Screen

From SysCAD Documentation

Navigation: Main Page -> Models -> Size Distribution Models

General Description

The screen may be defined as a simple splitter or as a full screening model. The user may also set the number of screens modelled by the unit. this allows the user to emulate a screen bank with a single unit.

The user may select Screen or Split mode:

If the Split mode is chosen, the solids in the screen feed need not have a size distribution, as the model will separate the solids and liquids based on a user defined split.
If the Screen mode is selected then the main requirement for using this option is that the feed must contain solids with size distribution information. Please see Size Distribution (PSD) and Size Configuration for more information on including a size distribution in the project.
- The model will calculate the split of solids between the top-size, mid-size (optional) and under-size flows based on the cut point (either calculated or defined) and the size distribution of the feed stream.
- The unit may simulate either a single or double deck screen.
  If streams are connected to the top and mid size products, the screen will automatically become a double deck screen. The user must then configure each deck of the screen separately.
- The user may specify different screening methods on each deck, i.e. the top deck may have a user-defined partition curve and the lower deck may use the Karra method to calculate the solids split.
- The user must define the amount of feed liquid reporting to the over size product on each deck. The balance of the liquid will report to the under size.

There are a number of screening methods available to define the solids split:

The Karra method (Note that this method is only valid for cut apertures > 1mm),
A partition curve is used to calculate the screen products,
Whiten method, and
Whiten Beta Method.

Diagram

The diagram shows the default drawing of the Screen, with all of the streams that are available for operation of the unit. The physical location of the streams connecting to the Screen is unimportant. The user may connect the streams to any position on the unit.

Inputs and Outputs

Label	Input / Output	No. of Connections		Description
		Min	Max.
Feed	In	1	5	The slurry feed to the Screen
Wash Water	In	0	5	Wash water to the Screen
Oversize	Out	0	1	The over size from the unit
Midsize	Out	0	1	The mid size from the Screen - only if a double deck screen is required.
Undersize	Out	1	1	The under size from the unit

Model Theory

The model will simulate a Screen using one of the user defined methods. All of the models calculate the solids separation based on a size distribution. The liquids separation is defined by the user as the amount of moisture reporting to the over size. The balance of the feed liquid will flow through the screen.

The d₅₀is defined as the particle size that has a 50% probability of reporting to either the Screen over or under size product. The majority of the particles finer than this size will report to the under size, while the majority of those coarser will report to the over size.

1. Karra Method

This method is based on a model proposed by V.K Karra¹. The solids split is calculated using the d₅₀ of the screen. This may either be defined by the user, d50_Method, or calculated by the model using the physical screen dimensions and feed size distribution.

Note: The Karra method is only valid for screen cut apertures greater than 1mm.

With the d50_Method the user defines the cut point of the Screen, the d₅₀. The model then calculates the solids split directly, as shown in equation (3).

With the ScreenArea option the user defines:

The Screen area
The cut aperture (> 1mm - the model will not allow the user to specify a smaller aperture), and
Whether it is a wet screening application.

The model will then calculate the d₅₀ based on these user-defined parameters and on the size distribution of the feed. This d₅₀ is then used to calculate the solids split, as shown in equation (3).

The model calculates the d₅₀ of the Screen from the following equations¹

(1) $\mathbf{\mathit{d_{50} = h_T\left(\frac{TheoreticalUndersize(tph)/ScreenArea(m^2)}{ABCDEFG}\right)^{-0.148}}}$

where the Theoretical Undersize is the mass of solids with sizes less than h_T

The Cut aperture h_T, in mm, is given by:

(2) $\mathbf{\mathit{h_T=\left(h+d\right)cos\varphi-d}}$

h - Aperture of square mesh, mm

d - Wire diameter, mm

$\mathbf{\mathit{\varphi}}$ - Screen angle of inclination to the horizontal

The modifying factors in the denominator of equation (1) are obtained as follows:

