a-Al2O3中空纤维支撑体的制备与表征 |
作者:徐吉上,何勇,顾学红, 金万勤 |
单位: 南京工业大学化学化工学院, 材料化学工程国家重点实验室, |
关键词: 干-湿法纺丝; ?-Al2O3; 中空纤维支撑体; NaA; 分子筛膜 |
DOI号: |
分类号: TQ343.41 |
出版年,卷(期):页码: 2011,31(2):19-23 |
摘要: |
采用干-湿法纺丝技术制备了?-Al2O3中空纤维支撑体, 系统研究了Al2O3/PESf(聚醚砜)原料比、焙烧温度、保温时间以及原料粒径等因素对支撑体结构性能的影响. 优化的支撑体渗透性为4.09×10-5 mol•s-1•m-2•Pa-1, 弯曲强度为142.7 MPa, 最大孔径与平均孔径分别为0.66 μm和0.56 μm. 在该支撑体上合成了NaA分子筛膜, 其水/乙醇分离因子>5000, 通量达7.37 kg•m-2 •h-1. |
a-Al2O3 hollow fiber supports were prepared by dry-wet spinning process. Effects of Al2O3/PESf(polyethersulfone) ratio, sintering temperature, holding time and particle size of raw material on structure and performances of supports were studied systematically. The optimized hollow fiber support had the permeance of 4.09×10-5 mol•s-1•m-2•Pa-1, bending strength of 142.7 MPa, maximum pore diameter of 0.66 μm and average pore diameter of 0.56 μm. The NaA zeolite membrane was synthesized on the optimized support, which showed the separation factor of water/ethanol of >5000 and the flux up to 7.37 kg•m-2 •h-1. |
基金项目: |
国家自然科学基金(20706030, U0834004); 973计划(2009CB623403); 江苏省高校自然科学基金(09KJA530002); 教育部和南京市留学回国人员基金. |
作者简介: |
徐吉上(1984-), 男, 江苏徐州人, 在读硕士, 从事膜材料制备与分离. *通讯联系人 |
参考文献: |
[1] 徐南平, 邢卫红, 赵宜江. 无机膜分离技术与应用[M]. 北京:化学工业出版社, 2004.1~4. [2] Hsieh H P. General characteristics of inorganic membranes, in: Ramesh R. Bhave (Ed.), Book of Inorganic membranes synthesis, characteristics and applications[M]. New York: Elsevier Science, 1991. 65~93. [3] Mulder M. 膜技术基本原理[M]. 第二版. 北京:清华大学出版社, 1999. 302~303. [4] Tan Xiaoyao, Liu Shaomin, Li K. Preparation and characterization of inorganic hollow fiber membranes[J]. J Membr Sci, 2001, 188 (1):87~95. [5] Smid J, Avci C G, Günay V, et al. Preparation and characterization of microporous ceramic hollow fibre membranes[J]. J Membr Sci, 1996, 112(1):85~90. [6] 李健生, 郝艳霞, 王连军, 等. 反应结合制备增强氧化铝中空纤维膜[J]. 无机材料学报, 2002, 17(1):180~184. [7] Liu Shaomin, Li K, Hughes R. Preparation of porous aluminium oxide (Al2O3) hollow fiber membranes by a combined phase-inversion and sintering method[J]. Ceram Int, 2003, 29 (9):875~881. [8] Wei C C, Chen O Y, Liu Y, et al. Ceramic asymmetric hollow fiber membranes—One step fabrication process[J]. J Membr Sci, 2008, 320(1~2):191~197. [9] Yin Weining, Meng Bo, Meng Xiuxia, et al. Highly asymmetric yttria stabilized zirconia hollow fiber membranes[J]. J Alloys Compd, 2009, 476(1~2):566~570. [10] Schiestel T, Kilgus M, Peter S, et al. Hollow fiber perovskite membranes for oxygen separation [J]. J Membr Sci, 2005, 258(1~2):1~4. [11] Alshebani A, Pera-Titus M, Landrivon E, et al. Nanocomposite MFI – ceramic hollow fibers: prospects for CO2 separation[J]. Microporous Mesoporous Mater, 2008, 115 (1~2):197~205. [12] Daramola M O, Burger A J, Pera-Titus M, et al. Nanocomposite MFI–ceramic hollow fiber membranes via pore-plugging synthesis: Prospects for xylene isomer separation[J]. J Membr Sci, 2009, 337(1~2):106~112. [13] Xu Xiaochun, Yang Weishen, Liu Jie, et al. Synthesis of NaA zeolite membrane on a ceramic hollow fiber[J]. J Membr Sci, 2004, 229 (1~2):81~85. [14] Wang Zhengbao, Ge Qinqin, Shao Jia, et al. High performance zeolite LTA pervaporation membranes on ceramic hollow fibers by dipcoating-wiping seed deposition[J]. J Am Chem Soc, 2009, 131(20):6910~6911. [15] 张叶, 刘艳梅, 陆双佳,等. NaA分子筛膜的制备及其在醇水脱水中的应用[J]. 南京工业大学学报, 2010, 32(1):41~45. [16] Kondo M, Komori M, Kita H, et al. Tubular-type pervaporation module with zeolite NaA membrane[J]. J Membr Sci, 1997, 133(1):133~141. [17] Sato K, Nakane T. A high reproducible fabrication method for industrial production of high flux NaA zeolite membrane[J]. J Membr Sci, 2007, 301(1~2):151~161. |
服务与反馈: |
【文章下载】【加入收藏】 |
《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-64426130/64433466 传真:010-80485372邮箱:mkxyjs@163.com
京公网安备11011302000819号