Abstract
A rigorous approach to mathematical modeling of an open channel cassette module for use in a membrane bioreactor is reported. The idea is to apply the resistance-in-series approach to both forward filtration and backflushing. Additionally, the geometry of the module is modeled using an one-dimensional approach to gain more detailed information of permeate flux, cake mass and transmembrane pressure as a function of the module length. The modeling approach is in good agreement with experimental data for different operating points. Simulation is used to discuss backflushing pressure and efficiency as well as the cake formation as function of the module length.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
