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W. Richard Bowen and Nidal Hilal 4

W. Richard Bowen and Nidal Hilal 4

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4.7 THE UsE OF AFM IN MEMbRANE dEvELOPMENT 125<br />

CH 3<br />

O C O S<br />

CH3<br />

PSU<br />

O O C<br />

SO 3H<br />

SPEEK<br />

FIgURE 4.19 Structures of polysulphone <strong>and</strong> sulphonated poly (ether ether) ketone.<br />

Jw / ms –1<br />

1.2e−4<br />

1.0e−4<br />

8.0e−5<br />

6.0e−5<br />

4.0e−5<br />

2.0e−5<br />

P-O<br />

P-P<br />

S0.5-20<br />

S2-20<br />

S5-20<br />

ΔP / kN m –2<br />

0.0e+0<br />

0 100 200 300 400 500 600<br />

FIgURE 4.20 Water flux as a function of applied pressure for five membranes of various<br />

percentages of SPEEK. P-O <strong>and</strong> P-P: 0%; S0.5-20: 0.5%; S2-20: 2.0%; S5-20: 5%.<br />

The adhesion of a range of colloid probes, both inorganic <strong>and</strong> biological,<br />

is greatly reduced at the PSU/SPEEK membranes, as shown by the<br />

data in Table 4.5.<br />

Such low adhesion forces show that the membranes are well suited to<br />

many types of separation. The removal of humic acid has been investigated<br />

as an example of a challenging separation. The blend membranes<br />

O<br />

O<br />

O<br />

n<br />

n

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