利用沸石前躯体溶液和未除模板剂的实心介孔硅球(MSS)为原料,自模板水热法制备具有酸性介孔壳层的中空球形分子筛(HMSS)。对所得材料进行XRD、TEM、N2-吸脱附、27Al MAS NMR、Py-FTIR和NH_3-TPD表征。结果表明:HMSS具有良好的有序性介...利用沸石前躯体溶液和未除模板剂的实心介孔硅球(MSS)为原料,自模板水热法制备具有酸性介孔壳层的中空球形分子筛(HMSS)。对所得材料进行XRD、TEM、N2-吸脱附、27Al MAS NMR、Py-FTIR和NH_3-TPD表征。结果表明:HMSS具有良好的有序性介孔壳层,比表面积高达945.6m^2/g,介孔分布集中在2.7nm,且HMSS表现出中强酸性。合成MSS时留在其介孔孔道中的十六烷基三甲基溴化铵(CTAB)在制备HMSS的过程中起着非常重要的作用,如果使用除去CTAB的MSS为原料,MSS则会完全溶蚀而不能得到HMSS。当萘/异丙醇摩尔比为2、反应温度350℃时,萘的转化率达到95.33%。展开更多
NaA zeolite membranes were prepared by secondary growth method on the outer surface of α-Al2O3 hollow fiber supports. Vacuum seeding method was used for planting zeolite seeds on the support surfaces. Hydrothermal cr...NaA zeolite membranes were prepared by secondary growth method on the outer surface of α-Al2O3 hollow fiber supports. Vacuum seeding method was used for planting zeolite seeds on the support surfaces. Hydrothermal crystallization was then carried out in a synthesis solution with molar ratio of Al2O3：SiO2：Na2O：H2O = 1：2：2：120 at 100 ℃ for 4 h. Effects of seeding conditions on preparation of hollow fiber NaA zeolite membranes were extensively investigated. Moreover, hollow fiber membrane modules with packing membrane areas of ca. 0.1 and 0.2 m2 were fabricated to separate ethanol/water mixture. It is found that the thickness of seed layer is obviously affected by seed suspension concentration, coating time and vacuum degree. Close-packing seed layer is required to obtain high-quality membranes. The optimized seeding conditions （seed suspension mass concentration of 0.5%-0.7% coating time of 5 s and vacuum degree of 10 kPa） lead to dense NaA zeolite layer with a thickness of 6-8 gin. Typically, an as-synthesized hollow fiber NaA zeolite membrane exhibits good pervaporation performance with a permeation flux of 7.02 kg· m^- 2· h^- 1 and separation factor 〉 10000 for sepa- ration of 90%; （by mass） ethanol/water mixture at 75 ℃ High reproducibility has been achieved for batch-scale production of hollow fiber NaA zeolite membranes by the hydrothermal synthesis approach.展开更多
This work presents the design of hollow fiber T-type zeolite membrane modules with different geometric configurations. The module performances were evaluated by pervaporation dehydration of ethanol/water mixtures. Str...This work presents the design of hollow fiber T-type zeolite membrane modules with different geometric configurations. The module performances were evaluated by pervaporation dehydration of ethanol/water mixtures. Strong concentration polarization was found for the modules with big membrane bundles. The concentration polarization was enhanced at high temperature due to the higher water permeation flux. The increase of feed flow could improve water permeation flux for the membrane modules with small membrane bundle.Computational fluid dynamics was used to visualize the flow field distribution inside of the modules with different configurations. The membrane module with seven bundles exhibited highest separation efficiency due to the uniform distribution of flow rate. The packing density could be 10 times higher than that of the tubular membrane module. The hollow fiber membrane module exhibited good stability for ethanol dehydration.展开更多
文摘利用沸石前躯体溶液和未除模板剂的实心介孔硅球(MSS)为原料,自模板水热法制备具有酸性介孔壳层的中空球形分子筛(HMSS)。对所得材料进行XRD、TEM、N2-吸脱附、27Al MAS NMR、Py-FTIR和NH_3-TPD表征。结果表明:HMSS具有良好的有序性介孔壳层,比表面积高达945.6m^2/g,介孔分布集中在2.7nm,且HMSS表现出中强酸性。合成MSS时留在其介孔孔道中的十六烷基三甲基溴化铵(CTAB)在制备HMSS的过程中起着非常重要的作用,如果使用除去CTAB的MSS为原料,MSS则会完全溶蚀而不能得到HMSS。当萘/异丙醇摩尔比为2、反应温度350℃时,萘的转化率达到95.33%。
