Gravity Classifier (Plitt-Flintoff): Difference between revisions
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== Model theory == | == Model theory == | ||
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[[File:GravityClassifierPlittFlintoff1.png|thumb|425px|Figure 1. Example partition curve predicted by the Plitt-Flintoff gravity classifier model.]] | [[File:GravityClassifierPlittFlintoff1.png|thumb|425px|Figure 1. Example partition curve predicted by the Plitt-Flintoff gravity classifier model.]] | ||
Plitt and Flintoff proposed a model that describes the classification of particles based on a consideration of settling velocity and flow conditions in gravity classification devices.{{Plitt and Flintoff (1985)}} | Plitt and Flintoff proposed a model that describes the classification of particles based on a consideration of settling velocity and flow conditions in gravity classification devices.{{Plitt and Flintoff (1985)}} | ||
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=== Classification === | === Classification === | ||
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Plitt and Flintoff's formulation applies the Reid-Plitt (1971) efficiency curve to describe the classification of particles by size.{{Reid (1971)}}{{Plitt (1971)}} | Plitt and Flintoff's formulation applies the Reid-Plitt (1971) efficiency curve to describe the classification of particles by size.{{Reid (1971)}}{{Plitt (1971)}} | ||
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The value of the sharpness parameter, <math>m</math>, can be specified for a given application, or estimated as described below. | The value of the sharpness parameter, <math>m</math>, can be specified for a given application, or estimated as described below. | ||
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=== Corrected cut size === | === Corrected cut size === | ||
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Plitt and Flintoff assume the corrected cut size (<math>d_{\rm 50c}</math>) is the size of a particle which has a settling velocity equal to the mean upward rising velocity of pulp, <math>v</math> (m/h), i.e.: | Plitt and Flintoff assume the corrected cut size (<math>d_{\rm 50c}</math>) is the size of a particle which has a settling velocity equal to the mean upward rising velocity of pulp, <math>v</math> (m/h), i.e.: | ||
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The <math>d_{\rm 50c}</math> term is implicit in the settling velocity equation. Therefore a numerical root-finding algorithm is applied to approximate the value of <math>d_{\rm 50c}</math> for a given settling velocity and pulp conditions. | The <math>d_{\rm 50c}</math> term is implicit in the settling velocity equation. Therefore a numerical root-finding algorithm is applied to approximate the value of <math>d_{\rm 50c}</math> for a given settling velocity and pulp conditions. | ||
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=== Water recovery === | === Water recovery === | ||
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The Plitt and Flintoff model requires the volume fraction of solids in the underflow, <math>\phi_{\rm UF}</math> (v/v), to be specified as an input. | The Plitt and Flintoff model requires the volume fraction of solids in the underflow, <math>\phi_{\rm UF}</math> (v/v), to be specified as an input. | ||
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The Reid-Plitt classification equation itself features the <math>R_{\rm f}</math> term, and therefore an iterative scheme is required to fully compute the Plitt and Flintoff model. | The Reid-Plitt classification equation itself features the <math>R_{\rm f}</math> term, and therefore an iterative scheme is required to fully compute the Plitt and Flintoff model. | ||
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=== Sharpness estimation === | === Sharpness estimation === | ||
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Plitt and Flintoff suggest using the following relationship to estimate values of <math>m</math>, the separation sharpness: | Plitt and Flintoff suggest using the following relationship to estimate values of <math>m</math>, the separation sharpness: | ||
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Plitt (1971) found the value of <math>m</math> was in the range of 1 - 3.8 for classifiers. As such, the sharpness estimation above may not be appropriate for larger values of <math>S</math>, depending on the application. User caution is recommended. | Plitt (1971) found the value of <math>m</math> was in the range of 1 - 3.8 for classifiers. As such, the sharpness estimation above may not be appropriate for larger values of <math>S</math>, depending on the application. User caution is recommended. | ||
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=== Density-specific classification === | === Density-specific classification === | ||
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Plitt and Flintoff's original model formulation purposely assumed that a mixture of particles of differing densities could be represented by a singular solid density value (<math>\rho_{\rm S}</math>). | Plitt and Flintoff's original model formulation purposely assumed that a mixture of particles of differing densities could be represented by a singular solid density value (<math>\rho_{\rm S}</math>). | ||
