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Solids Handling & Processing

Novel and Unique Method to Predict and Manage Segregation in Hoppers, Silos and Stockpiles

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Experts at The Wolfson Centre for Bulk Solids Handling Technology have recently developed a new Cellular Automata (CA) based model to predict segregation in bulk materials handling.

The tendency for bulk solids that have a range of particle sizes to naturally segregate in handling causes a variety of common problems, including excessive dust emission leading to risks of explosion and fire, also variation in handling properties causing flow hang-ups, processing problems and cargo specification violations.

Predicting segregation is the first essential to managing it and minimising its effects.  This model, which has been validated against full scale tests on 30,000 tones silos at Immingham port in the UK.  The use of the model has allowed a clear assessment of where in the handling chain the most influential operations are, and demonstrated that careful management of the filling and discharging procedures can significantly reduce the problem.  Especially where there are silos with multiple outlets, great improvements in material consistency can be made by optimising the order of discharge.

The model works by tracking the in-flow, piling up and out-flow of the material through a volume of calculation cells in a storage space, the transfer of particles of different sizes between these cells, and hence predicts the distribution of material sizes or species in the discharge.  

The validation against the operation of the full scale silos has shown the accuracy of the model and its ability to accurately predict the effect of different operating conditions.

segregated materials
Segregation upon discharge

Simulation results:

Silo filling

The cross sections of a silo are shown in Fig 1. Dark brown areas in figures show higher fines accumulation compared to the light brown areas. Cells with very pale brown colour are coarse materials.

Silo 2 cross section - for text

Figure 1: Three cross sections of a silo after filling with a mix of fines and coarse particles;

Light colour = low fines, dark = high fines, white = empty space

Silo emptying

  1. The output arrays of the simulations were captured, and the calibrated model predicted outcomes against experimental data were plotted.
  2. The solid line in Figures 2 is the model predicted fines content and red stars are the experimental data points.

Silo2 Validation

Silo 2
Number of Cells Discharged

(a) Silo 2 Validation with experiment data.

Silo3 Validation

Silo 3
Number of Cells Discharged

(b) Silo 3 Validation with experiment data

Figure 2: 3D CA model validation against 30,000 tonne industrial silos

If you would like to know more, please contact Dr. (Jeff) Susantha Dissanayake via email: wolfson-enquiries@gre.ac.uk 

or phone +44 20 8331 8646

Alternatively, you can attend a free seminar on this subject on 30 September by registering here

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    Richard Farnish

    Richard Farnish has been employed at The Wolfson Centre for Bulk Solids Handling Technology since January 1996 and teaches the science of and technologies for handling powders and granular materials in the process industry sector. In conjunction with these academic lecturing duties, he teaches a large number of industrial short courses at the Medway Campus and at clients’ premises
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