CN111974455A - Catalyst PCuMo for catalyzing epoxidation reaction of cyclooctene and cyclododecene11@PC - Google Patents
Catalyst PCuMo for catalyzing epoxidation reaction of cyclooctene and cyclododecene11@PC Download PDFInfo
- Publication number
- CN111974455A CN111974455A CN202010822716.5A CN202010822716A CN111974455A CN 111974455 A CN111974455 A CN 111974455A CN 202010822716 A CN202010822716 A CN 202010822716A CN 111974455 A CN111974455 A CN 111974455A
- Authority
- CN
- China
- Prior art keywords
- pcumo
- catalyst
- cyclooctene
- cyclododecene
- catalyzing
- 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.)
- Pending
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 37
- 238000006735 epoxidation reaction Methods 0.000 title claims abstract description 27
- URYYVOIYTNXXBN-UPHRSURJSA-N cyclooctene Chemical compound C1CCC\C=C/CC1 URYYVOIYTNXXBN-UPHRSURJSA-N 0.000 title claims abstract description 26
- 239000004913 cyclooctene Substances 0.000 title claims abstract description 26
- HYPABJGVBDSCIT-UPHRSURJSA-N cyclododecene Chemical compound C1CCCCC\C=C/CCCC1 HYPABJGVBDSCIT-UPHRSURJSA-N 0.000 claims abstract description 23
- 238000002360 preparation method Methods 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 13
- DHRLEVQXOMLTIM-UHFFFAOYSA-N phosphoric acid;trioxomolybdenum Chemical class O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.OP(O)(O)=O DHRLEVQXOMLTIM-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 10
- 239000002131 composite material Substances 0.000 claims abstract description 9
- 239000013310 covalent-organic framework Substances 0.000 claims abstract description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910052802 copper Inorganic materials 0.000 claims abstract description 6
- 239000010949 copper Substances 0.000 claims abstract description 6
- RLNDAEAVPRIWSX-UHFFFAOYSA-N C1CCCCC=CCCCCC1.[O] Chemical compound C1CCCCC=CCCCCC1.[O] RLNDAEAVPRIWSX-UHFFFAOYSA-N 0.000 claims abstract 2
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- AMIMRNSIRUDHCM-UHFFFAOYSA-N Isopropylaldehyde Chemical compound CC(C)C=O AMIMRNSIRUDHCM-UHFFFAOYSA-N 0.000 claims description 8
- GLUUGHFHXGJENI-UHFFFAOYSA-N Piperazine Chemical compound C1CNCCN1 GLUUGHFHXGJENI-UHFFFAOYSA-N 0.000 claims description 8
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 4
- MGNCLNQXLYJVJD-UHFFFAOYSA-N cyanuric chloride Chemical compound ClC1=NC(Cl)=NC(Cl)=N1 MGNCLNQXLYJVJD-UHFFFAOYSA-N 0.000 claims description 4
- 238000004817 gas chromatography Methods 0.000 claims description 4
- 239000012528 membrane Substances 0.000 claims description 4
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 3
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical group [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 claims description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical class [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 2
- 229910001431 copper ion Inorganic materials 0.000 claims description 2
- 239000013078 crystal Substances 0.000 claims description 2
- 229910001882 dioxygen Inorganic materials 0.000 claims description 2
- 239000012065 filter cake Substances 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 239000011541 reaction mixture Substances 0.000 claims description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 2
- 235000011152 sodium sulphate Nutrition 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 2
- 239000008367 deionised water Substances 0.000 claims 1
- 229910021641 deionized water Inorganic materials 0.000 claims 1
- 238000001514 detection method Methods 0.000 claims 1
- 239000012265 solid product Substances 0.000 claims 1
- 238000000967 suction filtration Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- 150000001336 alkenes Chemical class 0.000 abstract description 10
- 230000003197 catalytic effect Effects 0.000 abstract description 8
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract description 7
- 230000007613 environmental effect Effects 0.000 abstract 1
