Facile preparation of hierarchically porous IM-5 zeolite with enhanced catalytic performance in methane aromatization
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摘要: 采用一步水热晶化法、不添加第二模板剂、仅通过控制合成条件,制备了具有多级孔道结构的IM-5-H分子筛。多级孔IM-5-H材料展现了与常规IM-5-C分子筛不同的形貌、结构和酸性质。由于IM-5-H分子筛载体介孔结构的促进作用,钼基Mo-IM-5-H催化剂在甲烷无氧芳构化反应中表现出较高的甲烷转化率(13.1%)、芳烃产率(7.5%)和稳定性。该研究为合成多级孔IM-5材料提供了一种简便的方法,同时扩展了微孔-介孔复合材料在甲烷芳构化反应中的应用。Abstract: A novel hierarchically porous IM-5-H zeolite material was prepared through one-step crystallization route by means of adjusting the synthesis parameters without introducing any secondary template.The hierarchical IM-5-H zeolite is quite different from the conventional IM-5-C in morphology, textural and acidic properties.After loading Mo, the Mo-IM-5-H catalyst exhibits high activity and stability in non-oxidative aromatization of methane, with a methane conversion of 13.1% and aromatics yield of 7.5%, owing to the mesopores in the IM-5-H zeolite crystals.This work provides a simple way to synthesize hierarchical IM-5 zeolite and expands the application of micro-mesoporous composite material in methane dehydroaromatization.
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Key words:
- hierarchical pore structure /
- IM-5 /
- zeolite /
- methane aromatization
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Table 1 Surface areas (ABET), microporous surface areas (vmicro), microporous volumes (vmicro), total pore volumes (vtotal), micropore size (dmicro) and average pore size (daver) of the IM-5-C, Mo-IM-5-C, IM-5-H and Mo-IM-5-H samples
Sample ABET
/(m2·g-1)Amicro
/(m2·g-1)vmicro
/(cm3·g-1)vtotal
/(cm3·g-1)dmicro
/nmdaver
/nmIM-5-C 359 318 0.16 0.20 0.48 2.1 Mo-IM-5-C 302 274 0.14 0.17 0.45 1.9 IM-5-H 393 306 0.15 0.29 0.47 5.2 Mo-IM-5-H 321 265 0.13 0.24 0.45 4.7 note: dmicro is calculated from Horvath-Kawazoe report, whereas daver from BJH method based on the desorption branch Table 2 Acidity capacities of H-IM-5-C, Mo-IM-5-C, H-IM-5-H and Mo-IM-5-H
Sample Peak area /(a.u.) L M H H-IM-5-C 466 - 570 Mo-IM-5-C 408 245 303 H-IM-5-H 395 - 397 Mo-IM-5-H 352 191 184 Table 3 Quantitative results from pyridine-FT-IR spectra of H-IM-5-C, Mo-IM-5-C, H-IM-5-H and Mo-IM-5-H samples
Sample Acidity quantity /(mmol·g-1) Brönsted acid sites Lewis acid sites H-IM-5-C 0.2723 0.2552 Mo-IM-5-C 0.2154 0.2179 H-IM-5-H 0.1917 0.2316 Mo-IM-5-H 0.1282 0.1975 -
[1] MA S, GUO X, ZHAO L, SCOTTC S, BAO X. Recent progress in methane dehydroaromatization:From laboratory curiosities to promising technology[J]. J Energy Chem, 2013, 22(1):1-20. doi: 10.1016/S2095-4956(13)60001-7 [2] MAMONOV N A, FADEEVA E V, GRIGORIEV D A, MIKHAILOV M N, KUSTOV L M, ALKHIMOV S A. Metal-zeolite catalysts for dehydroaromatization of methane[J]. Russ Chem Rev, 2013, 82(6):567-585. doi: 10.1070/RC2013v082n06ABEH004346 [3] WANG L, TAO L, XIE M, XU G, HUANG J, XU Y. Dehydrogenation and aromatization of methane under non-oxidizing conditions[J]. Catal Lett, 1993, 21(1):35-41. doi: 10.1007/BF00767368 [4] LIU H, WU S, GUO Y, SHANG F, YU X, MA Y, XU C, GUAN J, KAN Q. Synthesis of