CN112844486B - For CO 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 Composite material and method for producing the same - Google Patents
For CO 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 Composite material and method for producing the same Download PDFInfo
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- 239000013154 zeolitic imidazolate framework-8 Substances 0.000 title claims abstract description 64
- MFLKDEMTKSVIBK-UHFFFAOYSA-N zinc;2-methylimidazol-3-ide Chemical compound [Zn+2].CC1=NC=C[N-]1.CC1=NC=C[N-]1 MFLKDEMTKSVIBK-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 239000002131 composite material Substances 0.000 title claims abstract description 56
- 239000003054 catalyst Substances 0.000 title claims abstract description 28
- 238000004519 manufacturing process Methods 0.000 title description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 132
- 239000000843 powder Substances 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 40
- 238000003756 stirring Methods 0.000 claims abstract description 29
- 238000002360 preparation method Methods 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 239000006185 dispersion Substances 0.000 claims abstract description 22
- 238000006352 cycloaddition reaction Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 12
- 150000003751 zinc Chemical class 0.000 claims abstract description 8
- LXBGSDVWAMZHDD-UHFFFAOYSA-N 2-methyl-1h-imidazole Chemical compound CC1=NC=CN1 LXBGSDVWAMZHDD-UHFFFAOYSA-N 0.000 claims abstract description 5
- 238000001035 drying Methods 0.000 claims description 27
- 239000011259 mixed solution Substances 0.000 claims description 20
- 239000011701 zinc Substances 0.000 claims description 20
- 238000005406 washing Methods 0.000 claims description 19
- 238000001354 calcination Methods 0.000 claims description 14
- 239000000243 solution Substances 0.000 claims description 14
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 12
- 239000004202 carbamide Substances 0.000 claims description 12
- 229910001220 stainless steel Inorganic materials 0.000 claims description 11
- 239000010935 stainless steel Substances 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000008367 deionised water Substances 0.000 claims description 10
- 229910021641 deionized water Inorganic materials 0.000 claims description 10
- 239000012295 chemical reaction liquid Substances 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 9
- 239000002086 nanomaterial Substances 0.000 claims description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- 239000002149 hierarchical pore Substances 0.000 claims description 4
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- -1 polytetrafluoroethylene Polymers 0.000 claims description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- XIOUDVJTOYVRTB-UHFFFAOYSA-N 1-(1-adamantyl)-3-aminothiourea Chemical compound C1C(C2)CC3CC2CC1(NC(=S)NN)C3 XIOUDVJTOYVRTB-UHFFFAOYSA-N 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 2
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- 238000005119 centrifugation Methods 0.000 claims description 2
- 238000002425 crystallisation Methods 0.000 claims description 2
- 230000008025 crystallization Effects 0.000 claims description 2
- YZYKBQUWMPUVEN-UHFFFAOYSA-N zafuleptine Chemical compound OC(=O)CCCCCC(C(C)C)NCC1=CC=C(F)C=C1 YZYKBQUWMPUVEN-UHFFFAOYSA-N 0.000 claims description 2
- 239000011592 zinc chloride Substances 0.000 claims description 2
- 235000005074 zinc chloride Nutrition 0.000 claims description 2
- 150000002118 epoxides Chemical class 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 21
- 230000003197 catalytic effect Effects 0.000 abstract description 14
- 238000002156 mixing Methods 0.000 abstract description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 10
- 239000002244 precipitate Substances 0.000 description 9
- 238000010335 hydrothermal treatment Methods 0.000 description 8
- 150000005676 cyclic carbonates Chemical class 0.000 description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000002441 X-ray diffraction Methods 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 4
- AWMVMTVKBNGEAK-UHFFFAOYSA-N Styrene oxide Chemical compound C1OC1C1=CC=CC=C1 AWMVMTVKBNGEAK-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000012512 characterization method Methods 0.000 description 3
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- 239000012621 metal-organic framework Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000002841 Lewis acid Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 2
- 239000002638 heterogeneous catalyst Substances 0.000 description 2
- 150000007517 lewis acids Chemical class 0.000 description 2
- 238000003760 magnetic stirring Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 150000002924 oxiranes Chemical class 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000004451 qualitative analysis Methods 0.000 description 2
- 238000004445 quantitative analysis Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000005863 Friedel-Crafts acylation reaction Methods 0.000 description 1
