Conveying of De-oiled Bleaching Earth

Hi,

We have an application wherein we have de-oiled Spent Bleaching Earth which is to be conveyed.

This material is finer than talcum powder and is at almost 80-90 degC.

WHat would be the correct method of conveying such material?

We are presently using screw conveyor which discharges into a redler with an upward incline.

Both do not work very well since the powder has a tendency to flow like water.

Thanks in advance.

Re: Conveying Of De-Oiled Bleaching Earth

Posted on 10. Oct. 2009 - 11:19

Dear onyxgaze,

Pneumatic conveying loves materials that flow like water.

The set up of such a pneumatic conveying system depends on the project conditions.

However, there are a number of solutions for various situations.

If you describe the particle size, conveying rate and application conditions, the forum members will certainly come up with suggestions.

Have a nice day

Teus

Teus

Re: Conveying Of De-Oiled Bleaching Earth

Posted on 10. Oct. 2009 - 07:27
Quote Originally Posted by onyxgazeView Post
We are presently using screw conveyor which discharges into a redler with an upward incline.

Interesting, I've know quite a few such arrangements work with fine powders that can fluidise? Who supplied the 'redler' (remembering that Redler is registered trade mark)

Re: Conveying Of De-Oiled Bleaching Earth

Posted on 10. Oct. 2009 - 08:31
Quote Originally Posted by onyxgazeView Post
Hi,

We have an application wherein we have de-oiled Spent Bleaching Earth which is to be conveyed.

This material is finer than talcum powder and is at almost 80-90 degC.

WHat would be the correct method of conveying such material?

We are presently using screw conveyor which discharges into a redler with an upward incline.

Both do not work very well since the powder has a tendency to flow like water.

Thanks in advance.

==========================================================

A diapragm pump can and will move powders easily and their are many manufacturers including Warren Rupp, Wilden, and Ingersoll Rand.

These pumps use single or double diapragm pumps to move powders with ease reducing dust and handling problems.

Here are a few links;

warrenrupp.com

wildenpump.com

ingersollrand.com

lzaharis

Re: Conveying Of De-Oiled Bleaching Earth

Posted on 13. Oct. 2009 - 01:34
Quote Originally Posted by Teus TuinenburgView Post
Dear onyxgaze,

Pneumatic conveying loves materials that flow like water.

The set up of such a pneumatic conveying system depends on the project conditions.

However, there are a number of solutions for various situations.

If you describe the particle size, conveying rate and application conditions, the forum members will certainly come up with suggestions.

Have a nice day

Teus

Thanks Teus and others.

The complete application is one in which we are first running a slurry made of spent bleaching clay in hexane through a Rotary Vaccuum Drum Filter. The cake as it falls of the drum is conveyed by a drag link conveyor into a desolventiser from where it discharges in the form of a fine powder into a screw conveyor built to seal at the inlet. The sealing screw discharges the fine powder at approx 95 degC (now free of all hexane) into the "redler".

The particle size of the powder would be from 5 to 25 microns, with a bulk density of approx 0.5 and the flow rate would be upto 50 Tons/day. The temperature is 95 degC.

We are facing problems in the slurry handling part too, due to the presence of sand in the feed material, but I guess will need a separate forum for getting answers to that one.

Would appreciate any further inputs here.

Regards.

Re: Conveying Of De-Oiled Bleaching Earth

Posted on 13. Oct. 2009 - 09:40

Dear onyxgaze,

You have not described the problems, which you experience with the conveying of the bleach with the screw and the chain conveyor.

However, I assume it is related to irregular rates, due to the fluidizability of the bleach, causing volumetric filling problems in the screw and flow back in the inclined chain conveyor.

The capacity of 50 tons/hr # 2.1 tons/hr # 0.58 kg/sec # 1.16 dm3/sec is not much.

Also assuming that the transport distance is rather short, a pneumatic conveying system, designed for a very low pressure could work with a solid conveying eductor.

Have a look at: http://www.foxvalve.com/iindex2.html

The eductor creates a slight under pressure at the outlet of the feeding screw and thereby improves the functioning of the screw.

The receiving hopper needs to be closed and equipped with a self cleaning de-dusting filter with fan, pressure safety valve and level-testers.

A blow pot system is also an option, but probably more expensive.

Ask a quotation from a respectable vendor.

Success

Teus

Teus