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This implementation can retain Plitt and Flintoff singular density value assumption, or compute classification curves separately for each density class, <math>(\rho_{\rm S})_j</math> (t/m<sup>3</sup>), where <math>j=\{1,2,\dots,p\}</math> and <math>p</math> is the number of density classes (or ore types, minerals etc). | This implementation can retain Plitt and Flintoff singular density value assumption, or compute classification curves separately for each density class, <math>(\rho_{\rm S})_j</math> (t/m<sup>3</sup>), where <math>j=\{1,2,\dots,p\}</math> and <math>p</math> is the number of density classes (or ore types, minerals etc). | ||
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=== Coarse solids removal capacity === | === Coarse solids removal capacity === | ||
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If the computed mass flowrate of solids to the underflow stream, <math>(Q_{\rm M,UF})_{\rm S}</math> (t/h), exceeds the solids removal capacity of the classifier, <math>(Q_{\rm M,UF})_{\rm S}^{\rm Max}</math> (t/h), the <math>{d_{\rm 50c}}</math> value is increased by a small fraction. This process repeats until the underflow mass flowrate of solids is less than the removal capacity, i.e. | If the computed mass flowrate of solids to the underflow stream, <math>(Q_{\rm M,UF})_{\rm S}</math> (t/h), exceeds the solids removal capacity of the classifier, <math>(Q_{\rm M,UF})_{\rm S}^{\rm Max}</math> (t/h), the <math>{d_{\rm 50c}}</math> value is increased by a small fraction. This process repeats until the underflow mass flowrate of solids is less than the removal capacity, i.e. | ||
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This action simulates a buildup of solids in the classifier which effectively reduces the settling pool area, driving up the cut size. | This action simulates a buildup of solids in the classifier which effectively reduces the settling pool area, driving up the cut size. | ||
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=== Sands solid content === | === Sands solid content === | ||
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Plitt and Flintoff provide the following table as a guide to the volume fraction of solids that may be expected from a classifier with a given cut size: | Plitt and Flintoff provide the following table as a guide to the volume fraction of solids that may be expected from a classifier with a given cut size: | ||
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|} | |} | ||
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=== Partition metrics === | === Partition metrics === | ||
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{{Model theory (Text, Hydrocyclone, Partition Metrics)}} | {{Model theory (Text, Hydrocyclone, Partition Metrics)}} | ||
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== Excel == | == Excel == | ||
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{{SysCAD (Text, Help Link)}} | {{SysCAD (Text, Help Link)}} | ||
|- | |||
! colspan="3" style="text-align:left;" |''Parameters'' | |||
|- | |- | ||
|EffPoolArea / A | |EffPoolArea / A | ||
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|Number of internal iterations required to converge the Plitt-Flintoff model. | |Number of internal iterations required to converge the Plitt-Flintoff model. | ||
|- | |- | ||
|Feed.SRho | |Feed.SolidDensity / Feed.SRho | ||
|style="background: #eaecf0" | Display | |style="background: #eaecf0" | Display | ||
|Density of solids in the feed stream | |Density of solids in the feed stream | ||
|- | |- | ||
|Feed.Rho | |Feed.Density / Feed.Rho | ||
|style="background: #eaecf0" | Display | |style="background: #eaecf0" | Display | ||
|Density of slurry in the feed stream | |Density of slurry in the feed stream | ||
|- | |- | ||
|Feed.Svf | |Feed.SolidVolFrac / Feed.Svf | ||
|style="background: #eaecf0" | Display | |style="background: #eaecf0" | Display | ||
|Volume fraction of solids in the feed stream | |Volume fraction of solids in the feed stream | ||
|- | |- | ||
|Overflow. | |Overflow.VolFlow / OF.Qv | ||
|style="background: #eaecf0" | Display | |style="background: #eaecf0" | Display | ||
|Volumetric flowrate of slurry in the overflow stream. | |Volumetric flowrate of slurry in the overflow stream. | ||
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* [[Partition (Size, Reid-Plitt)]] | * [[Partition (Size, Reid-Plitt)]] | ||
== External links == | |||
* [https://help.syscad.net/Met_Dynamics_-_Classifier Met Dynamics - Classifier (help.syscad.net)] | |||
* [https://help.syscad.net/Example_-_09_Met_Dynamics_Projects#Gravity,_Dense_Medium_and_Magnetic_Separation_Example Gravity, Dense Medium, and Magnetic Separation Example project (help.syscad.net)] | |||
== References == | == References == |
Latest revision as of 13:31, 1 May 2025
Description
This article describes a model of gravity classifiers proposed by Plitt and Flintoff (1985).[1][2]
Gravity classifiers use the differential settling velocity of particles in a pool to separate feed pulp into coarse and fine product streams.
Mechanical gravity classifiers use a mechanical action to both agitate pulp in the pool and convey the gravity-settled coarse particles away from the machine and the remaining fine particles in the overflow. Examples of mechanical gravity classifiers include spiral, rake and bowl machines.
