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Membrane and Desalination Technologies - TCE Moodle Website

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<strong>Membrane</strong> <strong>Technologies</strong> for Oil–Water Separation 655<br />

hydrophilic microfiltration membrane could effectively separate the diethyl sebacate/water<br />

emulsion. Diethyl sebacate concentrations in the permeate were lowest when the transmembrane<br />

pressure was low <strong>and</strong> when the membrane was frequently backflushed. <strong>Membrane</strong><br />

fouling during oil–water emulsion filtration is mainly due to adsorption of oil on membrane<br />

structure, which causes modification of the critical surface tension. This process exhibits a<br />

good example to apply membrane bioreactor as an effective oil–water separation method (76).<br />

4. ADVANCES IN MEMBRANE TECHNOLOGY<br />

4.1. Modification of <strong>Membrane</strong><br />

P<br />

P<br />

I<br />

A P<br />

P B II<br />

S3 S4<br />

S1 S2<br />

Fig. 15.7. Schematic of dual-membrane bioreactor (76).<br />

The most serious limitation of membranes is the continuous decline of flow through the<br />

membrane due to fouling. Permeation rates of macromolecular solutions through membranes<br />

are much smaller than pure water permeation rates <strong>and</strong> decrease rapidly as the operation<br />

continues. Flux decline has a significant negative impact on the feasibility <strong>and</strong> economics of<br />

the membrane process. Recently, many works have focused on membrane modification with<br />

a fundamental approach to reduce membrane fouling. Numerous attempts have been undertaken<br />

to modify membrane materials aimed at producing membranes less susceptible to<br />

fouling. One technique widely used for this purpose is blending of the original polymer<br />

with polymers to achieve the required properties (77, 78). For example, to enhance the<br />

membrane hydrophilicity, the polyether sulfonamide) is blended with the original polymer<br />

to obtain a modified poly(etherimide) ultrafiltration membrane (79). To change the adsorption<br />

<strong>and</strong> permeation properties of the membrane, the addition of polymeric layers on the active<br />

surfaces of membranes is performed (80). Adsorbed hydrophilic polymers were assessed as a<br />

possible means of reducing protein fouling in microfiltration <strong>and</strong> ultrafiltration membranes<br />

(81–85). Polysulfone ultrafiltration <strong>and</strong> microfiltration membranes were modified by preadsorption<br />

of water-soluble polymers (85). The preadsorbed polymers cause the narrowing of<br />

pore sizes on the membrane surface. In addition, the desirable anti-fouling effect of the<br />

P<br />

P

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