您的位置: 专家智库 > >

国家重点基础研究发展计划(G2003CB615802)

作品数:6 被引量:12H指数:3
相关作者:陈红亮杨维慎李砚硕刘杰朱广奇更多>>
相关机构:中国科学院沈阳大学更多>>
发文基金:国家重点基础研究发展计划国家高技术研究发展计划更多>>
相关领域:理学化学工程电子电信更多>>

文献类型

  • 6篇中文期刊文章

领域

  • 4篇理学
  • 2篇化学工程
  • 1篇电子电信

主题

  • 3篇渗透汽化
  • 3篇SILICA...
  • 3篇PERVAP...
  • 2篇渗透汽化性能
  • 2篇SILICA
  • 2篇MEMBRA...
  • 1篇石英管
  • 1篇SEPARA...
  • 1篇SYNTHE...
  • 1篇TUBES
  • 1篇高性能
  • 1篇FILLIN...
  • 1篇REPROD...
  • 1篇HIGH-Q...
  • 1篇HIGH-

机构

  • 3篇中国科学院
  • 2篇沈阳大学

作者

  • 3篇李砚硕
  • 3篇杨维慎
  • 3篇陈红亮
  • 2篇朱广奇
  • 2篇刘杰

传媒

  • 2篇中国科学(B...
  • 2篇Scienc...
  • 1篇科学通报
  • 1篇Scienc...

年份

  • 1篇2009
  • 3篇2008
  • 1篇2007
  • 1篇2006
6 条 记 录,以下是 1-6
排序方式:
Preparation and pervaporation performance of high-quality silicalite-1 membranes
2007年
High-performance silicalite-1 membranes were successfully synthesized on novel porous silica tubes by two-step in-situ hydrothermal synthesis.The flux and separation factor towards ethanol/water mix- ture at 60℃were 0.56 kg/(m2·h)and 84,respectively.The as-synthesized silicalite-1 membranes were characterized by scanning electron microscopy(SEM).The influence of different synthesis conditions on the separation performance of the silicalite-1 membranes was investigated.It was found that the average flux of silicalite-1 membranes was improved by about 26%after filling the silica tubes with mixed solution containing glycerol and water.After calcinating at 400℃for 5 h repeatedly,membrane synthesized on silica tube still showed high pervaporation performance towards ethanol/water mixture even at a calcination rate of 4℃/min,which suggested that silica support was more suitable for pre- paring high-performance silicalite-1 membranes.
CHEN HongLiangLI YanShuoLIU JieYANG WeiShen
关键词:SILICASILICALITE-1MEMBRANEFILLINGPERVAPORATION
高重复性silicalite-1分子筛膜的制备及其渗透汽化性能被引量:4
2008年
利用原位水热合成法在二氧化硅陶瓷管上制备出具有较高重复性的silicalite-1分子筛膜,8个分子筛膜平均分离系数的相对标准偏差(R.S.D.)仅为7.5%.与没有进行填充所制备的分子筛膜相比,通过利用有效的"溶液填充"方法,膜的平均透量提高了49%,80℃分离乙醇/水混合物时,膜的最高透量达到了1.49kg/(m2·h).渗透汽化实验结果表明,silicalite-1分子筛膜60℃分离甲醇/水,乙醇/水,2-丙醇/水和1-丙醇/水混合物时,膜的透量分别为2.63,0.87,0.24和0.20kg/(m2·h),对应的分离系数分别为22,69,81和159.
陈红亮李砚硕朱广奇刘杰杨维慎
高性能silicalite-1分子筛膜的合成及其渗透汽化性能被引量:3
2006年
采用两步原位水热合成法在新型多孔二氧化硅陶瓷管上成功合成出高性能的silicalite-1分子筛膜,60℃时乙醇/水的分离系数达到了84,透量达到了0.56kg/(m2·h).利用扫描电子显微镜(SEM)对其进行了表征;研究了不同合成条件对silicalite-1分子筛膜乙醇/水分离性能的影响.实验结果表明,在相同的合成条件下,利用甘油-水的混合溶液填充陶瓷管载体后,可以提高膜的平均透量约26%.多次活化结果表明,二氧化硅载体上合成的分子筛膜以活化速率4℃/min升温到400℃并活化5h,仍然保持原来的分离选择性.由此说明,二氧化硅载体更适合高性能silicalite-1分子筛膜的制备.
陈红亮李砚硕刘杰杨维慎
关键词:渗透汽化
Synthesis and pervaporation performance of high-reproducibility silicalite-1 membranes被引量:3
2008年
High-reproducibility silicalite-1 membranes were synthesized on silica tubes by in-situ hydrothermal synthesis, and the relative standard deviation (R.S.D.) of average separation factor for eight membranes was only 7.5%. By using an effective method called "solution-filling (SF)", the average flux of membranes prepared with SF method was improved by about 49% compared to membranes prepared without SF method, and the highest flux of membrane prepared with SF method towards ethanol/H2O mixture at 80℃ was 1.49 kg/(m2·h). Pervaporation experiments showed that the fluxes of silicalite-1 membranes at 60℃ were 2.63, 0.87, 0.24, and 0.20 kg/(m2·h) towards methanol/H2O, ethanol/H2O, 2-propanol/H2O, and 1-propanol/H2O mixtures, respectively, and the corresponding separation factors were 22, 69, 81, and159, respectively.
CHEN HongLiangLI YanShuoZhu GuangQiLIU JieYANG WeiShen
关键词:石英管
Synthesis and separation performance of silicalite-1 membranes on silica tubes被引量:1
2009年
High-performance silicalite-1 membranes were synthesized on silica tubes by in-situ hydrothermal synthesis. By using the "solution-filling (SF)" method, the average flux of membranes with the SF method was improved by about 25% compared to that of the membranes without using the SF method; the flux and the separation factor of the membranes prepared with the SF method for an ethanol/water mixture at 60 ℃ were 0.99 kg/(m2·h) and 73, respectively. It was found that the membranes synthesized on silica tubes exhibited high thermal stability and high reproducibility, and the relatively standard deviations (R.S.D.) of the average flux and separation factor were only 9.6% and 5.6%, respectively, which suggests that the silica support is more suitable than other kinds of supports for preparing high-performance silicalite-1 membranes.
CHEN HongLiangLI YanShuoZHU GuangQiYANG WeiShen
关键词:SILICALITE-1MEMBRANESEPARATIONPERVAPORATIONSILICA
二氧化硅陶瓷管上silicalite-1分子筛膜的制备及其分离性能被引量:1
2008年
利用原位水热合成在二氧化硅陶瓷管上制备出高性能的silicalite-1分子筛膜.使用溶液填充方法后,膜的平均透量提高了25%,60℃分离乙醇/水混合物时膜的透量和分离系数分别为0.99kg/(m2·h)和73.实验结果表明,二氧化硅陶瓷管上制备的分子筛膜具有很高的热稳定性和制备重复性,平均透量和分离系数的相对标准偏差(R.S.D.)分别为9.6%和5.6%.这一结果显示,二氧化硅载体更适合制备高性能silicalite-1分子筛膜.
陈红亮李砚硕朱广奇杨维慎
关键词:渗透汽化
共1页<1>
聚类工具0