Engee documentation

Smoothly Curved Elbow (G)

Pipe rotation (knee) in the gas network.

blockType: EngeeFluids.Gas.Fittings.Elbow

Sharp-Edged Elbow (G)

Path in the library:

/Physical Modeling/Fluids/Gas/Pipes & Fittings/Sharp-Edged Elbow (G)

Smoothly Curved Elbow (G)

Path in the library:

/Physical Modeling/Fluids/Gas/Pipes & Fittings/Smoothly Curved Elbow (G)

Description

The Elbow (G) block simulates the flow at the turn of a pipeline in a gas 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 (G).

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;

  • — average gas density;

  • — pressure drop in the pipe section.

Critical pressure drop It is the threshold value for the transition between laminar and turbulent flows.:

where:

  • — port pressure A;

  • — port pressure B;

  • — parameter value Laminar flow pressure ratio.

Energy conservation

The law of conservation of energy in the block:

where

  • — energy flow in port A;

  • — energy flow in port B.

Ports

Conserving

# B — input or output port
gas

Details

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

Program usage name

port_b

# A — input or output port
gas

Details

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

Program usage name

port_a

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 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

# 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 section.

Units

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

Default value

0.1 m

Program usage name

internal_diameter

Evaluatable

Yes

# Laminar flow pressure ratio — the pressure ratio at which the flow transitions between laminar and turbulent modes

Details

The pressure ratio at which the gas flow transitions between laminar and turbulent modes.

Default value

0.999

Program usage name

B_laminar

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.