CN106187783A - The application in the hydrogenation of aromatic nitro compound of the polyamic acid supported palladium nanocatalyst - Google Patents
The application in the hydrogenation of aromatic nitro compound of the polyamic acid supported palladium nanocatalyst Download PDFInfo
- Publication number
- CN106187783A CN106187783A CN201610514242.1A CN201610514242A CN106187783A CN 106187783 A CN106187783 A CN 106187783A CN 201610514242 A CN201610514242 A CN 201610514242A CN 106187783 A CN106187783 A CN 106187783A
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- CN
- China
- Prior art keywords
- polyamic acid
- palladium
- catalyst
- nanocatalyst
- acid
- 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.)
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Links
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 title claims abstract description 176
- 229910052763 palladium Inorganic materials 0.000 title claims abstract description 77
- 229920005575 poly(amic acid) Polymers 0.000 title claims abstract description 67
- 239000011943 nanocatalyst Substances 0.000 title claims abstract description 45
- 238000005984 hydrogenation reaction Methods 0.000 title claims abstract description 19
- -1 aromatic nitro compound Chemical class 0.000 title claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 42
- 239000003054 catalyst Substances 0.000 claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000002105 nanoparticle Substances 0.000 claims abstract description 14
- 239000006185 dispersion Substances 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 37
- 150000003839 salts Chemical class 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 23
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 239000002253 acid Substances 0.000 claims description 13
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical group Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 8
- MUJIDPITZJWBSW-UHFFFAOYSA-N palladium(2+) Chemical compound [Pd+2] MUJIDPITZJWBSW-UHFFFAOYSA-N 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- NWZSZGALRFJKBT-KNIFDHDWSA-N (2s)-2,6-diaminohexanoic acid;(2s)-2-hydroxybutanedioic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O.NCCCC[C@H](N)C(O)=O NWZSZGALRFJKBT-KNIFDHDWSA-N 0.000 claims description 7
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 7
- 229910052801 chlorine Inorganic materials 0.000 claims description 7
- 239000000460 chlorine Substances 0.000 claims description 7
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine monohydrate Substances O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 claims description 7
- 239000012279 sodium borohydride Substances 0.000 claims description 7
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000003607 modifier Substances 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 5
- 239000004952 Polyamide Substances 0.000 claims description 5
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 5
- 229920002647 polyamide Polymers 0.000 claims description 5
- 229910052708 sodium Inorganic materials 0.000 claims description 5
- 239000011734 sodium Substances 0.000 claims description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 239000002243 precursor Substances 0.000 claims description 4
- 230000004044 response Effects 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 3
- 150000001412 amines Chemical class 0.000 claims description 3
- 229910052700 potassium Inorganic materials 0.000 claims description 3
- 239000011591 potassium Substances 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 2
- 230000036571 hydration Effects 0.000 claims description 2
- 238000006703 hydration reaction Methods 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 150000002500 ions Chemical class 0.000 claims description 2
- 125000001453 quaternary ammonium group Chemical group 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 claims 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims 2
- 150000001413 amino acids Chemical class 0.000 claims 1
- 229910000027 potassium carbonate Inorganic materials 0.000 claims 1
- 238000004062 sedimentation Methods 0.000 claims 1
- 238000006555 catalytic reaction Methods 0.000 abstract description 9
- 239000000758 substrate Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 7
