phoenics pressure drop in 90 0 bend. introduction this presentation outlines the modeling of the...

9
PHOENICS Pressure Drop in 90 0 Bend

Upload: jaden-knight

Post on 28-Mar-2015

214 views

Category:

Documents


2 download

TRANSCRIPT

Page 1: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

PHOENICS

Pressure Drop in 900 Bend

Page 2: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

Introduction This presentation outlines the modeling of the

pressure drop in a 900 bend for a range of

configurations. The objective being to

illustrate how PHOENICS can provide

valuable data on alternative designs,

BEFORE any material is cut.

Page 3: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

The Geometry

An approximation of the current Walker Filtration inlet design in the PHOENICS VR viewer.

Inlet

Flow into filter unit

Air Passage

The inlet has a diameter of 20mm and is pressurised to 3Bar. The working fluid at the inlet is air at 200C.

Page 4: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

Results – Example 1

Pressure Drop = 23,353Pa.

Large drop due to the poor flow characteristics of the port.

Inlet

Flow into filter unit

Page 5: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

Results – Example 2

Pressure Drop = 7,494Pa.

The smoother geometry of the port results in a reduced pressure drop.

Inlet

Flow into filter unit

Page 6: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

Results – Example 3

Pressure Drop = 14,065Pa.

Although still an improvement on Example 1, the introduction of the vane has increased the pressure drop when compared to Example 2. This is probably due to the reduction in swept volume of the port due to the presence of the vane.

The position and profile of the vane(s) will also influence the flow rate, together with its effect on turbulence.

Inlet

Flow into filter unit

Page 7: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

Results – Example 4

Pressure Drop = 7,558Pa.

An attempt has been made to compensate for the presence of the vane by increasing the port size. This has improved the pressure drop and is close to that of Example 2.

This suggests that care is needed if the introduction of a turning vane(s) is to have a real benefit. Additional analysis is required to assess the effect on turbulence reduction, number of vanes, vane size, and position.

Inlet

Flow into filter unit

Page 8: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

Results – Example 4

Various views of velocity data based on Example 4.

Page 9: PHOENICS Pressure Drop in 90 0 Bend. Introduction This presentation outlines the modeling of the pressure drop in a 90 0 bend for a range of configurations

END

40 High Street, Wimbledon, London, SW19 5AUTel: 020 8947 7651Fax:020 8879 3497

Web: www.cham.co.uk E-mail: [email protected]