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See Derivation of Pressure Profile in Stationary Isothermal Homogenous Pipe Flow @model.

Alternative forms

LaTeX Math Block
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alignmentleft
-\frac{1}{c} \frac{d}{dl} \left( \frac{1}{\rho} \right) + \frac{\rho_s^2 q_s^2}{2A^2} \frac{d}{dl} \left( \frac{1}{\rho^2} \right) + \frac{\rho_s^2 q_s^2}{2A^2} \frac{f}{d} \left( \frac{1}{\rho^2} \right) - g \frac{dz}{dl} = 0

See derivation at 

LaTeX Math Block Reference
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pageDerivation of Pressure Profile in Stationary Quasi-Isothermal Homogenous Pipe Flow @model
.

It does not give much benefit in computations comparing to 

LaTeX Math Block Reference
anchorPP
 but it makes a starting point for derivation of some popular proxy models (like Slightly Compressible Fluid and  Ideal Gas). 


Approximations

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Incompressible pipe flow 

LaTeX Math Inline
body\rho(T, p) = \rho_s
with constant viscosity 
LaTeX Math Inline
body\mu(T, p) = \mu_s

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