CN111450894B - A Ce-based organometallic complex catalytic material and its preparation and application - Google Patents
A Ce-based organometallic complex catalytic material and its preparation and application Download PDFInfo
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- 230000003197 catalytic effect Effects 0.000 title claims abstract description 26
- 239000000463 material Substances 0.000 title claims abstract description 15
- 238000002360 preparation method Methods 0.000 title abstract description 6
- 125000002524 organometallic group Chemical group 0.000 title abstract description 3
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims abstract description 41
- 229910052751 metal Inorganic materials 0.000 claims abstract description 32
- 239000002184 metal Substances 0.000 claims abstract description 32
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 239000013078 crystal Substances 0.000 claims abstract description 8
- -1 cerium ions Chemical class 0.000 claims abstract description 3
- 238000004729 solvothermal method Methods 0.000 claims abstract description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 28
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 18
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 15
- 239000003054 catalyst Substances 0.000 claims description 12
- 230000000694 effects Effects 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 7
- 239000002244 precipitate Substances 0.000 claims description 6
- 238000003786 synthesis reaction Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 230000009467 reduction Effects 0.000 claims description 4
- 238000006722 reduction reaction Methods 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
- VYLVYHXQOHJDJL-UHFFFAOYSA-K cerium trichloride Chemical compound Cl[Ce](Cl)Cl VYLVYHXQOHJDJL-UHFFFAOYSA-K 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 3
- 230000008025 crystallization Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- 239000012265 solid product Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 238000001291 vacuum drying Methods 0.000 claims description 3
- 229910004664 Cerium(III) chloride Inorganic materials 0.000 claims description 2
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 3
- 150000004696 coordination complex Chemical class 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims 1
- 239000004810 polytetrafluoroethylene Substances 0.000 claims 1
- 239000000758 substrate Substances 0.000 claims 1
- 239000013110 organic ligand Substances 0.000 abstract description 9
- 229910052684 Cerium Inorganic materials 0.000 abstract description 5
- 239000000047 product Substances 0.000 description 9
- 239000012621 metal-organic framework Substances 0.000 description 8
- 239000013207 UiO-66 Substances 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 150000002500 ions Chemical class 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 238000000634 powder X-ray diffraction Methods 0.000 description 5
- 238000002411 thermogravimetry Methods 0.000 description 5
- 238000006555 catalytic reaction Methods 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052761 rare earth metal Inorganic materials 0.000 description 3
- 150000002910 rare earth metals Chemical class 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
- 238000004458 analytical method Methods 0.000 description 2
- XMPZTFVPEKAKFH-UHFFFAOYSA-P ceric ammonium nitrate Chemical compound [NH4+].[NH4+].[Ce+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O XMPZTFVPEKAKFH-UHFFFAOYSA-P 0.000 description 2
- HGCIXCUEYOPUTN-UHFFFAOYSA-N cyclohexene Chemical compound C1CCC=CC1 HGCIXCUEYOPUTN-UHFFFAOYSA-N 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 230000002468 redox effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- OOXLBCRRSIYSPI-UHFFFAOYSA-N 3,4-dimethylthiophene-2,5-dicarboxylic acid Chemical compound CC=1C(C)=C(C(O)=O)SC=1C(O)=O OOXLBCRRSIYSPI-UHFFFAOYSA-N 0.000 description 1
- NEQFBGHQPUXOFH-UHFFFAOYSA-N 4-(4-carboxyphenyl)benzoic acid Chemical compound C1=CC(C(=O)O)=CC=C1C1=CC=C(C(O)=O)C=C1 NEQFBGHQPUXOFH-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000013208 UiO-67 Substances 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000019445 benzyl alcohol Nutrition 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000007210 heterogeneous catalysis Methods 0.000 description 1
- 238000009396 hybridization Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000005389 magnetism Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 1
- RXOHFPCZGPKIRD-UHFFFAOYSA-N naphthalene-2,6-dicarboxylic acid Chemical compound C1=C(C(O)=O)C=CC2=CC(C(=O)O)=CC=C21 RXOHFPCZGPKIRD-UHFFFAOYSA-N 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001144 powder X-ray diffraction data Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000013074 reference sample Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 150000003573 thiols Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
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- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
- B01J31/2239—Bridging ligands, e.g. OAc in Cr2(OAc)4, Pt4(OAc)8 or dicarboxylate ligands
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
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- B01D53/8625—Nitrogen oxides
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/41—Preparation of salts of carboxylic acids
- C07C51/418—Preparation of metal complexes containing carboxylic acid moieties
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C63/00—Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
- C07C63/14—Monocyclic dicarboxylic acids
- C07C63/15—Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
- C07C63/26—1,4 - Benzenedicarboxylic acid
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Abstract
Description
技术领域Technical field
本发明为一种Ce金属与对苯二甲酸化合生成的金属有机配合物及其制备,并可作为催化材料。涉及到一种金属有机配合物的合成,并作为一种催化材料具有良好的催化反应性能。The invention relates to a metal organic complex generated by the combination of Ce metal and terephthalic acid and its preparation, and can be used as a catalytic material. It involves the synthesis of a metal-organic complex and has good catalytic reaction performance as a catalytic material.
