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Membrane and Desalination Technologies - TCE Moodle Website

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78 J. Ren <strong>and</strong> R. Wang<br />

Thickness of the sponge-like portion(µm)<br />

15<br />

10<br />

5<br />

I II<br />

III<br />

0<br />

0 10 LC 20 30 40 50 60<br />

Thickness of the entire membrane (µm)<br />

Fig. 2.26 Influence of membrane thickness on the membrane structure (20 wt% P84; solvent: NMP;<br />

coagulant bath: water; casting temperature: 25 C) [adapted from ref. (83)].<br />

thickness of 500 mm, but there were no macrovoids at thicknesses of 150 <strong>and</strong> 300 mm. Li et al.<br />

(83) investigated the thickness of sponge-like portions at different entire membranes with<br />

PES <strong>and</strong> copolyimide P84. When the membranes were prepared with 20% P84 in NMP<br />

(casting temperature, 25 C; coagulant, water), three regions could be identified along the<br />

abscissa corresponding to different membrane structures shown in Fig. 2.26. In region I, the<br />

cross sections of the membranes have a fully sponge-like structure. The membrane morphology<br />

transits from a sponge-like to a finger-like structure with some degrees of fluctuation in<br />

sponge thickness in region II. In region III, the membranes are of mainly finger-like structure<br />

with an almost constant thickness of sponge-like portion, which is independent of overall<br />

membrane thickness. There exists a critical structure-transition thickness, Lc, that reflects the<br />

transition of membrane morphology from a sponge-like to a finger-like structure during the<br />

formation of asymmetric flat membranes.<br />

5. PREPARATION OF ASYMMETRIC MEMBRANES BY PHASE<br />

INVERSION TECHNIQUE<br />

5.1. Preparation of Hollow Fiber <strong>Membrane</strong>s<br />

Polymeric hollow membranes were first mentioned in 1966 (84). They were prepared by<br />

extruding a polymer solution through an annular spinneret <strong>and</strong> a bore fluid flowed in the<br />

annular centre. The spinning of hollow fiber membranes is a very complicated process, which<br />

involves many spinning parameters as shown in Fig. 2.27. Basically, the fabrication of hollow<br />

fiber membranes involves the thermodynamics of the polymer solution <strong>and</strong> the phase<br />

inversion process, the rheologies of the polymer solution inside the spinneret <strong>and</strong> at the air<br />

gap, <strong>and</strong> other spinning conditions as well. The thermodynamics of the polymer solution <strong>and</strong>

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