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Basics of Fluid Mechanics, 2014a

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11.9. RAYLEIGH FLOW 471<br />

Table -11.6. Fanno Flow Standard basic Table (continue)<br />

M<br />

4fL<br />

D<br />

P<br />

P ∗ P 0<br />

P 0<br />

∗<br />

ρ<br />

ρ ∗<br />

U<br />

U ∗<br />

T<br />

T ∗<br />

60.00 0.82052 0.000680 3.6E+6 0.40853 2.448 0.00166<br />

65.00 0.82066 0.000579 5.4E+6 0.40849 2.448 0.00142<br />

70.00 0.82078 0.000500 7.8E+6 0.40846 2.448 0.00122<br />

11.9 Rayleigh Flow<br />

Rayleigh flow is a model describing a frictionless flow with heat transfer through a<br />

pipe <strong>of</strong> constant cross sectional area. In practice, Rayleigh flow isn’t a really good<br />

model to describe real situations. Yet, Rayleigh flow is practical and useful concept in<br />

a obtaining trends and limits such as the density and pressure change due to external<br />

cooling or heating. As opposed to the two previous models, the heat transfer can be in<br />

two directions not like the friction (there is no negative friction). This fact creates a<br />

different situation as compared to the previous two models. This model can be applied<br />

to cases where the heat transfer is significant and the friction can be ignored. Flow <strong>of</strong><br />

steam in steam boiler is good examle where Rayleigh flow can be used.<br />

11.10 Introduction<br />

½<br />

È ½<br />

Ì ½<br />

Fig. -11.37.<br />

Flow.<br />

flow<br />

direction<br />

É<br />

heat transfer<br />

(in and out)<br />

¾<br />

È ¾<br />

Ì ¾<br />

The control volume <strong>of</strong> Rayleigh<br />

The third simple model for 1–dimensional<br />

flow with a constant heat transfer for frictionless<br />

flow. This flow is referred to in<br />

the literature as Rayleigh Flow (see historical<br />

notes). This flow is another extreme<br />

case in which the friction effects are neglected<br />

because their relative magnitute is<br />

significantly smaller than the heat transfer<br />

effects. While the isothermal flow model<br />

has heat transfer and friction, the main<br />

assumption was that relative length is enables<br />

significant heat transfer to occur between the surroundings and tube. In contrast,<br />

the heat transfer in Rayleigh flow occurs between unknown temperature and the tube<br />

and the heat flux is maintained constant. As before, a simple model is built around the<br />

assumption <strong>of</strong> constant properties (poorer prediction to case where chemical reaction<br />

take a place).<br />

This model is used to roughly predict the conditions which occur mostly in situations<br />

involving chemical reaction. In analysis <strong>of</strong> the flow, one has to be aware that<br />

properties do change significantly for a large range <strong>of</strong> temperatures. Yet, for smaller<br />

range <strong>of</strong> temperatures and lengths the calculations are more accurate. Nevertheless,

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