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or , _r3•vw•“wc/73 °W 1 ST•g J s -r3•VW'“WC11/3 wmax 1(ST - DOO + SF) gJ The mean velocities of the film are ReW ' y¥ Wc 2 [(ST - DOO) + SF] The volumetric flow rate on one side is *- “WC 2p„ and the thickness of the water film can he expressed by (4o) (41) (42) (43) and g v=— W4av 3 g ^ Vax '•av.cr The flow should remain laminar and therefore the Re number must be 3 • VW less or equal to 250 at the critical cross section vw •<$w wav,er "max (44) (45) ReW-i ReW„ and in areas above and below the tube Re should be not less than 10-30 [6] (otherwise the film will break up and dry spots occur). in the above equation is the kinematic viscosity of the water at its respective temperature. The film heat transfer coefficient h^ between water film and fin can be evaluated from [4]: 0.0l[^ 4*,i/3 \=2J yW C-24PDF Image | Development of the Zinc-Chlorine Battery for Utility
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