SELECTIVE CATALYTIC OXIDATION PERFORMANCE OF N-BUTYLAMINE OVER Cu-ZSM-5 CATALYSTS WITH DIFFERENT COPPER LOADINGS
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摘要: 采用等体积浸渍法制备不同Cu负载量(1%、2%、5%和10%)的系列Cu-ZSM-5催化剂,并考察了Cu负载量对催化剂的正丁胺催化氧化性能的影响。通过XRD、N2吸脱附、EPR、H2-TPR、NH3-TPD表征方法对催化剂的晶相结构和物化性质进行表征并研究构效关系。结果表明:Cu负载量为10%的催化剂催化活性最高,在300℃下实现了正丁胺的完全转化;而Cu负载量为5%的催化剂N2选择性最佳,低温时N2选择性明显高于其他催化剂。表征结果表明,催化剂的氧化还原性能主要影响正丁胺的转化率,Cu负载量影响催化材料的氧化还原性能,Cu负载量高的催化剂氧化还原性能优异。高N2选择性主要归属于催化剂孤立态Cu2+物种和弱酸性位,催化剂的弱酸性位有利于正丁胺的吸附活化和深度氧化。
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关键词:
- 正丁胺 /
- 选择催化氧化 /
- Cu-ZSM-5催化剂 /
- 铜物种 /
- 酸性
Abstract: A series of Cu-ZSM-5 catalysts with different Cu loadings (1%, 2%, 5% and 10%) were synthesized by equal volume impregnation method, and the effect of Cu loading on n-butylamine catalytic oxidation was investigated. The crystal structure and physicochemical properties of the catalysts were characterized by XRD, N2 adsorption desorption, EPR, H2-TPR and NH3-TPD, and the structure-activity relationship was studied. The catalyst with Cu loading of 10% had the highest catalytic activity, and the complete conversion of n-butylamine was achieved at 300℃. The catalyst with 5% Cu loading had the best N2 selectivity, and the N2 selectivity at low temperature was significantly higher than that of the other catalysts. The characterization results showed that the redox performance of the catalyst mainly affected the n-butylamine conversion, the different Cu loading affected the redox performance of the catalyst materials, and the catalyst with higher Cu loading had excellent redox performance. The high N2 selectivity could be attributed to the isolated Cu2+ species and the weak acid sites of the catalyst, which was conducive to the adsorption activation and deep oxidation of n-butylamine to form N2.-
Key words:
- n-butylamine /
- selective catalytic oxidation /
- Cu-ZSM-5 catalyst /
- copper species /
- acidity
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[1] LI S D, WANG D D, WU X F, et al. Recent advance on VOCs oxidation over layered double hydroxides derived mixed metal oxides[J]. Chinese Journal of Catalysis, 2020, 41(4):550-560. [2] PARMAR G R, RAO N N. Emerging control technologies for volatile organic compounds[J]. Critical Reviews in Environmental Science and Technology, 2008, 39(1):41-78. [3] 王海林,张国宁,聂磊,等.我国工业VOCs减排控制与管理对策研究[J].环境科学, 2011, 32(12):3462-3468. [4] LIOTTA L F. Catalytic oxidation of volatile organic compounds on supported noble metals[J]. Applied Catalysis B:Environmental, 2010, 100(3/4):403-412. [5] 李娟娟,张梦,蔡松财,等.光热催化氧化VOCs的研究进展[J].环境工程, 2020, 38(1):13-20. [6] HE C, CHENG J, ZHANG X, et al. Recent advances in the catalytic oxidation of volatile organic compounds:a review based on pollutant sorts and sources[J]. Chemical Reviews, 2019, 119(7):4471-4568. [7] SCIRÈ S, LIOTTA L F. Supported gold catalysts for the total oxidation of volatile organic compounds[J]. Applied Catalysis B:Environmental, 2012, 125:222-246. [8] 曹利,连子,黄学敏, MnCeOx/沸石催化剂对工业典型VOCs的催化性能[J].环境工程, 2020, 38(1):48-53. [9] ZHU L L, SHEN D K, LUO K H. A critical review on VOCs adsorption by different porous materials:species, mechanisms and modification methods[J]. Journal of Hazardous Materials, 2020, 389:122102. [10] 许子飏,莫胜鹏,付名利,等.稀土材料在挥发性有机废气降解中的应用及发展趋势[J].