Factor A.	h_T < 50.8mm	A = 12.1286 * (h_T)^0.3162 - 10.2991
Factor A.	h_T >= 50.8mm	A = 0.3388 * h_T + 14.4122
Factor B.	Where Q - % Oversize in feed to screen deck.
	Q =< 87	B = 1.6 - 0.012 * Q
	Q > 87	B = 4.275 + 0.0425 * Q
Factor C	Where R - % half size feed to the screen deck.
	R =< 30	C = 0.012 * R + 0.7
	30 < R < 55	C = 0.1528 (R)^0.564
	55 =< R < 80	C = 0.0061 (R)^1.37
	R >= 80	C = 0.05 * R - 1.5
Factor D.	Where S is deck location, top deck S = 1, second deck S = 2
Factor D.		D = 1.1 - 0.1 * S
Factor E.	Wet Screening Factor, T = 1.26 * h_T
	T < 1	E = 1.0
	1 =< T =< 2	E = T
	2 < T < 4	E = 1.5 + 0.25T
	4 =< T =< 6	E = 2.5
	6 < T =< 10	E = 3.25 - 0.125T
	10 < T < 12	E = 4.5 - 0.25T
	12 =< T =< 16	E = 2.1 - 0.05T
	16 < T < 24	E = 1.5 - 0.125T
	24 =< T =< 32	E = 1.35 - 0.00625T
	T > 32	E = 1.15
Factor F		F = U/1602, where U = Bulk Density (kg/m²
Factor G Near-Mesh factor		G = 0.844 * (1.0 - X_n/100)^3.453, where X_n = % near size feed to the screen deck, % in the size interval 1.25h_T to 0.75h_T

Split Efficiency

The model then uses the d₅₀, either defined as in (1) or calculated in (2), to calculate the recovery to the over size in each size range (y_i) using the following equations:

(3) $\mathbf{\mathit{y_i = 1-exp\left(-0.693(x_i)^{5.846}\right)}}$

where

$\mathbf{\mathit{x_i = \frac{Particle Diameter_i}{d_{50}}}}$

Fines Bypass

The mass of solid material reporting to the over size product may be influenced by the amount of liquid reporting to the over size. The fine material often bypasses to the over size with the liquid, or by adhering to the coarse material. The model allows the user to define the method of compensating for fines bypass in one of three ways:

None
In this case the amount of material reporting to the oversize products is defined by equation (3).
Fines in Moisture
This assumes that some of the solid material will always follow the liquid split. The corrected recovery to over size is calculated using equation (4):
(4) $\mathbf{\mathit{y'_i =y_i + R_f(1 - y_i)}}$
where y_i = Recovery to the over size, calculated in equation (3)
R_f = fraction of feed liquid reporting to the over size product
Minimum Fraction reports to Over size
This method allows the user to set a minimum fraction of the feed material that will report to the over size product. For example, if the user sets the minimum fraction at 5%, then the model will calculate the recovery to over size using equation (3). If this figure is under 5%, the model will increase the value to 5%, otherwise it will use the calculated value.

Assumptions

The equations are based on screening crushed stone. While the characteristics of metallic ores are very similar, this may not be true for sand and gravel applications.
The Cut Aperture, h_T is greater than 1mm.

Reference:

1. V.K.Karra., "Development of a model for predicting the screening performance of a vibrating screen", CIM Bulletin, April 1979.

2. User Defined Partition Curve

In the case of the partition curve, the model will distribute the feed material based on the user defined partition curve. The user defines the screen partition curve as the fraction of the feed to the screen reporting to the over size product. The screen model will ensure that the products follow this curve.

3. Whiten Method

This method is based on a model proposed by Whiten. The solids split is calculated using the user specified d₅₀ of the screen with correction factors for efficiency and water bypass.

The Reduced Efficiency curve to the oversize is given in equation (1):

(1) $\mathbf{\mathit{E_{o a i}=\frac{exp(\alpha x_i)-1}{exp(\alpha x_i)+exp(\alpha)-2}}}$

where

$\mathbf{\mathit{x_i = \frac{Particle Diameter_i}{d_{50}}}}$

d₅₀ = cut-size or separation size, the size which divides equally between oversize and undersize.