- 238000006000 Knoevenagel condensation reaction Methods 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000012377 drug delivery Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical group 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- JBFYUZGYRGXSFL-UHFFFAOYSA-N imidazolide Chemical compound C1=C[N-]C=N1 JBFYUZGYRGXSFL-UHFFFAOYSA-N 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007783 nanoporous material Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 229910001428 transition metal ion Inorganic materials 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1805—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
- B01J31/181—Cyclic ligands, including e.g. non-condensed polycyclic ligands, comprising at least one complexing nitrogen atom as ring member, e.g. pyridine
- B01J31/1815—Cyclic ligands, including e.g. non-condensed polycyclic ligands, comprising at least one complexing nitrogen atom as ring member, e.g. pyridine with more than one complexing nitrogen atom, e.g. bipyridyl, 2-aminopyridine
-
- 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
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
- C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
- C07D317/10—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings
- C07D317/32—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D317/34—Oxygen atoms
- C07D317/36—Alkylene carbonates; Substituted alkylene carbonates
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/20—Complexes comprising metals of Group II (IIA or IIB) as the central metal
- B01J2531/26—Zinc
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- Chemical & Material Sciences (AREA)
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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
Abstract
The invention discloses a catalyst for catalyzing CO 2 ZIF-8/CeO for cycloaddition reaction 2 A composite material and a method for preparing the same. The preparation method comprises the following steps: 1) Preparation of spindle-shaped CeO 2 (ii) a 2) Preparation of ZIF-8/CeO 2 The composite material comprises the following components: adding CeO 2 Dispersing the powder in a methanol solution, adding inorganic zinc salt, and stirring at room temperature to obtain a dispersion liquid; mixing the dispersion liquid with a methanol solution of 2-methylimidazole, and performing post-treatment after the reaction is finished to obtain ZIF-8/CeO 2 A composite material. ZIF-8/CeO obtained by the preparation method 2 The material has high specific surface area and porosity and catalyzes CO 2 The yield of the product of the cycloaddition reaction can reach more than 90 percent, the catalytic activity is not obviously reduced when the catalyst is used for the fifth time, the reusability of the catalyst is obviously higher than that of a ZIF-8 material, and the catalyst is a catalytic material with high stability.
Description
Technical Field
The invention belongs to the technical field of metal organic framework materials, and particularly relates to a catalyst for CO 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 Composite materials and methods for making the same.
Background
Zeolite-like imidazolate framework materials (ZIFs) are a common class of Metal Organic Frameworks (MOFs), are formed by coordination of transition metal ions and imidazole-like organic compounds, and have a zeolite framework structure. ZIFs not only have the advantages of large specific surface area, high porosity, high crystallinity and the like, but also have the characteristics of adjustable pore diameter and structural and functional diversity. Therefore, the ZIFs material has huge development potential in the fields of adsorption, separation, catalysis, drug delivery and the like, and is a research hotspot of the current novel nano porous material.
The ZIFs have Lewis acid sites derived from metal ions and basic sites derived from nitrogen on the skeleton, and thus can be used as the materialAs heterogeneous catalysts for various types of catalytic reactions, e.g. CO 2 Cycloaddition reaction, knoevenagel condensation reaction, friedel-Crafts acylation reaction, ester exchange reaction of vegetable oil and the like. CO 2 2 Conversion of cycloaddition to cyclic carbonate is CO 2 One of the important methods for chemical fixation has important significance for reducing carbon emission and reasonably utilizing carbon resources. ZIFs are useful for catalyzing CO 2 The conversion to cyclic carbonates is due to the catalytic CO of Lewis acid sites in the backbone 2 Reaction with epoxide to produce propylene carbonate and other precursors of polycarbonate. In addition, ZIFs have very high CO due to the basic sites of their imidazole ligands 2 Adsorption capacity and therefore ability to adsorb CO 2 The reaction to convert to cyclic carbonates shows higher CO 2 Absorption rate. And the polar nature of ZIFs favors CO 2 Binding and preferential adsorption of polar carbon-oxygen bonds.
