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NAMS 2002 Workshop - ICOM 2008

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Membrane Fouling IV - RO & Desalination – 6<br />

Friday July 18, 12:15 PM-12:45 PM, Moloka’i<br />

Effect of Foulant-Foulant Interaction on the Limiting Flux for RO and NF<br />

Membranes during Organic Fouling - Model Development and AFM<br />

Adhesion Force Measurement<br />

C. Tang (Speaker), Nanyang Technological University, Thailand - cytang@ntu.edu.sg<br />

Y. Kwon, Stanford University, Palo Alto, California, USA<br />

J. Leckie, Stanford University, Palo Alto, California, USA<br />

A limiting flux model has been recently developed to predict the fouling behavior<br />

of reverse osmosis and nanofiltration membranes by organic macromolecules<br />

(Tang and Leckie, 2007). Several interesting results have been observed: a)<br />

there was a maximum pseudo stable flux (the limiting flux) beyond which further<br />

increase in applied pressure did not translate to a greater stable flux; b) all<br />

membrane samples attained the limiting flux under constant pressure conditions<br />

as long as their initial flux was greater than the limiting flux; c) the limiting flux did<br />

not depend on the properties of membranes; d) the limiting flux had strong<br />

dependence on the feedwater composition, such as pH, ionic strength, and<br />

divalent ion concentration. The current study investigates the dependence of<br />

limiting flux on intermolecular interaction between foulant molecules. It was<br />

observed that the limiting flux was directly proportional to the intermolecular<br />

electrostatic repulsive force and that conditions enhancing foulant-depositedfoulant<br />

repulsion resulted in greater limiting flux values. Such observations agree<br />

well with a theoretical model capturing both hydrodynamic and DLVO<br />

interactions. Adhesion force measurements by atomic force microscopy (AFM)<br />

were also performed. The limiting flux correlated well with AFM adhesion force<br />

between the model foulant and the fouled membrane surface. Finally, membrane<br />

fouling was primarily controlled by the initial-flux-over-limiting-flux ratio - a greater<br />

ratio inevitably resulted in more severe flux reduction, greater foulant<br />

accumulation, and greater density of the foulant layer.<br />

Reference:<br />

C. Y. Tang and J. O. Leckie, "Membrane independent limiting flux for RO and NF membranes<br />

fouled by humic acid," Environ. Sci. Technol., vol. 41, pp. 4767-4773, 2007.

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