$\mathbf{\mathit{\alpha}}$ = efficiency parameter. High values of $\mathbf{\mathit{\alpha}}$ (>4) indicate very good separations.

Fines Bypass

The mass of solid material reporting to the over size product may be influenced by the amount of liquid reporting to the over size. The fine material often bypasses to the over size with the liquid, or by adhering to the coarse material.

The corrected recovery to over size is calculated using equation (2):

(2) $\mathbf{\mathit{E_{o c i}=\frac{E_{o a i}-R_f}{1-R_f}}}$

where:

E_oci = corrected recovery to the over size

E_oai = actual recovery to the over size (calculated in equation (1) above)

R_f = Proportion of feed liquid reporting to the over size product

The Fraction of feed liquor reporting to the under size, C, can be found using equation (3):

(3) C = 1 - R_f

References:

1. Whiten W.J. "Lecture notes for winter school on mineral processing." Dept. Min & Eng, University of Queensland, Aug 1966 (Lynch and Bull)</span>

4. WhitenBeta Method

This is the modified method by Whiten to accommodate some abnormal "bumps" in the fine size end of the Efficiency curve.

The Reduced Efficiency curve to the oversize is then as follows:

(4) $\mathbf{\mathit{E_{o a i}=C\left[\frac{(1+\beta\beta^*x_i)(exp(\alpha)-1)}{exp(\alpha\beta^*x_i)+exp(\alpha)-2}\right]}}$

where:

Beta (β) - is the term introduced to control the initial rise in the curve at fine sizes. If this term is set to 0 then the equation is the same form as (5) in the previous heading.

BetaStar (β*) is derived iteratively from β so that E_oai = (1/2)C when d_i = d₅₀

Data Sections

The default access window consists of 4 or more sections,

The first section, which has the same name Screen, allows the user to set the number of screens to emulate and it also contains some general information relating to the unit.
The second section, TopDeck, displays the relevant input and results fields for the top deck of the screen.
The third section, PartCrv, displays the partition curve data for the top deck of the screen.
If the user connects a stream to the Midsize connection, then access windows for the Bottom Deck and its PartCrv will be added at this position.
The section, Info, fully described in Info Tab Page Section.
The section, Links, only visible in SysCAD 9.2, contains a summary table for all the input and output streams. See Links Table.
The last section is the Audit. See Model Examples for enthalpy calculation Examples.

Class: Screen - The first tab page in the access window will have this name.