- 239000002638 heterogeneous catalyst Substances 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- 239000011148 porous material Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 239000004593 Epoxy Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- CIHOLLKRGTVIJN-UHFFFAOYSA-N tert‐butyl hydroperoxide Chemical compound CC(C)(C)OO CIHOLLKRGTVIJN-UHFFFAOYSA-N 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000002329 infrared spectrum Methods 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000011149 active material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 239000011964 heteropoly acid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 1
- HSNVNALJRSJDHT-UHFFFAOYSA-N P(=O)(=O)[Mo] Chemical compound P(=O)(=O)[Mo] HSNVNALJRSJDHT-UHFFFAOYSA-N 0.000 description 1
- AWMVMTVKBNGEAK-UHFFFAOYSA-N Styrene oxide Chemical compound C1OC1C1=CC=CC=C1 AWMVMTVKBNGEAK-UHFFFAOYSA-N 0.000 description 1
- JNIQYRLMPFIVTE-UHFFFAOYSA-N [P].[W].[Mo] Chemical compound [P].[W].[Mo] JNIQYRLMPFIVTE-UHFFFAOYSA-N 0.000 description 1
- -1 alkyl hydrogen peroxide solution Chemical compound 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 150000001925 cycloalkenes Chemical class 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 150000003944 halohydrins Chemical class 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052747 lanthanoid Inorganic materials 0.000 description 1
- 150000002602 lanthanoids Chemical class 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
Images
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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1616—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts
- B01J31/1625—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts immobilised by covalent linkages, i.e. pendant complexes with optional linking groups
- B01J31/1633—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts immobilised by covalent linkages, i.e. pendant complexes with optional linking groups covalent linkages via silicon containing groups
-
- 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
- B01J31/1691—Coordination polymers, e.g. metal-organic frameworks [MOF]
-
- 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
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
-
- 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
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/633—Pore volume less than 0.5 ml/g
-
- 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
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
- C07D301/04—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen
- C07D301/06—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the liquid phase
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/04—Compounds containing oxirane rings containing only hydrogen and carbon atoms in addition to the ring oxygen atoms
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Epoxy Compounds (AREA)
Abstract
本发明公开了一种用于催化环辛烯和环十二烯氧化反应的催化剂PCuMo11的制备方法。包括:铜离子取代的磷钼酸PCuMo11的制备以及将PCuMo11负载共价有机骨架材料PC上得到PCuMo11@PC新型复合材料的方法;另外本发明将PCuMo11@PC用于催化环辛烯和环十二烯氧气环氧化反应。本发明具有操作简单、经济环保、催化性能好等特点,制备的新型复合材料PCuMo11@PC是一种高效且环境友好的烯烃环氧化反应多相催化剂。The invention discloses a preparation method of a catalyst PCuMo 11 for catalyzing the oxidation reaction of cyclooctene and cyclododecene. Including: the preparation of copper ion-substituted phosphomolybdic acid PCuMo 11 and the method of loading PCuMo 11 on covalent organic framework material PC to obtain PCuMo 11 @PC new composite material; In addition, the present invention uses PCuMo 11 @PC for catalyzing cyclooctene And cyclododecene oxygen epoxidation reaction. The invention has the characteristics of simple operation, economy and environmental protection, good catalytic performance and the like, and the prepared new composite material PCuMo 11 @PC is an efficient and environment-friendly heterogeneous catalyst for olefin epoxidation reaction.
Description
技术领域technical field
本发明属于多相催化材料技术领域,具体涉及一种共价有机骨架材料负载铜离子取代磷钼酸制备方法并应用催化环辛烯和环十二烯环氧化反应。The invention belongs to the technical field of heterogeneous catalytic materials, in particular to a method for preparing a covalent organic framework material supported by copper ions to replace phosphomolybdic acid and applying it to catalyze the epoxidation reaction of cyclooctene and cyclododecene.
