Effects of sugars on the structure of SAPO-34 and its MTO performance
-
摘要: 以廉价的木糖、蔗糖、淀粉和葡甘聚糖为硬模板剂成功合成出含多级孔道的SAPO-34分子筛,采用XRD、BET、SEM、TEM、ICP和NH3-TPD等手段对催化剂进行了表征,并在固定床上,研究了糖类硬模板剂对SAPO-34分子筛的结构以及MTO性能的影响。结果表明,糖类硬模板剂能够提升SAPO-34分子筛的比表面积、微孔和介孔体积。与常规SAPO-34分子筛相比,多级孔道SAPO-34分子筛的双烯选择性和寿命均高。介孔体积最大、酸量最少、酸性最弱的SAPO-34-z分子筛的寿命最长(130 min),高出常规SAPO-34分子筛(100 min)30%,分子筛寿命从长到短顺序为SAPO-34-z > SAPO-34-h > SAPO-34-d > SAPO-34-m > SAPO-34 > SAPO-34-p。含多级孔道的SAPO-34分子筛的双烯选择性均高于常规SAPO-34分子筛。Abstract: Hierarchical SAPO-34 zeolites were successfully synthesized using cheap xylose, sucrose, starch and glucomannan as hard template and characterized by means of XRD, BET, SEM, TEM, ICP and NH3-TPD. The effects of sugar hard template on the structure and MTO properties of as-prepared SAPO-34 zeolites were studied on a fixed bed. The results showed that introduction of carbohydrate hard template could increase the specific surface area, microporous and mesoporous volume of SAPO-34 zeolites. The olefin selectivity and lifetime of SAPO-34 were both higher than those of ordinary SAPO-34. The SAPO-34-z with the largest mesoporous volume, the least acidity amounts and the weakest acidity showed the longest lifetime (130 min), which was 30% longer than that of ordinary SAPO-34 (100 min). The lifetime of zeolites decreased in the order of SAPO-34-z > SAPO-34-h > SAPO-34-d > SAPO-34-m > SAPO-34 > SAPO-34-p. The olefin selectivity of hierarchical SAPO-34 zeolites is higher than that of conventional SAPO-34 zeolites.
-
Key words:
- methanol /
- SAPO-34 /
- olefin /
- hierarchical
-
表 1 SAPO-34分子筛的比表面积、孔体积和平均孔径
Table 1 Specific surface area, pore volume and average pore diameter of different SAPO-34
Zeolite Specific surface area A/(m2·g-1) Volume/(cm3·g-1) Average pore size d/nm vmicro vmeso SAPO-34 249.2 0.106 0.006 13.1 SAPO-34-p 467.3 0.212 0.009 26.7 SAPO-34-m 482.9 0.215 0.020 12.7 SAPO-34-z 441.7 0.201 0.024 13.5 SAPO-34-d 507.6 0.241 0.012 24.3 SAPO-34-h 499.4 0.223 0.012 12.5 表 2 SAPO-34分子筛的ICP分析
Table 2 ICP of different SAPO-34
Zeolite Chemical composition /% Si Al P O SAPO-34 9.82 18.81 18.96 52.41 SAPO-34-p 7.02 20.84 19.90 52.23 SAPO-34-m 5.3 21.81 20.73 52.17 SAPO-34-z 4.25 22.67 20.98 52.09 SAPO-34-d 8.00 20.23 19.49 52.27 SAPO-34-h 5.35 21.48 20.94 52.23 表 3 不同SAPO-34分子筛的产物分布
Table 3 Product distribution of different SAPO-34
Product Yield w/% SAPO-34 SAPO-34-p SAPO-34-m SAPO-34-z SAPO-34-d SAPO-34-h CH4 1.6 1.7 0.7 0.3 0.8 0.1 C2H4 37.8 38.6 41.5 39.9 40.5 42.6 C2H6 2.0 2.3 2.0 1.6 1.6 1.7 C3H6 36.8 36.1 36.1 36.5 36.0 35.4 C3H8 6.8 7.2 7.0 7.7 5.5 7.8 C4 13.2 8.6 11.1 12.4 11.8 10.2 C5+C5+ 1.7 5.4 1.5 1.5 3.7 2.1 H2 0.1 0.1 0.1 0.1 0.1 0.1 ΣC2=+C3= 74.7 74.8 77.6 76.3 76.5 78.0 -
[1] SUN C, WANG Y Q, WANG Z, CHEN H B, WANG X, LI H Y, SUN L Y, FAN C Y, WANG C, ZHANG X. Fabrication of hierarchical ZnSAPO-34 by alkali treatment with improved catalytic performance in the methanol-to-olefin reaction[J]. C R Chim, 2018, 21(1):61-70. doi: 10.1016/j.crci.2017.11.006 [2] ANDREW H, THUY T L, SHI Z N, DAI H, JEFFREY D R, ADITYA B. Effects of diffusional constraints on lifetime and selectivity in methanol-to-olefins catalysis on HSAPO-34[J]. J Catal, 2019, 369:122-132. doi: 10.1016/j.jcat.2018.10.031 [3] REN S, LIU G J, WU X, CHEN X Q, WU M H, ZENG G F, LIU Z Y, SUN Y H. Enhanced MTO performance over acid treated hierarchical SAPO-34[J]. Chin J Catal, 2017, 38(1):123-130. doi: 10.1016/S1872-2067(16)62557-3 [4] WANG J, YANG M F, SHANG W J, SU X P, HAO Q Q, CHEN H Y, MA X X. Synthesis, characterization, and catalytic application of hierarchical SAPO-34 zeolite with three-dimensionally ordered mesoporous-imprinted structure[J]. Microporous Mesoporous Mater, 2017, 