- 230000004913 activation Effects 0.000 abstract description 2
- 239000008346 aqueous phase Substances 0.000 abstract description 2
- 238000009792 diffusion process Methods 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract 1
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 150000002828 nitro derivatives Chemical class 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 238000006722 reduction reaction Methods 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- ANSXAPJVJOKRDJ-UHFFFAOYSA-N furo[3,4-f][2]benzofuran-1,3,5,7-tetrone Chemical compound C1=C2C(=O)OC(=O)C2=CC2=C1C(=O)OC2=O ANSXAPJVJOKRDJ-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000007172 homogeneous catalysis Methods 0.000 description 3
- 230000035945 sensitivity Effects 0.000 description 3
- ZDFBKZUDCQQKAC-UHFFFAOYSA-N 1-bromo-4-nitrobenzene Chemical compound [O-][N+](=O)C1=CC=C(Br)C=C1 ZDFBKZUDCQQKAC-UHFFFAOYSA-N 0.000 description 2
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- DPJCXCZTLWNFOH-UHFFFAOYSA-N 2-nitroaniline Chemical compound NC1=CC=CC=C1[N+]([O-])=O DPJCXCZTLWNFOH-UHFFFAOYSA-N 0.000 description 2
- IQUPABOKLQSFBK-UHFFFAOYSA-N 2-nitrophenol Chemical compound OC1=CC=CC=C1[N+]([O-])=O IQUPABOKLQSFBK-UHFFFAOYSA-N 0.000 description 2
- XJCVRTZCHMZPBD-UHFFFAOYSA-N 3-nitroaniline Chemical compound NC1=CC=CC([N+]([O-])=O)=C1 XJCVRTZCHMZPBD-UHFFFAOYSA-N 0.000 description 2
- RTZZCYNQPHTPPL-UHFFFAOYSA-N 3-nitrophenol Chemical compound OC1=CC=CC([N+]([O-])=O)=C1 RTZZCYNQPHTPPL-UHFFFAOYSA-N 0.000 description 2
- YQYGPGKTNQNXMH-UHFFFAOYSA-N 4-nitroacetophenone Chemical compound CC(=O)C1=CC=C([N+]([O-])=O)C=C1 YQYGPGKTNQNXMH-UHFFFAOYSA-N 0.000 description 2
- BXRFQSNOROATLV-UHFFFAOYSA-N 4-nitrobenzaldehyde Chemical compound [O-][N+](=O)C1=CC=C(C=O)C=C1 BXRFQSNOROATLV-UHFFFAOYSA-N 0.000 description 2
- JKTYGPATCNUWKN-UHFFFAOYSA-N 4-nitrobenzyl alcohol Chemical compound OCC1=CC=C([N+]([O-])=O)C=C1 JKTYGPATCNUWKN-UHFFFAOYSA-N 0.000 description 2
- BTJIUGUIPKRLHP-UHFFFAOYSA-N 4-nitrophenol Chemical compound OC1=CC=C([N+]([O-])=O)C=C1 BTJIUGUIPKRLHP-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 208000035126 Facies Diseases 0.000 description 2
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 description 2
- 125000003368 amide group Chemical group 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000009905 homogeneous catalytic hydrogenation reaction Methods 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 239000012046 mixed solvent Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 125000000636 p-nitrophenyl group Chemical group [H]C1=C([H])C(=C([H])C([H])=C1*)[N+]([O-])=O 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- WGTYBPLFGIVFAS-UHFFFAOYSA-M tetramethylammonium hydroxide Chemical compound [OH-].C[N+](C)(C)C WGTYBPLFGIVFAS-UHFFFAOYSA-M 0.000 description 2
- GEYOCULIXLDCMW-UHFFFAOYSA-N 1,2-phenylenediamine Chemical compound NC1=CC=CC=C1N GEYOCULIXLDCMW-UHFFFAOYSA-N 0.000 description 1
- CBCKQZAAMUWICA-UHFFFAOYSA-N 1,4-phenylenediamine Chemical compound NC1=CC=C(N)C=C1 CBCKQZAAMUWICA-UHFFFAOYSA-N 0.000 description 1
- HLBLWEWZXPIGSM-UHFFFAOYSA-N 4-Aminophenyl ether Chemical compound C1=CC(N)=CC=C1OC1=CC=C(N)C=C1 HLBLWEWZXPIGSM-UHFFFAOYSA-N 0.000 description 1
- CZGCEKJOLUNIFY-UHFFFAOYSA-N 4-Chloronitrobenzene Chemical compound [O-][N+](=O)C1=CC=C(Cl)C=C1 CZGCEKJOLUNIFY-UHFFFAOYSA-N 0.000 description 1
- TYMLOMAKGOJONV-UHFFFAOYSA-N 4-nitroaniline Chemical compound NC1=CC=C([N+]([O-])=O)C=C1 TYMLOMAKGOJONV-UHFFFAOYSA-N 0.000 description 1
- ZPTVNYMJQHSSEA-UHFFFAOYSA-N 4-nitrotoluene Chemical compound CC1=CC=C([N+]([O-])=O)C=C1 ZPTVNYMJQHSSEA-UHFFFAOYSA-N 0.000 description 1
- VQVIHDPBMFABCQ-UHFFFAOYSA-N 5-(1,3-dioxo-2-benzofuran-5-carbonyl)-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(C(C=2C=C3C(=O)OC(=O)C3=CC=2)=O)=C1 VQVIHDPBMFABCQ-UHFFFAOYSA-N 0.000 description 1
- QQGYZOYWNCKGEK-UHFFFAOYSA-N 5-[(1,3-dioxo-2-benzofuran-5-yl)oxy]-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(OC=2C=C3C(=O)OC(C3=CC=2)=O)=C1 QQGYZOYWNCKGEK-UHFFFAOYSA-N 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- FOIXSVOLVBLSDH-UHFFFAOYSA-N Silver ion Chemical compound [Ag+] FOIXSVOLVBLSDH-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000006184 cosolvent Substances 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- CRVGTESFCCXCTH-UHFFFAOYSA-N methyl diethanolamine Chemical compound OCCN(C)CCO CRVGTESFCCXCTH-UHFFFAOYSA-N 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000003053 piperidines Chemical class 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000001338 self-assembly Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000004936 stimulating effect Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
