Fly ash Unloading by Using Pneumatic system

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Posted in: , on 27. Oct. 2005 - 13:43

I want your help for checking Fly ash unloading system design.

Specification given below:-

Material specification:-

Type of material: Dry Fly ash

Finesse:- 3000 Blaine

Temp.:-45 Deg.C

System Description: - We are planning for install the Fly ash Addition system at our cement mill Discharge. For this Fly ash transport by tanker Capacity: 30 to 40T from nearest power plant and unload into storage Bin (Cap.:-100 T/ 5.5Mtr. Dia X 8.5M Ht. With Areation system) by using the Pneumatic system. System air supplied by Root Blower/ Air compressor. System design for 25-30 Minutes Tanker unloading times..

Total Height of Hopper:-16M

Piping geometry:- Vertical Length:- 16.5M

Horizontal Length:-5 M (From Tanker Outlet to Unloading Header)

No. Of Bend: - 3 Nos. Angle: - 90 Deg.

Our system designer given following specification for same system.

Pipe Dia: 100 NB(4” NB)

Air compressor Specification: - 19 Cub.M /Min FAD, Pressure: - 2.5 Bar.

Please following confirm:-

1.Air compressor suitable for this system? As per my opinion Root Blower suitable for this system. Because Root Blower give continues pressure and Air flow. Please confirm

2.Recommended Air requirement & pressure (19 Cub.M/Min FAD and pressure-2.5 Bar) is sufficient? May be it very higher? Please check.

3.Air pressure is higher for Tanker vessel pressure design. Also please check.

I hope & waiting for your favorable reply immediate.

Re: Fly Ash Unloading By Using Pneumatic System

Erstellt am 27. Oct. 2005 - 01:16

I think your are after the same information as Mr Bharat kindly check the thread

"Unloading Fly Ash from Bulk Tanker "

It seams Your designer has already had plenty of feedback.

Mantoo

Re: Fly Ash Unloading By Using Pneumatic System

Erstellt am 27. Oct. 2005 - 07:36

dear me patel

Indeed, as mr Mantoo said, it seems to be the same information as discussed with mr bharat.

To answer your questions :

1)Air compressor is OK (see also Mr bharat)

The compressor must be a oil free compressor with internal adiabatic compression, as a Roots blower (with isochoric compression) can deliver pressures up to 0,8 to 1,0 bar(o) maximum, against high temperatures and high energy consumption.

A screw compressor also delivers a constant flow of air (displacement principle compressor)

The delivered pressure is caused by the flow resistance of the fly-ash/air mixture in the pipeline and varies with the loading ratio (not constant)

2)If the design pressure of the system is higher than the allowable pressure of the tanker, then a lower pressure system must be designed for the required capacity.

This will result normally in a higher air flow, lower pressure and bigger pipelines and filters on the silo.

The pipeline diameter of 4” combined with 19 m3/min is certainly not the optimum (see also Mr bharat)

If you would like me to calculate 4”, please let me know.

best regards

Teus