Engee documentation

Pipe Bend (IL)

Bending of a pipe in an isothermal fluid network.

blockType: EngeeFluids.IsothermalLiquid.Pipes.Bend

Path in the library:

/Physical Modeling/Fluids/Isothermal Liquid/Pipes & Fittings/Pipe Bend (IL)

Description

In the block Pipe Bend (IL) The hydrodynamics of a curved pipe in an isothermal fluid network is modeled. The characteristics of the pipe can be determined in such a way as to calculate hydraulic losses due to friction and pipe curvature, as well as to simulate the flow of a compressible fluid.

Pipe curvature loss coefficient

The coefficient of local resistance (pressure loss) of the curved section of the channel includes a correction factor for the angle of rotation of the channel and the channel bending coefficient :

In the coefficient block calculated as follows:

where — the angle of rotation of the channel in degrees, the value of the parameter Bend angle.

Ratio It is calculated on the basis of experimental data – a table of the dependence of the desired coefficient on the ratio of the bending radius. to the pipe diameter for channel rotation angles 90° according to [1]:

pipe bend il 1

1 1.5 2 3 4 6 8 10 12 14 16 20 24

20

14

12

12

14

17

24

30

34

38

42

50

58

Coefficient of friction It is interpolated based on tabular data taken for technical steels, depending on the pipe diameter [1]. The table below shows the data for the coefficient of friction of a fluid flow with developed turbulence in pipes made of technical steels.

Nominal size, mm 5 10 15 20 25 32 40 50 72.5 100 125 150 225 350 609.5

Coefficient of friction

0.035

0.029

0.027

0.025

0.023

0.022

0.021

0.019

0.018

0.017

0.016

0.015

0.014

0.013

0.012

The correction factor of the channel rotation angle is valid for curved pipes (channels) in which the ratio of the bending radius to the pipe diameter ranges from 1 before 24. Outside of this range, nearest neighbor extrapolation is used.

Friction losses in the laminar flow regime

The pressure loss expressions are the same for the flows in ports A and B.

In the case of a laminar flow regime in a pipe bend, or when the Reynolds number is below the critical value , the pressure loss at the bend of the pipe is determined as follows:

where

  • — dynamic viscosity of the liquid;

  • is the constant of the coefficient of friction (Darcy coefficient), which is equal to 64 for laminar flow mode;

  • — the density of the liquid inside the pipe;

  • — pipe diameter;

  • — the length of the curved section of the pipe (pipe bend), is defined as the product of the bending radius and the angle of rotation of the channel (bend): ;

  • — the cross-sectional area of the pipe, ;

  • — mass flow rate at the appropriate port.

Friction losses in the turbulent flow regime

For flows with developed turbulence, or if the Reynolds number exceeds the critical value , the pressure loss in the pipe bend is determined as follows:

where — Darcy’s coefficient of friction. It is approximated by the empirical Haaland equation and is determined by the absolute roughness of the inner surface (the value of the parameter Internal surface absolute roughness). The pressure drop is taken in half of the pipe section, between port A and the inner node, as well as between the inner node and port B.

Pressure drop for incompressible liquids

In the case of an incompressible fluid, the pressure loss at the bend of the pipe is determined as follows:

Pressure drop for compressible liquids

In the case of a compressible fluid, the pressure inside the curved pipe is also taken into account when calculating the pressure loss at the bend. :



Conservation of mass

In the case of an incompressible fluid, the mass flow rate through the block is maintained.:

In the case of a compressible liquid, the difference in flow rates at the inlet and outlet of the block is determined by the change in the density of the liquid inside the curved section of the pipe (pipe bend):

where — the volume of the curved section of the pipe (pipe bend), which is defined as the product of the cross-sectional area of the pipe and the length of the bend, .

Ports

Conserving

# A — input or output port
Isothermal liquid

Details

The port of the isothermal liquid corresponds to the inlet or outlet of the liquid into the bend of the pipe. This unit has no internal orientation.

Program usage name

port_a

# B — input or output port
Isothermal liquid

Details

The port of the isothermal liquid corresponds to the inlet or outlet of the liquid into the bend of the pipe. This unit has no internal orientation.

Program usage name

port_b

Parameters

Main

# Pipe diameter — pipe diameter
m | um | mm | cm | km | in | ft | yd | mi | nmi

Details

Pipe diameter.

Units

m | um | mm | cm | km | in | ft | yd | mi | nmi

Default value

0.1 m

Program usage name

pipe_diameter

Evaluatable

Yes

# Bend radius — bending radius
m | um | mm | cm | km | in | ft | yd | mi | nmi

Details

The radius of the circle formed by the bend of the pipe.

Units

m | um | mm | cm | km | in | ft | yd | mi | nmi

Default value

0.04 m

Program usage name

bend_radius

Evaluatable

Yes

# Bend angle — bending angle
rad | deg | rev | mrad | arcsec | arcmin | gon

Details

The angle of rotation of the channel or the bend of the pipe.

Units

rad | deg | rev | mrad | arcsec | arcmin | gon

Default value

90.0 deg

Program usage name

bend_angle

Evaluatable

Yes

# Internal surface absolute roughness — the roughness of the walls of a curved pipe
m | um | mm | cm | km | in | ft | yd | mi | nmi

Details

The parameter is used to determine the Darcy coefficient, which is used to determine the local resistance in a turbulent flow regime.

Units

m | um | mm | cm | km | in | ft | yd | mi | nmi

Default value

1.5e-05 m

Program usage name

roughness

Evaluatable

Yes

# Fluid dynamic compressibility — consideration of dynamic compressibility of a liquid

Details

The parameter determines whether the dynamic compressibility of the liquid will be taken into account. In the case of dynamic compressibility of a liquid, the mass flow rate through the block in short periods of time can be variable, and is determined by a change in the density of the liquid. The volume of the curved pipe section is constant. In the library of isothermal fluid components in all blocks, the density of the fluid is considered as a function of pressure.

Default value

false (switched off)

Program usage name

dynamic_compressibility

Evaluatable

No

# Initial liquid pressure — the pressure of the liquid at the initial moment of time
Pa | uPa | hPa | kPa | MPa | GPa | kgf/m^2 | kgf/cm^2 | kgf/mm^2 | mbar | bar | kbar | atm | ksi | psi | mmHg | inHg

Details

The pressure of the liquid in the pipe at the initial time.

Dependencies

To use this option, check the box Fluid dynamic compressibility.

Units

Pa | uPa | hPa | kPa | MPa | GPa | kgf/m^2 | kgf/cm^2 | kgf/mm^2 | mbar | bar | kbar | atm | ksi | psi | mmHg | inHg

Default value

0.101325 MPa

Program usage name

p_start

Evaluatable

Yes

Literature

  1. Crane Co. Flow of Fluids Through Valves, Fittings, and Pipe TP-410. Crane Co., 1981.