背景技术Background technique
环氧化合物是化工中一种用途十分广泛的重要中间产物,广泛用于医药,材料和化工等领域。烯烃环氧化反应是生产环氧化合物的主要来源,其中合成烯烃环氧化合物有卤醇法、过酸法等方法,但使用的氧化剂存在环境污染、设备腐蚀、生产复杂、产率低且耗能高等问题。为了改善上述问题,人们在烯烃环氧化反应上开发了许多新兴催化剂。CN110433826A利用共沉淀法制备了一种单原子金催化剂,催化以空气为氧化剂的苯乙烯环氧化反应。虽然催化性能好、稳定性好,但金价格昂贵且耗能高;CN110694676A公开了一种TUD-1掺杂镧系金属的介孔催化剂,在烷基过氧化氢溶液中可以催化C3-C10的链烯烃或环烯烃。该催化剂制备过程复杂且耗时较长,不利于工业化生产。Epoxy compound is an important intermediate product with a wide range of uses in the chemical industry, and is widely used in the fields of medicine, material and chemical industry. Olefin epoxidation reaction is the main source of producing epoxy compounds, among which there are methods such as halohydrin method and peracid method for synthesizing olefin epoxy compounds, but the oxidant used has environmental pollution, equipment corrosion, complex production, low yield and consumption. Can higher issues. In order to improve the above problems, many new catalysts have been developed for olefin epoxidation. CN110433826A utilizes co-precipitation method to prepare a single-atom gold catalyst, which catalyzes the epoxidation of styrene with air as the oxidant. Although it has good catalytic performance and good stability, gold is expensive and energy-intensive; CN110694676A discloses a TUD-1 doped lanthanide metal mesoporous catalyst, which can catalyze C 3 -C in alkyl hydrogen peroxide solution 10 alkene or cycloalkene. The catalyst preparation process is complicated and time-consuming, which is not conducive to industrial production.
杂多酸是由杂原子(如P、Si、Fe、Co等)和多原子(如Mo、W、V、Nb、Ta等)组成的含氧多酸绿色催化剂。因杂多酸独特的酸性、“准液相”行为、多功能等优点在催化研究领域以及烯烃环氧化领域中受到研究者们的广泛重视。CN106975522A开发了一种磷钼钨杂多酸催化剂,并催化以叔丁基过氧化氢为氧化剂烯烃环氧化反应,其中叔丁基过氧化氢污染环境且耗能较高。Heteropolyacids are oxygen-containing polyacid green catalysts composed of heteroatoms (such as P, Si, Fe, Co, etc.) and polyatoms (such as Mo, W, V, Nb, Ta, etc.). Due to the unique acidity, "quasi-liquid phase" behavior, and multifunctionality of heteropolyacids, they have been widely valued by researchers in the field of catalysis research and olefin epoxidation. CN106975522A developed a phosphorus-molybdenum-tungsten heteropolyacid catalyst, and catalyzed the epoxidation of olefins with tert-butyl hydroperoxide as the oxidant, wherein the tert-butyl hydroperoxide polluted the environment and consumed high energy.
本发明利用价廉易得的过渡金属铜取代的Keggin型磷钼杂多酸制备性能优异的烯烃环氧化催化剂PCuMo11@PC,该催化剂可利用氧气直接催化环辛烯和环十二烯,催化剂的制备过程简单,生产成本低廉且催化过程绿色环保,具有推广应用价值。The invention utilizes cheap and readily available transition metal copper-substituted Keggin-type phosphomolybdenum heteropolyacid to prepare an olefin epoxidation catalyst PCuMo 11 @PC with excellent performance, and the catalyst can utilize oxygen to directly catalyze cyclooctene and cyclododecene, The preparation process of the catalyst is simple, the production cost is low, and the catalytic process is green and environmentally friendly, and has popularization and application value.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种经济绿色,易于操作并高效催化以氧气为氧源的环辛烯和环十二烯环氧化反应的催化剂。该催化剂是以微介孔的共价有机骨架材料PC为载体,固载铜取代的磷钼酸而得到的多相催化材料。The purpose of the present invention is to provide an economical, green, easy-to-operate and highly efficient catalyst for the epoxidation reaction of cyclooctene and cyclododecene using oxygen as an oxygen source. The catalyst is a heterogeneous catalytic material obtained by using a micro-mesoporous covalent organic framework material PC as a carrier and immobilizing copper-substituted phosphomolybdic acid.
