Self-forming dynamic membrane for ultrafiltration of pineapple juice

The formation of self-forming dynamic membrane an a porous ceramic support was studied. Pineapple juice of 12 degrees Brix concentration was used in the experiments which were carried out at 25 degrees C by circulating the pineapple juice at the applied pressure of 100, 200, and 300 kPa and at cross-flow velocities of 1.30-3.95 m s(-1) through the ceramic membrane module for 1 h. The experimental data of flux and rejections showed that the dynamic membrane was well-formed after 30 min of circulation under the applied pressure of 300 kPa and at a cross-flow velocity of 2.0 m s(-1) in which the steady values of flux and rejections of macromolecules and sugars obtained from the filtration mode were 6.0 x 10(-3) m(3)/m(2) h, 84-87% and 6%, respectively. The corresponding values for ultrafiltration by alumina membrane of MW cut-off 50,000, using equivalent conditions, were 15.8 x 10(-3) m(3)/m(2) h, 91% and 10.5%. Ultrafiltration was found to be more promising. The stability of the self-forming dynamic membrane was acceptable when subjected to change of filtration conditions. The permeation flux increased with cross-Sow velocity and decreased when the applied pressure was reduced. The resistances for filtration by dynamic membrane and by ultrafiltration were calculated. For a porous support of large pore sizes, an in-pore blockage of solutes which were smaller than the membrane pores reduced the pore volume and induced fouling. Internal fouling resistance (R-f) was, therefore significant and responsible for the values of flux and rejection and was approximately 70% of total resistance. While in ultrafiltration, in which membrane with a smaller pore diameter was used, R-f was only 20% but R-p, the polarized layer resistance, was as high as 60% of total resistance.