WO2023280276A1 - 一种3-甲基哌啶脱氢催化剂及其制备方法与应用 - Google Patents
一种3-甲基哌啶脱氢催化剂及其制备方法与应用 Download PDFInfo
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- WO2023280276A1 WO2023280276A1 PCT/CN2022/104415 CN2022104415W WO2023280276A1 WO 2023280276 A1 WO2023280276 A1 WO 2023280276A1 CN 2022104415 W CN2022104415 W CN 2022104415W WO 2023280276 A1 WO2023280276 A1 WO 2023280276A1
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- Prior art keywords
- methylpiperidine
- dehydrogenation catalyst
- active component
- methylpyridine
- catalyst
- Prior art date
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- 239000003054 catalyst Substances 0.000 title claims abstract description 80
- JEGMWWXJUXDNJN-UHFFFAOYSA-N 3-methylpiperidine Chemical compound CC1CCCNC1 JEGMWWXJUXDNJN-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 238000006356 dehydrogenation reaction Methods 0.000 title claims abstract description 35
- 238000002360 preparation method Methods 0.000 title claims description 9
- ITQTTZVARXURQS-UHFFFAOYSA-N 3-methylpyridine Chemical compound CC1=CC=CN=C1 ITQTTZVARXURQS-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000000034 method Methods 0.000 claims abstract description 24
- 238000006243 chemical reaction Methods 0.000 claims abstract description 22
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 18
- 238000011068 loading method Methods 0.000 claims abstract description 17
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 14
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 14
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims abstract description 14
- 150000001342 alkaline earth metals Chemical class 0.000 claims abstract description 14
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims abstract description 3
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 3
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 18
- 239000002904 solvent Substances 0.000 claims description 14
- 229910052749 magnesium Inorganic materials 0.000 claims description 12
- 229910052700 potassium Inorganic materials 0.000 claims description 12
- 239000002243 precursor Substances 0.000 claims description 12
- 229910052763 palladium Inorganic materials 0.000 claims description 10
- 238000010521 absorption reaction Methods 0.000 claims description 7
- 150000003841 chloride salts Chemical class 0.000 claims description 7
- 229920006395 saturated elastomer Polymers 0.000 claims description 7
- 239000000654 additive Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 229910052707 ruthenium Inorganic materials 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 229910052697 platinum Inorganic materials 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 4
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 3
- 150000001242 acetic acid derivatives Chemical class 0.000 claims description 3
- 150000002823 nitrates Chemical class 0.000 claims description 3
- 229910052703 rhodium Inorganic materials 0.000 claims description 3
- 230000000996 additive effect Effects 0.000 claims description 2
- 229910021529 ammonia Inorganic materials 0.000 claims description 2
- 229910052791 calcium Inorganic materials 0.000 claims description 2
- 239000012456 homogeneous solution Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims 1
- 229910002651 NO3 Inorganic materials 0.000 claims 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims 1
- 125000001309 chloro group Chemical class Cl* 0.000 claims 1
- 238000005470 impregnation Methods 0.000 abstract description 4
- 230000008016 vaporization Effects 0.000 abstract description 4
- 238000009834 vaporization Methods 0.000 abstract description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 18
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 14
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 14
- 238000003756 stirring Methods 0.000 description 11
- 239000011777 magnesium Substances 0.000 description 10
- 239000008188 pellet Substances 0.000 description 10
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 8
- 229910001629 magnesium chloride Inorganic materials 0.000 description 7
- 239000001103 potassium chloride Substances 0.000 description 7
- 235000011164 potassium chloride Nutrition 0.000 description 7
- 239000012159 carrier gas Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 230000000977 initiatory effect Effects 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 238000011156 evaluation Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000011017 operating method Methods 0.000 description 5
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 5
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 238000001354 calcination Methods 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000010970 precious metal Substances 0.000 description 4
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 4
- UJPKMTDFFUTLGM-UHFFFAOYSA-N 1-aminoethanol Chemical compound CC(N)O UJPKMTDFFUTLGM-UHFFFAOYSA-N 0.000 description 3
- BSKHPKMHTQYZBB-UHFFFAOYSA-N 2-methylpyridine Chemical compound CC1=CC=CC=N1 BSKHPKMHTQYZBB-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 150000004687 hexahydrates Chemical class 0.000 description 3
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 description 3