Tag / Symbol	Input / Calc	Description/Calculated Variables / Options
Common First Data Section
NumScreen	Input	The number of Screens represented by the model. This number is important if the Karra Method is used, as it will affect the Screen Area, and hence the calculation of the d₅₀. The default is 1.
ShowQFeed	Tickbox	Show the total feed to the screen.
Top and Bottom Deck The parameters in this section change depending on the Screen mode chosen by the user. The parameters for each mode will be detailed separately. Fields that are common to all modes and Methods are described in the Common Data section. Single or Double Deck screen: If there is no connection to the Midsize, then this unit emulates a single deck screen and only the Top Deck is visible. If a connection is also made to the Midsize, then a double deck screen is emulated and a further section becomes visible, Bottom Deck.
Mode	Screen	The unit is required to model a screen with the feed having a size distribution. If the user selects this mode then they may choose between a number of options to model the screen. These are described separately.
Mode	Split	The unit is a simple mass splitter. The feed does not need size distribution. If the user chooses this mode then they must define the solids and liquids split from the unit.
Split Mode
OSSolids	Input	Fraction of Feed solids reporting to the over size product.
OSMoist	Input	Fraction of Feed liquids reporting to the over size product.
Screen Method
Method	Karra	The screen model will calculate the solids split using the Karra method. The user may either specify the d₅₀ or set the screen area and cut aperture and allow the model to calculate the d₅₀.
	PartitionCrv	The user inputs a Partition curve for the screen products. The screen will use this curve, so the size distribution in the feed to the screen has no effect on products. Note: In this case a single partition curve is used for all the size distributions.
	Individual_PartCrv	The user inputs individual Partition curves for the screen products for each size distribution. The screen will use these curves, so the size distribution in the feed to the screen has no effect on products.
	Whiten	The screen model will calculate the solids split using the Whiten method. The user must specify the d₅₀ and alpha, a measure of the sharpness of separation.
	WhitenBeta	The screen model will calculate the solids split using the Whiten method, with an additional parameter, beta, to account for inconsistencies in the fine fractions.
OSMoist	Input	Fraction of Feed liquids reporting to the over size product.
Requirements - Karra Method
Karra Method	Define_d50	The user specifies the d₅₀ of the screen.
Karra Method	ScreenArea	The user specifies the Area and the throughfall aperture, h_T, of the screen and the model calculates the d₅₀.
d50	Input	The d₅₀ of the screen. (Only visible if the user has selected Define_d50.)
SArea	Input	The Screen area of a single screen deck. (Only visible if the user has selected ScreenArea.)
Total Area	Calc	The product of the area of a single screen deck and the number of screens. (Only visible if the user has selected ScreenArea.)
CutAper	Input	The throughfall aperture h_T of the screen. This MUST be greater than 1mm - the model will not allow the user to specify a value less than 1mm. (Only visible if the user has selected ScreenArea.)
Wet	Tickbox	If this is enabled then this is a wet screening application, otherwise it is treated as dry screening. This has implications in calculating the d₅₀. Wet screening has the effect of decreasing the d₅₀. (Only visible if the user has selected ScreenArea.)
Both the Screen Area and the d50Method require a further parameter to calculate the distribution of the fine fraction in the feed.
FinesMethod	None	The model will calculate the distribution based on the d₅₀ with no further compensation for the fine material.
	Fines_in_Moist	The model will use the corrected recovery to oversize given in equation (4). This assumes that some of the solid material will always follow the liquid split. Note: With this method, if the user specifies the over size moisture such that all of the feed liquid reports to the over size, then all of the solids will also report to the over size.
	Min_to_O/S	The model will ensure that a minimum fraction of solids in each size distribution reports to the oversize product. For example, if the user specifies a minimum of 5%, then at least 5% of each size distribution will report to oversize.
Requirements - Whiten Method
d50	Input	The required cut point of the screen, or the particle size with 50% probability of reporting to the over or under size.
Alpha	Input	The Efficiency parameter, alpha. A value > 4 indicates very good separation.
Rf	Input/Calc	The proportion of feed liquid reporting to the over size product to be used in the fines calculation. The user may set this value or the C value. If C is changed, then Rf will be adjusted.
C (=1-Rf)	Input/Calc	The proportion of feed liquid reporting to the under size product to be used in the fines calculation. If Rf is changed, C will be adjusted.
Requirements - Whiten Beta Method
d50	Input	The required cut point of the screen, or the particle size with 50% probability of reporting to the over or under size.
Alpha	Input	Efficiency parameter, alpha. A value > 4 indicates very good separation.
Beta	Input	The Beta Efficiency parameter. This value takes into account uncertainties in the finer size fractions.
Beta*	Calc	Efficiency parameter.
Rf	Input/Calc	The proportion of feed liquid reporting to the over size product to be used in the fines calculation. The user may set this value or the C value. If C is changed, then Rf will be adjusted.
C (=1-Rf)	Input/Calc	The proportion of feed liquid reporting to the under size product to be used in the fines calculation. If Rf is changed, C will be adjusted.
Requirements - Other
CalcIntersectPt	Tickbox	The user may enable this parameter if they wish to see the calculated Intersection Point for the screen.
RateCorrection	Tickbox	The user may enable this parameter if they wish to take into account the rate of feed to the screen.
Capacity	Input	The user defined capacity of each screen deck.
TotalCap	Calc	The calculated capacity of all of the screen decks. This is the user defined capacity per screen deck multiplied by the number of screens.
Screen Feed	Output	The Solids feed to the screen deck.
Track Status	Tick Box	If this box is checked, the Screen will flag a warning if the Screen Feed is greater than the Total Capacity.
Results
Calc d50	Calc	The calculated d₅₀ of the screen. This is the particle size that has a 50% probability of reporting to either the Screen over or under size product.
IntersectPt	Calc	The calculated intersection point of the screen. This is the size at which the cumulative percentage oversize of the fine product (under size) is equal to the cumulative percentage undersize of the coarse product (over flow). Note: This field is only visible if the user has enabled the CalcIntersectPt tickbox.
SoltoO/S	Calc	The calculated fraction of solids in the Feed that reports to the over size product.
LiqtoO/S	Calc	The calculated fraction of liquids in the Feed that reports to the over size product.
OSDens	Calc	The density of the over size stream. (This is the density of the slurry stream.)
USDens	Calc	The density of the under size stream. (This is the density of the slurry stream.)
Underflow Efficiency
UF_Size	Input	The particle size of interest.
UF_Efficiency	Calc	The fraction of solids in the feed that report to the screen undersize of the user defined particle size (UF_Size)

