Article ID Journal Published Year Pages File Type
633945 Journal of Membrane Science 2014 8 Pages PDF
Abstract

•A model was developed to simulate N-nitrosamine rejection by RO membrane systems.•The model was validated using a pilot system under a range of operating conditions.•The model showed that rejection was sensitive to changes in flux and recovery.•In addition, the localised rejection decreased along the membrane vessel.•The developed model can be used to guide system design and regulatory monitoring.

A mathematical model was developed based on the irreversible thermodynamic principle and hydrodynamic calculation to predict the rejection of N-nitrosamines by spiral-wound reverse osmosis (RO) membrane systems. The developed model is able to accurately describe the rejection of N-nitrosamines under a range of permeate flux and system recovery conditions. The modelled N-nitrosamine rejections were in good agreement with values obtained experimentally using a pilot-scale RO filtration system. Simulation from the model revealed that an increase in permeate flux from 10 to 30 L/m2h led to an increase in the rejection of low molecular weight N-nitrosamines such as N-nitrosodimethylamine (NDMA) (from 31% to 54%), which was validated by experimental results. The modelling results also revealed that an increase in recovery caused a decrease in the rejection of these N-nitrosamines, which is consistent with the experimental results. Further modelling investigations suggested that NDMA rejection by a spiral-wound system can drop from 49% to 35% when the overall recovery increased from 10% to 50%. The model developed from this study can be a useful tool for water utilities and regulators for system design and evaluating the removal of N-nitrosamine by RO membranes.

Related Topics
Physical Sciences and Engineering Chemical Engineering Filtration and Separation
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