But are currently mostly used for CO 2 ZIFs catalysts for cycloaddition reaction still have the problems of low catalytic activity or selectivity, low recycling capability and the like. In addition, the thermal stability of ZIFs materials has certain limitations and is easily decomposed in strong acid and strong base environments, which greatly limits their applications in the field of catalysis. Therefore, heterogeneous catalyst systems with high efficiency and high stability were developed for chemically fixing CO under mild conditions 2 It remains challenging.
Disclosure of Invention
The invention aims to solve the technical problem of providing ZIF-8/CeO aiming at the defects in the prior art 2 A micro-nano structure material and a preparation method thereof. The ZIF-8/CeO 2 The material has high specific surface area and porosity, high stability, and can catalyze CO 2 The cycloaddition reaction has good catalytic activity and reusability.
In order to solve the technical problem, the invention provides a method for CO 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 Composite material, ZIF-8/CeO 2 CeO in composite material 2 Is in a spindle shape, and ZIF-8 particles are uniformly loaded on CeO 2 An outer surface of (a); ZIF-8/CeO 2 The composite material is of a micro-nano structure and has a hierarchical pore structure; wherein the ZIF-8 particles have a microporous structure of CeO 2 Has a mesoporous structure.
Wherein the particle size of the ZIF-8 particles is 200-300nm and is uniform; in which spindle-shaped CeO 2 The diameter of (A) is 1-2um, and the length of (B) is 8-12um.
The invention provides a method for catalyzing CO 2 ZIF-8/CeO for cycloaddition reaction 2 The preparation method of the micro-nano structure material comprises the following steps:
1) Preparation of spindle-shaped CeO 2 : ce (NO) 3 ) 3 ·6H 2 Dissolving O and urea in deionized water, and stirring for 30-60 min to form homogeneous mixed solution; then transferring the mixed solution into a polytetrafluoroethylene lining of a stainless steel reaction kettle, and crystallizing under a hydrothermal condition; self-heating and cooling the reaction kettle to room temperature, and then centrifuging, ultrasonically washing and drying to obtain white powder; calcining the white powder in a muffle furnace at a certain temperature to obtain light yellow powder, namely CeO 2 。
2) Preparation of ZIF-8/CeO 2 The composite material is as follows: subjecting the CeO obtained in the step 1) 2 Dispersing the powder in a certain amount of methanol solution, then adding inorganic zinc salt, and stirring at room temperature for 1-2 h to obtain dispersion liquid; slowly adding the methanol solution of 2-methylimidazole (2-Mim) into the dispersion liquid, continuously stirring for 5-90 min, centrifuging, ultrasonically washing and drying the reaction liquid after the reaction is finished to obtain ZIF-8/CeO 2 A composite material.
Further, ce (NO) in step 1) 3 ) 3 ·6H 2 The concentrations of the O and urea aqueous solutions are respectively 30mmol/L and 80mmol/L, the crystallization temperature is 120 ℃, and the time is 8h;
preferably, the drying temperature in the step 1) is 60-80 ℃, and preferably 70 ℃; the drying time is 12-36 h, preferably 24h.
Further, the calcining temperature in the step 1) is 600 ℃, and the calcining time is 5h.
Further, ceO in the dispersion liquid in the step 2) 2 The concentration of (2) is 1-2 wt%, and the dosage of methanol is 2-10 mL.
Further, the inorganic zinc salt in the step 2) is zinc nitrate hexahydrate (Zn (NO) 3 ) 2 ·6H 2 O), zinc acetate dihydrate (Zn (OAc) 2 ·2H 2 O) or zinc chloride.
Further, the inorganic zinc salt and CeO in the step 2) 2 In a molar ratio of (0.1-3): 1; the molar ratio of the inorganic zinc salt to the 2-Mim is 1: (4-8); the dosage of the methanol in the methanol solution of the 2-methylimidazole is 2-10 mL.