Non-mechanical gravity classifiers rely on free or hindered settling against a rising current and draw settled coarse particles through an underflow spigot. Finer particles report to the overflow. Examples of non-mechanical gravity classifiers include devices variously referred to as hydraulic classifiers, elutriators, hydrospearators, hydrosizers, upcurrent classifiers, teeter-bed separators, hindered-bed separators, or cone classifiers.
Model theory
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Classification
Corrected cut size
Water recovery
Sharpness estimation
Density-specific classification
Coarse solids removal capacity
Sands solid content
Partition metrics
Excel
The Plitt-Flintoff gravity classifier model may be invoked from the Excel formula bar with the following function call:
=mdUnit_GravityClassifier_PlittFlintoff(Parameters as Range, Size as Range, Feed as Range, OreSG as Range)
Invoking the function with no arguments will print Help text associated with the model, including a link to this page.
Inputs
The required inputs are defined below in matrix notation with elements corresponding to cells in Excel row () x column () format:
where:
- is the index to the particle shape factors in Table 1 (0-6)
- indicates whether to compute classification separately for each solids density class (True) or use a singular representative solids density (False)
- indicates whether to estimate the sharpness of separation () (True) or apply a user-specified value (False)
- is a user-specified value of the sharpness of separation () which is applied if is False and ignored otherwise (-)
- is the size of the square mesh interval that feed mass is retained on (mm)
- is feed solids mass flow rate by size and ore type (t/h)
- is the mass flow feed rate of liquids into the classifier (t/h)
Results
The results are displayed in Excel as an array corresponding to the matrix notation below:
where:
- is the number of iterations required to converge the Plitt-Flintoff model
- is the mass flow rate of liquids to the overflow stream (t/h)
- is the mass flow rate of liquids to the underflow stream (t/h)
- is mass flow rate of solids to the underflow stream (t/h)
- is mass flow rate of solids to the overflow stream (t/h)
- is the actual partition of all particles of size to the underflow stream, computed as (frac)
Example
The images below show the selection of input arrays and output results in the Excel interface.
SysCAD
The sections and variable names used in the SysCAD interface are described in detail in the following tables.
MD_Classifier page
The first tab page in the access window will have this name.
Tag (Long/Short) | Input / Display | Description/Calculated Variables/Options |
---|---|---|
Tag | Display | This name tag may be modified with the change tag option. |
Condition | Display | OK if no errors/warnings, otherwise lists errors/warnings. |
ConditionCount | Display | The current number of errors/warnings. If condition is OK, returns 0. |
GeneralDescription / GenDesc | Display | This is an automatically generated description for the unit. If the user has entered text in the 'EqpDesc' field on the Info tab (see below), this will be displayed here.
If this field is blank, then SysCAD will display the unit class ID. |
Requirements | ||
On | CheckBox | This enables the unit. If this box is not checked, then the MassFracToUF option appears below. |
MassFracToUF | Input | Only appears if the On field above is not checked. Specifies the fraction of feed mass that reports to the underflow stream when the model is off. |
NumParallelUnits | Input | The number of parallel, identical units to simulate:
|
Method | Partition (User) | The partition to underflow for each size interval is defined by the user. Different values can be used for different solids. |
Partition (Reid-Plitt) | The partition to underflow for each size interval is defined by a Reid-Plitt efficiency curve. Different parameters can be used for different solids. | |
Partition (Whiten-Beta) | The partition to underflow for each size interval is defined by a Whiten-Beta efficiency curve. Different parameters can be used for different solids. | |
Air Classifier (Altun) | The Altun air classifier model is used to determine the partition of solids to underflow for each size interval. | |
Gravity (Plitt-Flintoff) | The Plitt-Flintoff gravity classifier model is used to determine the partition of solids to underflow for each size interval. | |
Options | ||
ShowQFeed | CheckBox | QFeed and associated tab pages (eg Sp) will become visible, showing the properties of the combined feed stream. |
ShowQOF | CheckBox | QOF and associated tab pages (eg Sp) will become visible, showing the properties of the overflow stream. |
ShowQUF | CheckBox | QUF and associated tab pages (eg Sp) will become visible, showing the properties of the underflow stream. |
SizeForPassingFracCalc | Input | Size fraction for % Passing calculation. The size fraction input here will be shown in the Stream Summary section. |
FracForPassingSizeCalc | Input | Fraction passing for Size calculation. The fraction input here will be shown in the Stream Summary section. |
Stream Summary | ||
MassFlow / Qm | Display | The total mass flow in each stream. |
SolidMassFlow / SQm | Display | The Solids mass flow in each stream. |
LiquidMassFlow / LQm | Display | The Liquid mass flow in each stream. |
VolFlow / Qv | Display | The total Volume flow in each stream. |
Temperature / T | Display | The Temperature of each stream. |
Density / Rho | Display | The Density of each stream. |
SolidFrac / Sf | Display | The Solid Fraction in each stream. |
LiquidFrac / Lf | Display | The Liquid Fraction in each stream. |
Passing | Display | The mass fraction passing the user-specified size (in the field SizeForPassingFracCalc) in each stream. |
Passes | Display | The user-specified (in the field FracForPassesSizeCalc) fraction of material in each stream will pass this size fraction. |
Classifier page
The Classifier page is used to specify the input parameters for the classifier model.
