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Basics of Fluid Mechanics, 2014a

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13.7. HOMOGENEOUS MODELS 549<br />

There are several suggestions for the average viscosity. For example, Duckler suggest<br />

the following<br />

μ m =<br />

μ G Q G<br />

+<br />

μ L Q L<br />

(13.32)<br />

Q G + Q L Q G + Q L<br />

Duckler linear formula does not provide always good approximation and Cichilli suggest<br />

similar to equation (13.18) average viscosity as<br />

1<br />

μ average =<br />

(13.33)<br />

X<br />

μ G<br />

+ (1−X)<br />

μ L<br />

Or simply make the average viscosity depends on the mass fraction as<br />

Using this formula, the friction loss can be estimated.<br />

μ m = Xμ G +(1− X) μ L (13.34)<br />

13.7.1.2 Acceleration Pressure Loss<br />

The acceleration pressure loss can be estimated by<br />

− dP<br />

dx ∣ = ṁ dU m<br />

a<br />

dx<br />

(13.35)<br />

The acceleration pressure loss (can be positive or negative) results from change <strong>of</strong><br />

density and the change <strong>of</strong> cross section. Equation (13.35) can be written as<br />

− dP<br />

dx ∣ = ṁ d<br />

a<br />

dx<br />

(<br />

ṁ<br />

Aρ m<br />

)<br />

(13.36)<br />

Or in an explicit way equation (13.36) becomes<br />

⎡<br />

pressure loss due to<br />

− dP<br />

density change<br />

dx ∣ = ṁ 2 { }}<br />

⎢ ( ){<br />

a ⎣ 1 d 1<br />

A dx ρ m<br />

pressure loss due to<br />

area change<br />

{ }} {<br />

1 dA<br />

+<br />

ρ m A 2 dx<br />

⎤<br />

⎥<br />

⎦<br />

(13.37)<br />

There are several special cases. The first case where the cross section is constant,<br />

dA/ dx =0. In second case is where the mass flow rates <strong>of</strong> gas and liquid is constant<br />

in which the derivative <strong>of</strong> X is zero, dX/ dx =0. The third special case is for constant<br />

density <strong>of</strong> one phase only, dρ L / dx =0. For the last point, the private case is where<br />

densities are constant for both phases.

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