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Membrane and Desalination Technologies - TCE Moodle Website

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242 L.K. Wang et al.<br />

Cl –<br />

OH –<br />

HCl<br />

NaOH<br />

C A CA C A CA C A<br />

H +<br />

Na +<br />

NaCl<br />

dil HCl<br />

in temperature, pressure, <strong>and</strong> pH, especially under cleaning <strong>and</strong> sanitizing conditions; (b)<br />

membrane –solute interactions, which affect the rate of fouling, cleaning, yields, <strong>and</strong> rejection<br />

of individual feed substances, <strong>and</strong> (c) the acceptability of the membrane as a contact<br />

material for the final product, which essentially implies using membrane materials that are<br />

inert <strong>and</strong> do not leach out any toxic substances from the membrane into the final product. In<br />

this regard, there are new generations of membranes, made of expensive inorganic inert<br />

materials, such as ceramics, stainless steel, carbon–zirconia, etc.<br />

Cl –<br />

C : Cation-exchange membrane<br />

A : Anion-exchange membrane<br />

CA : bipolar membrane<br />

H +<br />

dil NaOH<br />

OH –<br />

Na +<br />

Fig. 6.3. Separation capabilities of ED <strong>and</strong> EDR.<br />

Table 6.1<br />

List of applied pressure for typical membrane filtration process<br />

<strong>Membrane</strong> process Pressure (atm)<br />

Microfiltration (crossflow) 0.7–1.7<br />

Ultrafiltration 1.7–10.2<br />

Nanofiltration 6.8–13.6<br />

Reverse osmosis 20.4–40.8

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