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Membrane and Desalination Technologies - TCE Moodle Website

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Preparation of Polymeric <strong>Membrane</strong>s 89<br />

where F, r <strong>and</strong> g are the elongation force, density of the polymer solution <strong>and</strong> the gravity<br />

constant, respectively. And the force in the air gap decreases from the exit of the spinneret<br />

(z = 0) to the bottom of the air gap (z = L). The elongation stress (tzzðzÞ) at point z can be<br />

described as:<br />

tzzðzÞ ¼ F<br />

ðL 1 dvzðzÞ<br />

¼ rgvzðzÞ dz ¼ k<br />

A vzðzÞ dz<br />

z<br />

n<br />

; ð47Þ<br />

where A is the cross-section area of the nascent hollow fiber membrane. With the low<br />

deformation at air gap, the elongation viscosity can be assumed to be a constant. And<br />

n = 1, the rheology equation can be obtained in the air gap:<br />

d 2 vzðzÞ<br />

dz2 1 dvzðzÞ rg<br />

þ ¼ 0:<br />

vzðzÞ dz k<br />

ð48Þ<br />

The boundary conditions are as follows:<br />

vzðzÞ ¼v0 at z ¼ 0; (48a)<br />

dvzðzÞ<br />

¼ 0<br />

dz<br />

at z ¼ L: (48b)<br />

To spin ultrafiltration <strong>and</strong> microfiltration hollow fiber membranes with a small air gap, the<br />

spinline velocity does not change greatly, <strong>and</strong> the extension stress can be described as:<br />

tzzðzÞ ¼ F<br />

A<br />

rgðL zÞ: ð49Þ<br />

And the velocity distribution in the air gap is written as:<br />

vzðzÞ ¼vzð0Þþ rg<br />

k<br />

The velocity at the bottom of the air gap:<br />

1<br />

n<br />

L nþ1<br />

n 1 1<br />

vzðLÞ ¼vzð0Þþ rg<br />

k<br />

z<br />

L<br />

nþ1<br />

n<br />

: ð50Þ<br />

1<br />

n<br />

L nþ1<br />

n : ð51Þ<br />

For the free-fall spinning process at the same air gap, with the increase of power number n,<br />

the velocity of the nascent hollow fiber membranes in the air gap will decrease. And the<br />

velocity at the bottom of the air gap increases as a power number (n þ 1/n) of the air gap<br />

distance (L). That is to say, for the free-falling process, the spinning velocity <strong>and</strong> the air gap<br />

are coupled each other, which is different from the drawing process. When the factors of<br />

solvent evaporation, temperature decrease, solvent <strong>and</strong> nonsolvent exchange between the<br />

polymeric solution <strong>and</strong> the bore fluid, the phase inversion <strong>and</strong> solidification are considered,<br />

the velocity of the nascent fibers will decrease.<br />

For the free-fall wet spinning process, there is almost no elongation stress existing <strong>and</strong> the<br />

spinning velocity is almost the same as that of the spinneret exit (die-swell). A small drawing<br />

velocity change caused by the spinning roll or drum will cause a greatly increase of the tensile

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