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种用于催化环辛烯和环十二烯环氧化反应的催化剂PCuMo11@PC制备方法通过如下步骤实现:A catalyst PCuMo 11 @PC preparation method for catalyzing the epoxidation reaction of cyclooctene and cyclododecene is achieved by the following steps:
(1)共价有机骨架材料PC的制备:将碳酸钾、三聚氰酰氯和无水哌嗪溶解到1,4-二氧六环溶剂中,混合物被恒温加热,反应结束后减压抽滤,滤饼经丙酮、四氢呋喃和二氯甲烷洗涤,真空干燥,得到黄色粉末PC;(1) Preparation of covalent organic framework material PC: Potassium carbonate, cyanuric chloride and anhydrous piperazine are dissolved in 1,4-dioxane solvent, the mixture is heated at a constant temperature, and the reaction is completed and filtered under reduced pressure , the filter cake was washed with acetone, tetrahydrofuran and dichloromethane, and dried in vacuo to obtain yellow powder PC;
(2)铜离子取代磷钼酸PCuMo11的制备:通过滴加饱和碳酸氢钠溶液调PMo12溶液pH为4-5,再与CuSO4·5H2O溶液混合,恒温搅拌,静置除去析出的硫酸钠杂质,收集PCuMo11晶体;(2) Preparation of copper ion-substituted phosphomolybdic acid PCuMo 11 : adjust the pH of PMo 12 solution to 4-5 by adding saturated sodium bicarbonate solution dropwise, then mix with CuSO 4 5H 2 O solution, stir at constant temperature, and let stand to remove precipitation Sodium sulfate impurity, collect PCuMo 11 crystal;
(3)催化剂PCuMo11@PC制备: 在均匀分散的PC水溶液中加PCuMo11水溶液,恒温加热搅拌、过滤、洗涤,真空干燥,得到新型复合材料PCuMo11@PC。(3) Preparation of catalyst PCuMo 11 @PC: Add PCuMo 11 aqueous solution to the uniformly dispersed PC aqueous solution, heat and stir at constant temperature, filter, wash, and vacuum dry to obtain a new composite material PCuMo 11 @PC.
优选的,在上述一种用于催化环辛烯和环十二烯环氧化反应的催化剂PCuMo11@PC制备方法,步骤(1)中碳酸钾、三聚氰酰氯和无水哌嗪的物质的量之比6:2:3,恒温搅拌温度100-130℃,反应时间24-72 h,进一步优选温度为110℃,反应时间48 h。Preferably, in the above-mentioned preparation method of a catalyst PCuMo 11 @PC for catalyzing the epoxidation reaction of cyclooctene and cyclododecene, the substances of potassium carbonate, cyanuric chloride and anhydrous piperazine in step (1) The ratio of the amount of the mixture is 6:2:3, the constant temperature stirring temperature is 100-130 °C, the reaction time is 24-72 h, and the more preferred temperature is 110 °C, and the reaction time is 48 h.
优选的,在上述一种用于催化环辛烯和环十二烯环氧化反应的催化剂PCuMo11@PC制备方法,步骤(2)中磷钼酸与CuSO4· 5H2O的物质的量比1:(0.5-3),恒温搅拌温度45-50℃,时间30-60min,进一步优选磷钼酸与CuSO4· 5H2O的物质的量比为1:3,恒温搅拌温度50℃,时间60min。Preferably, in the above-mentioned preparation method of a catalyst PCuMo 11 @PC for catalyzing the epoxidation reaction of cyclooctene and cyclododecene, the amount of phosphomolybdic acid and CuSO 4 · 5H 2 O in step (2) is Ratio 1:(0.5-3), constant temperature stirring temperature 45-50 ℃, time 30-60min, further preferably phosphomolybdic acid and CuSO 4.5H 2 O material ratio is 1:3, constant
上述技术方案的有益效果是:适量增加合成温度和温度有利于产物产率的增加,且CuSO4· 5H2O的比例增加能提高苯基环氧乙烷的产率。The beneficial effects of the above technical solutions are: an appropriate increase in synthesis temperature and temperature is beneficial to increase the product yield, and an increase in the ratio of CuSO 4 · 5H 2 O can improve the yield of phenyloxirane.
