein the weight of the active component M accounts for 5.0-50.0% of the weight of the catalyst, the weight of the active component Re accounts for 0.1-15.0% of the weight of the catalyst, and the weight of the auxiliary agent accounts for 0.2-10.0% of the weight of the catalyst, impregnating the carrier with the aqueous solution containing the active component and the auxiliary agent, and naturally airing and roasting the impregnated carrier.
Alternatively, the impregnation method may be one-time impregnation or multi-stage impregnation.
Optionally, the roasting temperature is usually 300-700 ℃, the heating rate is usually 0.5-20.0 ℃/min, and the roasting time is usually 0.5-10.0 h.
Alternatively, the catalyst precursor may also be supported on a carrier by a precipitation method.
Alternatively, the step of preparing the catalyst by the precipitation method can be as follows: the carrier material is suspended in water, soluble precursors of active components M-Re (M is one or more of transition metals Ni, Co and Cu) and auxiliary agents, such as metal salts, are added, and then a precipitant is added to precipitate the precursors on the suspended carrier. Wherein the weight of the active component M accounts for 5.0-50.0% of the weight of the catalyst, the weight of the active component Re accounts for 0.1-15.0% of the weight of the catalyst, and the weight of the auxiliary agent accounts for 0.2-10.0% of the weight of the catalyst. And (4) aging, washing, filtering, drying and roasting the precipitated sample.
Alternatively, the precipitant used is preferably an inorganic base, preferably sodium hydroxide, sodium carbonate, potassium hydroxide or potassium carbonate.
Optionally, the precipitating agent is an inorganic base.
Optionally, the precipitant is selected from at least one of sodium hydroxide, sodium carbonate, potassium hydroxide, and potassium carbonate.
Alternatively, the precipitant used may also be an ammonium salt, which may be ammonium carbonate, ammonium hydroxide or ammonium halide.
Alternatively, the precipitant used is an ammonium salt.
Optionally, the precipitant is selected from at least one of ammonium carbonate, ammonium hydroxide, ammonium halide. Optionally, the precipitation temperature may be 20 to 90 ℃, preferably 40 to 70 ℃.
Optionally, the roasting temperature is usually 300-700 ℃, the heating rate is usually 0.5-20.0 ℃/min, and the roasting time is usually 0.5-10.0 h.
According to still another aspect of the present application, there is provided a process for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile under ammonia-contacting conditions, characterized in that a feed comprising ammonia and 3-hydroxypropionitrile is reacted in the presence of a catalyst under a hydrogen atmosphere to produce an amine;
the catalyst is selected from the group consisting of the catalyst, the catalyst prepared according to the method. Optionally, the reaction conditions are: the reaction temperature is 50-200 ℃, the reaction pressure is 5.0-20.0 MPa, and the volume space velocity of hydrogen is 50.0-2000.0 h-1The molar ratio of ammonia to 3-hydroxypropionitrile is 1.0:20.0 to 80.0: 1.0.
Optionally, the catalyst is subjected to an activation treatment under the following conditions: reduction activation in hydrogen-containing atmosphere; the pressure is 0.1-1.0 MPa, the temperature is 300-700 ℃, and the volume space velocity of hydrogen gas is 500-5000 h-1The reduction time is 0.5-10.0 h.
Alternatively, the conditions of the activation treatment are: reduction activation in hydrogen-containing atmosphere; the pressure is normal pressure, the temperature is 350-550 ℃, and the volume space velocity of hydrogen gas is 1000-3000 h-1And the reduction time is 1.5-6.0 h.
Specifically, the catalyst prepared by the impregnation method or the precipitation method is usually activated in a reducing atmosphere before use.
The reducing atmosphere may be hydrogen or a mixture of hydrogen and other inert gases, preferably hydrogen.
