| 131 | 1 | 157 |
| 下载次数 | 被引频次 | 阅读次数 |
在大孔α-Al_2O3载体上采用二次水热生长法制备silicalite-1沸石膜。为了弥补沸石膜的缺陷并提高其疏水性,利用甲基三乙氧基硅烷(MTES)和正硅酸四乙酯(TEOS)水解共聚后的杂化有机硅Me-SiO2对沸石膜进行修饰改性。结果表明,形成的Me-SiO2溶胶平均粒径18 nm,经N2吸脱附等温线测试,表明其具有微介孔性质(孔径1.5和3.0 nm);经凝胶化后形成疏水性的Me-SiO2/silicalite-1复合膜,其厚度分别为500 nm/10μm,表面静态接触角可达134°。在渗透汽化分离低质量分数乙醇/水时,经Me-SiO2修饰的silicalite-1膜渗透侧的水通量约为未修饰前的1/4,而在增加的膜层阻力下乙醇通量仍然得到保持甚至提高。这说明Me-SiO2修饰了膜的亲水缺陷,增强了乙醇的吸附和对水的排斥,从而提高了脱醇性能。通过优化溶胶质量分数,2.0%Me-SiO2溶胶修饰silicalite-1膜的分离性能达到最佳,在温度为60℃、质量分数为5%乙醇/水溶液中,渗透通量达到4.3 kg·m-2·h-1,分离因子为24.5。
Abstract:Silicalite-1 zeolite membranes were prepared by a secondary hydrothermal growth method on macroporous α-Al_2O3 support.In order to improve defects and hydrophobicity,the zeolite membranes were modified by Me-Si O2 sols prepared via hydrolysis and copolymerization of methyl triethoxy silane (MTES) and tetraethyl orthosilicate (TEOS).The results show that the average particle size of the Me-SiO2 sols is 18 nm,and it has micro-mesoporous structures (1.5 and 3.0 nm) analyzed by N2 adsorption-desorption isotherms.The hydrophobic Me-SiO2/silicalite-1 composite membranes were formed with a composite thickness of 500 nm/10μm and surface static contact angles up to 134°after gelation.In pervaporation of low-concentration ethanol/water,the water flux on the permeate side of the Me-SiO2 modified silicalite-1 membrane was 4 times lower than that of the unmodified one,while the ethanol flux was maintained or even increased with increased layer resistance.The results indicate that Me-SiO2 layer reduced hydrophilic defects,which enhances ethanol adsorption and water repulsion.2.0%Me-Si O2 modified silicalite-1 membranes showed optimized separation performance.In the pervaporation of 5%ethanol/water mixtures at 60℃,the permeation flux was 4.3 kg·m-2·h-1 with a separation factor of 24.5.
[1]陈俊任,陈清.中国燃料乙醇行业健康发展途径探析[J].国际石油经济, 2017, 58(4):52-58.CHEN J R, CHEN Q. Approach to healthy development of China’s fuel ethanol industry[J]. International Petroleum Economics,2017, 58(4):52-58.
[2] UENO K, NEGISHI H, MIYAMOTO M, et al. Effect of Si/Al ratio and amount of deposited MFI-type seed crystals on the separation performance of silicalite-1 membranes for ethanol/water mixtures in the presence of succinic acid[J]. Microporous and Mesoporous Materials, 2018, 267:1-8.
[3] KHAN A, ALI M, ILYAS A, et al. ZIF-67 filled PDMS mixed matrix membranes for recovery of ethanol via pervaporation[J].Separation and Purification Technology, 2018, 206:50-58.
[4] LI J, ZHOU W, FAN S, et al. Bioethanol production in vacuum membrane distillation bioreactor by permeate fractional condensation and mechanical vapor compression with polytetrafluoroethylene(PTFE)membrane[J]. Bioresource Technology, 2018, 268:708-714.
[5] ZHUANG X J, CHEN X R, SU Y, et al. Surface modification of silicalite-1 with alkoxysilanes to improve the performance of PDMS/silicalite-1 pervaporation membranes:Preparation, characterization and modeling[J]. Journal of Membrane Science, 2016,499:386-395.
[6]韶晖,周轶,钟璟,等.用于分离DMF/H2O体系的Me-silicalite-1渗透汽化分子筛膜的制备[J].高校化学工程学报, 2014,28(5):965-970.SHAO H, ZHOU Y, ZHONG J, et al. Preparation of Me-silicalite-1 zeolite membrane for pervaporation separation of DMF/H2O mixtures[J]. Journal of Chemical Engineering of Chinese Universities, 2014, 28(5):965-970.
