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The base driving equations are:
Euler equation |
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(1) |
\frac{d p}{d l} =
-\rho \, u \, \frac{d u}{d l} + \rho \, g \, \cos \theta + f_{\rm cnt, \, l} |
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(2) |
\left( 1 - \frac{c(p) \, \rho_s^2 \, q_s^2}{\rho \, A^2} \right ) \frac{dp}{dl} = \rho \, g \, \frac{dz}{dl} - \frac{\rho_s^2 \, q_s^2 }{2 A^2 d} \frac{f(p)}{\rho} |
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(3) |
q(l) = \frac{\rho_s \cdot q_s}{\rho} |
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(4) |
u(l) = \frac{\rho_s \cdot q_s}{\rho(p) \cdot A} |
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See Also
Petroleum Industry / Upstream / Pipe Flow Simulation / Water Pipe Flow @model / Stationary Isothermal Homogenous Pipe Flow Pressure Profile @model
[ Darcy friction factor ] [ Darcy friction factor @model ]
[ Euler equation ]