Efficiency Screen

Summary

The Efficiency Screen model is an empirical screening model that splits the feed stream into undersize and oversize products from a user-defined undersize efficiency, screen opening and oversize bypass.

The model builds a size-by-size partition curve to oversize. Material coarser than the screen opening reports to oversize, material finer than a calculated minimum-size point reports according to the bypass, and the interval between the minimum-size point and the screen opening is represented by a log-linear transition.

The model should be used when screen performance is known by an overall undersize efficiency rather than by equipment geometry or a detailed partition curve. It is suitable for calibrated flowsheet studies, simplified screening stages and cases where measured or assumed efficiency is the main available performance parameter.

DPSIM model key: DPSIM.Classification.EfficiencyScreen
Category: Classification
Subcategory: Screens
Display name: Efficiency Screen

Parameters

# Parameter Description
1 Bypass to oversize (%) Fraction of fine material below the calculated minimum-size point that reports to oversize.
2 Minimum screen opening (mm) Nominal screen opening used as the upper limit of the partition transition and as the size defining theoretical undersize.
3 Undersize efficiency (%) Target undersize efficiency used by the model when the variable efficiency curve is disabled.
4 Efficiency Perturbation (%) Optional random perturbation applied to the target efficiency. A value of zero gives deterministic static behavior.
5 Coarse stream solids (%) Target solids percentage of the oversize stream. The model calculates the water assigned to the oversize stream from this value, limited by the water available in the feed.
6 Use efficiency v.s. Feed tph curve (0-no/1-yes) Enables calculation of target undersize efficiency from a linear efficiency-versus-feed-rate curve.
7 Variable Efficiency Ax (tph) Feed solids flowrate coordinate of point A on the variable efficiency curve.
8 Variable Efficiency Ay (%efficiency) Undersize efficiency coordinate of point A on the variable efficiency curve.
9 Variable Efficiency Bx (tph) Feed solids flowrate coordinate of point B on the variable efficiency curve.
10 Variable Efficiency By (%efficiency) Undersize efficiency coordinate of point B on the variable efficiency curve.
11 B point is minimum efficiency (0-no/1-yes) When the variable efficiency curve is enabled, this option limits the adopted efficiency so that it does not fall below the B-point efficiency.

Derived parameters

# Derived parameter Description Unit
1 Calculated undersize efficiency Actual undersize efficiency obtained from the final partition curve. %
2 Minimum size for partition slope Calculated lower size of the log-linear transition region. µm
3 Correlated Undersize Efficiency Efficiency calculated from the fixed parameter or from the variable efficiency curve, before perturbation. %
4 Perturbation in Efficiency Random efficiency perturbation applied in the current calculation. %
5 Target Undersize Efficiency Final target efficiency used to build the partition curve after optional perturbation and limiting. %

Model Description

The Efficiency Screen model receives one feed stream and generates two product streams. In DPSIM, the product port represents the undersize stream and the tail port represents the oversize stream.

The screen opening is converted from millimetres to micrometres:

h=1000h_mm

Where:

Symbol Description Unit
h Screen opening used in the partition curve. µm
h_mm User-defined screen opening. mm

If the variable efficiency curve is disabled, the correlated efficiency is the user-defined undersize efficiency:

η_corr=η_set

If the variable efficiency curve is enabled, the correlated efficiency is calculated by linear interpolation between points A and B:

η_corr=η_A+(η_B-η_A)(M_S^F-M_A)/(M_B-M_A)

Where:

Symbol Description Unit
η_corr Correlated undersize efficiency before perturbation. %
η_set User-defined undersize efficiency. %
η_A Efficiency at point A. %
η_B Efficiency at point B. %
M_A Feed solids flowrate at point A. tph
M_B Feed solids flowrate at point B. tph
M_S^F Feed dry solids flowrate. tph

An optional random perturbation can be applied around the correlated efficiency:

η_target=η_corr+δ

with:

-Δη≤δ≤Δη

The target efficiency is then limited to the range from 0 to 100%.

Where:

Symbol Description Unit
η_target Final target undersize efficiency used by the model. %
δ Efficiency perturbation. %
Δη Maximum absolute perturbation entered by the user. %

The model searches for the minimum-size point d_min that gives the requested undersize efficiency when combined with the selected bypass and screen opening. This point defines the lower end of the transition region in the partition curve.

The partition curve gives the fraction of each size class reporting to oversize:

E_i^O=1, d_i>h

E_i^O=B, d_i<d_min

E_i^O=B+(1-B)(log d_i-log d_min)/(log h-log d_min), d_min≤d_i≤h

Where:

Symbol Description Unit
E_i^O Fraction of size class i reporting to oversize. fraction
B Bypass to oversize. fraction
d_i Representative particle size of size class i. µm
d_min Calculated minimum-size point for the transition region. µm
h Screen opening. µm

The partition curve is limited internally to the interval from 0 to 1.

The undersize efficiency associated with a trial partition curve is calculated as:

η=100 sum_i M_i^F(1-E_i^O)/sum_(d_i<h) M_i^F

Where:

Symbol Description Unit
η Calculated undersize efficiency. %
M_i^F Feed solids mass flowrate retained in size class i. tph
E_i^O Fraction of size class i reporting to oversize. fraction

After the partition curve is established, the oversize and undersize retained masses are calculated size by size:

M_i^O=E_i^O M_i^F

M_i^U=M_i^F-M_i^O

Where:

Symbol Description Unit
M_i^O Oversize solids mass flowrate retained in size class i. tph
M_i^U Undersize solids mass flowrate retained in size class i. tph

The retained size distributions are normalized as:

p_i^O=M_i^O/sum_i M_i^O

p_i^U=M_i^U/sum_i M_i^U

The same partition curve is applied to the component-by-size matrix. For each component c:

M_(c,i)^O=E_i^O M_(c,i)^F

M_(c,i)^U=M_(c,i)^F-M_(c,i)^O

Where:

Symbol Description Unit
M_(c,i)^F Feed mass flowrate of component c in size class i. tph
M_(c,i)^O Oversize mass flowrate of component c in size class i. tph
M_(c,i)^U Undersize mass flowrate of component c in size class i. tph

The model calculates the water assigned to the oversize stream from the requested coarse stream solids percentage:

W_O=M_S^O(1-X_O)/X_O

with:

X_O=S_O/100

Where:

Symbol Description Unit
W_O Water flowrate assigned to the oversize stream. tph
M_S^O Oversize solids flowrate. tph
X_O Target oversize solids fraction. fraction
S_O Target oversize solids percentage. %

If the calculated oversize water is greater than the feed water, all feed water is assigned to the oversize stream and the undersize stream receives no water. If the target oversize solids percentage is zero, the model also assigns all feed water to the oversize stream.

The model preserves total solids and water by splitting the feed into undersize and oversize streams. The separation response is empirical and should be calibrated against screen survey data when used for design or reconciliation.

The model does not calculate screen capacity, deck loading or geometric correction factors. For capacity-based screen calculations, use the King Screen model. For a Karra partition-based screen model, use the Karra Screen model.