期刊文献+

NaA 沸石膜的制备及在一氯甲烷脱水中的应用 被引量:9

Preparation of NaA Membrane and Application on Dehydration of Chloromethane
原文传递
导出
摘要 以氢氧化钠、铝酸钠和硅溶胶为原料,利用热浸渍提拉法预涂晶种,在孔径为2~3μm的亲水性α-Al2O3载体和孔径为800nm的疏水性炭载体上制备NaA沸石膜。借助于X射线衍射和扫描电子显微镜对合成的沸石膜进行了表征,采用单组分气体渗透法对NaA沸石膜的气体渗透性能进行了检测。结果表明:当H2渗透通量相近时,在亲水性α-Al2O3载体上制备的NaA沸石膜对H2/n-C4H10的分离因数为27.6,远远高于在疏水性炭载体上制备的NaA沸石膜的分离因数。NaA沸石膜在α-Al2O3载体上的生长速率为1.0μm/h,比在炭载体上生长速率快1倍,说明亲水性α-Al2O3载体更适合作为制备致密的强亲水性NaA沸石膜的载体。将在α-Al2O3载体上制备的NaA沸石膜用于一氯甲烷脱水实验,当进料水含量为0.252%(质量分数)时,水/一氯甲烷的分离因数为7.5×104。 Zeolite NaA membranes were synthesized on a hydrophilic α-Al2O3 support of 2-3 μm aperture and the hydrophobic car- bon support of 800 nm aperture with NaOH, NaAlO2 and colloidal silica as raw materials by a hot dip-coating pulling seeding method. The as-synthesized membranes were characterized by X-ray diffraction and scanning electron microscope. The gas permeation per- formance of NaA membranes was examined via the single component gas permeation experiments. The results indicate that when H2 flux of the membranes are similar, a H2/n-C4H10 separation factor of the membranes grown on α-Al2O3 support is 27.6, which is greater than that of the membranes grown on carbon support. The growth rate of NaA membrane on the α-Al2O3 support was 1.0 μm/h, which was twice greater than that on the carbon support. This indicated that the hydrophilic α-Al2O3 support was more suitable for the preparation of compact highly-hydrophilic NaA membranes rather than the hydrophobic carbon support. The dehydration of chloro- methane with the NaA membrane grown on the α-Al2O3 support was investigated. The separation factor of 7.5 × 10^4 was obtained at a water feed concentration of 0.252% (in mass).
出处 《硅酸盐学报》 EI CAS CSCD 北大核心 2012年第9期1363-1368,共6页 Journal of The Chinese Ceramic Society
基金 武汉科技大学绿色制造与节能减排科技研究中心开放基金(B0917) 武汉市科技攻关项目(20081113462)资助
关键词 NAA 沸石膜 亲水性载体 热浸渍提拉法 蒸汽渗透 一氯甲烷 脱水 NaA membrane hydrophilic support hot dip-coating pulling method vapor permeation chloromethane dehydration
  • 相关文献

参考文献21

  • 1ZHANG Xiongfu, WANG Jinqu, LIU Haiou, et al. Factors affecting the synthesis of hetero-atom zeolite Fe-ZSM-5 membrane [J]. Sep Purif Teehnol, 2003, 32(1/3): 151-158.
  • 2SHIFLETT M B, FOLEY H C. Ultrasonic deposition of high-selectivity nanoporous carbon membranes [J]. Science, 1999, 285(5435): 1902-1905.
  • 3路绪旺,汤志刚.支撑ZSM-5沸石膜在不同载体上的一次水热合成[J].硅酸盐学报,2004,32(10):1209-1213. 被引量:1
  • 4周荣飞,陈祥树,刘丹,漆虹,林晓,徐南平.清液体系中高性能T型沸石分子筛膜的合成(英文)[J].硅酸盐学报,2007,35(9):1270-1272. 被引量:6
  • 5李显明,王正宝,郑洁,邵世群,王胤超,严玉山.动态水热合成b轴取向MFI型分子筛膜[J].催化学报,2011,32(2):217-223. 被引量:8
  • 6LI Yongsheng, WANG Jinqu, SHI Jianlin, et al, Synthesis of ZSM-5 zeolite membranes with large area on porous, tubular α-Al2O3 supports [J]. Sep Purif Technol, 2003, 32(1/3): 397-401.
  • 7HASEGAWA Y, NAGASE T, KIYOZUMI Y, et al. Influence of acid on the permeation properties of NaA-type zeolite membranes [J]. J Membr Sci, 2010, 349(1/2): 189-194.
  • 8PINA M P, ARRUEBO M, FELIPE M, et al. A semi-continuous method for the synthesis of NaA zeolite membranes on tubular supports [J]. J Membr Sei, 2004, 244(1/2): 141-150.
  • 9GE Qinqin, SHAO Jia, WANG Zhengbao, et al. Effects of the synthesis hydrogel on the formation of zeolite LTA membranes [J]. Microporous Mesoporous Mater, 2012, 151: 303-310.
  • 10XU Xiaochun, BAO Yun, SONG Chunshan, et al. Synthesis, characterization and single gas permeation properties of NaA zeolite membrane [J]. J Membr Sci, 2005, 249(1/2): 51-64.

二级参考文献15

  • 1陈红亮,李砚硕,刘杰,杨维慎,林励吾.利用原位水热合成在二氧化硅陶瓷管上制备高性能的Silicalite-1分子筛膜(英文)[J].催化学报,2005,26(12):1039-1041. 被引量:1
  • 2[1]LAI Zhiping,BONILLA G.Microstructural optimization of a zeolite membrane for organic vapor separation .Science,2003,300:456-460.
  • 3[2]BERNAL M P,CORONAS J.Coupling of reaction and separation at the microscopic level: esterification processes in a HZSM5 membrane reactor .Chem Eng Sci,2002,57(9): 1 557-1 562.
  • 4[5]OUDSHOORN O L,JANISSEN M.A novel structured catalyst packing for catalytic distillation of ETBE .Chem Eng Sci,1999,54(10): 1 413-1 418.
  • 5KONDO M,MORIGAMI Y,OKAMOTO K I,et al.Process for producing a T-type zeolite membrane on a porous support for separating a mixture[P].Eur Patent,0976440.2000-02-20.
  • 6KITA H,OKAMOTO K I,YAMAMURA T,et al.Zeolite membranes for fuel ethanol production[J].Fuel Chem Division Preprints,2003,35(1):p438.
  • 7CUI Y,KITA H,OKAMOTO K I.Zeolite T membrane:preparation,characterization,pervaporation of water/organic liquid mixtures and acid stability[J].J Membr Sci,2004,236(1-2):17-27.
  • 8CUI Y,KITA H,OKAMOTO K I.Preparation and gas separation performance of zeolite T membrane[J].J Mater Chem,2004,14(5):924-932.
  • 9BRECK D W,ACARA N A,KENMORE N Y,et al.Crystalline zeolite T[P].US Patent,2950952.1960-08-30.
  • 10VEDA S,NISHIMURA M,KOIZUMI M.Synthesis of offretite-erionite type zeolite from solution phase[J].Stud Surf Sci Catal,1985,24:105-110.

共引文献17

同被引文献74

引证文献9

二级引证文献15

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部