[7] LIU Y, QIANG W L, JI T T, et al. Uniform hierarchical MFI nanosheets prepared via anisotropic etching for solution-based sub-100-nm-thick oriented MFI layer fabrication[J]. Science Advances, 2020, 6(7):5993.
[8] ALGIERI C, DRIOLI E. Zeolite membranes:Synthesis and applications[J]. Separation and Purification Technology, 2021, 278:119295.
[9] MA X, WU X, CARO J, et al. Seeding-free synthesis of high-performance MFI zeolite membranes on super hydrophobic supports inspired by “like grows like” principle[J]. Microporous and Mesoporous Materials, 2019, 288:109589.
[10] PENG P, LAN Y Q, LIANG L, et al. Membranes for bioethanol production by pervaporation[J]. Biotechnology for Biofuels, 2021,14(1):10.
[11] LI Y C, ZHU G F, WANG Y, et al. Preparation mechanism and applications of oriented MFI zeolite membranes:A review[J].Microporous and Mesoporous Materials, 2021, 312:110790.
[12] UENO K, NEGISHI H, OKUNO T, et al. Effects of seed crystal type on the growth and microstructures of silicalite-1 membranes on tubular silica supports via gel-free steam-assisted conversion[J]. Microporous and Mesoporous Materials, 2019, 289:109645.
[13]张雄福,刘海鸥,王安杰,等.沸石晶种层形成的影响因素及其对silicalite-1型沸石膜生长的影响[J].高校化学工程学报,2006, 20(4):520-526.ZHANG X F, LIU H O, WANG A J, et al. Factors affecting the formation of zeolite seed layers on different porous supports and effects of seed layers on the growth of zeolite membranes[J]. Journal of Chemical Engineering of Chinese Universities, 2006,20(4):520-526.
[14]刘剑,鄢瑛,张会平.二次生长法制备微纤复合纯硅分子筛膜[J].高校化学工程学报, 2015, 29(2):431-436.LIU J, YAN Y, ZHANG H P. Preparation of microfibrous supported silicalite-1 zeolite membrane by secondary growth method[J].Journal of Chemical Engineering of Chinese Universities, 2015, 29(2):431-436.
[15] ZHOU H L, SU Y, CHEN X R, et al. Modification of silicalite-1 by vinyltrimethoxysilane(VTMS)and preparation of silicalite-1 filled polydimethylsiloxane(PDMS)hybrid pervaporation membranes[J]. Separation and Purification Technology, 2010, 75(3):286-294.
[16] CHOI J, JEONG H K, MARK A, et al. Grain boundary defect elimination in a zeolite membrane by rapid thermal processing[J].Science, 2009, 325(5940):590-593.
[17] NG E P, MINTOVA S. Nanoporous materials with enhanced hydrophilicity and high water sorption capacity[J]. Microporous and Mesoporous Materials, 2008, 114(1/2/3):1-26.
[18] KOLLER H, LOBO R F, BURKETT S L, et al. SiO-...HOSi hydrogen bonds in As-synthesized high-silica zeolites[J]. Journal of Physical Chemistry, 1995, 99(33):12588-12596.
[19] LAN J, SAULAT H, WU H, et al. Manipulation on microstructure of MFI membranes by binary structure directing agents[J].Microporous and Mesoporous Materials, 2020, 299:110128.
[20]刘秀凤,柳伟,郑孟瑶,等.多孔α-Al2O3载体上silicalite-1膜表面改性与选择性透醇分析[J].无机化学学报, 2014, 30(12):2706-2712.LIU X F, LIU W, ZHENG M Y, et al. α-Al2O3 supported silicalite-1 membrane:Surface modification and performance on selective permeation of ethanol[J]. Chinese Journal of Inorganic Chemistry, 2014, 30(12):2706-2712.
[21]龚亮,赵明,柴丽均,等.透醇silicalite-2沸石膜制备及其疏水改性[J].膜科学与技术, 2021, 41(1):24-32.GONG L, ZHAO M, CHAI L J, et al. Preparation and hydrophobic modification of ethanol perm-selective silicalite-2 zeolite membrane[J]. Membrane Science and Technology, 2021, 41(1):24-32.
[22] REN X X, TSURU T. Organosilica-based membranes in gas and liquid phase separation[J]. Membranes, 2019, 9(9):107.