本发明还提供了上述铜离子取代的磷钼酸负载到共价有机骨架材料PC上的复合材料应用环辛烯和环十二烯环氧化反应,其步骤如下:The present invention also provides the epoxidation reaction of cyclooctene and cyclododecene in the composite material in which the above-mentioned copper ion-substituted phosphomolybdic acid is loaded on the covalent organic framework material PC, and the steps are as follows:
(1)向双颈瓶中加入催化剂、乙腈、异丁醛、烯烃,并通入10 mL/min的分子氧。烯烃为环辛烯和环十二烯;(1) Add catalyst, acetonitrile, isobutyraldehyde, and olefin into the double-necked flask, and introduce molecular oxygen at 10 mL/min. The olefins are cyclooctene and cyclododecene;
(2)反应温度为40℃-70℃,反应一段时间后,取出适量的反应混合物,滤膜过滤并进行气相色谱检测。(2) The reaction temperature is 40°C-70°C. After a period of reaction, an appropriate amount of the reaction mixture is taken out, filtered through a filter membrane, and detected by gas chromatography.
经由上述的方案可知,与现有技术相比,本发明公开提供了一种用于催化环辛烯和环十二烯环氧化反应的催化剂PCuMo11@PC复合材料的制备方法及其在环辛烯和环十二烯氧气环氧化反应中的应用,具有以下优势:As can be seen from the above scheme, compared with the prior art, the present invention discloses a preparation method of a catalyst PCuMo 11 @PC composite material for catalyzing the epoxidation reaction of cyclooctene and cyclododecene, and a method for preparing the same in a cyclooctene epoxidation reaction. The application in the oxygen epoxidation of octene and cyclododecene has the following advantages:
(1)在催化剂制备方面,制备的原料经济且易于获取,催化活性物质PCuMo11价廉易得,由于微介孔载体PC含氮量丰富,因此铜取代的磷钼酸活性物质负载较为牢固;(1) In terms of catalyst preparation, the raw materials prepared are economical and easy to obtain, and the catalytic active material PCuMo 11 is cheap and easy to obtain. Since the micro-mesoporous carrier PC is rich in nitrogen, the copper-substituted phosphomolybdic acid active material is loaded relatively firmly;
(2)在催化环辛烯和环十二烯环氧化反应方面,以价格低廉、绿色环保氧气为氧源,催化效果好,所制备的新型催化剂在环辛烯和环十二烯环氧化反应中催化性能均具有较高的反应活性和选择性。(2) In terms of catalyzing the epoxidation of cyclooctene and cyclododecene, low-cost, green and environmentally friendly oxygen is used as the oxygen source, and the catalytic effect is good. The prepared new catalyst is in cyclooctene and cyclododecene epoxy. The catalytic performance in the chemical reaction has high reactivity and selectivity.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the following briefly introduces the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only It is an embodiment of the present invention. For those of ordinary skill in the art, other drawings can also be obtained according to the provided drawings without creative work.
图1 附图为本发明PCuMo11@PC的红外光谱图。Fig. 1 is an infrared spectrum diagram of PCuMo 11 @PC of the present invention.
图2 附图为本发明PCuMo11、PC和PCuMo11@PC的XRD图。Figure 2 Figure 2 shows the XRD patterns of PCuMo 11 , PC and PCuMo 11 @PC of the present invention.
图3 附图为本发明(a)PC和(b)PCuMo11@PC的氮气吸附脱附曲线以及孔径分布图,相关数据在附表1中列出。Figure 3 Figure 3 shows the nitrogen adsorption and desorption curves and pore size distribution diagrams of (a) PC and (b) PCuMo 11 @PC of the present invention, and the relevant data are listed in attached table 1.
图4 附图为本发明PC和PCuMo11@PC的表面积、孔径和孔容。Figure 4 shows the surface area, pore diameter and pore volume of PC and PCuMo 11 @PC of the present invention.
图5 附图为本发明PCuMo11@PC催化环辛烯和环十二烯的评价。Figure 5 The accompanying drawing is the evaluation of PCuMo 11 @PC catalyzing cyclooctene and cyclododecene of the present invention.
