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Membrane and Desalination Technologies - TCE Moodle Website

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116 L. Song <strong>and</strong> K.Guan Tay<br />

Fouling potential k f (Pa.sm –2 )<br />

1.5×10 10<br />

1.2×10 10<br />

9.0×10 9<br />

6.0×10 9<br />

3.0×10 9<br />

4.0×105 8.0×105 1.2×106 1.6×106 2.0×106 0.0<br />

Pressure (Pa)<br />

Fig. 3.9. Fouling potentials at different driving pressures measured with AG membrane.<br />

the experiments. The rapid flux decline can be attributed to the increase in particle deposition,<br />

which is caused by the increase in permeate flux that carries the colloidal particles onto the<br />

membrane surface when pressure is increased. Fouling potential at different pressures is<br />

calculated <strong>and</strong> presented in Fig. 3.9.<br />

It is shown in Fig. 3.9 that fouling potential determined with AG membrane is not sensitive<br />

to driving pressure in the pressure range tested. The compaction of fouling layer is not<br />

noticeable in the measured fouling potentials in this case. Increase in the permeate flux at<br />

higher pressures is balanced by the same increase in the resistance of the fouling layer. This<br />

nonchalant response of fouling potential to increasing pressure suggests that the duration of<br />

fouling tests to determine fouling potential can be shortened by increasing the driving pressure,<br />

so that permeate flux can decline sufficiently to give meaningful results. However, the lack of<br />

method to determine the critical pressure that gives rise to compaction of fouling layer means<br />

precaution has to be taken when operating the fouling tests at high pressure. For most accurate<br />

measurement, driving pressure should be identical to that used in the full-scale RO process.<br />

4. PREDICTION OF FOULING IN FULL-SCALE REVERSE OSMOSIS<br />

PROCESSES<br />

Fouling in the full-scale RO processes is commonly indicated by the decline of permeate<br />

flux under constant driving pressure or increase in driving pressure to maintain constant<br />

permeate flux. It has been known for a long time that the flux decline in the full-scale RO<br />

processes is quite different from that observed from the fouling test in the laboratory-scale<br />

RO device. This fact makes it impossible to quantitatively predict flux decline in the full-scale

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