- PAMIQIKDUOTOBW-UHFFFAOYSA-N 1-methylpiperidine Chemical compound CN1CCCCC1 PAMIQIKDUOTOBW-UHFFFAOYSA-N 0.000 description 2
- JZUHIOJYCPIVLQ-UHFFFAOYSA-N 2-methylpentane-1,5-diamine Chemical compound NCC(C)CCCN JZUHIOJYCPIVLQ-UHFFFAOYSA-N 0.000 description 2
- ZTWQTBDEQSLEAF-UHFFFAOYSA-N C(=O)C=C.N Chemical compound C(=O)C=C.N ZTWQTBDEQSLEAF-UHFFFAOYSA-N 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000011280 coal tar Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000012847 fine chemical Substances 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000010948 rhodium Substances 0.000 description 2
- 238000007363 ring formation reaction Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- PVNIIMVLHYAWGP-UHFFFAOYSA-N Niacin Chemical compound OC(=O)C1=CC=CN=C1 PVNIIMVLHYAWGP-UHFFFAOYSA-N 0.000 description 1
- DFPAKSUCGFBDDF-ZQBYOMGUSA-N [14c]-nicotinamide Chemical compound N[14C](=O)C1=CC=CN=C1 DFPAKSUCGFBDDF-ZQBYOMGUSA-N 0.000 description 1
- YAIQCYZCSGLAAN-UHFFFAOYSA-N [Si+4].[O-2].[Al+3] Chemical compound [Si+4].[O-2].[Al+3] YAIQCYZCSGLAAN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003398 denaturant Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 235000005152 nicotinamide Nutrition 0.000 description 1
- 239000011570 nicotinamide Substances 0.000 description 1
- 229960003512 nicotinic acid Drugs 0.000 description 1
- DFPAKSUCGFBDDF-UHFFFAOYSA-N nicotinic acid amide Natural products NC(=O)C1=CC=CN=C1 DFPAKSUCGFBDDF-UHFFFAOYSA-N 0.000 description 1
- 238000013040 rubber vulcanization Methods 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 238000003786 synthesis reaction Methods 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/58—Platinum group metals with alkali- or alkaline earth metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or 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
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
- C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
- C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D213/06—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom
- C07D213/133—Preparation by dehydrogenation of hydrogenated pyridine compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
- C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
- C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D213/06—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom
- C07D213/16—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom containing only hydrogen and carbon atoms in addition to the ring nitrogen atom containing only one pyridine ring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/066—Zirconium or hafnium; Oxides or hydroxides thereof
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Definitions
- the invention belongs to the field of fine chemical industry, and relates to a 3-methylpiperidine dehydrogenation catalyst and a preparation method thereof, and an application of the catalyst for preparing 2-methylpyridine through dehydrogenation.
- 3-picoline is an important fine chemical raw material, mainly used for the preparation of nicotinic acid and nicotinamide, and also used as an intermediate for the synthesis of spices, dyes, solvents, alcohol denaturants and rubber vulcanization accelerators, etc., with a wide range of uses .
- the reported preparation methods of 3-picoline include coal tar extraction method, acrolein ammonia method, 2-methyl-1,5-pentanediamine cyclization method and aldehyde ammonia method to produce pyridine base co-production of 3-picoline .
- the co-production of 3-picoline by aldehyde ammonia method to pyridine base is the main production method.
- the coal tar extraction method is an early production method, which is inefficient and has long been abandoned.
- the main problem of the acrolein ammonia method and the cyclization method of 2-methyl-1,5-pentanediamine is that the reaction conditions are harsh and the yield of 3-picoline is low.
- 3-picoline is only a by-product of this method.
- the low selectivity of the catalyst is a prominent shortcoming, and there is a problem of separation from pyridine.
- the dehydrogenation of 3-methylpiperidine to prepare 3-methylpyridine has high selectivity and can avoid separation problems, thus becoming an efficient method for preparing 3-methylpyridine.
- the 3-methylpiperidine dehydrogenation catalyst has been publicly reported as follows: U.S. Patent No. 8,530,664 discloses a 3-methylpiperidine dehydrogenation catalyst, with silicon-aluminum oxide as a carrier, and noble metal Pd as an active component. 7.5%, using a mixed gas of nitrogen and hydrogen as the carrier gas, the mass space velocity of 3-methylpiperidine is 3h -1 , reacted at 300°C for 509h, and the yield of 3-methylpyridine was stable at 98%.
- patent US8324388 disclose a kind of 3 -methyl piperidine dehydrogenation catalyst, with ZrO2 as carrier, with precious metal Pd as active component, loading capacity 0.9%, with nitrogen, hydrogen mixed gas as carrier gas,
- the volume space velocity of 3-methylpiperidine is 0.3h -1 , the conversion rate is 99.5%, and the volume space velocity is 1.2h -1 , the conversion rate is 78%.
- U.S. Patent No. 4,762,929 discloses a catalyst for preparing 3-picoline by dehydrogenation of 3-methylpiperidine.
- the noble metal Pd is used as an active component, and the loading capacity is 1%.
