By R. T. Lahey Jr., D. A. Drew (auth.), Jeffery Lewins, Martin Becker (eds.)

ISBN-10: 1461399254

ISBN-13: 9781461399254

ISBN-10: 1461399270

ISBN-13: 9781461399278

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**Extra resources for Advances in Nuclear Science and Technology**

**Example text**

L nd d + ~k. + ~k l nd d + ~k + ~k w i (147 ) w The momentum equation of interest in one-dimensional analysis is normally the linear momentum equation in the axial direction. This equation can be derived from Equation (147) by taking the dot product of each term in that equation with the unit vector, ~z. The resultant axial momentum equation is 1 +-A x-s <">p l + n • --z • T =k. l S'" -k. • n S"'· n k. -k. -z 1 8 + -- A l -z l x-s 8z • n [A Ct k (T x-s nd -z + ~k. l nd + ~k w d • ~ + ~k w ZZk n --z • n -z + T ~ ZZk) 1 n --z (148) In Equation (148) we have used the fact that - gk sine (149) where e is the angle made between the flow direction (n ) and the horizontal.

J(~,t) /:, 1 V Sf 1- a. (x,t) 1- If a. (x,t) ~k /:,~d k. 1 (m" /:'~k. ::'k dS, (65d) 1 ~k W (65c) dS, ~k 1- V a. (x,t) ~k (65b) dS, . q" V a. (x,t) ~k If 1 -1 ff 1 /:, 1 d /:, r\ -k. v. 1 w . ,9;"k dS ' .

I l Thus, i f . r ~k. l d (119a) ~k. k is a b. nd T vd • (119b) = v U. k -l ~k. -k. -k. k . Qi b. n ~l + (l-n) ~2 ' . 5 (13) (for both evaporation and condensation). As can be noted in Figure 4, for the case of ideal annular flow the parameter n represents the weighting relationship between the spatially averaged phasic velocities, ~k' and the interfacial velocity, U .. For highly turbulent flows, in which the velocity pr6file of phase-2 is fairly flat, we might expect n to be close to unity, for both evaporation and condensation.

### Advances in Nuclear Science and Technology by R. T. Lahey Jr., D. A. Drew (auth.), Jeffery Lewins, Martin Becker (eds.)

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