252(1):10-16. http://cn.bing.com/academic/profile?id=a6fe05c77d12582d143382329816a12f&encoded=0&v=paper_preview&mkt=zh-cn [5] YANG B, ZHAO P B, MA J H, LI R F. Synthesis of hierarchical SAPO-34 nanocrystals with improved catalytic performance for methanol to olefins[J]. Chem Phys Lett, 2016, 665:59-61. doi: 10.1016/j.cplett.2016.10.052 [6] ALI Z V, JAFAR T, SAEED S. Carbon nanotube templated synthesis of metal containing hierarchical SAPO-34 catalysts:Impact of the preparation method and metal avidities in the MTO reaction[J]. Microporous Mesoporous Mater, 2016, 236:1-12. doi: 10.1016/j.micromeso.2016.08.027 [7] FENG R, WANG X X, LIN J W, LI Z, HOU K, YAN X L, HU X Y, YAN Z F, MARK J, ROOD S. Two-stage glucose-assisted crystallization of ZSM-5 to improve methanol to propylene (MTP)[J]. Microporous Mesoporous Mater, 2018, 270:57-66. doi: 10.1016/j.micromeso.2018.05.003 [8] ZHANG C, LU X C, WANG T Z. Synthesis of SAPO-34 using metakaolin in the presence of β-cyclodextrin[J]. J Energy Chem, 2015, 24(4):401-406. doi: 10.1016/j.jechem.2015.06.008 [9] VENNA S R, CARREON M A. Synthesis of SAPO-34 crystals in the presence of crystal growth inhibitors[J]. J Phys Chem B, 2008, 112(51):16261-16265. doi: 10.1021/jp809316s [10] LIU X F, DU S Y, ZHANG B Q. Seeded growth of dense and thin SAPO-34 membranes on porous α-Al2O3 substrates under microwave irradiation[J]. Mater Lett, 2013, 91:195-197. doi: 10.1016/j.matlet.2012.09.076 [11] 张强, 马晓月, 刘璐.晶种存在形态对所合成的SAPO-34分子筛性质及其甲醇转化催化性能的影响[J].燃料化学学报, 2018, 46(10):1225-1230. doi: 10.3969/j.issn.0253-2409.2018.10.010ZHANG Qiang, MA Xiao-yue, LIU Lu. Effect of seed form on the structure and properties of as-synthesized SAPO-34 molecular sieves and their catalytic performance in the conversion of methanol to olefins[J]. J Fuel Chem Technol, 2018, 46(10):1225-1230. doi: 10.3969/j.issn.0253-2409.2018.10.010 [12] LEE Y J, BAEK S C, JUN K L. Methanol conversion on SAPO-34 catalysts prepared by mixed template method[J]. Appl Catal A:Gen, 2009, 329:130-136. [13] HUSSEIN B, JAFAR T D, MEHDI S. Simultaneous effects of water, TEAOH and morpholine on SAPO-34 synthesis and its performance in MTO process[J]. Microporous Mesoporous Mater, 2018, 261:111-118. doi: 10.1016/j.micromeso.2017.11.011 [14] IZADBAKHSH A, FARHADI F, KHORASHEH F, SAHEBDELFAR S, ASADI M, YAN Z F. Effect of SAPO-34's composition on its physicochemical properties and deactivation in MTO process[J]. Appl Catal A:Gen, 2009, 364(1/2):48-56. http://cn.bing.com/academic/profile?id=f6732c39d3010bde15988716d8ada759&encoded=0&v=paper_preview&mkt=zh-cn [15] AGHAMOHAMMADI S, HAGHIGHI M. Dual-template synthesis of nanostructured CoAPSO-34 used inmethanol to olefins:Effect of template combinations on catalytic performance and coke formation[J]. Chem Eng J, 2015, 264:359-375. doi: 10.1016/j.cej.2014.11.102 [16] MARCHESE L, CHEN J, WRIGHT P A, THAMOS J M. Formation of hydronium at the broensted site in SAPO-34 catalysts[J]. J Chem Phys, 1993, 97(31):8109-8112. doi: 10.1021/j100133a001 [17] WANG W, SEILER M, HUNGER M. Role of surfacemethoxy species in the conversion of methanol todimethyl ether on acidic zeolites investigated by in situstopped-flow MAS NMR spectroscopy[J]. J Phys Chem B, 2001, 105:12553-12558. doi: 10.1021/jp0129784 [18] SONG W, HAW J F, NICHOLAS J B, HENEGHAN C S. Methylbenzenes are the organic reaction centers for methanol-to-olefin catalysis on H-SAPO-34[J]. J Am Chem Soc, 2000, 122(43):10726-10727. doi: 10.1021/ja002195g [19] TAN J, LIU Z M, BAO X H, LIU X C, HAN X W, HE C Q, ZHAI R S. Crystallization and Si Incorporation mechanisms of SAPO-34[J]. Microporous Mesoporous Mater, 2002, 53(1/3):97-108. http://cn.bing.com/academic/profile?id=4ce859a7636293cd8fdc9e05542f558f&encoded=0&v=paper_preview&mkt=zh-cn