具体实施方式Detailed ways
为了对本发明得到更清楚、更完整的描述,以下的实例仅是本发明的部分实例,通过以下实例做出的均等变化和修饰,皆属于本发明专利的范围。In order to obtain a clearer and more complete description of the present invention, the following examples are only partial examples of the present invention, and equivalent changes and modifications made by the following examples all belong to the scope of the patent of the present invention.
实施例1Example 1
向双颈瓶中加入20 mg PCuMo11@PC催化剂、10 mL乙腈、2 mmol 环辛烯和6 mmol异丁醛,通入10 mL/min氧气,60℃反应1 h时;从烧瓶中取出少量的溶液,经滤膜过滤进气相色谱分析,转化率98%,选择性>99%。20 mg of PCuMo 11 @PC catalyst, 10 mL of acetonitrile, 2 mmol of cyclooctene and 6 mmol of isobutyraldehyde were added to the double-necked flask, 10 mL/min of oxygen was introduced, and the reaction was performed at 60 °C for 1 h; a small amount was taken out from the flask The solution was filtered through a filter membrane and analyzed by gas chromatography, the conversion rate was 98%, and the selectivity was >99%.
实施例2Example 2
向双颈瓶中加入20 mg PCuMo11@PC催化剂、10 mL乙腈、2 mmol 环十二烯和6 mmol异丁醛,通入10 mL/min氧气,60℃反应1 h时;从烧瓶中取出少量的溶液,经滤膜过滤进气相色谱分析,转化率95%,选择性>99%。Add 20 mg PCuMo 11 @PC catalyst, 10 mL acetonitrile, 2 mmol cyclododecene and 6 mmol isobutyraldehyde to the double-necked flask, pass 10 mL/min oxygen, and react at 60 °C for 1 h; take out from the flask A small amount of solution was filtered through a membrane and analyzed by gas chromatography, the conversion rate was 95%, and the selectivity was >99%.
另外本发明还对PCuMo11@PC的原料和PCuMo11@PC催化剂进行了红外光谱测试、XRD及氮气吸附脱附曲线以及孔径分布,参见图1-3,图1为本发明PCuMo11@PC的红外光谱谱图,在催化剂PCuMo11@PC中,保持了载体PC的主要骨架结构;图2为本发明PCuMo11@PC的XRD谱图,催化剂PCuMo11@PC保持了载体PC的主要骨架结构;图3和表1为本发明PCuMo11@PC的氮气吸附脱附曲线以及孔径分布图,相比载体PC的表面积、孔径和孔容,催化剂PCuMo11@PC的表面积、孔径和孔容均减小,证明PCuMo11已经负载到载体PC上,同时而且PCuMo11与载体PC间均具有化学相互作用。In addition, in the present invention, the raw materials of PCuMo 11 @PC and the PCuMo 11 @PC catalyst were tested by infrared spectrum, XRD, nitrogen adsorption and desorption curves, and pore size distribution, as shown in Figs. Infrared spectrum, in the catalyst PCuMo 11 @PC, the main framework structure of the carrier PC is maintained; Figure 2 is the XRD pattern of the PCuMo 11 @PC of the present invention, the catalyst PCuMo 11 @PC maintains the main framework structure of the carrier PC; Figure 3 and Table 1 are the nitrogen adsorption and desorption curves and pore size distribution of PCuMo 11 @PC of the present invention. Compared with the surface area, pore size and pore volume of the support PC, the surface area, pore size and pore volume of the catalyst PCuMo 11@PC are all reduced, which proves that PCuMo 11 has been loaded on the carrier PC, and there is a chemical interaction between PCuMo 11 and the carrier PC.