背景技术Background technique
无机金属与有机配体进行配合形成稳定的金属有机配合物,金属的坚固和稳定与有机配体的易修饰结合,实现了有机和无机的杂化,使其性能互补,在气体吸附与分离、光学、电学、磁学、化学传感和多相催化等领域表现出巨大的应用潜力。例如金属有机配体和碱基对气体中的氢气进行质子化,然后H和CO2反应,达到加氢效果;金属有机框架(MOFs)材料可以直接作为催化剂或者作为催化剂载体被广泛应用于化学、材料学及一些工程应用领域。近年来金属有机配合物往往在多相催化反应中表现出高活性及高选择性而受到广泛关注,同时具有产物易分离、催化剂便于回收再利用和金属流失量少等优点。Inorganic metals and organic ligands cooperate to form stable metal-organic complexes. The solidity and stability of the metal are combined with the easy modification of the organic ligands to realize the hybridization of organic and inorganic, making their properties complementary. They are used in gas adsorption and separation, The fields of optics, electricity, magnetism, chemical sensing and heterogeneous catalysis show great application potential. For example, metal organic ligands and bases protonate hydrogen in the gas, and then H reacts with CO 2 to achieve the hydrogenation effect; metal organic frameworks (MOFs) materials can be used directly as catalysts or as catalyst carriers and are widely used in chemistry, Materials science and some engineering applications. In recent years, metal-organic complexes have attracted widespread attention due to their high activity and selectivity in heterogeneous catalytic reactions. They also have the advantages of easy separation of products, easy recovery and reuse of catalysts, and low metal loss.
Ce的氧化物具有良好的储氧能力和优异的氧化还原性,特别是还原态的Ce3+离子可提高催化剂表面空穴位数量和化学吸附氧量,如在NH3-SCR(脱硝)反应中,稀土金属Ce组分作为活性组分或助剂往往表现出优异的NOx转化为N2的活性和选择性等催化性能(DOI:10.1016/j.apcatb.2017.02.060,DOI:10.1016/S1002-0721(16)60024-8),包括Ce组分的掺杂调变催化剂的酸性和氧化还原性,增强了催化剂对NOx分子的吸附作用,加快吸附的-NH4 +物种与NO和O2的反应,改善催化剂的性能(http://dx.doi.org/10.1016/j.jre.2017.06.004)等等。因此,近年来,稀土铈基金属有机配合物也作为一类新型的催化材料而被研究和开发。如硝酸铈铵为Ce源与对苯二甲酸(H2BDC)(或2,6-萘二甲酸(H2NDC)和4,4′-联苯二羧酸(H2BPDC))生成的六核[Ce6O4(OH)4]12+簇八配位金属有机框架Ce(IV)-MOFs,具有UiO-66拓扑结构,PXRD图谱也与UiO-66(Zr)(六核锆簇MOFs)一致,这类铈基金属有机配合物Ce(IV)-UiO-66显示出氧化还原活性,并应用于苯甲醇有氧氧化表现出催化活性,金属节点Ce(IV)参与了催化循环(DOI:10.1039/c5cc02606g)。其他如Ce金属与3,4-二甲基噻吩-2,5二羧酸生成的具有UiO-66拓扑结构的金属有机配合物(Ce6O4(OH)4(DMTDC)6)对硫醇的氧化具有催化作用(DOI:10.1039/c7ce01053b)、Ce金属与配体H2BDC-(CH3)2生成的UiO-66拓扑结构的金属有机配合物具有苯乙烯和环己烯氧化催化性能(DOI:10.1039/c6ce01704e)等等。金属有机配合物UiO-67(Zr)上负载Ce组分制备的Ce@UiO-67催化剂具有较好的低温SCR性能,并且抗水抗硫性能良好,催化剂中三价Ce离子的占比(Ce3+/Ce4+)与催化性能相关(http://dx.doi.org/10.1016/j.cej.2017.05.128)。金属有机配合物多相催化材料的合成及应用是当前需要进一步广泛研究开发的领域,但以三价Ce离子为来源合成的稀土铈基金属有机配合物并应用于大气污染物NOx净化催化尚未见报道。有鉴于此,本发明以三价Ce离子为金属节点来源与对苯二甲酸有机配体连接成一种具有高热稳定性Ce(III)-BDC金属有机配合物,并将其作为SCR活性优良的NOx转化催化材料。