采用在多孔载体上预涂分子筛晶种及合成分子筛的前驱态溶胶液,再进行水热晶化合成X型分子筛膜.预涂液为0.2%~0.5%的中性悬浮水溶液,预负载晶种的载体二次生长的条件是在95℃下水热处理24~96 h.通过晶化操作3~4次后,多孔载体上负载生长的分子筛膜厚为10~25 μm.采用二次生长成膜法,减少晶化次数,从而缩短了成膜时间.在三次晶化操作后,分子筛膜对He和N2的渗透通量下降为载体渗透通量的1%以下,纯(C4H9)3N和(C4F9)3N的渗透通量之比可达21(350℃);而四次晶化后,渗透侧已检测不出(C4F9)3N存在.
参考文献
[1] | Jia M D;Noble R D;Falconer J L .[P].US 5464798,1995. |
[2] | Yan Y Sh;Davis M E;Gavalas G R .[J].Industrial and Engineering Chemistry Research,1995,34(05):1652. |
[3] | Haag W O;Tsikoyiannis J G .[P].US:5019263,5110478,1990. |
[4] | Kondo M.;Kita H.;Okamoto K.;Komori M. .TUBULAR-TYPE PERVAPORATION MODULE WITH ZEOLITE NAA MEMBRANE[J].Journal of Membrane Science,1997(1):133-141. |
[5] | Aoki K.;Morooka S.;Kusakabe K. .Gas permeation properties of A-type zeolite membrane formed on porous substrate by hydrothermal synthesis[J].Journal of Membrane Science,1998(2):197-205. |
[6] | 许中强,陈庆龄,卢冠忠,MA Yi-Hua.多孔不锈钢载体上X型分子筛的生长成膜[J].催化学报,2000(02):151-155. |
[7] | Deckman H W;Jacobson A J;McHenry J A et al.[P].PCT Int Appl EP 94-01 301,1994. |
[8] | Lovallo M C;Tsapatsis M .[J].AICHE Journal,1996,42(11):3020. |
[9] | Boudreau L C;Tsapatsis M .[J].Chemistry of Materials,1997,9(08):1705. |
[10] | Lovallo MC.;Tsapatsis M.;Gouzinis A. .Synthesis and characterization of oriented MFI membranes prepared by secondary growth[J].AIChE Journal,1998(8):1903-1913. |
[11] | Lovallo M C;Tsapatsis M;Okubo T .[J].Chemistry of Materials,1996,8(08):1579. |
[12] | Lai R;GavalasGR .[J].Industrial and Engineering Chemistry Research,1998,37(11):4275. |
[13] | 许中强,陈庆龄,卢冠忠,MA Yi-hua.在多孔陶瓷载体上X型分子筛生长成膜的研究[J].石油化工,2000(08):578-581. |
上一张
下一张
上一张
下一张
计量
- 下载量()
- 访问量()
文章评分
- 您的评分:
-
10%
-
20%
-
30%
-
40%
-
50%