摘要
分别以硅溶胶和异丙醇铝为硅源和铝源,采用预涂晶种的方式,用水热合成法在氧化铝载体上合成出小晶粒NaX分子筛膜.各组分配比为:SiO2:A12O3=3.85~4.2,Na2O:SiO2=1.2~1.5,H2O:Na2O=40~60,用扫描电镜、X射线衍射等手段对沸石膜进行了表征,可以看到分子筛膜生长的晶粒细小,沸石晶体的大小在500~800 nm,生长致密良好,覆盖完全,膜厚约为10 μm.小晶粒NaX沸石膜的H2渗透率为2.45×10-6 mol·m2/(s·Pa),H2/N2的理想分离系数达到4.21,H2/C3H8的理想分离系数达到7.56,超过对应的努森扩散值3.74和4.69.
Continuous ultrafine crystal NaX membrane was synthesized hydrothermally on the outer surface of α-alumina tube support(12 mm o.d., 8 mm i.d.). Surface-modified tubes were seeded with ultrafine zeolite X crystals prior to the membrane synthesis. The molar composition of the starting gel of NaX membrane was SiO2:Al2O3=3.85~4.2, Na2O:SiO2=1.2~1.5, H2O:Na2O=40~60. The outer surface of the tube was completely covered with zeolite crystals, which were about 500~800 nm in size and about 10 μm in thickness of the membrane as judged by a scanning electron microscope (SEM). The tests on permeation of H2, N2 and C3H8 were carried out to get the ideal separation selectivity of H2/N2 and H2/C3H8 systems. The measured permeability of H2 was about 2.45×10^-6 mol·m2/(s·Pa)and the ideal selectivity of H2/N2 and H2/C3H8 was 4.21 and 7.56, which are higher than the respective Knudsen diffusion ratios of 3.74 and 4.69.
出处
《过程工程学报》
EI
CAS
CSCD
北大核心
2005年第4期403-406,共4页
The Chinese Journal of Process Engineering