By Charcosset, Catherine (Auth.)
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Additional info for Membrane Processes in Biotechnologies and Pharmaceutics
Example text
62 (2008) 47–55. [74] V. Puspitasari, A. Granville, P. Le-Clech, V. Chen, Cleaning and ageing effect of sodium hypochlorite on polyvinylidene fluoride (PVDF) membrane, Sep. Purif. Technol. 72 (2010) 301–308. C. Kaplan, A. Jegou, B. Chaufer, M. C. Michalsky, Adsorption of lysozyme on membrane material and cleaning with non-ionic surfactant characterized through contact angle measurements, Desalination 146 (2002) 149–154. S. Madaeni, E. Rostami, A. Rahimpour, Surfactant cleaning of ultrafiltration membranes fouled by whey, Int.
The model was a tool for understanding the cubic shape of the plot of flux versus log (xanthan concentration) rather than for a priori flux prediction. Charcosset and Choplin [24] reported UF experiments with newtonian and non-newtonian fluids (pectin, xanthan and polyacrylamide solution). For non-newtonian pseudoplastic fluids, the shape of the plot of flux versus log (bulk concentration) was different from the linear decline in flux which would occur for newtonian fluids. Electrostatic interactions Protein transport through UF membranes is strongly affected by electrostatic interactions.
To linearly scale a cross-flow process [14], all fluid dynamic and membrane module parameters must be kept constant. Fluid dynamic parameters are set to be the user. They include the ratio of feed volume to membrane area, feed rate per membrane area, filtrate flux, and retentate and filtrate pressures. Membrane module parameters are inherent to the membrane device. 4 Two-stage closed-loop cascade configuration. Ultrafiltration 49 channel height, channel length, and feed and filtrate flow geometries.