- C07C209/30—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds
- C07C209/32—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups
- C07C209/36—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups by reduction of nitro groups bound to carbon atoms of six-membered aromatic rings in presence of hydrogen-containing gases and a catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/393—Metal or metal oxide crystallite size
-
- 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
- B01J37/009—Preparation by separation, e.g. by filtration, decantation, screening
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
- C07C209/30—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds
- C07C209/32—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups
- C07C209/36—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups by reduction of nitro groups bound to carbon atoms of six-membered aromatic rings in presence of hydrogen-containing gases and a catalyst
- C07C209/365—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups by reduction of nitro groups bound to carbon atoms of six-membered aromatic rings in presence of hydrogen-containing gases and a catalyst by reduction with preservation of halogen-atoms in compounds containing nitro groups and halogen atoms bound to the same carbon skeleton
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C221/00—Preparation of compounds containing amino groups and doubly-bound oxygen atoms bound to the same carbon skeleton
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/60—Reduction reactions, e.g. hydrogenation
- B01J2231/64—Reductions in general of organic substrates, e.g. hydride reductions or hydrogenations
- B01J2231/641—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes
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Abstract
The present invention discloses the application in the hydrogenation of aromatic nitro compound of a kind of polyamic acid supported palladium nanocatalyst.Catalyst of the present invention comprises the Pd nano particle that particle diameter is less, dispersion is higher, and reaction system is in the diffusion of quasi-homodisperse state, beneficially reaction substrate and product;Catalyst carrier has the activation to reaction substrate of higher polarity, beneficially catalyst active center.The catalysis activity of catalyst is apparently higher than commercialization Pd/C catalyst.Catalyst has the water solublity that pH is sensitive, can realize well repeatedly reclaiming and repeat catalysis use.Catalytic reaction is normal temperature and pressure (H in aqueous phase2Implement under the conditions of), environment protecting and power-saving.
Description
Technical field
The invention belongs to metal nano catalyst application, be specifically related to a kind of accurate homogeneous, recyclable and recycling
Palladium nanocatalyst and application in the hydrogenation of aromatic nitro compound.
Background technology
The reduction reaction of aromatic nitro compound is an important reaction, because its aniline and its derivatives obtained is
The chemical intermediate that one class is important.The method of reducing of aromatic nitro compound substantially can be divided into metering type reducing process and catalytic type also
Former method.The reducing agent that metering type reducing process uses is mainly metal or the sulfide such as iron powder, glass putty, zinc powder, generally requires big
Amount acid medium, the requirement to equipment is the highest, also can discharge substantial amounts of waste water and dregs, environment is caused severe contamination.Compare it
Under, the reaction of catalytic type reducing process is simple, and environment friendly is high, and the especially catalytic hydrogenation process with hydrogen as reducing agent, at nitre
Based compound reduction aspect increasingly comes into one's own.
