Pneumatic Conveying of Calcined Alumina

Posted in: , on 23. Jan. 2009 - 02:09

Lean Phase Pneumatic Conveying for Calcined Alumina

Hello Everyone,

I have already posted this question on a different thread about Lean phase conveyors for Calcined Alumina.

I am learning how to design pneumatic conveyors. I don’t have any experience in this field (I am a new graduate mechanical engineer). I need to determine the air flow rate and the pipe diameter for the following system:

- Pressure System (not Vacuum)

- Conveying rate : 11 t/h

- Horizontal Distance : 80 m

- Vertical distance : 19 m

- Number of 90 degree bends: 6

- Material: Al2O3: Size: 15 micrometer

Density: 3900 kg/m3

Bulk Density: 1000 kg/m3

Material temperature: 120 C

I need know the solid loading ratio so i can calculate the mass flow rate of air (because i already know the conveying rate). I assume that the ratio for calcined alumina is low. So i tried to use a ratio of 5. This gave air flow rate of 24.39 m3/min and a 180 mm diameter pipe. Does this looks right to anyone?

i also need to select a blower or a fan for the system. I am assuming that an axial fan with low pressure and high volume flow rate will do the job. Does anyone have any suggestion concerning this issue?

I choose a rotary valve as a feeding device, but Teus Tuinenburg (from the previous thread) did not recommend a rotary valve for alumina because of high abrasive properties. I may have to reconsider the rotary valve then.

I hope someone can put me on the right track. Any information, equation, suggestion will be much appreciated.

Regards,

Tony

Re: Pneumatic Conveying Of Calcined Alumina

Posted on 23. Jan. 2009 - 10:18

Dear Tony,

I calculated your installation.

The required 11 tons/hr results in a conveying pressure of approx 0.32 bar. (see attachment)

The installation design conveys approx 50 tons/hr at 1.2 bar

The application of a rotary valve for a 15 micron sized product is very questionable.

The clearance between the rotor and the housing is also in that order of magnitude and the high temperature of the alumina does not make it easier to maintain that clearance under all circumstances.

Using a fan in a pneumatic conveying system is a bit problematic, because the fan volume decreases with rising pressure.

A positive displacement pump (blower. screw compressor) is therefore preferred.

Rather than designing and building a system on your own, it might be advisable to contact a manufacturer with proven experience in this field.

Have a nice day

Teus

Attachments

aluminapnconvinst (PDF)

Teus

Re: Pneumatic Conveying Of Calcined Alumina

Posted on 27. Jan. 2009 - 12:52

Tthanks Teus, I think your data will help me in learning the design of pneumatic conveyors

Conveying Possibilities.

Posted on 28. Jan. 2009 - 02:03

Hello Tony,

If you do decide to opt for conveying with rotary valves and associated pipewrk we can assist with the internal linings for both.

Alternatively you coul sned to us your details and we can make a proposal.

Please send to; trevor@densit.co.uk