Partition Curve Section/s

Each screen deck has a section showing the partition curve. If the PartitionCrv option is chosen for screening the user must input a partition curve here. Otherwise, the model will calculate the partition curve/s for the screen deck and display them on this page.

The user may either configure the partition curve as fraction Passing, or fraction Retained.

Tag / Symbol	Input or Calc	Description
The black rectangle at the top of the page is for display purposes only. The user can configure the 'Information' data to display the discharge partition curve. The two white boxes below the window allow the user to configure the lower and upper display limits of the curve.
Log > Lin	Button	This button toggles the x display between log and ln.
Auto > Fixed Scale	Button	This button toggles the display between auto scaling and user defined fixed scale.
Stepped > Smooth	Button	Toggles the display between discrete points (Stepped) and a smooth curve.
Mode	Passing	The partition curve is displayed as the fraction passing each size interval.
Mode	Retained	The partition curve is displayed as the fraction retained in each size interval.
Size Intervals	Button	> Ascending - The numbers are displayed with the large sizes at the top.
Size Intervals	Button	> Descending - The numbers are displayed with the smaller sizes at the top.
If the user has chosen to define the screening application using an overall partition curve or individual partition curves, then they can enter the size Fractions for the Discharge Partition Curve. The product from the Screen will have the same size distribution as the one defined here. If the model is using any of the other screening methods to calculate the products, then this page will display partition curves for each size distribution defined for the project.

Adding this Model to a Project

Insert into Configuration file

Sort either by DLL or Group.

	DLL:	Separ2.dll	→	Units/Links	→	Size Separation: Screen (Single/Double Deck)
OR	Group:	Size Distribution	→	Units/Links	→	Size Separation: Screen (Single/Double Deck)

See Project Configuration for more information on adding models to the configuration file.

Insert into Project

Insert Unit

→

Size Separation

→

Screen (Single/Double Deck)

See Insert Unit for general information on inserting units.

Hints and Comments

If the user selects the Fines_in_Moist method of splitting the fine solids fraction, then the following situation may arise: If the user specifies the over size moisture such that all of the feed liquid reports to the over size, then all of the solids will also report to the over size.

Screen

From SysCAD Documentation

Contents

General Description

Diagram

Inputs and Outputs

Model Theory

1. Karra Method

Split Efficiency

Fines Bypass

2. User Defined Partition Curve

3. Whiten Method

Fines Bypass

4. WhitenBeta Method

Data Sections

Top and Bottom Deck

Split Mode

Screen Method

Requirements - Karra Method

Requirements - Whiten Method

Requirements - Whiten Beta Method

Requirements - Other

Results

Underflow Efficiency

Partition Curve Section/s

Adding this Model to a Project

Hints and Comments

Views

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