The method for hydrogenation of current industrial nitro compound is divided into vapour phase hydrogenation method and liquid-phase hydrogenation method.Vapour phase hydrogenation technique
Typically use activated carbon or oxide carried cuprio or palladium-based catalyst, need 200 300 DEG C of high temperature and the hydrogen of 1 3Mpa
Pressure;Liquid-phase hydrogenation technique typically uses the nickel-base catalyst of tripolite loading, activated carbon supported palladio or platinum based catalyst, needs
Want the hydrogen pressure that high temperature and 0.1 0.6Mpa in 90 200 DEG C are relatively low.On the whole, the industrial hydrogen chemical industry of current nitro compound
Skill still suffers from shortcomings, as high in reaction temperature, hydrogen pressure high (gas phase process) and solvent not environmentally, (the liquid phase work such as inflammable
Skill).Therefore, the synthesis technique developing active higher hydrogenation catalyst and mild condition, solvent green will be that this field is long-term
Target.Owing to having higher catalysis activity, load type palladium catalyst is the most frequently used hydrogenation catalyst.Traditional is heterogeneous
Pd/C catalyst is it is generally required to just have higher hydrogenation activity under the conditions of high pressure hydrogen.(Liquid phase
Hydrogenation of nitrobenzene, Applied Catalysis A:General, 2015,499,66 76) the most several
Year, the palladium nanocatalyst of quasi-homodisperse demonstrates the activity advantage become apparent from.Such as, F.A.Harraz et al. finds poly-
The palladium nanocatalyst that ethylene glycol (PEG) loads is at normal temperature and pressure (H2Under the conditions of), the hydrogenation of p-nitrophenyl just has higher urging
Change activity, need remain for machine solvent (ethanol) hydrotropy.(Palladium nanoparticles stabilized by
polyethylene glycol:Efficient,recyclable catalyst for hydrogenation of
Styrene and nitrobenzene, Journal of Catalysis, 2012,286,184 192)
Polyamic acid is a kind of containing a large amount of carboxyls with the macromolecule of amide groups active function groups, has both had adjustable water
Dissolubility, has again stronger complexing to metal, and therefore polyamic acid aqueous solution is to prepare quasi-homodisperse metal in situ to receive
The good medium system of rice corpuscles.(Synthesis of silver nanocubes with controlled size
using water-soluble poly(amic acid)salt as the intermediate via a novel ion-
Exchange self-assembly technique, Nanoscale, 2013,5,12,132 12135) additionally, polyamic acid is
A kind of stimulating responsive macromolecule, its water solublity has significant pH sensitivity, can give metal nano catalyst more rich
Functional (such as adjustable water dispersible and micro-reaction environment etc.) so that it is catalytic performance is more efficient and intelligent.(Poly
(amic acid)salt-stabilized silver nanoparticles as efficient and recyclable
quasi-homogeneous catalysts for the aqueous hydration of nitriles to amides,
New Journal of Chemistry,2016,40(1),358–364)
Therefore, the palladium nanocatalyst of polyamic acid load is suitable under aqueous phase and temperate condition, shows efficient standard
Homogeneous catalysis activity, and the recyclable of palladium nanocatalyst can be realized by pH sensitivity and reuse.Up to the present,
The palladium nanocatalyst of polyamic acid load and apply and still do not have document to report in catalyst field.
Summary of the invention
It is an object of the invention to provide the hydrogenation at aromatic nitro compound of a kind of polyamic acid supported palladium nanocatalyst
Application in reaction.The technical scheme that the present invention provides is:
In described polyamic acid supported palladium nanocatalyst molal quantity is polyamic acid carboxyl molal quantity the 0.1 20 of palladium
Times, preferably 2 times.Wherein, the physical characteristic parameter of described polyamic acid supported palladium nanocatalyst is: Pd nano particle is class
Spherical, mean diameter is 1 20nm;Chemical feature parameter is: Pd nano particle is zero-valent state, contains in polyamic acid molecular structure
There are a large amount of carboxyl and amide groups.
