Engee documentation

Smoothly Curved Elbow (IL)

Pipe rotation (elbow) in the isothermal fluid network.

blockType: EngeeFluids.IsothermalLiquid.Fittings.Elbow

Sharp-Edged Elbow (IL)

Path in the library:

/Physical Modeling/Fluids/Isothermal Liquid/Pipes & Fittings/Sharp-Edged Elbow (IL)

Smoothly Curved Elbow (IL)

Path in the library:

/Physical Modeling/Fluids/Isothermal Liquid/Pipes & Fittings/Smoothly Curved Elbow (IL)

Description

The Elbow (IL) block simulates the flow at the turn of a pipeline in an isothermal liquid network. In this case, pressure losses are calculated when the pipe is rotated, but the influence of viscous friction is not taken into account.

Two types of knee are available: Smoothly curved (smoothly curved) and Sharp-edged (Miter) (acute-angled or oblique). For modeling a smooth pipe with a bend 90°, which takes into account losses due to friction, you can also use the block Pipe Bend (IL).

Loss coefficients

If for the parameter Elbow type the value is set Smoothly curved, the block calculates the loss factor as follows:

where — the angle correction coefficient calculated by the Keller block [2] as

where — parameter value Bend angle in degrees. The block determines the coefficient of friction as a value for pure commercial steel. The block then interpolates the values from the tabular data depending on the inner diameter of the elbow for [1]. The table below shows data on friction in a pipe for pure commercial steel during flow in a zone of complete turbulence.

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

The values given are valid for diameters up to 600 The coefficient of friction for large diameters or for wall roughness outside this range is calculated by extrapolating the nearest neighbors.

If for the parameter Elbow type the value is set Sharp-edged (Miter), the block calculates the loss coefficient for the bending angle according to [1] as follows:

, ° 0 15 30 45 60 75 90

2

4

8

15

25

40

60

sharp edged elbow il 1

Conservation of mass

The mass conservation equation for a section of pipe has the form:

The mass flow through the knee is

where

  • — flow area;

  • — the average density of the liquid;

  • — pressure drop in the pipe section.

Critical pressure drop — this is the pressure drop associated with the critical Reynolds number (parameter value Critical Reynolds number), the point of transition of the flow regime between laminar and turbulent flow:

where

  • — kinematic viscosity of the liquid;

  • — the inner diameter of the knee.

Ports

Conserving

# A — input or output port
Isothermal liquid

Details

A non-directional port connected to the inlet or outlet of the liquid in the pipe section.

Program usage name

port_a

# B — input or output port
Isothermal liquid

Details

A non-directional port connected to the inlet or outlet of the liquid in the pipe section.

Program usage name

port_b

Parameters

Main

# Elbow type — bending geometry
Smoothly curved | Sharp-edged (Miter)

Details

The geometry of the bend of the pipe section. If the value is set to Sharp-edged (Miter) The block makes a drastic change in the flow direction, for example, at the pipe junction, and flow losses are modeled by a separate set of empirical data obtained on pipe sections with gradual rotation.

Values

Smoothly curved | Sharp-edged (Miter)

Default value

Program usage name

type

Evaluatable

No

# Elbow internal diameter — inner diameter of the pipe
m | um | mm | cm | km | in | ft | yd | mi | nmi

Details

The inner diameter of the pipe.

Units

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

Default value

0.1 m

Program usage name

d

Evaluatable

Yes

# Elbow angle — pipe rotation angle
rad | deg | rev | mrad | arcsec | arcmin | gon

Details

The angle of rotation of the pipe.

Units

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

Default value

90.0 deg

Program usage name

angle

Evaluatable

Yes

# Critical Reynolds number — the upper limit of the Reynolds number for laminar flow

Details

The Reynolds number for the transition between laminar and turbulent modes in a pipe section.

Default value

150

Program usage name

Re_critical

Evaluatable

Yes

Literature

  1. Crane Co. Flow of Fluids Through Valves, Fittings, and Pipe: Technical Paper No. 410. Crane Co., 1981.

  2. Keller, G. R. Hydraulic System Analysis. Penton, 1985.