Abstract:High strength and high porous alumina ceramic membrane was prepared with the raw material of average particle size of 20 μm α- Al2O3, the solvent of deionized water, the binding agent of kaolin and silica fume. The effect of binding agent on phase composition, microstructure, porosity and compressive strength of ceramic membranes were discussed. The results showed that alumina ceramic membranes with high porosity ranging from 36. 3%- 36. 7% were prepared by adjusting the content of binding agent. The compressive strength of the sample was between 59 to 105. 9 MPa, which showed a first increasing and then decreasing trend with the content of binding agent increasing and reached 105. 9 MPa at the 7. 5% (mass fraction) binding agent.
康峰,刘开琪,罗志勇. 结合剂含量对陶瓷膜结构及性能影响[J]. , 2015, 22(5): 41-44.
KANG Feng, LIU Kai- qi, LUO Zhi- yong. Effect of the content of binding agent on structure and properties of ceramic membranes. , 2015, 22(5): 41-44.
Tiraferri A, Elimelech M.Direct quantification of negatively charged functional groups on membrane surfaces[J].Journal of Membrane Science, 2012, 389:499-508
[2]
Coronell O, Gonza?lez M I, Mari?as B J, et al.Ionization behavior,stoichiometry of association,and accessibility of functional groups in the active layers of reverse osmosis and nanofiltration membranes[J].Environmental science & technology, 2010, 44(17):6808-6814
[3]
De Freitas N L, Gon?alves J A S, Innocentini M D M, et al.Development of a double-layered ceramic filter for aerosol filtration at high-temperatures: The filter collection efficiency[J].J Hazard Mater, 2006, 136(3):747-756
[4]
Dong Y, Feng X, Dong D, et al.Elaboration and chemical corrosion resistance of tubular macro-porous cordierite ceramic membrane supports[J].J Membrance Sci, 2007, 304(1):65-75
[5]
Ruiz J C, Blanc P, Prouzet E, et al.Solid aerosol removal using ceramic filters[J].Sep Purif Technol, 2000, 19(3):221-227
[6]
Shen H D.Pollutant emission control system: U.S. Patent 5, 171, 446[P]. 1992-12-15.
[7]
Cabassud C.Flux enhancement by a tangential gas flow in ultrafiltration hollow fibers for drinking water production [J].Proc.-World Filrt. Congr, 1996, 2(2):496-500