The preparation method of described polyamic acid supported palladium nanocatalyst comprises the steps:
(1) water-soluble polyamic acid salt is dissolved in deionized water, is configured to the polyamide that concentration is 0.013-1.3wt%
Acid salt aqueous solution;
(2) in polyamic acid saline solution, add the precursor solution of palladium, stir under room temperature, obtain palladium ion with
The complex solution of polyamic acid;
(3) complex solution obtained in step (2) is reacted with sodium borohydride or hydrazine hydrate, obtain polyamic acid load
Palladium nano-catalytic agent dispersing liquid;
(4) being 25 with the palladium nano dispersion fluid pH value obtained in acid-base modifier regulating step (3), polyamic acid loads
Palladium nanocatalyst settle, by crossing cleaner liquid, remove various water-solubility impurity ions in dispersion liquid, the palladium collected
Nanocatalyst precipitum rejoins in the acid-base modifier that pH value is 7 12 again and is heavily disperseed, and finally returns to
The polyamic acid supported palladium nanocatalyst of quasi-homodisperse state.
Wherein, step (1) described water-soluble polyamic acid salt is by polyamic acid and amine (such as triethylamine, piperidines etc.), alcohol
Amine (such as triethanolamine, N methyldiethanol amine, diethanolamine, ethanolamine etc.), quaternary ammonium bases are (such as Tetramethylammonium hydroxide
Deng) reacting prepared, polyamic acid is obtained by polycondensation reaction well known to those skilled in the art, including any one or more of diamidogen
The polyamic acid obtained with any one or more of dianhydride polycondensation.As diamidogen can be 4,4 '-diaminodiphenyl ether (ODA),
Phenylenediamine (m-PDA), p-phenylenediamine (p-PDA) etc.;Dianhydride can be pyromellitic acid dianhydride (PMDA), 3,3 ', 4,4 '-benzophenone
Tetracarboxylic dianhydride (BTDA), 3,3 ', 4,4 '-two methyl phenyl ethers anisole tetracarboxylic dianhydrides (ODPA) etc..
The precursor solution of step (2) described palladium is the one in the acid of chlorine palladium, chlorine palladium acid sodium, potassium chloropalladate aqueous solution.
During step (3) described complex solution reacts with sodium borohydride, the palladium ion in complex solution and sodium borohydride
Mol ratio be 1:(0.5 20), preferably 1:(1 2), reaction temperature is-5 100 DEG C, preferably 0 DEG C, and the response time is
0.5 24h, preferably 2h.During described complex solution reacts with hydrazine hydrate, the palladium ion in complex solution and hydrazine hydrate
Mol ratio is 1:(1 50), preferably 1:(5 10), reaction temperature is-5 100 DEG C, preferably 40 DEG C, and the response time is
0.5 24h, preferably 12h.
Step (4) described acid-base modifier is hydrochloric acid, acetic acid, triethylamine, sodium hydroxide, potassium hydroxide, sodium carbonate or carbon
Acid potassium.It is preferably acetic acid and sodium hydroxide.
In the present invention, the preparation principle of catalyst is as follows:
In polyamic acid saline solution, the preparation process of Pd nano particle mainly experiences 2 stages, as shown in Figure 6: (a) palladium
Ion (Pd2+) and polyamic acid salt (PAAS) complexation, form palladium macromole (PAA Pd N) complex;(b) palladium-macromole network
Compound is reduced agent reduction, and under the Stabilization of polyamic acid salt, and forming core and grow into Pd nano particle (PdNPs), from
And obtain the palladium nanocatalyst (PdNPs PAAS) of polyamic acid load.The final size of Pd nano particle, shape and dispersion
State is relevant with the kind of polyamic acid salt, the consumption of palladium presoma, the consumption of reducing agent, reduction reaction temperature etc..
It is anti-that polyamic acid supported palladium nanocatalyst of the present invention can be used for the catalytic hydrogenation to aromatic nitro compound
Ying Zhong.This application comprises the following steps:
(1) joining in Schlenk pipe by PdNPs PAAS catalyst solution and aromatic nitro compound, Schlenk manages
Connect H2Balloon, then uses oil pump evacuation, repeatedly replaces H2More than three times.Reaction solution is subsequently at room temperature, normal pressure H2Under the conditions of
It is stirred vigorously reaction.For the substrate that indivedual water solublity are excessively poor, need to additionally add organic solvent hydrotropy the most miscible with water.