Mo/IM-5 catalyst and its catalytic behavior in methane non-oxidative aromatization[J]. Fuel, 2011, 90:1515-1521. doi: 10.1016/j.fuel.2010.11.027 [5] LIU H, YANG S, WU S, SHANG F, YU X, XU C, GUAN J, KAN Q. Synthesis of Mo/TNU-9(TNU-9 Taejon National University No. 9) catalyst and its catalytic performance in methane non-oxidative aromatization[J]. Energy, 2011, 36(3):1582-1589. doi: 10.1016/j.energy.2010.12.073 [6] LIU H, HU J, LI Z, WU S, LIU L, GUAN J, KAN Q. Synthesis of zeolite IM-5 under rotating and static conditions and the catalytic performance of Mo/H-IM-5 catalyst in methane non-oxidative aromatization[J]. Kinet Catal, 2013, 54(4):443-450. doi: 10.1134/S0023158413040083 [7] LI B, LI S, LI N, CHEN H, ZHANG W, BAO X, LIN B. Structure and acidity of Mo/ZSM-5 synthesized by solid state reaction for methane dehydrogenation and aromatization[J]. Micropor Mesopor Mat, 2006, 88(1/3):244-253. http://www.sciencedirect.com/science/article/pii/S1387181105004567 [8] HU J, WU S, MA Y, YANG X, LI Z, LIU H, HUO Q, GUAN J, KAN Q. Effect of the particle size of MoO3 on the catalytic activity of Mo/ZSM-5 in methane non-oxidative aromatization[J]. New J Chem, 2015, 39(7):5459-5469. doi: 10.1039/C5NJ00672D [9] WU P, KAN Q, WANG X, WANG D, XING H, YANG P, WU T. Acidity and catalytic properties for methane conversion of Mo/HZSM-5 catalyst modified by reacting with organometallic complex[J]. Appl Catal A, 2005, 282(1/2):39-44. http://www.sciencedirect.com/science/article/pii/S0926860X04009639 [10] LIU B, ZHANG Y, LIU J, TIAN M, ZHANG F, AU C T, CHEUNG A S C. Characteristic and mechanism of methane dehydroaromatization over Zn-based/HZSM-5 catalysts under conditions of atmospheric pressure and supersonic jet expansion[J]. J Phys Chem C, 2011, 115(34):16954-16962. doi: 10.1021/jp2027065 [11] LUZGIN M V, GABRIENKO A A, ROGOV V A, TOKTAREV A V, Parmon V N, STEPANOV A G. The "alkyl" and "carbenium" pathways of methane activation on Ga-modified zeolite BEA:13C solid-state NMR and GC-MS study of methane aromatization in the presence of higher alkane[J]. J Phys Chem C, 2010, 114(49):21555-21561. doi: 10.1021/jp1078899 [12] SU L, LIU L, ZHUANG J, WANG H, LI Y, SHEN W, XU Y, BAO X. Creating mesopores in ZSM-5 zeolite by alkali treatment:a new way to enhance the catalytic performance of methane dehydroaromatization on Mo/HZSM-5 catalysts[J]. Catal Lett, 2003, 91(3):155-167. doi: 10.1023/B%3ACATL.0000007149.48132.5a [13] LI Y, LIU D, LIU S, WANG W, XIE S, ZHU X, XU L. Thermal and hydrothermal stabilities of the alkali-treated HZSM-5 zeolites[J]. J Nat Gas Chem, 2008, 17(1):69-74. doi: 10.1016/S1003-9953(08)60028-6 [14] SERRANO D P, GARCÍAR A, VICNETE G, LINARES M, PROCHÁZKOVÁ D, ČJ. Acidic and catalytic properties of hierarchical zeolites and hybrid ordered mesoporous materials assembled from MFI protozeolitic units[J]. J Catal, 2011, 279(2):366-380. doi: 10.1016/j.jcat.2011.02.007 [15] ZHU H, LIU Z, WANG Y, KONG D, YUAN X, XIE Z. Nanosized CaCO3 as hard template for creation of intracrystal pores within silicalite-1 crystal[J].Chem Mater, 2008, 20(3):1134-1139. doi: 