Alternatively, the reaction conditions are: the catalyst loading was 05 to 10.0ml, the reaction temperature is 50 to 200 ℃, the reaction pressure is 5.0 to 20.0MPa, and the volume space velocity of the 3-hydroxypropionitrile liquid is 0.1 to 10.0h-1The volume space velocity of the hydrogen gas is 50.0-2000.0 h-1The molar ratio of ammonia to 3-hydroxypropionitrile is 1.0:20.0 to 80.0: 1.0.
Preferably, the filling amount of the catalyst is 2.0-5.0 ml, the reaction temperature is 70-150 ℃, the reaction pressure is 6.0-10.0 MPa, and the liquid volume space velocity of the 3-hydroxypropionitrile is 0.2-1.0 h-1The volume space velocity of the hydrogen gas is 200.0-800.0 h-1The molar ratio of ammonia to 3-hydroxypropionitrile is 1.0:1.0 to 20.0: 1.0.
The catalyst is applied to the reaction of preparing 3-aminopropanol by catalytic hydrogenation of 3-hydroxypropionitrile. The reaction is carried out in a fixed bed reactor, and the reactant 3-hydroxypropionitrile can be hydrogenated and converted into a 3-aminopropanol product with high activity and high selectivity under the ammonia critical condition. With the formation of small amounts of by-products.
Specifically, the product is mainly 3-aminopropanol, and the by-products may be n-propylamine, propylenediamine, dipropylenetriamine (H)2N(CH2)3NH(CH2)3NH2) And hydroxypropyl propylenediamine (HO (CH)2)3NH(CH2)3NH2) And the like.
As an embodiment, the catalyst is used for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile, and is characterized in that a liquid mixture of the 3-hydroxypropionitrile and ammonia is pumped into a preheater, mixed with hydrogen, preheated to 100 ℃, and then fed into a fixed bed reactor. 3-hydroxypropionitrile and ammonia are dissolved and diluted without adding any solvent.
Alternatively, the reaction conditions are: the filling amount of the catalyst can be 0.5-10.0 ml, preferably 2.0-5.0 ml; the reaction temperature can be 50-200 ℃, and preferably 70-150 ℃; the reaction pressure is 5.0-20.0 MPa, preferably 6.0-10.0 MPa; the liquid volume space velocity of the 3-hydroxypropionitrile is 0.1-10.0 h-1Preferably 0.2 to 1.0 hour-1(ii) a The volume space velocity of the hydrogen gas is 50.0-2000.0 h-1Preferably 200.0 to 800.0 hours-1(ii) a The molar ratio of ammonia to 3-hydroxypropionitrile is 1.0:20.0 to 80.0:1.0, preferably 1.0:1.0 to 20.0: 1.0.
Compared with the prior art, the catalyst provided by the invention can obviously improve the conversion rate of 3-hydroxypropionitrile, improve the yield of the target product 3-aminopropanol and prolong the service life of the catalyst to more than 5000 h.
In the present application, an "element" is present in the form of a simple substance or a compound;
for example, "reactive metal elements include M, Re; m comprises at least one of Ni, Co and Cu, and represents that the active metal element can be an active metal simple substance or an active metal compound; the active metal compound can be an active metal oxide or an active metal salt;
for example, "the additive comprises at least one of Fe, Cr, W, Ru, B, Mg, Ba, Mn, La and Mo elements", and means that the additive is a simple substance or a compound of Fe, Cr, W, Ru, B, Mg, Ba, Mn, La and Mo; the compound may be an oxide or a salt.
The beneficial effects that this application can produce include:
1) the catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile provided by the application can improve the conversion rate of 3-hydroxypropionitrile;
2) the catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile provided by the application improves the yield of the target product 3-aminopropanol;
3) the catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile provided by the application reduces the selectivity of by-product amines;
4) the catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile provided by the application reduces the cost of the catalyst;
5) the catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile provided by the application has the advantages that the service life of the catalyst is prolonged;
6) the catalyst for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile provided by the application is easy to operate.
Detailed Description
The present application will be described in detail with reference to examples, but the present application is not limited to these examples.