Preferably, the drying temperature in the step 2) is 80-110 ℃, and preferably 110 ℃; the drying time is 12h to 18h, preferably 12h.
The invention also protects the high-stability catalyst ZIF-8/CeO prepared by the method 2 A composite material.
The invention also protects the high-stability catalyst ZIF-8/CeO 2 Use of composite materials for CO 2 Use of chemical fixation in the cycloaddition reaction of carbon dioxide and an epoxide. .
The obtained ZIF-8/CeO 2 The composite material was tested for catalytic performance as follows:
mixing a certain amount of ZIF-8/CeO 2 Catalyst and styrene oxide are put into a reaction kettle; using 0.2MPa CO for the reaction kettle 2 Purging 5 times to remove air, then adding 0.7MPa CO in one portion 2 Filling into a reaction kettle; the mixture reacts under the magnetic stirring of 300 r/min; after the reaction was complete, the reactor was cooled to ambient temperature and excess CO was vented 2 (ii) a Centrifuging the residual liquid and performing qualitative and quantitative analysis by GC-MS; the catalyst was washed three times with ethanol and dried.
Wherein the liquid-solid ratio of the catalyst to the styrene oxide is (0.1-1.5): 20.5 (g: mL), preferably 1:20.5 (g: mL).
Wherein the reaction temperature is 80-140 ℃, and preferably 120 ℃; the reaction time is 4h to 10h, preferably 6h.
Compared with the prior art, the invention has the beneficial effects that:
1. the invention synthesizes ZIF-8/CeO with a micro-nano structure by adopting a simpler method 2 The ZIF-8/CeO composite material is prepared by controlling the raw material ratio and the synthesis conditions 2 The composite material is uniformly and stably synthesized;
2. ZIF-8/CeO synthesized by the invention 2 The composite material has higher specific surface area and porosity and a hierarchical pore structure, so that the stability of the ZIF-8 is improved;
3、ZIF-8/CeO 2 composite material catalysis of CO 2 The cyclic carbonate is prepared by cycloaddition reaction, the yield can reach more than 90 percent, the catalytic activity is not obviously reduced when the cyclic carbonate is repeatedly used for the fifth time, the apparent structure is not obviously changed, the repeated use performance of the cyclic carbonate is obviously higher than that of a ZIF-8 material, and the cyclic carbonate is a catalytic material with high stability.
Drawings
FIG. 1 is a scanning electron micrograph of materials prepared in examples 1 to 9.
FIG. 2 is an X-ray diffraction pattern of the materials prepared in examples 1, 4 and 9.
FIG. 3 is a thermogravimetric plot of the materials prepared in examples 1, 4 and 9.
Fig. 4 shows the catalytic performance and the results of recycling of the catalysts prepared in examples 1, 4 and 9.
Detailed Description
The foregoing aspects of the present invention are described in further detail below by way of examples, but it should not be construed that the scope of the subject matter of the present invention is limited to the following examples, and that all the technologies realized based on the above aspects of the present invention are within the scope of the present invention.
The experimental procedures used in the following examples are conventional procedures unless otherwise specified, and reagents, methods and equipment used therein are conventional in the art unless otherwise specified.
1. For CO 2 Synthesis of catalytic materials for cycloaddition reactions
Example 1
Spindle shaped CeO 2 Preparation method ofThe method comprises the following steps:
(1) 1.04g Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.38g of urea in 80mL of deionized water, and stirring for 60min at room temperature to form a homogeneous mixed solution;
(2) Transferring the mixed solution into a polytetrafluoroethylene lining of a 100mL stainless steel reaction kettle, placing the stainless steel reaction kettle in an oven, and performing hydrothermal treatment for 8 hours at 120 ℃;
(3) Cooling the reaction kettle to room temperature by self-heating, taking out the lower-layer precipitate, centrifuging, ultrasonically washing with water and ethanol for several times, and then drying in an oven at 70 ℃ for 24 hours to obtain white powder;
(4) Placing the white powder in a muffle furnace, calcining for 5 hours at 600 ℃ to obtain light yellow powder, namely spindle-shaped CeO 2 。
CeO prepared in example 1 2 The scanning electron micrograph of (A) is shown in figure 1, the X-ray diffraction micrograph is shown in figure 2, the thermogravimetric curve is shown in figure 3, and the structural characterization test data is shown in table 1.