以上所述,仅为本发明较好的具体实施方式,对本发明催化剂原料、各组分的配比以及制备方法等均在本发明申请保护和公开范围之内。如果通过实例做出等同替换或改变,都应涵盖在本发明的保护范围之内。The above descriptions are only preferred specific embodiments of the present invention, and the catalyst raw materials, the proportions of components, and the preparation methods of the present invention are all within the scope of protection and disclosure of the present invention. If equivalent replacements or changes are made through examples, they should all be included within the protection scope of the present invention.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010822716.5A CN111974455A (en) | 2020-08-17 | 2020-08-17 | Catalyst PCuMo for catalyzing epoxidation reaction of cyclooctene and cyclododecene11@PC |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010822716.5A CN111974455A (en) | 2020-08-17 | 2020-08-17 | Catalyst PCuMo for catalyzing epoxidation reaction of cyclooctene and cyclododecene11@PC |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111974455A true CN111974455A (en) | 2020-11-24 |
Family
ID=73433988
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010822716.5A Pending CN111974455A (en) | 2020-08-17 | 2020-08-17 | Catalyst PCuMo for catalyzing epoxidation reaction of cyclooctene and cyclododecene11@PC |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111974455A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113731454A (en) * | 2021-09-22 | 2021-12-03 | 吉林化工学院 | Preparation and catalytic application of nitrogen-doped carbon composite material loaded with heteropoly acid |
| CN113751068A (en) * | 2021-09-22 | 2021-12-07 | 吉林化工学院 | Supported polyoxometallate material for preparing aniline by nitrobenzene hydrogenation |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES316484A1 (en) * | 1964-08-13 | 1965-11-16 | Halcon International Inc | Procedure for the preparation of olefin oxides. (Machine-translation by Google Translate, not legally binding) |
| JP2008179644A (en) * | 2008-02-05 | 2008-08-07 | Daicel Chem Ind Ltd | Method for producing epoxy compound |
| CN107362829A (en) * | 2016-05-13 | 2017-11-21 | 中国科学院大连化学物理研究所 | Covalent organic frame bimetallic catalyst of support type and its preparation method and application |
| CN109317207A (en) * | 2018-11-02 | 2019-02-12 | 吉林化工学院 | A kind of high-efficiency recyclable olefin epoxidation catalyst and its preparation method and application |
| CN109317206A (en) * | 2018-10-15 | 2019-02-12 | 吉林化工学院 | A kind of styrene epoxidation catalyst and its preparation method and application |
-
2020
- 2020-08-17 CN CN202010822716.5A patent/CN111974455A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES316484A1 (en) * | 1964-08-13 | 1965-11-16 | Halcon International Inc | Procedure for the preparation of olefin oxides. (Machine-translation by Google Translate, not legally binding) |
| JP2008179644A (en) * | 2008-02-05 | 2008-08-07 | Daicel Chem Ind Ltd | Method for producing epoxy compound |
| CN107362829A (en) * | 2016-05-13 | 2017-11-21 | 中国科学院大连化学物理研究所 | Covalent organic frame bimetallic catalyst of support type and its preparation method and application |
| CN109317206A (en) * | 2018-10-15 | 2019-02-12 | 吉林化工学院 | A kind of styrene epoxidation catalyst and its preparation method and application |
| CN109317207A (en) * | 2018-11-02 | 2019-02-12 | 吉林化工学院 | A kind of high-efficiency recyclable olefin epoxidation catalyst and its preparation method and application |
Non-Patent Citations (4)
| Title |
|---|
| SONG XIAOJING 等: "Epoxidation of olefins with oxygen/isobutyraldehyde over transition-metal-substituted phosphomolybdic acid on SBA-15", 《CATALYSIS TODAY》 * |
| XIWEI HU 等: "Two-dimensional covalent organic frameworks as self-template derived nitrogen-doped carbon nanosheets for eco-friendly metal-free catalysis", 《APPLIED CATALYSIS B: ENVIRONMENTAL》 * |
| 王静: "咪唑功能化有机—无机杂化材料固载磷钼杂多化合物催化剂的制备及烯烃环氧化性能", 《中国博士学位论文全文数据库工程科技Ⅰ辑》 * |
| 高文秀 等: "分子氧环氧化烯烃多相催化剂PCuMo11/富氮类共价有机骨架材料的制备及应用", 《复合材料学》 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113731454A (en) * | 2021-09-22 | 2021-12-03 | 吉林化工学院 | Preparation and catalytic application of nitrogen-doped carbon composite material loaded with heteropoly acid |