Examples of the present application are not specifically describedThe raw materials in the examples were all purchased commercially. Al (Al)2O3Purchased from Shandong aluminum industries; SiO 22Purchased from Qingdao ocean chemical; al (Al)2O3-SiO2Purchased from Shandong aluminum industries, Inc.
The mesh number refers to the number of meshes in a length of 1 inch, for example, 20-40 mesh has a particle size of 0.425-0.850 mm;
the percentage of the catalyst composition is the weight percentage of each component in the catalyst.
Example 1
The catalyst is 10% Ni-2% Re/Al2O3. Weighing 8.8 g of 20-40 mesh Al2O3Oven-drying at 120 deg.C for 4 hr before use, and preparing 20ml solution containing 4.955 g Ni (NO)3)2·6H2O, 0.288 g NH4ReO4With which the above-mentioned Al is impregnated2O3And naturally airing the carrier, drying at 100 ℃ for 2 hours, roasting at 400 ℃ for 3 hours, and raising the temperature at the rate of 5 ℃/min.
Example 2
The catalyst is 15 percent of Ni-1 percent of Re-1.5 percent of B/SiO2. Weighing 8.25 g of 20-40 mesh SiO2Dried at 120 ℃ for 4 hours before use to prepare 20ml of Ni (NO) containing 7.432 g3)2·6H2O, 0.144 g NH4ReO40.859 g H3BO3By impregnating the above SiO with the aqueous solution2And naturally airing the carrier, drying at 100 ℃ for 4 hours, roasting at 400 ℃ for 5 hours, and raising the temperature at the rate of 5 ℃/min.
Example 3
The catalyst is 8 percent of Ni-8 percent of Co-2 percent of Re-1 percent of Mn/Al2O3. Weighing 8.9 g of 20-40 mesh Al2O3Dried at 120 ℃ for 4 hours before use to prepare 20ml of Ni (NO) containing 3.964 g3)2·6H2O, 3.951 g Co (NO)3)2·6H2O, 0.288 g NH4ReO40.651 g of Mn (NO)3)2With which the above-mentioned Al is impregnated2O3Naturally drying the carrier at 100 deg.C for 4 hr, and cooling to 400 deg.CRoasting for 1 hour, wherein the heating rate is 10 ℃/min.
Example 4
The catalyst is 20 percent of Ni-2.5 percent of Re-1 percent of Ru-1 percent of B/SiO2. Weighing 7.55 g of 20-40 mesh SiO2Dried at 120 ℃ for 4 hours before use to prepare 20ml of Ni (NO) containing 9.909 g3)2·6H2O, 0.360 g NH4ReO40.205 g RuCl3·3H2O, 0.573 g H3BO3By impregnating the above SiO with the aqueous solution2And naturally airing the carrier, drying at 120 ℃ for 4 hours, roasting at 500 ℃ for 10 hours, and raising the temperature at a rate of 10 ℃/min.
Example 5
The catalyst is 10 percent of Co-10 percent of Cu-1.5 percent of Re-1.5 percent of Cr/SiO2-Al2O3. Weighing 7.7 g of 20-40 mesh SiO2-Al2O3Dried at 120 ℃ for 4 hours before use to prepare 20ml of solution containing 4.939 g of Co (NO)3)2·6H2O, 2.951 g Cu (NO)3)20.216 g NH4ReO40.687 g Cr (NO)3)3By impregnating the above SiO with the aqueous solution2-Al2O3And naturally airing the carrier, drying at 120 ℃ for 4 hours, roasting at 500 ℃ for 8 hours, and raising the temperature at the rate of 15 ℃/min.
Example 6
The catalyst is 10 percent of Ni-10 percent of Cu-3 percent of Re/SiO2-Al2O3. Weighing 7.7 g of 100 mesh SiO2-Al2O3Drying at 120 deg.C for 4 hr before use to remove SiO2-Al2O3Dispersing in water to form a suspension, and stirring at a constant temperature of 50 deg.C with medium speed. The formulation contained 4.955 g of Ni (NO)3)2·6H2O, 2.951 g Cu (NO)3)20.432 g NH4ReO4The precursor liquid of (4). The precipitant is 4mol/L KOH solution. Dripping precursor liquid and precipitant into the suspension at 2mL/min, keeping pH at 9 until precipitation is complete, washing the precipitate with deionized water to neutrality, filtering, air drying, oven drying at 120 deg.C for 4 hr, baking at 500 deg.C for 8 hr, and heating at high speedThe rate was 2 ℃/min.
