Pneumatic Transport Phase

Section summary
1. Geldart Classification
2. The different solids / air phases in a pneumatic transport line


Pneumatic Transport
Types of pneumatic transport
Conveying phases
Dilute Phase transport
Dense Phase transport
Air mover
Roots Blower
After Cooler
Airlock Rotary Valve
Product inlet / Injector
Piping
Pick-up velocity
Conveying speed / velocity
Air volumetric and mass flowrate
Pipe Equivalent Length
Solids velocity in pipe
Bends
Solids Breakage
Pressure drop
Pipe Diameter or Bore
Design methods
Pipe Blockage
Powder Build-up
Selecting dilute or dense phase
Horizontal Conveying
Vertical Conveying

1. Geldart Classification

Be careful, not all the solids can be transported with any technology. Actually, the adequacy of a particular technology will depend on the fluidization properties of the solid to be transported. Before designing a system, the class of the solid must be established. Such class is determined thanks to a classification proposed by Geldart in 1973.

Class A : powders adapted to dense phase conveying, they have a very high and lasting aeration. They can be transported at high concentration but do not form naturally some plugs, an active system is therefore require to create them.

Class B : powders adapted to dense phase conveying, will naturally flow in plugs (dune)

Class C : these cohesive powders are probably not transportable in dense phase, however some exceptions exist

Class D : these powders can be transported in dense phase at concentration in between class B and class A

Fluidization of powders Geldart Classification

Figure 1 : Geldart classification

2. The different solids / air phases in a pneumatic transport line

It is important to understand how the concepts of lean phase and dense phase translate on the way the product is flowing in the pipe. Basically, depending on the velocity of the transporting gas, 5 flow regimes can be identified.

Table 1 : Conveying phases

Gas speed Flow regime Conveying pipe Aspect Comments
High speed (15-40 m/s) Dilute Phase Pneumatic conveying lean phase flow regime aspect Basically, any solid can be transported in dilute phase, however the constraints applied to the solid make it suitable only for product which are not sensitive to breakage and which are not too hard and abrasive for the piping.
Particles are in suspension in the gas and are not depositing on the transport pipes.
Medium speed (8-15 m/s) Dense phase (saltating flow) Pneumatic conveying dense phase saltation flow regime aspect When the gas velocity decreases, the pressure drop decreases to a minimum and some particles form a continuous layer in horizontal pipe sections. Deposits are not permanent and conveying is actually happening. The concentration is not constant over a pipe section since more particles are at the bottom of the pipe.
Low speed (3-8 m/s) Dense phase discontinuous - Dune Pneumatic conveying dense phase ondulating flow regime aspect When decreasing further the gas velocity, the pressure drop increases again and a flow regimes where plugs are formed is appearing. The dune flow actually happens for fine products. The pressure drop will depend on the length of the plugs formed, thus the incentive to actively control them thanks to the process. One common method for this kind of flow regime is to install regular air injection in the pipe that will help to "cut" the plugs.
Low speed (3-8 m/s) Dense phase discontinuous - Pulsating Pneumatic conveying dense phase pulsating flow regime aspect This flow regime is close to the dune flow presented above but is this time more happening with coarse materials. Observing the flow, it is clearly observed that it starts / stops, thus "pulsating". Plugs are created naturally thanks to the higher porosity of the solid compared to other more cohesive powders.
Very low speed (3-8 m/s) Dense phase continuous Pneumatic conveying dense phase continuous flow regime aspect Decreasing further the gas velocity, and for solids that are able to be conveyed under this regime, a continuous dense phase flow is established. Basically there is only one big plug. However, this creates very large pressure drops, which makes this regime limited to very short distances.

It must be noted that the particles circulate at a lower speed than the gas. Depending on the flow regime, the particle average speed can be 0.4 to 0.8 times the gas velocity.




Do you want to know more ?
www.powderprocess.net is covering all aspects of solids and powder processing and handling
The pages below will probably interest you !
SOLIDS MIXING HANDBOOK
Answers ALL your questions on solids and powder mixing
QUALITY of MIX / MEASURING DEGREE OF MIXING
All you need to know about measuring the degree of mixing (Coefficient of Variation) of a dry mix
SEGREGATION OF POWDERS / DEMIXING
All on the physical phenomena causing segregation of particles and how to avoid them
GRINDING and MILLING
All on main size reduction processes, key equipement, design consideration..etc..
POWDER Properties
All on powder key physical characteristics, among others : flowability, density...etc..
EQUIPMENT HANDBOOK
All equipment found in bulk solids handling industries, explained, with design tips...
You can find much more through the menus at the top of the page !