The oxide of Ce has good oxygen storage capacity and excellent redox properties. In particular, the reduced Ce 3+ ions can increase the number of holes on the catalyst surface and the amount of chemically adsorbed oxygen, such as in the NH 3 -SCR (denitrification) reaction. , the rare earth metal Ce component as an active component or additive often shows excellent catalytic properties such as activity and selectivity in converting NO x to N 2 (DOI:10.1016/j.apcatb.2017.02.060, DOI:10.1016/S1002 -0721(16)60024-8), including the doping of Ce components to modulate the acidity and redox properties of the catalyst, enhance the adsorption of NO x molecules by the catalyst, and accelerate the interaction of the adsorbed -NH 4 + species with NO and O 2 reaction, improve the performance of the catalyst (http://dx.doi.org/10.1016/j.jre.2017.06.004) and so on. Therefore, in recent years, rare earth cerium-based metal organic complexes have also been researched and developed as a new type of catalytic materials. For example, ceric ammonium nitrate is generated from Ce source and terephthalic acid (H 2 BDC) (or 2,6-naphthalenedicarboxylic acid (H 2 NDC) and 4,4′-biphenyldicarboxylic acid (H 2 BPDC)). Six-core [Ce 6 O 4 (OH) 4 ] 12+ cluster eight-coordinated metal-organic framework Ce(IV)-MOFs, with UiO-66 topology, the PXRD pattern is also consistent with UiO-66(Zr) (hexa-core zirconium cluster MOFs), this type of cerium-based metal organic complex Ce(IV)-UiO-66 shows redox activity and is used in the aerobic oxidation of benzyl alcohol to show catalytic activity. The metal node Ce(IV) participates in the catalytic cycle ( DOI:10.1039/c5cc02606g). Others, such as the metal-organic complex (Ce 6 O 4 (OH) 4 (DMTDC) 6 ) with UiO-66 topology generated by Ce metal and 3,4-dimethylthiophene-2,5dicarboxylic acid, have a strong response to thiols. The oxidation of has a catalytic effect (DOI: 10.1039/c7ce01053b). The UiO-66 topological metal-organic complex generated by Ce metal and ligand H 2 BDC-(CH 3 ) 2 has catalytic performance for the oxidation of styrene and cyclohexene ( DOI:10.1039/c6ce01704e) and so on. The Ce@UiO-67 catalyst prepared by loading the Ce component on the metal organic complex UiO-67 (Zr) has good low-temperature SCR performance and good water and sulfur resistance. The proportion of trivalent Ce ions in the catalyst (Ce 3+ /Ce 4+ ) is related to catalytic performance (http://dx.doi.org/10.1016/j.cej.2017.05.128). The synthesis and application of metal-organic complex heterogeneous catalytic materials are currently areas that require further extensive research and development. However, rare earth cerium-based metal-organic complexes synthesized from trivalent Ce ions and used in catalysis for the purification of atmospheric pollutants NO x have not yet been used. See report. In view of this, the present invention uses trivalent Ce ions as the source of metal nodes and connects them with terephthalic acid organic ligands to form a Ce(III)-BDC metal-organic complex with high thermal stability, and uses it as a NO with excellent SCR activity. x conversion catalytic materials.