Example 2
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1: 10 2 Composite material
(1) 1.0479g of Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.3825g of urea in 80mL of deionized water, and stirring at room temperature for 60min to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, and calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.1034g of the obtained CeO was taken 2 The powder was dispersed in 10mL of methanol, followed by the addition of 0.0223g of Zn (NO) 3 ) 2 ·6H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.0245g of 2-Mim into 10mL of methanol, slowly adding the methanol solution of 2-Mim into the dispersion liquid, continuously stirring for 1h, centrifuging the reaction liquid after the reaction is finished, ultrasonically washing and drying to obtain faint yellow powder ZIF-8/CeO 2 A composite material.
EXAMPLE 2 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in FIG. 1.
Example 3
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1:4 2 Composite material
(1) 1.0476g of Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.3829g of urea in 80mL of deionized water, and stirring at room temperature for 60min to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, and calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.1025g of the obtained CeO was taken 2 The powder was dispersed in 10mL of methanol, followed by the addition of 0.0516g of Zn (NO) 3 ) 2 ·6H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.0572g of 2-Mim in 10mL of methanol, slowly adding the methanol solution of 2-Mim into the dispersion liquid, continuously stirring for 1h, centrifuging, ultrasonically washing and drying the reaction liquid after the reaction is finished to obtain faint yellow powder ZIF-8/CeO 2 A composite material.
Example 3 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in FIG. 1.
Example 4
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1 2 Composite material
(1) 1.0465g of Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.3834g of urea in 80mL of deionized water, and stirring for 60min at room temperature to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.1054g of the obtained CeO was taken 2 The powder was dispersed in 10mL of methanol,followed by the addition of 0.1088g Zn (NO) 3 ) 2 ·6H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.1200g of 2-Mim into 10mL of methanol, slowly adding the methanol solution of 2-Mim into the dispersion liquid, continuously stirring for 1h, centrifuging, ultrasonically washing and drying the reaction liquid after the reaction is finished to obtain faint yellow powder ZIF-8/CeO 2 A composite material.
EXAMPLE 4 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in figure 1, the X-ray diffraction map is shown in figure 2, the thermogravimetric curve is shown in figure 3, and the structural characterization test data is shown in table 1.
Example 5
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1 2 Composite material
(1) 1.0436g of Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.3843g of urea in 80mL of deionized water, and stirring at room temperature for 60min to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.1001g of the obtained CeO was taken 2 The powder was dispersed in 10mL of methanol, followed by the addition of 0.2040g Zn (NO) 3 ) 2 ·6H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.2289g of 2-Mim in 10mL of methanol, slowly adding the methanol solution of 2-Mim into the dispersion liquid, continuously stirring for 1h, centrifuging the reaction liquid after the reaction is finished, ultrasonically washing and drying to obtain a light yellow powder ZIF-8/CeO 2 A composite material.
Example 5 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in FIG. 1.
Example 6
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1 2 Composite material
(1) 1 is added.0447g Ce(NO 3 ) 3 ·6H 2 Dissolving O and 0.3831g of urea in 80mL of deionized water, and stirring for 60min at room temperature to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, and calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.0876g of the obtained CeO was taken 2 The powder was dispersed in 10mL of methanol, followed by the addition of 0.3719g of Zn (OAc) 2 ·2H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.5562g of 2-Mim in 10mL of methanol, slowly adding the methanol solution of 2-Mim into the dispersion liquid, continuously stirring for 1h, centrifuging the reaction liquid after the reaction is finished, ultrasonically washing and drying to obtain a light yellow powder ZIF-8/CeO 2 A composite material.
Example 6 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in FIG. 1.