环境工程, 2020, 38(1):1-12, 36. [11] NANBA T, MASUKAWA S, UCHISAWA J, et al. Screening of catalysts for acrylonitrile decomposition[J]. Catalysis letters, 2004, 93:195-201. [12] NANBA T, MASUKAWA S, OGATA A, et al. Active sites of Cu-ZSM-5 for the decomposition of acrylonitrile[J]. Applied Catalysis B:Environmental, 2005, 61(3/4):288-296. [13] NANBA T, MASUKAWA S, UCHISAWA J, et al. Mechanism of acrylonitrile decomposition over Cu-ZSM-5[J]. Journal of Molecular Catalysis A:Chemical, 2007, 276(1/2):130-136. [14] ZHANG R D, SHI D J, LIU N, et al. Mesoporous SBA-15 promoted by 3d-transition and noble metals for catalytic combustion of acetonitrile[J]. Applied Catalysis B:Environmental, 2014, 146:79-93. [15] WANG Q, WANG X Q, WANG L L, et al. Catalytic oxidation and hydrolysis of HCN over LaxCuy/TiO2 catalysts at low temperatures[J]. Microporous and Mesoporous Materials, 2019, 282:260-268. [16] MA M D, HUANG H, CHEN C W, et al. Highly active SBA-15-confined Pd catalyst with short rod-like micro-mesoporous hybrid nanostructure for n-butylamine low-temperature destruction[J]. Molecular Catalysis, 2018, 455:192-203. [17] MA M D, JIAN Y F, CHEN C W, et al. Spherical-like Pd/SiO2 catalysts for n-butylamine efficient combustion:effect of support property and preparation method[J]. Catalysis Today, 2020, 339:181-191. [18] XING X, LI N, SUN Y G, et al. Selective catalytic oxidation of n-butylamine over Cu-zeolite catalysts[J]. Catalysis Today, 2020,339:192-199. [19] XING X, LI N, CHENG J, et al. Synergistic effects of Cu species and acidity of Cu-ZSM-5 on catalytic performance for selective catalytic oxidation of n-butylamine[J]. Journal of Environmental Sciences, 2020, 96:55-63. [20] LAI S S, MENG D M, ZHAN W C, et al. The promotional role of Ce in Cu/ZSM-5 and in situ surface reaction for selective catalytic reduction of NOx with NH3[J]. RSC Advances, 2015, 5(110):90235-90244. [21] XUE H Y, GUO X M, WANG S D, et al. Poisoning effect of CaO on Cu/ZSM-5 for the selective catalytic reduction of NO with NH3[J]. Catalysis Communications, 2018, 112:53-57. [22] NAVLANI-GARCÍA M, MARTIS M, LOZANO-CASTELLÓ, et al. Investigation of Pd nanoparticles supported on zeolites for hydrogen production from formic acid dehydrogenation[J]. Catalysis Science&Technology, 2015, 5(1):364-371. [23] YASHNIK S A, ISMAGILOV Z R, ANUFRIENKO V F. Catalytic properties and electronic structure of copper ions in Cu-ZSM-5[J]. Catalysis Today, 2005, 110(3/4):310-322. [24] YASHNIK S A, SALNIKOV A V, VASENIN N T, et al. Regulation of the copper-oxide cluster structure and DeNOx activity of Cu-ZSM-5 catalysts by variation of OH/Cu2+[J]. Catalysis Today, 2012, 197(1):214-227. [25] LIU X, WU X, WENG D, et al. Modification of Cu/ZSM-5 catalyst with CeO2 for selective catalytic reduction of NOx with ammonia[J]. Journal of Rare Earths, 2016, 34(10):1004-1009. [26] DOU B J, LV G, WANG C, et al. Cerium doped copper/ZSM-5 catalysts used for the selective catalytic reduction of nitrogen oxide with ammonia[J]. Chemical Engineering Journal, 2015, 270:549-556. [27] DE LA TORRE U, URRUTXUA M, PEREDA-AYO B, et al. On the Cu species in Cu/beta catalysts related to DeNOx performance of coupled NSR-SCR technology using sequential monoliths and dual-layer monolithic catalysts[J]. Catalysis Today, 2016, 273:72-82. [28] BLANCH-RAGA N, PALOMARES A E, MARTÍNEZ-TRIGUERO J, et al. Cu and Co modified beta zeolite catalysts for the trichloroethylene oxidation[J]. Applied Catalysis B:Environmental, 2016, 187:90-97. [29] HAN S, CHENG J, ZHENG C K, et al. Effect of Si/Al ratio on catalytic performance of hydrothermally aged Cu-SSZ-13 for the NH3-SCR of NO in simulated diesel exhaust[J]. Applied Surface Science, 2017, 419:382-392. [30] BAI Y T, WU W Y, BIAN X. Investigation of the interactions in CeO2-Fe2O3 binary metal oxides supported on ZSM-5 for NO removal by CO in the presence of O2, SO2 and steam[J]. RSC Advances, 2017, 7(89):56447-56456. [31] LIU J X, SONG W Y, XU C, et al. The selective catalytic reduction of NOx over a Cu/ZSM-5/SAPO-34 composite catalyst[J]. RSC Advances, 2015, 5(127):104923-104931. [32] HUANG Q Q, ZUO S F, ZHOU R X. Catalytic performance of pillared interlayered clays (PILCs) supported CrCe catalysts for deep oxidation of nitrogen-containing VOCs[J]. Applied Catalysis B:Environmental, 2010, 95(3/4):327-334.
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