- the conversion rate of 3-methylpiperidine is 95%.
- the methylpiperidine selectivity is 93%, and the catalyst life is 100 days.
- the above-mentioned 3-methylpiperidine dehydrogenation catalysts all use a single noble metal palladium as an active component, and have a high loading capacity. During the reaction process, a mixed gas of nitrogen and hydrogen needs to be continuously fed as a carrier gas, which is not conducive to industrial production.
- the object of the present invention is to provide a 3-methylpiperidine dehydrogenation catalyst, which solves the disadvantages of high loading capacity of noble metals in the prior art and the need to continuously feed nitrogen and hydrogen as carrier gas during the reaction.
- a kind of 3-methylpiperidine dehydrogenation catalyst is carrier with metal oxide, is active component with precious metal, is auxiliary agent with alkali metal and alkaline earth metal, and the load capacity of active component (with precious metal element quality and The carrier mass ratio) is 0.05-0.5%, and the loading amount of the auxiliary agent (calculated by the ratio of the alkali metal and alkaline earth metal element mass to the carrier mass ratio) is 0.1-1.0%.
- the loading amount of the active component is 0.05-0.1%; the loading amount of the auxiliary agent is 0.1-0.5%.
- the mass ratio of the alkali metal to the alkaline earth metal is 1:1-5.
- the carrier is one of Al 2 O 3 , ZrO 2 , TiO 2 , preferably Al 2 O 3 .
- the carrier is a small spherical carrier with a diameter of 1-5 mm.
- the noble metal is one of Ru, Pt, Pd, Rh, preferably Pd.
- the alkali metal is a combination of at least one of Na or K and at least one of alkaline earth metals Mg and Ca; more preferably, the additive is a combination of K and Mg.
- the 3-methylpiperidine dehydrogenation catalyst described in the present invention is prepared by an equal-volume impregnation method.
- Another object of the present invention is to provide the preparation method of the described 3-methylpiperidine dehydrogenation catalyst, comprising: taking a solvent equal to the volume of the saturated absorption of the carrier to be impregnated, the active component precursor, the auxiliary agent precursor 3-Methylpiperidine dehydrogenation catalyst is prepared by dissolving the body in a solvent to form a homogeneous solution, dispersing the carrier in the solution, fully turning and stirring the carrier, so that the solution is fully impregnated on the carrier, and then naturally air-dried, dried, and roasted .
- the active component precursor is one of noble metals such as chloride salts, nitrates or acetates corresponding to Ru, Pt, Pd and Rh, preferably a chloride salt.
- noble metals such as chloride salts, nitrates or acetates corresponding to Ru, Pt, Pd and Rh, preferably a chloride salt.
- the auxiliary agent precursor is one of chloride salts, nitrates or acetates of alkali metals and alkaline earth metals, preferably chloride salts.
- the solvent is one or a mixture of water, hydrochloric acid, ethanol, and ammonia, preferably water or hydrochloric acid.
- hydrochloric acid is 5% hydrochloric acid.
- the drying temperature is 120-140° C., and the drying time is 6-12 hours.
- the calcination temperature is 500-600° C., and the calcination time is 4-6 hours.
- Another object of the present invention is to provide the application of the 3-methylpiperidine dehydrogenation catalyst in the preparation of 3-methylpyridine by dehydrogenating 3-methylpyridine.
- a method for preparing 3-methylpyridine, using 3-methylpiperidine as a raw material, heating and vaporizing, and preparing 3-methylpyridine through a fixed-bed reactor filled with a 3-methylpiperidine dehydrogenation catalyst wherein, the mass space velocity of 3 - methylpiperidine is 1-5h -1 , preferably 2-4h -1 , the process conditions are: normal pressure, and the reaction temperature is 180-300°C, preferably 200-260°C.
- the present invention has the following beneficial effects:
- the 3-methylpiperidine dehydrogenation catalyst of the present invention can greatly reduce the noble metal loading by adding cheap and easily available alkali metals and alkaline earth metals as additives, so that the noble metal loading is ⁇ 0.1%.
- the reaction process does not require a carrier gas.
- 3-methylpiperidine is produced by fixed-bed reaction.
- the catalyst's long-term transport activity does not decay, and its lifespan is more than 3000h.
- the yield of picoline >98%.
- the 3-methylpiperidine dehydrogenation catalyst of the invention has significant cost advantages and industrial application prospects.
- Example 1 The support of Example 1 was replaced by dry ZrO pellets with a diameter of 3 mm. Take 100g of dry ZrO pellets with a diameter of 3mm, use water as a solvent, and measure its saturated water absorption to be 87g.