Example 7
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1 2 Composite material
(1) 1.0420g of Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.3834g of urea in 80mL of deionized water, and stirring at room temperature for 60min to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, and calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.1004g of the obtained CeO was taken 2 The powder was dispersed in 10mL of methanol, followed by the addition of 0.0512g of Zn (NO) 3 ) 2 ·6H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.0568g of 2-Mim in 10mL of methanol, slowly adding the 2-Mim methanol solution into the dispersion liquid, continuously stirring for 20min, centrifuging the reaction liquid after the reaction is finished, ultrasonically washing and drying to obtain light yellow powder ZIF-8/CeO 2 A composite material.
Example 7 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in FIG. 1.
Example 8
According to the mol ratio of Zn (NO) 3 ) 2 ·6H 2 O:2-Mim:CeO 2 Methanol =1:4 2 Composite material
(1) 1.0429g Ce (NO) 3 ) 3 ·6H 2 Dissolving O and 0.3853g of urea in 80mL of deionized water, and stirring at room temperature for 60min to form a homogeneous mixed solution; then transferring the mixed solution into a 100mL stainless steel reaction kettle, and carrying out hydrothermal treatment at 120 ℃ for 8h; taking out the lower layer precipitate, centrifuging, washing and drying for 24h to obtain white powder, and calcining at 600 deg.C for 5h to obtain yellowish CeO 2 And (3) powder.
(2) 0.1013g of the resulting CeO was taken 2 The powder was dispersed in 10mL of methanol, followed by the addition of 0.0524g of Zn (NO) 3 ) 2 ·6H 2 O, stirring for 1 hour at room temperature to obtain a dispersion liquid; dissolving 0.0585g of 2-Mim in 10mL of methanol, slowly adding the 2-Mim methanol solution into the dispersion liquid, continuously stirring for 90min, centrifuging the reaction liquid after the reaction is finished, ultrasonically washing and drying to obtain faint yellow powder ZIF-8/CeO 2 A composite material.
Example 8 preparation of ZIF-8/CeO 2 The scanning electron micrograph of the composite material is shown in FIG. 1.
Example 9
Synthesis of ZIF-8 material, comprising the steps of:
4.13g of Zn (NO) are added separately 3 ) 2 ·6H 2 O and 4.67g of 2-Mim are added to 200mL of methanol and stirred until completely dissolved. Zn (NO) 3 ) 2 ·6H 2 The molar ratio of O to 2-Mim to methanol is 1. Then, the two clear solutions were mixed and stirred at room temperature for 1h. The white precipitate obtained was collected by centrifugation and washed three times with methanol. Finally, the sample was dried at 70 ℃ for 24 hours to obtain ZIF-8 as a white powder.
ZIF-8/CeO prepared in example 9 2 The scanning electron micrograph of the composite material is shown in figure 1, the X-ray diffraction diagram is shown in figure 2, and the thermogravimetric curve is shown in figure 3As shown, the structural characterization test data is shown in table 1.
2. The materials prepared in examples 1, 4 and 9 were evaluated for their catalytic performance by the following method:
0.10g of catalyst and 18mmol of styrene oxide are put into a reaction kettle; using 0.2MPa CO for the reaction kettle 2 Purging 5 times to remove air, then 0.7MPa CO in one portion 2 Filling into a reaction kettle; the mixture is reacted for 6 hours at 120 ℃ under the magnetic stirring of 300 r/min; after the reaction was complete, the reactor was cooled to ambient temperature and excess CO was vented 2 (ii) a 0.1mL of toluene and 6mL of acetone were added to the reaction vessel, and the liquid in the reaction vessel was washed into a centrifuge tube, centrifuged, and the supernatant was removed, followed by qualitative and quantitative analysis by GC-MS, and the results are shown in Table 1. The catalyst was washed with ethanol three times, dried and reused, and the catalytic results are shown in fig. 4.