Example 7
The catalyst is 15 percent of Cu-2 percent of Re/SiO2. Weighing 8.3 g of 100 mesh SiO2Drying at 120 deg.C for 4 hr before use to remove SiO2Dispersing in water to form a suspension, and stirring at a constant temperature of 50 deg.C with medium speed. The formulation contained 4.427 g of Cu (NO)3)20.288 g NH4ReO4The precursor liquid of (4). The precipitant is 4mol/L (NH)4)2·CO3And (3) solution. And (3) slowly dripping the precursor liquid and a precipitator into the suspension liquid at the same time, keeping the pH value at 7-9 until the precipitation is complete, washing the precipitate to be neutral by using deionized water, filtering, airing, drying for 4 hours at 120 ℃, roasting for 5 hours at 600 ℃, and raising the temperature at the rate of 2 ℃/min.
Example 8
The catalyst is 15 percent of Co-15 percent of Cu-5 percent of Re-2.5 percent of La/Al2O3. Weighing 6.25 g of 20-40 mesh Al2O3Dried at 120 ℃ for 4 hours before use to prepare 20ml of a mixture containing 7.408 g of Co (NO)3)2·6H2O, 4.427 g Cu (NO)3)20.720 g NH4ReO40.779 g La (NO)3)3·6H2An aqueous solution of O, and impregnating the Al with the aqueous solution2O3And naturally airing the carrier, drying at 120 ℃ for 4 hours, roasting at 600 ℃ for 10 hours, and raising the temperature at the rate of 20 ℃/min.
Example 9
The catalyst is 25 percent of Ni-2.5 percent of Re-2 percent of W/SiO2. Weighing 7.05 g of 20-40 mesh SiO2Dried at 120 ℃ for 4 hours before use to prepare 20ml of Ni (NO) containing 12.387 g3)2·6H2O, 0.360 g NH4ReO40.359 g Na2WO4·2H2An aqueous solution of O, impregnating the above SiO with the aqueous solution2And naturally airing the carrier, drying at 120 ℃ for 4 hours, roasting at 600 ℃ for 3 hours, and raising the temperature at a rate of 10 ℃/min.
Comparative example 1
The catalyst is 20 percent of Ni-5 percent of Ru/SiO2-Al2O3. Weighing 7.5 g of 20-40 mesh SiO2-Al2O3Dried at 120 ℃ for 4 hours before use to prepare 20ml of Ni (NO) containing 9.909 g3)2·6H2O, 1.026 g RuCl3·3H2An aqueous solution of O, impregnating the above SiO with the aqueous solution2-Al2O3And naturally airing the carrier, drying at 100 ℃ for 4 hours, roasting at 400 ℃ for 8 hours, and raising the temperature at a speed of 10 ℃/min.
Comparative example 2
The catalyst is 15 percent of Ni-15 percent of Cu-3 percent of Ba/Al2O3. 6.7 g of 100 mesh Al are weighed out2O3Drying at 120 deg.C for 4 hr before use, and mixing Al2O3Dispersing in water to form a suspension, and stirring at a constant temperature of 50 deg.C with medium speed. The formulation contained 7.432 g of Ni (NO)3)2·6H2O, 4.427 g Cu (NO)3)20.571 g of Ba (NO)3)2The precursor liquid of (4). The precipitant is 4mol/L KOH solution. And (3) slowly dripping the precursor liquid and a precipitator into the suspension liquid at the same time, keeping the pH value at 7-9 until the precipitation is complete, washing the precipitate to be neutral by using deionized water, filtering, airing, drying for 4 hours at 120 ℃, roasting for 5 hours at 500 ℃, and raising the temperature at the rate of 5 ℃/min.