发明内容Contents of the invention
本发明的目的是为了合成出一种以三价Ce离子为金属节点来源与对苯二甲酸有机配体连接成一种具有高热稳定性的Ce(III)-BDC金属有机配合物,并将其作为SCR活性优良的NOx转化催化材料。本发明通过对苯二甲酸有机配体与三价铈离子以溶剂热法合成Ce(III)-BDC金属有机配合物,利用还原态的Ce3+离子可提高催化剂表面空穴位数量和化学吸附氧量、以及金属节点对NOx分子的吸附作用,可作为SCR活性优良的NOx转化催化材料。The purpose of the present invention is to synthesize a Ce(III)-BDC metal-organic complex with high thermal stability using trivalent Ce ions as a metal node source and connected with terephthalic acid organic ligands, and use it as a NO x conversion catalytic material with excellent SCR activity. The present invention synthesizes Ce(III)-BDC metal organic complex by solvothermal method through terephthalic acid organic ligand and trivalent cerium ions. The reduced Ce 3+ ions can be used to increase the number of hole sites on the catalyst surface and chemically adsorbed oxygen. The amount, as well as the adsorption effect of metal nodes on NO x molecules, can be used as a NO x conversion catalytic material with excellent SCR activity.
本发明提供的一种Ce基有机金属配合物催化材料及其制备与应用按以下步骤进行:A Ce-based organometallic complex catalytic material provided by the invention and its preparation and application are carried out according to the following steps:
(1)对苯二甲酸(H2BDC)溶于N,N′-二甲基甲酰胺(DMF)中,常温搅拌直至对苯二甲酸全部溶解,再将Ce盐(CeCl3·7H2O)加入以上混合液,常温搅拌直至三氯化铈全部溶解,最后加入乙酸调节剂,搅拌均匀。其中,H2BDC与CeCl3·7H2O的投料摩尔比为1:2,DMF体积用量与H2BDC质量比例约为60~90mL:1g,乙酸体积用量与H2BDC质量比例约为1.5~2.0mL:1g。(1) Dissolve terephthalic acid (H 2 BDC) in N,N′-dimethylformamide (DMF), stir at room temperature until all terephthalic acid is dissolved, and then add Ce salt (CeCl 3 ·7H 2 O ) Add the above mixture and stir at room temperature until all cerium trichloride is dissolved. Finally, add acetic acid regulator and stir evenly. Among them, the molar ratio of H 2 BDC to CeCl 3 ·7H 2 O is 1:2, the volume ratio of DMF to H 2 BDC is about 60-90mL:1g, and the volume ratio of acetic acid to H 2 BDC is about 1.5 ~2.0mL:1g.
(2)将步骤(1)所得混合液转移至聚四氟乙烯衬底的反应釜中,将反应釜移至烘箱中,程序升温至100~120℃,静置晶化12~24小时,然后程序降温至室温将反应釜取出。其中,程序升温和降温速率为0.2~1℃/min。(2) Transfer the mixed solution obtained in step (1) to a polytetrafluoroethylene-backed reaction kettle, move the reaction kettle to an oven, program the temperature to 100-120°C, and let it stand for crystallization for 12-24 hours. Program to cool down to room temperature and take out the reaction kettle. Among them, the programmed heating and cooling rates are 0.2 to 1°C/min.
(3)将步骤(2)所得白色沉淀物离心分离,沉淀物用DMF洗涤三次,去除未反应的原料,然后再用无水甲醇交换三次,再离心过滤。其中,每次洗涤用DMF体积用量和无水甲醇体积用量约为合成反应中DMF用量的三分之一。(3) Centrifuge the white precipitate obtained in step (2), wash the precipitate three times with DMF to remove unreacted raw materials, then exchange it with anhydrous methanol three times, and then centrifuge and filter. Among them, the volume of DMF used for each washing and the volume of anhydrous methanol used are about one-third of the amount of DMF used in the synthesis reaction.