Table 1 performance test data for materials prepared in examples 1, 4 and 9
As can be seen from Table 1, the ZIF-8/CeO of the present invention 2 The composite material has large specific surface area and porosity, and has a hierarchical pore structure for CO 2 The cycloaddition reaction has higher catalytic activity, and the product yield can reach more than 90 percent. FIG. 4 shows the results of catalyst reuse, and it can be seen that ZIF-8/CeO 2 The cycle performance of the composite material is obviously higher than that of a ZIF-8 material, and the composite material is a catalytic material with high stability.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention in any way, and any simple modifications, equivalents and improvements made by those skilled in the art without departing from the technical scope of the present invention are all within the scope of the present invention.
Claims (9)
1. Is used forCO 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 A composite material characterized by: ZIF-8/CeO 2 CeO in composite material 2 Is in a spindle shape, and ZIF-8 particles are uniformly loaded on CeO 2 An outer surface of (a); ZIF-8/CeO 2 The composite material is of a micro-nano structure and has a hierarchical pore structure; wherein the ZIF-8 particles have a microporous structure of CeO 2 Then has a mesoporous structure; wherein the particle size of the ZIF-8 particles is 200-300nm, and the particle size is uniform; in which CeO is in the form of a spindle 2 The diameter of (2) is 1-2um, and the length is 8-12um.
2. Use according to claim 1 for CO 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: the method comprises the following steps:
1) Preparation of spindle-shaped CeO 2 : adding Ce (NO) 3 ) 3 ·6H 2 Dissolving O and urea in deionized water, and stirring for 30-60min to form a homogeneous mixed solution; then transferring the mixed solution into a polytetrafluoroethylene lining of a stainless steel reaction kettle, and crystallizing under a hydrothermal condition; cooling the reaction kettle to room temperature by self-heating, and then performing centrifugation, ultrasonic washing and drying treatment to obtain white powder; calcining the white powder in a muffle furnace at a certain temperature to obtain light yellow powder which is CeO 2 ;
2) Preparation of ZIF-8/CeO 2 The composite material comprises the following components: subjecting the CeO obtained in the step 1) 2 Dispersing the powder in a certain amount of methanol solution, then adding inorganic zinc salt, and stirring at room temperature for 1 to 2h to obtain a dispersion liquid; slowly adding the methanol solution of the 2-methylimidazole into the dispersion liquid, continuously stirring for 5-90min, centrifuging the reaction liquid after the reaction is finished, ultrasonically washing and drying to obtain ZIF-8/CeO 2 A composite material.
3. Use for CO according to claim 2 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: ce (NO) in step 1) 3 ) 3 ·6H 2 The concentrations of the aqueous solutions of O and urea were 30mm, respectivelyol/L and 80mmol/L, the crystallization temperature is 120 ℃, and the time is 8h.
4. Use for CO according to claim 2 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: the drying temperature in the step 1) is 60 to 80 ℃; drying time is 12h to 36h; the calcining temperature in the step 1) is 600 ℃, and the calcining time is 5h.
5. Use for CO according to claim 2 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: ceO in the dispersion liquid in the step 2) 2 The concentration of the methanol is 1 to 2wt percent, and the dosage of the methanol is 2 to 10mL.
6. Use for CO according to claim 2 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: the inorganic zinc salt in the step 2) is zinc nitrate hexahydrate Zn (NO) 3 ) 2 •6H 2 O, zinc acetate dihydrate Zn (OAc) 2 •2H 2 At least one of O or zinc chloride.
7. Use for CO according to claim 2 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: the inorganic zinc salt and CeO in the step 2) 2 The molar ratio of (1) to (3) is: 1; the dosage of methanol in the methanol solution of the 2-methylimidazole is 2-10mL.
8. Use for CO according to claim 2 2 Chemically fixed high-stability catalyst ZIF-8/CeO 2 The preparation method of the composite material is characterized by comprising the following steps: the drying temperature in the step 2) is 80-110 ℃; the drying time is 12h to 18h.
9. The high stability catalyst as claimed in any one of claims 1 and 2ZIF-8/CeO 2 Composite material in CO 2 Use in chemical fixation, characterized in that: used in the cycloaddition reaction of carbon dioxide and epoxide.
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