[23] CASTRICUM H L, SAH A, MITTELMEIJER-HAZELEGER M C, et al. Microporous structure and enhanced hydrophobicity in methylated SiO2 for molecular separation[J]. Journal of Materials Chemistry, 2007, 17(15):1509-1517.
[24] MA Y, KANEZASHI M, TSURU T. Preparation of organic/inorganic hybrid silica using methyltriethoxysilane and tetraethoxysila ne as co-precursors[J]. Journal of Sol-Gel Science and Technology, 2010, 53(1):93-99.
[25]张晓晓,王晓东,任春风,等.合成条件对Silicalite-1沸石分子筛形貌的影响[J].太原理工大学学报, 2014, 45(3):315-318.ZHANG X X, WANG X D, REN C F, et al. Influence of synthesis conditions on the morphology of silicalite-1 zeolite[J]. Journal of Taiyuan University of Technology, 2014, 45(3):315-318.
[26] KANEZASHI M, YONEDA Y, NAGASAWA H, et al. Gas permeation properties for organosilica membranes with different Si/C ratios and evaluation of microporous structures[J]. American Institute of Chemical Engineers Journal, 2017, 63(10):4491-4498.
[27] WANG J H, KANEZASHI M, YOSHIOKA T, et al. Effect of calcination temperature on the PV dehydration performance of alcohol aqueous solutions through BTESE-derived silica membranes[J]. Journal of Membrane Science, 2012, 415:810-815.
[28] KANEZASHI M, KAWANO M, YOSHIOKA T, et al. Organic-inorganic hybrid silica membranes with controlled silica network size for propylene/propane separation[J]. Industrial Engineering&Chemistry Research, 2021, 51(2):944-953.
[29] DENG Z, NICOLAS C H, GUO Y, et al. Synthesis and characterization of nanocomposite B-MFI-alumina hollow fiber membranes and application to xylene isomer separation[J]. Microporous and Mesoporous Materials, 2010, 133(1/2/3):18-26.
[30] YI S L, SU Y, WAN Y H. Preparation and characterization of vinyltriethoxysilane(VTES)modified silicalite-1/PDMS hybrid pervaporation membrane and its application in ethanol separation from dilute aqueous solution[J]. Journal of Membrane Science,2010, 360(1/2):341-351.
[31]任秀秀,夏凌云,钟璟.平板陶瓷载体上SiO2-ZrO2膜的制备及其纳滤性能研究[J].膜科学与技术, 2021, 41(6):110-117.REN X X, XIA L Y, ZHONG J. Nanofiltration performance of SiO2-ZrO2 membrane prepared on flat ceramic support[J]. Membrane Science and Technology, 2021, 41(6):110-117.
[32] SUN W G, WANG X W, YANG J H, et al. Pervaporation separation of acetic acid-water mixtures through Sn-substituted ZSM-5zeolite membranes[J]. Journal of Membrane Science, 2009, 335(1/2):83-88.
[33] PENG Y, ZHAN Z Y, SHAN L J, et al. Preparation of zeolite MFI membranes on defective macroporous alumina supports by a novel wetting-rubbing seeding method:Role of wetting agent[J]. Journal of Membrane Science, 2013, 444:60-69.
[34] ZHOU H, ZHANG J Q, WAN Y H, et al. Fabrication of high silicalite-1content filled PDMS thin composite pervaporation membrane for the separation of ethanol from aqueous solutions[J]. Journal of Membrane Science, 2017, 524:1-11.
[35] SHEN D, XIAO W, YANG J H, et al. Synthesis of silicalite-1 membrane with two silicon source by secondary growth method and its pervaporation performance[J]. Separation and Purification Technology, 2011, 76(3):308-315.
[36] KOSINOV N, SRIPATHI V G P, HENSEN E J M. Improving separation performance of high-silica zeolite membranes by surface modification with triethoxyfluorosilane[J]. Microporous and Mesoporous Materials, 2014, 194:24-30.
基本信息:
中图分类号:TQ028.8;TQ223.122
引用信息:
[1]于欢,任秀秀,徐荣,等.疏水微介孔Me-SiO_2改性silicalite-1膜用于脱醇性能研究[J],2022,36(05):675-683.
基金信息:
中国石油化工股份有限公司科技项目(420037);; 武进区科技支撑(社会发展)项目(WS2018327);; 江苏省精细石油化工重点实验室开放课题(KF1904)