(4)将步骤(3)所得固体产物在100~120℃烘箱中干燥6~12小时,再于180~220℃真空干燥箱中干燥10~14小时,得到脱除溶剂的Ce(III)-BDC金属有机配合物。(4) Dry the solid product obtained in step (3) in an oven at 100-120°C for 6-12 hours, and then dry it in a vacuum drying oven at 180-220°C for 10-14 hours to obtain Ce(III)- from which the solvent is removed BDC metal-organic complexes.
(5)将步骤(4)所得到Ce(III)-BDC金属有机配合物在一定的反应条件下进行NOx的NH3还原消除为N2的催化性能试验。反应条件为:固定床反应器,操作压力0.1MPa,原料气组成0.05~0.1vol.%NOx、NH3/NO摩尔比1.0~1.1,3~6vol.%O2,平衡气为N2,检测反应前后NOx浓度计算转化率。(5) The Ce(III)-BDC metal-organic complex obtained in step (4) is subjected to a catalytic performance test of NH 3 reduction and elimination of NO x to N 2 under certain reaction conditions. The reaction conditions are: fixed bed reactor, operating pressure 0.1MPa, raw gas composition 0.05~0.1vol.% NOx , NH3 /NO molar ratio 1.0~1.1, 3~6vol.% O2 , balance gas is N2 , The NOx concentration before and after the reaction was detected to calculate the conversion rate.
附图说明Description of the drawings
图1为实施例所得Ce(III)-BDC金属有机配合物的NH3还原消除NOx催化性能。Figure 1 shows the catalytic performance of NO x reduction by NH 3 of the Ce(III)-BDC metal organic complex obtained in the Example.
图2为实施例所得Ce(III)-BDC金属有机配合物的PXRD晶相结构。Figure 2 is the PXRD crystal phase structure of the Ce(III)-BDC metal organic complex obtained in the example.
图3为实施例所得Ce(III)-BDC金属有机配合物的SEM形貌图。Figure 3 is an SEM morphology image of the Ce(III)-BDC metal organic complex obtained in the example.
图4为对照的文献报道Ce(IV)-UiO-66金属有机框架的SEM形貌图。Figure 4 shows the SEM morphology of the Ce(IV)-UiO-66 metal-organic framework reported in the literature.
图5为实施例所得Ce(III)-BDC金属有机配合物的TG热稳定性能。Figure 5 shows the TG thermal stability performance of the Ce(III)-BDC metal organic complex obtained in Examples.
图6为实施例的制备流程图。Figure 6 is a preparation flow chart of the embodiment.
具体实施方式Detailed ways
以下通过具体实施例对本发明进行详细说明,但应了解本发明不仅仅限定于所述实施例。The present invention will be described in detail through specific examples below, but it should be understood that the present invention is not limited only to the examples.
实施例1Example 1
(1)原料(1) Raw materials
对苯二甲酸(H2BDC)为上海麦克林生化科技有限公司生产,分析纯(99%);N,N’-二甲基甲酰胺(DMF)为西陇科学股份有限公司生产,分析纯(99.8%);CeCl3·7H2O为上海麦克林生化科技有限公司生产,分析纯(99.9%);乙酸(CH3COOH)为西陇科学股份有限公司生产,分析纯(99.8%)。Terephthalic acid (H 2 BDC) was produced by Shanghai McLean Biochemical Technology Co., Ltd. and was of analytical purity (99%); N,N'-dimethylformamide (DMF) was produced by Xilong Science Co., Ltd. and was of analytical purity. (99.8%); CeCl 3 ·7H 2 O was produced by Shanghai McLean Biochemical Technology Co., Ltd., with analytical purity (99.9%); acetic acid (CH 3 COOH) was produced by Xilong Science Co., Ltd., with analytical purity (99.8%).
(2)合成液配制(2) Preparation of synthetic liquid
对苯二甲酸(4mmol,0.6644g)溶于50mL N,N′-二甲基甲酰胺中,常温磁力搅拌直至对苯二甲酸全部溶解,再将CeCl3·7H2O(8mmol,2.9808g)加入以上混合液,常温搅拌直至氯化铈全部溶解,最后再加入1.2mL乙酸,搅拌均匀。Terephthalic acid (4mmol, 0.6644g) was dissolved in 50mL N,N′-dimethylformamide, stirred magnetically at room temperature until all terephthalic acid was dissolved, and then CeCl 3 ·7H 2 O (8mmol, 2.9808g) Add the above mixture and stir at room temperature until all cerium chloride is dissolved. Finally, add 1.2 mL acetic acid and stir evenly.