| CN113751068A (en) * | 2021-09-22 | 2021-12-07 | 吉林化工学院 | Supported polyoxometallate material for preparing aniline by nitrobenzene hydrogenation |
| CN113731454B (en) * | 2021-09-22 | 2023-05-05 | 吉林化工学院 | Preparation and catalytic application of heteropolyacid-loaded nitrogen-doped carbon composite material |
| CN113751068B (en) * | 2021-09-22 | 2024-05-14 | 吉林化工学院 | Supported polyoxometallate material for preparing aniline by nitrobenzene hydrogenation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Liu et al. | Metal-free imidazolium hydrogen carbonate ionic liquids as bifunctional catalysts for the one-pot synthesis of cyclic carbonates from olefins and CO 2 | |
| Xiang et al. | Enantioselective epoxidation of olefins catalyzed by Mn (salen)/MCM-41 synthesized with a new anchoring method | |
| CN111905822B (en) | Preparation method of polyoxometallate/covalent organic framework material and application of polyoxometallate/covalent organic framework material in styrene air epoxidation reaction | |
| CN111974455A (en) | Catalyst PCuMo for catalyzing epoxidation reaction of cyclooctene and cyclododecene11@PC | |
| CN109772459B (en) | Chiral polyacid-based metal organic framework material and preparation method and application thereof | |
| CN112280052B (en) | Hierarchical pore ZIF-8 material and preparation method and application thereof | |
| CN112521263A (en) | CO catalyzed by Ir complex supported by MOF2Method for preparing formate/formic acid by hydrogenation reduction | |
| CN107188849B (en) | Mesoporous ionic liquid heteropoly acid salt catalyst for benzene hydroxylation reaction, preparation method and application thereof | |
| JP7629655B2 (en) | Pyridine-pyrrole-ruthenium complexes, methods for their preparation, and their application as catalysts for electrocatalysis of ammonia oxidation to produce hydrazine | |
| CN109317207B (en) | A kind of high-efficiency recyclable olefin epoxidation catalyst and its preparation method and application | |
| Sun et al. | Sulfonic-functionalized MIL-101 as bifunctional catalyst for cyclohexene oxidation | |
| CN109317206B (en) | A kind of styrene epoxidation catalyst and its preparation method and application | |
| Wang et al. | A recyclable cobalt (iii)–ammonia complex catalyst for catalytic epoxidation of olefins with air as the oxidant | |
| CN109160926B (en) | Preparation and application of iron-iron hydrogenase simulant and carbon nano tube composite simulant thereof | |
| CN105749973A (en) | Immobilization method for assembling metal complex in meso-porous material | |
| CN103554059A (en) | Method for synthetizing 1,2-cyclopentene oxide by novel titanium silicalite (HTS)-1/ligand catalytic cyclopentene | |
| CN1401640A (en) | Process for preparing epoxy cyclohexane by catalytic cyclooxidation of cyclohexene | |
| CN109499609B (en) | A kind of SBA-15 immobilized 2-azaadamantane nitroxide radical catalyst and its preparation and application | |
| CN113372218A (en) | Preparation method of methyl methacrylate | |
| CN103121979A (en) | Method for realizing epoxidation of olefins and air through catalysis of cobalt-contained catalyst under assistance of ultrasonic waves | |
| KR101170486B1 (en) | Production method of mesoporous organic polymer catalyst, mesoporous organic polymer catalyst produced using the method, and process for epoxidation of olefins using the catalyst | |
| Hu et al. | Efficient and convenient transformation of CO2 into α‑alkylidene cyclic carbonates over reusable and heterogeneous Cu-MCM-41 supported ionic liquid catalyst | |
| CN111217769B (en) | A kind of method utilizing nano-alumina to catalyze olefin epoxidation to synthesize epoxy compound | |
| CN108586344A (en) | Hydroxy functionalized pyrazolium ion liquid and the method for utilizing its catalytically synthesizing cyclic carbonate ester | |
| CN116603555B (en) | A sulfur- and nitrogen-co-doped carbon catalyst, its preparation method and application |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20201124 |
|
| WD01 | Invention patent application deemed withdrawn after publication |