10.1021/cm071385o [16] CHOI M, CHO H S, SRIVASTAVA R, VENKATESAN C, CHOI D, RYOO R. Amphiphilic organosilane-directed synthesis of crystalline zeolite with tunable mesoporosity[J]. Nature Mater, 2006, 5(9):718-723. doi: 10.1038/nmat1705 [17] CHEN L, LI X, ROOKE J C, ZHANG Y, YANG X, TANG Y, XIAO F, SU B. Hierarchically structured zeolites:synthesis, mass transport properties and applications[J]. J Mater Chem, 2012, 22(34):17381-17403. doi: 10.1039/c2jm31957h [18] CHU N, YANG J, LI C, CUI J, ZHAO Q, YIN X, LU J, WANG J. An unusual hierarchical ZSM-5 microsphere with good catalytic performance in methane dehydroaromatization[J]. Micropor Mesopor Mat 2009, 118(1):169-175. http://www.sciencedirect.com/science/article/pii/S1387181108004277 [19] CHU N, WANG J, ZHANG Y, YANG J, LU J, YIN D. Nestlike hollow hierarchical MCM-22 microspheres:synthesis and exceptional catalytic properties[J]. Chem Mater, 2010, 22(9):2757-2763. doi: 10.1021/cm903645p [20] XU C, LIU H, JIA M, GUAN J, WU S, WU T, KAN Q. Methane non-oxidative aromatization on Mo/ZSM-5:Effect of adding triethoxyphenylsilanes into the synthesis system of ZSM-5[J]. Appl Surf Sci, 2011, 257(7):2448-2454. doi: 10.1016/j.apsusc.2010.10.001 [21] LIU H, YANG S, HU J, SHANG F, LI Z, XU C, GUAN J, KAN Q. A comparison study of mesoporous Mo/H-ZSM-5 and conventional Mo/H-ZSM-5 catalysts in methane non-oxidative aromatization[J]. Fuel Process Technol, 2012, 96:195-202. doi: 10.1016/j.fuproc.2011.12.034 [22] HU J, WU S, LIU H, DING H, LI Z, GUAN J, KAN Q. Effect of mesopore structure of TNU-9 on methane dehydroaromatization[J]. RSC Adv, 2014, 4(51):26577-26584. doi: 10.1039/c4ra03945a [23] FANG Y, HU H, CHEN G. In situ assembly of zeolite nanocrystals into mesoporous aggregate with single-crystal-like morphology without secondary template[J]. Chem Mater, 2008, 20(5):1670-1672. doi: 10.1021/cm703265q [24] CHU N, YANG J, WANG J, YU S, LU J, ZHANG Y, YIN D. A feasible way to enhance effectively the catalytic performance of methane dehydroaromatization[J]. Catal Commun, 2010, 11(6):513-517. doi: 10.1016/j.catcom.2009.12.004 [25] CUNDY C S, COX P A. The hydrothermal synthesis of zeolites:Precursors, intermediates and reaction mechanism[J]. Cheminform, 2005, 82(1/2):1-78. http://www.sciencedirect.com/science/article/pii/S1387181105000934 [26] WU J, WANG B, LI N, XIANG S. Effect of aging method on the synthesis of MCM-22 zeolite in fluoride system[J]. Chin J Catal, 2006, 27(7):585-590. http://en.cnki.com.cn/Article_en/CJFDTOTAL-CHUA200607013.htm [27] ALFARO S, RODRIGUEZ C, VALENZUELA M A, BOSCH P. Aging time effect on the synthesis of small crystal LTA zeolites in the absence of organic template[J]. Mater Lett, 2007, 61(23/24):4655-4658. http://www.sciencedirect.com/science/article/pii/S0167577X07002339 [28] YANG X, TIAN G, CHEN L, LI Y, ROOKE J C, WEI Y, LIU Z, DENG Z, VAN T G, SU B. Well-organized zeolite nanocrystal aggregates with interconnected hierarchically micro-meso-macropore systems showing enhanced catalytic performance[J]. Chemistry, 2011, 17(52):14987-14995. doi: 10.1002/chem.201101594