Comparative example 3
The catalyst is 1 percent of Ni-1 percent of Cu-5 percent of Re-2 percent of Mn/SiO2. Weighing 9.1 g of 20-40 mesh SiO2Dried at 120 ℃ for 4 hours before use, and prepared into 20ml containing 0.495 g of Ni (NO)3)2·6H2O, 0.295 g Cu (NO)3)20.720 g NH4ReO41.303 g Mn (NO)3)2By impregnating the above SiO with the aqueous solution2And naturally airing the carrier, drying at 100 ℃ for 4 hours, roasting at 600 ℃ for 3 hours, and raising the temperature at the rate of 2 ℃/min.
Example 10 evaluation of the Performance of the catalysts prepared in examples 1 to 9 and comparative examples 1 to 3
The catalyst prepared by the method adopts a fixed bed reactor for reaction evaluation. Before reaction, activating in hydrogen atmosphere at 500 deg.C, normal pressure and hydrogen gas volume space velocity of 1500h-1The activation time is 5 h. After activation treatmentThe temperature is lowered to the reaction temperature. The reaction temperature is 100 ℃, the reaction pressure is 8.0MPa, and the liquid volume space velocity of the 3-hydroxypropionitrile is 0.5h-1The volume space velocity of hydrogen gas is 1000h-1The molar ratio of ammonia to 3-hydroxypropionitrile was 5.0: 1.0. Sampling and analyzing by adopting an Agilent7890 gas chromatograph, wherein the chromatographic column is a DB-35 capillary chromatographic column, and the detector is a hydrogen flame detector. Quantitative analysis was performed using N, N-Dimethylformamide (DMFA) as an internal standard. The results are summarized in Table 1.
The terms conversion of 3-hydroxypropionitrile, n-propylamine, propylenediamine, dipropylenetriamine H in Table 12N(CH2)3NH(CH2)3NH2) And hydroxypropyl propylenediamine (HO (CH)2)3NH(CH2)3NH2) The selectivity of (a) is defined as follows:
table 1: evaluation results of the catalyst for preparing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile.
The evaluation results show that: the catalyst adopts M-Re (M is one or more than two of transition metals of Ni, Co and Cu) bimetal as an active component, the conversion rate of 3-hydroxypropionitrile is higher, and the selectivity of the product 3-aminopropanol is high; the catalyst adopts Ni-Re bimetal as an active component, and has high activity and high yield of the product 3-aminopropanol when Ru, B, Mn or Ba is added as an auxiliary agent; M-Re (M is one or more than two of transition metals of Ni, Co and Cu) bimetal is used as an active component, when one or more of additives of Ru, B, Mn or B is added, the catalyst prepared by adopting an impregnation method or a precipitation method is used for 3-hydroxypropionitrile hydrogenation reaction under the ammonia-contacting condition, and the catalyst has the characteristics of high activity, high 3-aminopropanol yield and good stability. The kind and content of the M component also have influence on the catalytic performance, as shown in comparative example 3, comparative example 5 and comparative example 7, the catalytic performance of M metal with Ni as the active component is better than that of Cu or Co catalysts, and when the Ni content is reduced, the catalyst activity is slightly reduced.
Although the present application has been described with reference to a few embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the application as defined by the appended claims.
Claims (10)
1. A catalyst for hydrogenation production of 3-aminopropanol by 3-hydroxypropionitrile is characterized in that the catalyst comprises an active component and a carrier;
the active component comprises an active metal element; the active metal elements include M and Re; m is at least one selected from Ni, Co and Cu; m accounts for 5.0-50.0% of the weight of the catalyst; re accounts for 0.1-15.0% of the weight of the catalyst;
the carrier is selected from at least one of inorganic porous materials.
2. The catalyst according to claim 1,
the weight percentage content of the active metal element M in the catalyst is 10.0-25.0%;
re accounts for 1.0-5.0% of the weight of the catalyst.
