Pick up velocity

dagiraldo
(not verified)
Posted in: , on 2. Aug. 2006 - 20:01

Dear all

I'd like to know when I perform calculations, I should consider the pick-up velocity at which point:

1. At the inlet of the system ?

2. At the inlet of the blower ?

3. At the rotary valve feeder ?

4. At the end of the line ?

Thanks in advance

Daniel Giraldo

Re: Pick Up Velocity

Posted on 2. Aug. 2006 - 07:33

Pick up velocities are calculated at solid feed point. This point has the maximum conveying line pressure and lowest air velocity.

Mantoo

Re: Pick Up Velocity

Posted on 2. Aug. 2006 - 07:54

Dear Mr giraldo,

The pick-up velocity is the air velocity at the location where the material-air mixture is formed.

Normally this is at the intake of the system, f.i. under a rotary lock.

The velocity at the intake of the blower is not important for the pneumatic conveying calculation. (there is no material there)

BUT, you should consider the air velocity at any location in the pipeline.

As the air expands along the pipeline, the velocity increases, if the pipeline diameter si kept constant.

If the air velocity becomes too high, the pipeline diameter can be increased (Stepped pipeline)

The air velocity at any location in the pipeline must be sufficiently above the local suspension velocity of the material, to prevent sedimentation, but low enough to prevent damaging the particles or using excessive energy.

This is the case for pressure conveying as well as vacuum conveying.

Best regards

teus

Teus

dagiraldo
(not verified)

Thanks

Posted on 2. Aug. 2006 - 11:57

Thanks a lot Mantoo


Originally posted by Mantoo

Pick up velocities are calculated at solid feed point. This point has the maximum conveying line pressure and lowest air velocity.

dagiraldo
(not verified)

Thanks

Posted on 2. Aug. 2006 - 11:59

So I have to find an operation point which assure that I overcome the minimal velocity of sedimentation not expending too much energy, nor damaging the particles or the pipes and equipment... Am I right ?

Thanks for your help


Originally posted by Teus Tuinenburg

Dear Mr giraldo,

The pick-up velocity is the air velocity at the location where the material-air mixture is formed.

Normally this is at the intake of the system, f.i. under a rotary lock.

The velocity at the intake of the blower is not important for the pneumatic conveying calculation. (there is no material there)

BUT, you should consider the air velocity at any location in the pipeline.

As the air expands along the pipeline, the velocity increases, if the pipeline diameter si kept constant.

If the air velocity becomes too high, the pipeline diameter can be increased (Stepped pipeline)

The air velocity at any location in the pipeline must be sufficiently above the local suspension velocity of the material, to prevent sedimentation, but low enough to prevent damaging the particles or using excessive energy.

This is the case for pressure conveying as well as vacuum conveying.

Best regards

teus