Solids Particle Velocity in pneumatic conveying (dilute phase)
Types of pneumatic transport
Dilute Phase transport
Dense Phase transport
Airlock Rotary Valve
Product inlet / Injector
Conveying speed / velocity
Air volumetric and mass flowrate
Pipe Equivalent Length
Solids velocity in pipe
Pipe Diameter or Bore
Selecting dilute or dense phase
During the pneumatic transport of a powder in a pneumatic conveying line, the air is bringing the energy necessary to move the solids all along the pipe. Air velocity can be calculated easily thanks to the air flowrate and pipe diameter but it would be wrong to assume that the solid speed in the pipe is equal to the conveying air velocity, particularly in dilute phase. Indeed, the particles of solids won't be carried out all the way at the same velocity than the air as the particles will resist the air flow (drag), bounce on the pipe walls, settle... which will slow them down. As a consequence the particle conveying velocity will be less than the air conveying velocity. The factor in between the 2 velocities is called slip factor.
The particle conveying velocity is calculated from the air conveying velocity thanks to the slip factor :
Equation 1 : calculation of the particle conveying velocity
- up = solid particles conveying velocity (m/s)
- fslip = slip factor
3. Usual values for dilute phase conveying
Typical values of slip factors and thus of solid particles conveying velocity can be found in litterature.
Table 1 : Usual values of
Source : Theory and Design of pneumatic conveying Systems, Agarwal, Powder Handling and Processing, 2005.
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