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Membrane and Desalination Technologies - TCE Moodle Website

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

• A few hours<br />

• Low cost<br />

• More alternatives<br />

New<br />

characterization<br />

method Pilot test<br />

Fouling<br />

index<br />

where j is the foulant deposition rate onto the membrane surface (g/m 2 s), v is the permeate<br />

flux (m 3 /m 2 s or m/s), <strong>and</strong> cf0 is the foulant concentration (mg/L) in the bulk flow. The foulant<br />

amount M (g/m 2 ) accumulated over time t is calculated by<br />

M ¼<br />

Simulation<br />

ð t<br />

0<br />

j dt ¼ cf0<br />

ð t<br />

0<br />

v dt: (3Þ<br />

Resistance of the fouling layer at any point of time is related to the amount of accumulated<br />

foulants with<br />

Rf ¼ rsM ¼ rscf0<br />

ð t<br />

0<br />

v dt ¼ kf<br />

ð t<br />

0<br />

v dt; (4Þ<br />

where Rf is the resistance of the fouling layer (Pa s/m), rs is the specific resistance of the<br />

fouling layer (Pa s m/g), <strong>and</strong> kf (= rscf0) is a new parameter (Pa s/m 2 ) introduced <strong>and</strong> is termed<br />

as the fouling potential of the feed water. Rearranging Eq. (4) gives (15, 16)<br />

kf ¼ Rf<br />

Ð t<br />

0<br />

Fouling in<br />

Full-scale<br />

System<br />

• A few months<br />

• Expensive<br />

• Limited coverage<br />

Fig. 3.3. Comparison of the new characterization method <strong>and</strong> the pilot test.<br />

: (5Þ<br />

v dt<br />

Because the integration term is the volume of permeate collected per unit area of membrane<br />

over time period t, Eq. (5) shows that the fouling potential of the feed water is defined<br />

as the resistance of the fouling layer caused by a unit volume of permeate collected per unit<br />

area of membrane.<br />

In the above derivation, the fouling potential is calculated as the product of the specific<br />

cake resistance (rs) <strong>and</strong> bulk foulant concentration (cf0). However, the calculation proves to<br />

be difficult with real feed water, primarily because it is really impossible to establish the<br />

specific cake resistance of all foulants in the feed water. Fortunately, the fouling potential of<br />

feed water can be easily determined with a simple fouling test using a small piece of RO<br />

membrane. The total hydraulic resistances at the beginning (R0) <strong>and</strong> the end (Rt) of the<br />

fouling test are determined <strong>and</strong> the difference between these two hydraulic resistances gives<br />

the resistance of the fouling layer:

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