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The pressure drop in pipe flow due to fluid friction with pipe walls depends on mass flux density and friction factor distribution along the pipe.

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anchordpdl
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\left(   \frac{dp}{dl} \right)_f = - \frac{ j_m^2}{2 d}  \cdot \frac{f}{\rho}

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where

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bodyj_m = \dot m / A

mass flux

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body \dot m (l) = \dot m = \rm const

mass flowrate 

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bodyd

pipe diameter

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body--uriencoded--A = 0.25 \, \pi \, d%5e2

pipe cross-section area

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body--uriencoded--f= f(%7B\rm Re%7D, \epsilon)

Darcy friction factor

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body\epsilon

inner pipe walls roughness

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body--uriencoded--\displaystyle %7B\rm Re%7D = \frac%7Bj_m \, d%7D%7B\mu%7D

Reynolds number 

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body\mu(T, p)

dynamic viscosity as function of fluid temperature 

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bodyT
 and pressure 
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bodyp


The accurate calculations require
solving of a self-consistent equation of Pressure Profile in Homogeneous Quasi-Isothermal Steady-State Pipe Flow @model.

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