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Basics of Fluid Mechanics, 2014a

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212 CHAPTER 7. ENERGY CONSERVATION<br />

7.3.2 Energy Equation in Frictionless Flow and Steady State<br />

In cases where the flow can be estimated without friction or where a quick solution is<br />

needed the friction and other losses are illuminated from the calculations. This imaginary<br />

fluid reduces the amount <strong>of</strong> work in the calculations and Ideal Flow Chapter is dedicated<br />

in this book. The second low is the core <strong>of</strong> “no losses” and can be employed when<br />

calculations <strong>of</strong> this sort information is needed. Equation (2.21) which can be written as<br />

Using the multiplication rule change equation (7.76)<br />

dq rev = Tds= dE u + Pdv (7.76)<br />

dq rev = dE u + d (P v) − vdP = dE u + d<br />

( P<br />

ρ<br />

)<br />

− vdP (7.77)<br />

integrating equation (7.77) yields<br />

∫ ∫<br />

dq rev =<br />

∫<br />

dE u +<br />

( ) ∫ P<br />

d −<br />

ρ<br />

vdP (7.78)<br />

( ) ∫ P dP<br />

q rev = E u + −<br />

ρ ρ<br />

(7.79)<br />

Integration over the entire system results in<br />

∫<br />

Q rev =<br />

V<br />

h<br />

{(<br />

}} ( )){<br />

P<br />

E u +<br />

ρ<br />

∫ (∫ dP<br />

ρdV −<br />

V ρ<br />

Taking time derivative <strong>of</strong> the equation (7.80) becomes<br />

h<br />

)<br />

ρdV (7.80)<br />

˙Q rev = D ∫ {(<br />

}} ( )){<br />

P<br />

E u + ρdV − D ∫ (∫ ) dP<br />

ρdV (7.81)<br />

Dt V ρ Dt V ρ<br />

Using the Reynolds Transport Theorem to transport equation to control volume results<br />

in<br />

˙Q rev = d ∫ ∫<br />

hρdV + hU rn ρdA+ D ∫ (∫ ) dP<br />

ρdV (7.82)<br />

dt V<br />

A Dt V ρ<br />

As before equation (7.81) can be simplified for uniform flow as<br />

[<br />

(∫ ∫ )]<br />

dP ˙Q rev = ṁ (h out − h in ) −<br />

dP ρ ∣ −<br />

out<br />

ρ ∣ (7.83)<br />

in<br />

or<br />

(∫ dP<br />

˙q rev =(h out − h in ) −<br />

ρ<br />

∫ dP<br />

∣ −<br />

out<br />

ρ<br />

)<br />

∣<br />

in<br />

(7.84)

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