Wherein, described reaction substrate aromatic nitro compound is Nitrobenzol, 4-nitrophenol, 3-nitrophenol, 2-nitrophenol, 4-nitre
Base aniline, 3-nitroaniline, 2-nitroaniline, 4-Methylnitrobenzene, 4-chloronitrobenzene, 4-Nitrobromobenzene, 4-nitro-acetophenone, 4-
Nitrobenzaldehyde, 4-nitrobenzyl alcohol etc..The mole dosage of described palladium catalyst and reaction substrate is than for 1:(10 1000), excellent
Elect 1:100 as.Cosolvent is ethanol, methanol, acetone, DMF, N,N-dimethylacetamide etc., preferably second
Alcohol, methanol.Reaction temperature is-5 100 DEG C, preferably 25 DEG C.
(2) identical with catalyst preparation step (4), can be by heavy for the acid of palladium nanocatalyst after catalytic reaction completes
Fall, it is achieved the recovery of palladium nanocatalyst, the palladium nanocatalyst of recovery heavily can disperse in alkaline aqueous solution, and under being used for
One takes turns quasi-homogeneous catalysis.After reaction terminates, with the hydrochloric acid regulation reaction solution of 1M to pH~2, subsequently reaction solution is stood sheet
Carve, after PdNPs PAAS catalyst settles completely, use and directly topple over or the side of low-speed centrifugal (5000rpm, 10min)
Method, can separate clear liquid with dark catalyst easily.The PdNPs PAAS catalyst separated rejoins water
In, adjust pH~8 by the NaOH solution of 1M, make catalyst heavily disperse, i.e. can be directly used for being catalyzed next time.
The present invention has a following superiority:
1) the palladium nanocatalyst prepared by the present invention has higher specific surface area, in quasi-homodisperse shape in water
State, the beneficially diffusion of reaction substrate, intermediate product and product;Polyamic acid carrier has higher polarity, is conducive to
Catalyst active center's activation to reaction substrate.
2) the palladium nanocatalyst prepared by the inventive method has pH sensitivity, can be effectively used for palladium nanocatalyst
Purification, accurate homogeneous efficient catalytic, recycle and reuse.
3) the inventive method is mainly with water as solvent, and environmental pollution is little;Reaction condition is normal temperature and pressure, saves the energy.
Accompanying drawing explanation
Fig. 1: the TEM image of polyamic acid supported palladium nanocatalyst in the present invention.
Fig. 2: the XRD figure spectrum of polyamic acid supported palladium nanocatalyst in the present invention.
With BTDA/ODA based polyamide hydrochlorate as carrier in Fig. 3: embodiment 2, the presoma with chlorine palladium acid sodium as palladium, prepare
The XPS Pd3d high resolution scanning collection of illustrative plates of Pd nano particle.
Fig. 4: under different solutions pH value, the Zeta potential of polyamic acid salt supported palladium nanoparticle is measured.
Fig. 5: polyamic acid supported palladium nanocatalyst and the reaction of commercialization Pd/C catalyst catalytic hydrogenation of nitrobenzene
Kinetic curve.
Fig. 6: the preparation principle figure of polyamic acid salt supported palladium nanoparticle.
Fig. 7: the catalytic applications schematic diagram of polyamic acid salt supported palladium nanoparticle.
The hydrogenation of Fig. 8: p-nitrophenyl repeats to be catalyzed the TEM figure of polyamic acid salt supported palladium nanoparticle after 6 times
Picture.
Detailed description of the invention
Below by specific embodiment, the present invention will be described, but the invention is not limited in this.
The raw material used in the embodiment of the present invention is commercially available.
Embodiment 1
The PMDA/ODA based polyamide triethylenetetraminehexaacetic acid amine salt dry silk taking 0.1g is dissolved in 80mL deionized water, after stirring and dissolving,
Adding the chlorine palladium acid sodium solution that 10mL concentration is 0.01M, after stirring, be cooled to 0 DEG C, adding 10mL concentration is 0.01M's
Sodium borohydride solution, continues stirring 2 hours, obtains the palladium nanocatalyst of polyamic acid salt load, for the quasi-homogeneous phase solution of black,
100mL altogether.