Partition page
The Partition page is used to display (or specify) the partition by species/component/element/individual phase and size values.
Tag (Long/Short) | Input / Display | Description/Calculated Variables/Options |
---|---|---|
Distribution | ||
Name | Display | Shows the name of the SysCAD Size Distribution (PSD) quality associated with the feed stream. |
IntervalCount | Display | Shows the number of size intervals in the SysCAD Size Distribution (PSD) quality associated with the feed stream. |
SpWithPSDCount | Display | Shows the number of species in the feed stream assigned with the SysCAD Size Distribution (PSD) quality. |
Partition | ||
Method | Model / User | Select model-calculated or user-defined partition to separate each solids species type. |
Density | Display | Density of each solid species. |
Size | Display | Size of each interval in mesh series. |
MeanSize | Display | Geometric mean size of each interval in mesh series.
|
All (All column) | Display |
|
Partition | Display |
|
All (All row, All column) | Display |
|
All (All row, per species) | Display |
|
CmpPartition | ||
Components | Hides or shows component partition table. | |
Size | Display | Size of each interval in mesh series. |
MeanSize | Display | Geometric mean size of each interval in mesh series. |
All (All column) | Display |
|
CmpPartition | Display |
|
All (All row, All column) | Display |
|
All (All row, per component) | Display |
|
ElePartition | ||
Elements | Hides or shows element partition table. | |
Size | Display | Size of each interval in mesh series. |
MeanSize | Display | Geometric mean size of each interval in mesh series. |
All (All column) | Display |
|
ElePartition | Display |
|
All (All row, All column) | Display |
|
All (All row, per element) | Display |
|
IPhPartition | ||
IPhases | Hides or shows individual phases partition table. | |
Size | Display | Size of each interval in mesh series. |
MeanSize | Display | Geometric mean size of each interval in mesh series. |
All (All column) | Display |
|
IPhPartition | Display |
|
All (All row, All column) | Display |
|
All (All row, per individual phase) | Display |
|
About page
This page is provides product and licensing information about the Met Dynamics Models SysCAD Add-On.
Tag (Long/Short) | Input / Display | Description/Calculated Variables/Options |
---|---|---|
About | ||
HelpLink | ![]() |
Opens a link to the Installation and Licensing page using the system default web browser. Note: Internet access is required. |
Information | ![]() |
Copies Product and License information to the Windows clipboard. |
Product | ||
Name | Display | Met Dynamics software product name |
Version | Display | Met Dynamics software product version number. |
BuildDate | Display | Build date and time of the Met Dynamics Models SysCAD Add-On. |
License | ||
File | ![]() |
This is used to locate a Met Dynamics software license file. |
Location | Display | Type of Met Dynamics software license or file name and path of license file. |
SiteCode | Display | Unique machine identifier for license authorisation. |
ReqdAuth | Display | Authorisation level required, MD-SysCAD Full or MD-SysCAD Runtime. |
Status | Display | License status, LICENSE_OK indicates a valid license, other messages report licensing errors. |
IssuedTo | Display | Only visible if Met Dynamics license file is used. Name of organisation/seat the license is authorised to. |
ExpiryDate | Display | Only visible if Met Dynamics license file is used. License expiry date. |
DaysLeft | Display | Only visible if Met Dynamics license file is used. Days left before the license expires. |
Additional notes
- Solid species that do not possess a particle size distribution property are split according to the overall mass split of the default particle size distribution species selected in the SysCAD Project Configuration.
- If the default particle size distribution species is not present in the unit feed, the overall split of all other species with particle size distributions combined is used, as determined by the model.
- Gas phase species report directly to the overflow stream without split.
See also
External links
- Met Dynamics - Classifier (help.syscad.net)
- Gravity, Dense Medium, and Magnetic Separation Example project (help.syscad.net)