Partition (Size, Bazin): Difference between revisions
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Revision as of 15:28, 17 May 2024
Description
This article describes the Bazin et al. (2014) empirical expression for the recovery of particles to the concentrate stream of a spiral concentrator.[1]
The form of the empirical equation may also be applicable to other gravity concentration processes exhibiting a similar reverse classification effect on coarser particles, such as shaking tables and the Falcon gravity concentrator.[2][3]
Model theory
Bazin et al. (2014) proposed an empirical expression for the partition of particles of a given size and density to the concentrate stream of a spiral concentrator. The concentrate stream is defined here as the inner part of the spiral trough.
The expression is formulated as the product of two counter-acting mechanisms that simultaneously force heavy minerals to the centre of the trough and coarse particles to the outer edge of the trough.
The partition of particles of a given size and density to the concentrate stream, (frac), is:
where:
- is the fraction of particles which should nominally report to the inner part of the trough (concentrate stream) due to gravitational forces, the classification action
- is the probability that a particle resists the inward forces and is directed towards the outer trough by the Bagnold force, the filtration action
- and are the diameter (mm) and density (t/m3) of the particle respectively
For series of size intervals, the and terms are computed as:
where:
- is the index of the size interval, , is the number of size intervals
- is the index of the density class, , is the number of density classes
- is the geometric mean size of particles in size interval (mm)
- is the sharpness parameter of the classification curve
- is the size of a particle of density which has a 50% probability of reporting to the concentrate stream (mm)
- is the fraction of fine particles of density which are entrained by the classification action towards the inner section of the spiral trough (frac)
- is the sharpness parameter of the filtration curve
- is the size of a particle of density for which 50% are rejected for classification by the Bagnold (or other counteracting) force (mm)
- is the fraction of the mass of particles in size class and density class which are partitioned (recovered) to the concentrate stream (frac)
A separate set of , , , , and parameters are required for each particle with a distinct density (e.g. mineral species).
Middlings
Gravity concentrators such as jigs, spirals and shaking tables produce a bed or band of partially stratified components at the point of discharge. Portions of the bed or band are then typically directed to product streams by a physical device, such as a weir, 'splitter' or 'cutter'. These devices are usually adjustable, and can be arranged to recover arbitrary fractions of the bed or band.
From a physical standpoint, adjusting the discharge device to recover more of the bed or band has the effect of recovering the both the portion from the previous position plus the portion in between the previous and new positions. As more mass is recovered by this process, the partition curve effectively 'shifts upwards'. The partition curve is thus representing the cumulative recovery of mass from all positions between the beginning of the bed/band and the discharge device position.
Mathematically, the partition curve generated by such a gravity concentration method should also be considered a cumulative recovery of mass to concentrate. When multiple product streams exist, e.g. concentrate and middlings, the partition of components to each individual product stream will be the difference between the cumulative partition curves at each product stream position.[4] That is,
where:
- is the index of the product stream, i.e. is the first concentrate stream, are subsequent lower-grade concentrate or middlings streams
- is the mass fraction of particles in the feed stream in size class and density class which are partitioned to the product stream (frac)
- is the cumulative mass fraction of particles in the feed stream in size class and density class which are partitioned to all the products streams up to and including (frac)
- The term prevents negative partition values
The cumulative recovery formulation described above is physically and mathematically distinct from staged recovery processes which apply partition curves to the unrecovered streams of previous partition steps.
Excel
The Bazin spiral partition model may be invoked from the Excel formula bar with the following function call:
=mdPartition_Bazin(MeanSize as Range, alphaS as Double, d50S as Double, Rp as Double, alphP as Double, d50P as Double)
Invoking the function with no arguments will print Help text associated with the model, including a link to this page.
The input parameters and model results are defined below in matrix notation, along with an example image showing the selection of the same cells in the Excel interface:
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SysCAD
The Bazin partition is available from the MetDynamics*GravityConcentrator unit model.
The sections and variable names used in the SysCAD interface are described in detail in the following tables.
Note that a Con and Partition page is provided provided for each connected concentrate discharge stream of a Gravity Concentrator unit model.