Embodiment 2
The BTDA/ODA based polyamide triethylenetetraminehexaacetic acid alcohol amine salt dry silk taking 0.1g is dissolved in 80mL deionized water, stirring and dissolving
After, add the chlorine palladium acid sodium solution that 10mL concentration is 0.01M, after stirring, be warming up to 40 DEG C, rapidly joining 10mL concentration is
The hydrazine hydrate solution of 0.1M, continues stirring 12 hours, obtains the palladium nanocatalyst of polyamic acid salt load, accurate homogeneous for black
Solution, altogether 100mL.
The catalytically active assessment of embodiment 3 pure water middle polyamic acid salt supported palladium nanocatalyst mutually
The polyamic acid salt supported palladium nanocatalyst obtained by above-described embodiment 1 is used for aromatic nitro compound (nitro
Benzene, 4-nitrophenol, 3-nitrophenol, 2-nitrophenol, 4-nitroaniline, 3-nitroaniline, 2-nitroaniline, 4-nitro first
Benzene, 4-nitro-acetophenone) quasi-homogeneous catalytic hydrogenation, it specifically comprises the following steps that
0.2mmol nitro compound and 2mL polyamic acid salt supported palladium nano-catalytic agent solution are joined Schlenk pipe
In.Schlenk pipe connects H2Balloon, then uses oil pump evacuation, repeatedly replaces H2More than three times.Reaction solution subsequently room temperature,
Normal pressure H2Under the conditions of be stirred vigorously reaction.For monitoring extent of reaction, each timing sampling~30 μ L, repeatedly extract by ethyl acetate
After, merging organic facies, by gas chromatogram, it is analyzed, its result is as shown in table 1.
In order to contrast the activity of polyamic acid salt supported palladium nanocatalyst and commercialization Pd/C catalyst, at the same terms
Lower employing same operation method, with the hydrogenation of commercialization Pd/C catalyst Nitrobenzol, the kinetics of catalytic reaction is bent
Line comparison diagram is as shown in Figure 5.
The table 1 pure water middle PdNPs-PAAS catalyst catalytic hydrogenation result to aromatic nitro compound mutually
Reaction condition: 0.2mmol substrate, 1mol% palladium catalyst, 2mL water, 1bar H2, 25 DEG C.
The catalytically active assessment of polyamic acid salt supported palladium nanocatalyst in embodiment 4 water and alcohol mixed solvent
The polyamic acid salt supported palladium nanocatalyst obtained by above-described embodiment 1 is used for aromatic nitro compound (4-nitre
Base chlorobenzene, 4-Nitrobromobenzene, 4-nitrobenzaldehyde, 4-nitrobenzyl alcohol) quasi-homogeneous catalytic hydrogenation, its concrete steps are such as
Under:
0.2mmol nitro compound, 2mL polyamic acid salt supported palladium nano-catalytic agent solution and 1mL ethanol are joined
In Schlenk pipe.Schlenk pipe connects H2Balloon, then uses oil pump evacuation, repeatedly replaces H2More than three times.Reaction solution with
After at room temperature, normal pressure H2Under the conditions of be stirred vigorously reaction.For monitoring extent of reaction, each timing sampling~30 μ L, use acetic acid second
After ester repeatedly extracts, merging organic facies, be analyzed it by gas chromatogram, its result is as shown in table 2.
The PdNPs-PAAS catalyst catalytic hydrogenation result to aromatic nitro compound in table 2 water and alcohol mixed solvent
Reaction condition: 0.2mmol substrate, 1mol% palladium catalyst, 2mL water and 1mL ethanol, 1bar H2, 25 DEG C.
Embodiment 5
The polyamic acid salt supported palladium nanocatalyst obtained by above-described embodiment 1 is used for the quasi-homogeneous catalysis hydrogen of Nitrobenzol
Change reaction, investigate the repeat performance of catalyst, specifically comprise the following steps that
0.2mmol Nitrobenzol and 2mL polyamic acid salt supported palladium nano-catalytic agent solution are joined in Schlenk pipe.