3. The catalyst according to claim 1,
the catalyst also comprises an auxiliary agent;
the auxiliary agent comprises an auxiliary agent element, and the auxiliary agent element comprises at least one of Fe, Cr, W, Ru, B, Mg, Ba, Mn, La and Mo;
the auxiliary agent comprises an oxide of the auxiliary agent element;
the weight percentage content of the auxiliary agent in the catalyst is 0.2-10.0%;
preferably, the weight percentage content of the auxiliary agent in the catalyst is 1.0-5.0%;
wherein, the weight percentage of the auxiliary agent is calculated by the weight percentage of the auxiliary agent element;
preferably, the auxiliary element is at least one selected from Ru, B, Mn and Ba.
4. The catalyst according to claim 1,
the specific surface area of the carrier is 50-600 m2The pore volume is 0.2-1.5 ml/g;
preferably, the specific surface area of the carrier is 200-500 m2The pore volume is 0.4-1.0 ml/g;
preferably, the support is selected from porous Al2O3Porous SiO2Porous Al2O3-SiO2At least one of (1).
5. The method for preparing the catalyst according to any one of claims 1 to 4, comprising at least one of an impregnation method and a precipitation method.
6. The method of claim 5, wherein the method comprises: soaking a carrier in a solution containing an active metal element source, and roasting to obtain the catalyst; or
Adding a solution containing an active metal element source and a precipitator into a suspension containing a carrier, and precipitating to obtain the catalyst;
preferably, the solution contains an auxiliary element source;
preferably, the roasting conditions are as follows: the temperature is 300-700 ℃, and the time is 0.5-10.0 h.
7. The method of claim 6, wherein the source of the active metal element is selected from at least one of soluble salts of the active metal element;
the auxiliary agent element source is selected from at least one of soluble salts of auxiliary agent elements;
preferably, the soluble salt of the active metal element Ni comprises at least one of nickel nitrate, nickel acetate, nickel chloride, nickel sulfate and nickel citrate;
preferably, the soluble salt of the active metal element Co comprises at least one of cobalt chloride, cobalt nitrate, cobalt carbonate and cobalt sulfate;
preferably, the soluble salt of the active metal element Cu comprises at least one of copper nitrate, copper chloride, copper carbonate and copper sulfate;
preferably, the soluble salt of the active metal element Re comprises at least one of ammonium rhenate, perrhenic acid, rhenium chloride;
preferably, the auxiliary element is a metal, and the soluble salt of the auxiliary element comprises at least one of nitrate of the auxiliary element and chloride of the auxiliary element;
the assistant element is B, and the assistant element source is boric acid.
8. A method for producing 3-aminopropanol by hydrogenating 3-hydroxypropionitrile under the ammonia-contacting condition is characterized in that raw materials containing ammonia and 3-hydroxypropionitrile react to prepare amine under the existence of a catalyst in a hydrogen atmosphere;
the catalyst is selected from the group consisting of the catalyst of any one of claims 1 to 4, the catalyst prepared according to the process of any one of claims 5 to 7.
9. The method according to claim 8, wherein the reaction conditions are: the reaction temperature is 50-200 ℃, the reaction pressure is 5.0-20.0 MPa, and the volume space velocity of hydrogen is 50.0-2000.0 h-1The molar ratio of ammonia to 3-hydroxypropionitrile is 1.0:20.0 to 80.0: 1.0.
10. The method according to claim 9, characterized in that the catalyst is subjected to an activation treatment under the conditions: reduction activation in hydrogen-containing atmosphere; the pressure is 0.1-1.0 MPa, the temperature is 300-700 ℃, and the volume space velocity of hydrogen gas is 500-5000 h-1The reduction time is 0.5-10.0 h;
preferably, the conditions of the activation treatment are: reduction activation in hydrogen-containing atmosphere; the pressure is normal pressure, the temperature is 350-550 ℃, and the volume space velocity of hydrogen gas is 1000-3000 h-1And the reduction time is 1.5-6.0 h.
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