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See Derivation of Pressure Profile in Stationary Isothermal Homogenous Pipe Flow @model.
Alternative forms
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-\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
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page | Derivation of Pressure Profile in Stationary Quasi-Isothermal Homogenous Pipe Flow @model |
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.It does not give much benefit in computations comparing to
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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
with constant viscosity ...