Schlenk pipe connects H2Balloon, then uses oil pump evacuation, repeatedly replaces H2More than three times.Reaction solution subsequently in room temperature, often
Pressure H2Under the conditions of be stirred vigorously reaction.After reaction 5h, with the hydrochloric acid regulation reaction solution of 1M to pH~2, subsequently by reaction solution
Stand a moment, after PdNPs PAAS catalyst settles completely, use and directly topple over or low-speed centrifugal (5000rpm, 10min)
Method, can easily clear liquid be separated with catalyst solid.The PdNPs PAAS catalyst separated rejoins
In 2mL water, with the NaOH solution of 1M adjust pH to~8, make catalyst heavily disperse, i.e. can be directly used for being catalyzed next time.(result is shown in
Table 3)
The repetition catalytic effect of table 3 polyamic acid salt supported palladium nanocatalyst catalysis nitrobenzene reaction
Reaction condition: 0.2mmol Nitrobenzol, 1mol% palladium catalyst, 2mL water, 1bar H2, 25 DEG C.
Claims (9)
1. polyamic acid supported palladium nanocatalyst application in the hydrogenation of aromatic nitro compound.
Apply the most as claimed in claim 1, it is characterised in that in described polyamic acid supported palladium nanocatalyst palladium mole
Number is 0.1 20 times of polyamic acid carboxyl molal quantity.
Apply the most as claimed in claim 1, it is characterised in that in described polyamic acid supported palladium nanocatalyst palladium mole
Number is 2 times of polyamic acid carboxyl molal quantity.
Apply the most as claimed in claim 1, it is characterised in that the physical features of described polyamic acid supported palladium nanocatalyst
Parameter is: Pd nano particle is near-spherical, and mean diameter is 1 20nm;Chemical feature parameter is: Pd nano particle is zeroth order
State.
5. the application described in claim 1, it is characterised in that the preparation method bag of described polyamic acid supported palladium nanocatalyst
Include following steps:
(1) water-soluble polyamic acid salt is dissolved in deionized water, is configured to the polyamic acid salt that concentration is 0.013-1.3wt%
Aqueous solution;
(2) in polyamic acid saline solution, add the precursor solution of palladium, stir under room temperature, obtain palladium ion and polyamides
The complex solution of amino acid;
(3) complex solution obtained in step (2) is reacted with sodium borohydride or hydrazine hydrate, obtain the palladium of polyamic acid load
Nano-catalytic agent dispersing liquid;
(4) it is 25 with the palladium nano dispersion fluid pH value obtained in acid-base modifier regulating step (3), the palladium of polyamic acid load
Nanocatalyst settles, and by crossing cleaner liquid, removes various water-solubility impurity ions in dispersion liquid, the palladium nanometer collected
Catalyst sedimentation thing rejoins in the acid-base modifier that pH value is 7 12 again and is heavily disperseed,
And finally return to the polyamic acid supported palladium nanocatalyst of quasi-homodisperse state.
6. method as claimed in claim 5, it is characterised in that step (1) described water-soluble polyamic acid salt is by polyamic acid
Prepare with amine, alcamines, the reaction of quaternary ammonium bases.
7. method as claimed in claim 6, it is characterised in that the precursor solution of step (2) described palladium is the acid of chlorine palladium, chlorine palladium
One in acid sodium, potassium chloropalladate aqueous solution.
8. method as claimed in claim 7, it is characterised in that step (3) described complex solution and sodium borohydride or hydration
In hydrazine reaction, the mol ratio of the palladium ion in complex solution and sodium borohydride is respectively 1:(0.5 20), reaction temperature is-
5 100 DEG C, the response time is 0.5 24h;Palladium ion during described complex solution reacts with hydrazine hydrate, in complex solution
It is 1:(1 50 with the mol ratio of hydrazine hydrate), reaction temperature is-5 100 DEG C, and the response time is 0.5 24h.
9. method as claimed in claim 8, it is characterised in that step (4) described acid-base modifier is hydrochloric acid, acetic acid, three second
Amine, sodium hydroxide, potassium hydroxide, sodium carbonate or potassium carbonate.
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CN115155662A (en) * | 2022-07-21 | 2022-10-11 | 江南大学 | Method for preparing arylamine compound by hydrogenating aromatic nitro compound and preparation method of palladium catalyst thereof |
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