TY - JOUR
T1 - Effect of electrostatic repulsive force on the permeate flux and flux modeling in the microfiltration of negatively charged microspheres
AU - Choi, Sung Wook
AU - Park, Jung Min
AU - Chang, Yongsu
AU - Yoon, Jeong Yeol
AU - Haam, Seungjoo
AU - Kim, Jung Hyun
AU - Kim, Woo Sik
N1 - Funding Information:
The authors acknowledge the financial support of Bioproducts Research Center (1994S0018), Yonsei University and the Korea Institute of S&T Evaluation and Planning (National Research Laboratory Program, M1-9911-00-0044).
PY - 2003/1
Y1 - 2003/1
N2 - A study on the permeate flux was performed in a stirred cell filled with monodispersed carboxylated microspheres (polystyrene/polymethacrylic acid, PS/PMAA), to investigate the effects of surface charge (the number density of surface carboxyl group, Nc; 0.45, 5.94, 9.14, and 10.25 nm-2) and the stirrer speed (300, 400, and 600 rpm) under constant transmembrane pressure. The permeate flux was found to be dependent on the surface charge, the ionic strength, and the stirrer speed. The permeate flux was proportional to the surface charge of microspheres and inversely proportional to the ionic strength because of electrostatic repulsive interaction and steric hindrance. The cake porosity was estimated by Kozeny-Carman equation from the steady-state permeate flux data. Experimental data elucidated that the cake porosity was extended from 0.211 to 3.04 upon the introduction of carboxyl group on the microsphere surface, leading to the high permeate flux. Consequently, resistance-in-series model was employed for the modeling of the permeate flux and showed a good agreement with the experimental results.
AB - A study on the permeate flux was performed in a stirred cell filled with monodispersed carboxylated microspheres (polystyrene/polymethacrylic acid, PS/PMAA), to investigate the effects of surface charge (the number density of surface carboxyl group, Nc; 0.45, 5.94, 9.14, and 10.25 nm-2) and the stirrer speed (300, 400, and 600 rpm) under constant transmembrane pressure. The permeate flux was found to be dependent on the surface charge, the ionic strength, and the stirrer speed. The permeate flux was proportional to the surface charge of microspheres and inversely proportional to the ionic strength because of electrostatic repulsive interaction and steric hindrance. The cake porosity was estimated by Kozeny-Carman equation from the steady-state permeate flux data. Experimental data elucidated that the cake porosity was extended from 0.211 to 3.04 upon the introduction of carboxyl group on the microsphere surface, leading to the high permeate flux. Consequently, resistance-in-series model was employed for the modeling of the permeate flux and showed a good agreement with the experimental results.
KW - Electrostatic interaction
KW - PS/PMAA microspheres
KW - Permeate flux
KW - Resistance-in-series model
KW - The number density of surface carboxyl group
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U2 - 10.1016/S1383-5866(02)00121-1
DO - 10.1016/S1383-5866(02)00121-1
M3 - Article
AN - SCOPUS:0037214473
SN - 1383-5866
VL - 30
SP - 69
EP - 77
JO - Separation and Purification Technology
JF - Separation and Purification Technology
IS - 1
ER -