(3)金属有机配合物合成(3) Synthesis of metal-organic complexes
将步骤(2)所得混合液转移至100mL聚四氟乙烯衬底的反应釜中,将反应釜移至烘箱中,以0.75℃/min升温速率程序升温至120℃,静置晶化24小时,然后以0.38℃/min降温速率程序降至室温将反应釜取出。Transfer the mixture obtained in step (2) to a 100mL polytetrafluoroethylene-backed reaction kettle, move the reaction kettle to an oven, program the temperature to 120°C at a heating rate of 0.75°C/min, and let it stand for crystallization for 24 hours. Then the temperature was lowered to room temperature using a cooling rate program of 0.38°C/min and the reaction kettle was taken out.
(4)产物的洗涤与过滤(4) Washing and filtration of product
将步骤(3)所得白色沉淀物离心分离,沉淀物用DMF洗涤三次(20mL/次),去除未反应的原料,然后再用无水甲醇交换三次(20mL/次),再离心过滤。Centrifuge the white precipitate obtained in step (3), wash the precipitate three times with DMF (20 mL/time) to remove unreacted raw materials, and then exchange it with anhydrous methanol three times (20 mL/time), and then centrifuge and filter.
(5)产物的催化性能评价(5) Evaluation of catalytic performance of the product
将步骤(4)所得固体产物在110℃烘箱中干燥12小时,再在200℃真空干燥箱中干燥12h,得到脱除溶剂的Ce(III)-BDC金属有机配合物。The solid product obtained in step (4) was dried in an oven at 110°C for 12 hours, and then dried in a vacuum drying oven at 200°C for 12 hours to obtain the Ce(III)-BDC metal organic complex from which the solvent was removed.
(6)将步骤(5)所得到Ce(III)-BDC金属有机配合物在反应条件下进行NOx的NH3还原消除为N2的催化性能试验。反应条件为:固定床微型反应器,操作压力0.1MPa,原料气组成0.075vol.%NOx、NH3/NO摩尔比1.05,3.0vol.%O2,平衡气为N2,空速5×104mL/(g·h),以FGA10型在线烟气分析仪(深圳市贝特分析仪器有限公司)检测反应前后NOx浓度计算转化率。催化性能评价结果见说明书附图1。(6) The Ce(III)-BDC metal-organic complex obtained in step (5) is subjected to a catalytic performance test of NH 3 reduction and elimination of NO x to N 2 under reaction conditions. The reaction conditions are: fixed bed microreactor, operating pressure 0.1MPa, raw gas composition 0.075vol.% NOx , NH3 /NO molar ratio 1.05, 3.0vol.% O2 , balance gas N2 , space velocity 5× 10 4 mL/(g·h), and the conversion rate was calculated by detecting the NO x concentration before and after the reaction with an FGA10 online flue gas analyzer (Shenzhen Better Analytical Instrument Co., Ltd.). The catalytic performance evaluation results are shown in Figure 1 of the description.
(7)产物金属有机配合物表征(7) Characterization of product metal organic complexes
将步骤(5)所得到Ce(III)-BDC金属有机配合物以如下仪仪器和方法分析产物的晶相结构(PXRD)、表面形貌(SEM)和热稳定性(TG),结果分别见说明书附图2、附图3和附图5。The Ce(III)-BDC metal organic complex obtained in step (5) was analyzed using the following instruments and methods to analyze the crystal phase structure (PXRD), surface morphology (SEM) and thermal stability (TG) of the product. The results are shown in Figure 2, Figure 3 and Figure 5 of the description.
粉末X射线衍射分析(PXRD):所用仪器为Philips X′pert pro X射线衍射仪,测定条件为Cu靶,Ni滤波片,管压40kV,管流40mA,扫描角度5°~60°;采用日立高新场发射扫描电镜SU5000(SEM)对产物外貌形状进行表征;热重分析(TG):采用美国SDT-Q600型同步TGA/DSC分析仪,在氮气气氛下,温度范围室温~700℃,升温速率10℃/min。Powder X-ray diffraction analysis (PXRD): The instrument used is Philips The high-tech field emission scanning electron microscope SU5000 (SEM) was used to characterize the appearance and shape of the product; thermogravimetric analysis (TG): using the American SDT-Q600 synchronous TGA/DSC analyzer, in a nitrogen atmosphere, the temperature range was room temperature to 700°C, and the heating rate 10℃/min.