基金Supported by the National Basic Research Program of China(2009CB623403)the National Natural Science Foundation of China(21176117,21222602)+3 种基金the Key Project of Chinese Ministry of Education(212060)the Outstanding Young Fund of Jiangsu Province(BK2012040)the"Six Top Talents"of Jiangsu Province,the Natural Science Foundation of the Jiangsu Higher Education Institutions of China(09KJA530002)a project funded by the Priority Academic Program Development of Jiangsu Higher Education Institutions(PAPD)
文摘NaA zeolite membranes were prepared by secondary growth method on the outer surface of α-Al2O3 hollow fiber supports. Vacuum seeding method was used for planting zeolite seeds on the support surfaces. Hydrothermal crystallization was then carried out in a synthesis solution with molar ratio of Al2O3：SiO2：Na2O：H2O = 1：2：2：120 at 100 ℃ for 4 h. Effects of seeding conditions on preparation of hollow fiber NaA zeolite membranes were extensively investigated. Moreover, hollow fiber membrane modules with packing membrane areas of ca. 0.1 and 0.2 m2 were fabricated to separate ethanol/water mixture. It is found that the thickness of seed layer is obviously affected by seed suspension concentration, coating time and vacuum degree. Close-packing seed layer is required to obtain high-quality membranes. The optimized seeding conditions （seed suspension mass concentration of 0.5%-0.7% coating time of 5 s and vacuum degree of 10 kPa） lead to dense NaA zeolite layer with a thickness of 6-8 gin. Typically, an as-synthesized hollow fiber NaA zeolite membrane exhibits good pervaporation performance with a permeation flux of 7.02 kg· m^- 2· h^- 1 and separation factor 〉 10000 for sepa- ration of 90%; （by mass） ethanol/water mixture at 75 ℃ High reproducibility has been achieved for batch-scale production of hollow fiber NaA zeolite membranes by the hydrothermal synthesis approach.
基金Supported by the National Natural Science Foundation of China(21222602,21490585 and 21176117)National High-tech R&D Program of China(2015AA03A602)+4 种基金the Key Project of Chinese Ministry of Education(212060)the Outstanding Young Fund of Jiangsu Province(BK2012040)Young Fund of Jiangsu Province(BK20130915)the "Six Top Talents" and "333 Talent Project" of Jiangsu Province,a project funded by the Priority Academic Program Development of Jiangsu Higher Education Institutions(PAPD)the Innovation Project for Graduate Student of Jiangsu Province(KYLX15-0790)
文摘This work presents the design of hollow fiber T-type zeolite membrane modules with different geometric configurations. The module performances were evaluated by pervaporation dehydration of ethanol/water mixtures. Strong concentration polarization was found for the modules with big membrane bundles. The concentration polarization was enhanced at high temperature due to the higher water permeation flux. The increase of feed flow could improve water permeation flux for the membrane modules with small membrane bundle.Computational fluid dynamics was used to visualize the flow field distribution inside of the modules with different configurations. The membrane module with seven bundles exhibited highest separation efficiency due to the uniform distribution of flow rate. The packing density could be 10 times higher than that of the tubular membrane module. The hollow fiber membrane module exhibited good stability for ethanol dehydration.