MD_GravityConcentrator 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 MassFracToCon option appears below. |
MassFracToCon | Input | Only appears if the On field above is not checked. Specifies the fraction of feed mass that reports to the concentrate stream when the model is off. |
NumParallelUnits | Input | The number of parallel, identical units to simulate:
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Options | ||
ShowQFeed | CheckBox | QFeed and associated tab pages (eg Sp) will become visible, showing the properties of the combined feed 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. |
Con page
The Con page is used to specify the required model method and associated input parameters.
Tag (Long/Short) | Input / Display | Description/Calculated Variables/Options |
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Stage | ||
On | Checkbox | This enables the stage. If off, the feed to this stage passes directly to the next stage (or tail) without partition. |
Method | Partition (User) | The partition to concentrate for each size interval is defined by the user. |
Partition (Rho50-Ep) | The partition to concentrate for each size interval is defined by the Rho50-Ep model. | |
Partition (Pivot) | The partition to concentrate for each size interval is defined by the Pivot model. | |
Partition (Stochastic) | The partition to concentrate for each size interval is defined by the Stochastic model. | |
Partition (Bazin) | The partition to concentrate for each size interval is defined by the Bazin model. | |
Jig (King) | The partition to concentrate for each size interval is defined by the King jig stratification model. | |
HelpLink | Opens a link to this page using the system default web browser. Note: Internet access is required. | |
Bazin | ||
OreSpecific | CheckBox |
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Parameters | ||
AlphaS | Input | The Bazin equation alphaS parameter for the classification curve. |
d50S | Input | The Bazin equation d50S cut size parameter for the classification curve. |
Rp | Input | The Bazin equation Rp parameter for the filtration curve. |
AlphaP | Input | The Bazin equation alphaP parameter for the filtration curve. |
d50P | Input | The Bazin equation d50P cut size parameter for the filtration curve. |
Liquids | ||
LiquidsSeparMethod | Split To Con (User) | Liquids are split to concentrate by a user-defined fraction of liquids in the feed. |
Con Solids Fraction | Sufficient liquids mass is recovered to the concentrate stream to yield the user-defined concentrate solids mass fraction value (if possible). | |
Con Liquids Fraction | Sufficient liquids mass is recovered to the concentrate stream to yield the user-defined concentrate liquids mass fraction value (if possible). | |
ConSolidsFracReqd / Con.SfReqd | Input | Required value of the mass fraction of solids in the concentrate stream. Only visible if Con Solids Fraction is selected. |
ConLiquidsFracReqd / Con.LfReqd | Input | Required value of the mass fraction of liquids in the concentrate stream. Only visible if Con Liquids Fraction is selected. |
LiqSplitToCon / Con.LiqSplit | Input/Display | The fraction of feed liquids recovered to the concentrate stream. |
Partition page
The Partition page is used to specify or display the partition by species and size values.
Tag (Long/Short) | Input / Display | Description/Calculated Variables/Options |
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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.
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CumulativePartition | ||
Method | Model/User | Select model-calculated or user-defined cumulative 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 |
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CumulativePartition | Display |
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All (All row, All column) | Display |
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All (All row, per species) | Display |
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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 |
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Partition | Display |
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All (All row, All column) | Display |
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All (All row, per species) | Display |
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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 tail stream without split.
References
- ↑ 1.0 1.1 Bazin, C., Sadeghi, M., Roy, P., Bourassa, M., Cataford, D., Lavoie, F., Rochefort, C., Gosselin, C., Renaud, M. and Mahieu, G., 2014. Simulation of an iron ore concentration circuit using mineral size recovery curves of industrial spirals. Proceedings of the 46th Canadian Mineral Processors, CIM, Ottawa, Canada, January, pp.21-23.
- ↑ Bergmann, C., Govender, V. and Corfield, A.A., 2016. Using mineralogical characterisation and process modelling to simulate the gravity recovery of ferrochrome fines. Minerals Engineering, 91, pp.2-15.
- ↑ Dehaine, Q., Foucaud, Y., Kroll-Rabotin, J.S. and Filippov, L.O., 2019. Experimental investigation into the kinetics of Falcon UF concentration: Implications for fluid dynamic-based modelling. Separation and Purification Technology, 215, pp.590-601.
- ↑ King, R.P., Juckes, A.H. and Stirling, P.A., 1992. A quantitative model for the prediction of fine coal cleaning in a spiral concentrator. Coal preparation, 11(1-2), pp.51-66.