(8)实施例结果分析(8) Analysis of Example Results
从实施例合成所得产物的晶相结构(PXRD)所见,本发明所得Ce(III)-BDC金属有机配合物的晶相结构与已报道和公开的六核[Ce6O4(OH)4]12+簇八配位Ce(IV)-MOFs金属有机配合物不一样,也与Ce的氧化物晶相结构不同。表面形貌(SEM)也表明,本发明所得Ce(III)-BDC产物为二核[Ce2O]4+簇与对苯二甲酸配位形成的金属有机配合物,其化学式为Ce2O(CO2)4,晶体形貌为六方棱柱体,与Ce(IV)-MOFs正八面体形貌(见说明书附图4)不相同。表明本发明所得Ce(III)-BDC金属有机配合物为一种金属有机配合物。从产物的TG结果可见,200℃前的失重应为没有洗脱干净的溶剂和有机配体的脱除,500℃以上的失重应为有机配体的分解,表明了本发明的Ce(III)-BDC金属有机配合物热稳定性较高。将本发明所得Ce(III)-BDC金属有机配合物应用于的NH3选择性催化还原NO的催化反应中,T50和T90分别为135℃和175℃,稳定转化率(98.7~100%)窗口达到300℃,相比参比样的T50为205℃和最高转化率86.6%来说,显示出优良的低温脱硝性能和稳定转化性能,是一种催化性能优良的金属有机配合物。From the crystal phase structure (PXRD) of the product synthesized in the Example, the crystal phase structure of the Ce(III)-BDC metal organic complex obtained in the present invention is consistent with the reported and disclosed hexanuclear [Ce 6 O 4 (OH) 4 ] The 12+ cluster eight-coordinated Ce(IV)-MOFs metal-organic complex is different, and it is also different from the Ce oxide crystal phase structure. The surface morphology (SEM) also shows that the Ce(III)-BDC product obtained in the present invention is a metal-organic complex formed by the coordination of dinuclear [Ce 2 O] 4+ clusters and terephthalic acid, and its chemical formula is Ce 2 O (CO 2 ) 4 , the crystal morphology is a hexagonal prism, which is different from the regular octahedral morphology of Ce(IV)-MOFs (see Figure 4 of the specification). It shows that the Ce(III)-BDC metal organic complex obtained in the present invention is a metal organic complex. It can be seen from the TG results of the product that the weight loss before 200°C should be due to the removal of solvent and organic ligands that have not been eluted cleanly, and the weight loss above 500°C should be due to the decomposition of organic ligands, indicating that Ce(III) of the present invention -BDC metal-organic complexes have high thermal stability. When the Ce(III)-BDC metal organic complex obtained by the present invention is used in the catalytic reaction of NH 3 selective catalytic reduction of NO, T 50 and T 90 are 135°C and 175°C respectively, and the stable conversion rate (98.7-100% ) window reaches 300°C. Compared with the reference sample with T 50 of 205°C and the highest conversion rate of 86.6%, it shows excellent low-temperature denitration performance and stable conversion performance. It is a metal-organic complex with excellent catalytic performance.
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Application publication date: 20200728 Assignee: GUANGXI GUOBO TECHNOLOGY Co.,Ltd. Assignor: GUILIN University OF TECHNOLOGY Contract record no.: X2023980045084 Denomination of invention: A Ce based organometallic complex catalytic material and its preparation and application Granted publication date: 20231013 License type: Common License Record date: 20231030 Application publication date: 20200728 Assignee: Guangxi Jikuan Energy Technology Co.,Ltd. Assignor: GUILIN University OF TECHNOLOGY Contract record no.: X2023980045082 Denomination of invention: A Ce based organometallic complex catalytic material and its preparation and application Granted publication date: 20231013 License type: Common License Record date: 20231030 |