- Example 1 The support of Example 1 was replaced by dry TiO pellets with a diameter of 3 mm. Take 100g of dry TiO pellets with a diameter of 3mm, use water as a solvent, and measure its saturated water absorption to be 82g.
- Example 1 The active component precursor palladium chloride in Example 1 was replaced by chloroplatinic acid hexahydrate to prepare a platinum-supported catalyst.
- Example 2 The active component precursor palladium chloride in Example 1 was replaced by anhydrous ruthenium trichloride to prepare a ruthenium-loaded catalyst.
- Example 1 The solvent of Example 1 was replaced with 5% hydrochloric acid. Take 100g of dry Al 2 O 3 pellets with a diameter of 3mm, and measure its saturated water absorption to be 102g.
- the noble metal Pd is not loaded, and only alkali metal and alkaline earth metal additives are impregnated on the carrier.
- Examples 1 to 3 show that with the same active components, additives and impregnation conditions, the initial activity of the catalyst prepared with Al 2 O 3 as the carrier is higher than that of the catalyst prepared with ZrO 2 and TiO 2 as the carrier. .
- the catalyst of the present invention greatly reduces the noble metal loading of the catalyst by adding alkali metals and alkaline earth metals, and the performance of the catalyst is significantly improved, and no carrier gas needs to be introduced during the reaction.
- reaction temperature 250°C and mass space velocity of 2h -1 for a long time
- the conversion rate of 3-methylpiperidine can be maintained at >99%, and the yield of 3-methylpyridine can be maintained at >98%.
- the catalyst of the invention has been operated for more than 3000 hours and still maintains stable catalytic activity.
- the present invention illustrates the detailed methods of the present invention through the above-mentioned examples, but the present invention is not limited to the above-mentioned detailed methods, that is, it does not mean that the present invention must rely on the above-mentioned detailed methods to be implemented.
- Those skilled in the art should understand that any improvement of the present invention, the equivalent replacement of each raw material of the product of the present invention, the addition of auxiliary components, the selection of specific methods, etc., all fall within the scope of protection and disclosure of the present invention.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Hydrogenated Pyridines (AREA)
Abstract
Description
Claims (10)
- 一种3-甲基哌啶脱氢催化剂,其特征在于所述的催化剂以金属氧化物为载体,以贵金属为活性组分,以碱金属和碱土金属为助剂,活性组分的负载量为0.05~0.5%,助剂的负载量为0.1~1.0%。
- 根据权利要求1所述的3-甲基哌啶脱氢催化剂,其特征在于所述的活性组分的负载量为0.05~0.1%;所述的助剂的负载量为0.1~0.5%。
- 根据权利要求1所述的3-甲基哌啶脱氢催化剂,其特征在于所述的碱金属和碱土金属的质量比为1:1~5。
- 根据权利要求1所述的3-甲基哌啶脱氢催化剂,其特征在于所述的载体为Al 2O 3、ZrO 2、TiO 2中的一种。
- 根据权利要求1所述的3-甲基哌啶脱氢催化剂,其特征在于所述的活性组分为Ru、Pt、Pd、Rh中的一种,优选为Pd。
- 根据权利要求1所述的3-甲基哌啶脱氢催化剂,其特征在于所述的助剂为碱金属Na、K中的至少一种与碱土金属Mg、Ca中的至少一种的组合,优选为K和Mg的组合。
- 权利要求1所述的3-甲基哌啶脱氢催化剂的制备方法,其特征在于包括:取与待浸渍载体的饱和吸收量等体积的溶剂,将活性组分前驱体、助剂前驱体溶于溶剂中配成均相溶液,将载体分散于溶液中使溶液充分浸渍到载体上,经自然风干、干燥、焙烧制得3-甲基哌啶脱氢催化剂。
- 根据权利要求7所述的3-甲基哌啶脱氢催化剂的制备方法,其特征在于所述的活性组分前驱体为贵金属对应的氯盐、硝酸盐或醋酸盐中的一种,优选为氯盐;所述的助剂前驱体为碱金属和碱土金属对应的氯盐、硝酸盐或醋酸盐中的一种,优选为氯盐;所述的溶剂为水、盐酸、乙醇、氨水中的一种或两种混合,优选为水或盐酸。
- 权利要求1-6任一项所述的3-甲基哌啶脱氢催化剂在3-甲基吡啶脱氢制备3-甲基吡啶的应用。
- 一种制备3-甲基吡啶的方法,其特征在于以3-甲基哌啶为原料,经加热汽化,经装填有权利要求1所述的3-甲基哌啶脱氢催化剂的固定床反应器,制得3-甲基吡啶;其中,3-甲基哌啶的质量空速为1~5h -1,优选为2~4h -1,工艺条件为:常压,反应温度为180~300℃,优选为200~260℃。
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