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There are few popular practical approximations based on assumption of constant friction factor and linear density-pressure equation of state.
Approximations
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c0left( \frac{dp}{dl} \right)_f = 2 d \cdot \frac{f_0 \, L}{2 \, d } |
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body | f(l)= f_0 = \rm const |
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| \Delta p (L) =- \frac{\rho_0}{c^*} \cdot \left[
1 - \sqrt{ 1 - j_m^2 \cdot \frac{c^* \rho^*}{\rho_ |
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0\, 2 \, } | LaTeX Math Inline |
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body | f(l)= f_0 = \rm const |
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body | --uriencoded--\rho(l)=\ |
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rho_0= \rm constrho%5e* \cdot (1 + c%5e* \, p) |
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body | --uriencoded--c%5e* \, p \ll 1 |
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c0left( \frac{dp}{dl} \right)_f = - \frac{ j_m^2}{2 d} Delta p (L) =- p_0 \cdot \left[ 1- \sqrt{ 1 -\frac{j_m^}{\rho_0 \, p_0} \cdot \frac{f_ |
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0}{\rho(p)} | LaTeX Math Inline |
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body | f(l)= f_0 = \rm const |
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body | --uriencoded--\displaystyle \rho(l)= \frac%7B\rho_0%7D%7Bp_0%7D \cdot p |
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| \Delta p (L) =- \frac{j_m^2}{\rho_0} \cdot \frac{f_0}{2 \, d} \cdot
\frac{ 1- \exp \left( - c^* \rho^* G \, L \right)}{c^* \rho^* G} |
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body | f(l)= f_0 = \rm const |
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body | --uriencoded--\rho(l)=\rho%5e* \cdot (1 + c%5e* \, p) |
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See also
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Physics / Fluid Dynamics / Pipe Flow Dynamics / Pipe Flow Simulation / Pressure Profile in Homogeneous Quasi-Isothermal Steady-State Pipe Flow @model
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