1 Qilong Bi and 2 Arno Talmon
1 Department of Ecosystem and Sediment Dynamics, Deltares
2 Department of mechanical engineering, TU Delft
11 November 2025 ∙ Delft, The Netherlands
Modelling Non-Newtonian
Slurry Beaching with
Delft3D-Slurry
What is non-Newtonian flow
• Newtonian fluids: Viscosity is constant (independent of shear rate)
− Examples: water, air
• Non-Newtonian fluids: Viscosity changes with shear rate or time
− Examples: mud, sludge, tailings, blood, polymer solutions
• Common Behaviors:
− Shear-thinning (pseudoplastic): Viscosity ↓ with shear (e.g., mud)
− Shear-thickening (dilatant): Viscosity ↑ with shear (e.g., cornstarch-water)
− Bingham plastic: Acts solid until yield stress is exceeded
− Thixotropic / Rheopectic: Time-dependent viscosity
2
Why we want to model it
• Non-Newtonian flow is common
• Environmental and Engineering Contexts:
− Tailings management
− Beneficial sediment re-use
− Pipeline transport of slurries and dredged materials
− Drilling fluids in drilling operations
− Fluid mud in natural water systems
3
Rijpdijk project
Theorical background of Delft3D-Slurry
Rheology, sand mobility in non-Newtonian flow, gelled bed, etc.
Carrier fluid & sand
5
• Rheology carrier fluid is a
• function of water content to the fines.
• Settling sand leads to inhomogeneous mixture: mixture rheology varies spatially:
a CFD model has to capture that.
clays
fines=clay + silt sand
carrier fluid
0.044 mm
0.002 mm
Sand: increases mixture rheology
Sand settling: is governed by rheology
of interstitial carrier fluid
Particle size distribution
Rheology: Carrier fluid
6
Clay colloids form flocs. Flocs determine the rheological properties.
Skip the colloid science: we start from flow curves
No sand yet
Wf= water content to fines
water
HE
LO
Y
Rheology: Sand influence
7
Sand via linear Bagnold sand
concentration effect
Similar:
Gillies,
Thomas
Sand can be difficult
(jamming, sand settling):
vane fissure is applied.
Base rheology (clay and silt)
in well defined element (bob-cup)
SFR= sand-to-fines ratio
water content w.r.t. the clay
yield
stress
Sand mobility: settling in non-Newtonian shear flow
8
Diagrams for different
direction of shear
(horizontal/vertical)
Talmon Huisman 2005, J Tunnelling and
Underground Space Technology
Ha ha superposition principle
Sand mobility: settling in non-Newtonian shear flow
• Fundamental of shear settling visualised
9
CSIRO, Dr Lionel Pullum, 2010, 2017
Before shearing
After shearing
Sand mobility: shear settling
10
Solids settling in laponite:
Shearing in Caroussel, and
Bob shearing in graduated glass.
Caroussel: endless horizontal
channel driven by rigid lid.
2 m
Talmon A.M. and M. Huisman, 2005, Fall velocity of particles in shear flow of drilling fluids, J. Tunnelling and
Underground Space Technology, including Horizontal Directional Drilling, vol. 20, no2, pp193-201.
Settling of concentrations of sand: shear cell
11
level 1
level 2
level 3
level 4
electrodes
broad PSD
Pennekamp Joh.G.S., Talmon A.M. and W.G.M. van Kesteren, 2010,
Determination of non-segregating tailings conditions, Wodcon XIX, Beijing
Gelled bed
12
low concentration
of clays
high concentration
of clays
Gelled bed
Granular bed
Gel: frozen,
immobile.
We can keep this in fluid domain
We need separate stagnant bed layer
(classic morphology)
Gelled bed
13
SFR= sand-to-fines ratio
water content w.r.t. clay
yield
stress
Gelled bed by
settling sand:
settling continues
until yield stress
equals
fluid shear stress
of the flow
Modelling non-Newtonian flow using Delft3D-Slurry
Assumptions, model set-ups, limitations and showcases
Delft3D-Slurry
• Laminar flow + non-Newtonian rheology
• Shear-induced sand settling, no settling of carrier fluid
• No-slip boundary + gelled bed condition
• Baroclinicity (density driven transport)
• Doesn’t include thixotropy, dewatering, consolidation
15
Constitutive law of non-
Newtonian sand-mud mixture
Shear-induced sand settling
Papanastasiou regularization
(red) of Bingham model (blue)
Delft3D-Slurry
Model set-ups:
• A .slu file for rheological model configuration
• Zero turbulence (Tkemod = Constant, Vicouv, Vicoww, Dicoww, and Dicouv = 0) – laminar flow
• Effect of sediment concentration on fluid density (DensIn = true) – baroclinic forcing
• Low Chezy coefficient (Ccofu and Ccofv = 0.5) - requested by no-slip bottom for achieving gelled
bed condition
• No bed level update in the calculation (MorUpd = false) - gelled bed condition
• Activate anti-creep (Sigcor = Y) - for minimizing artificial vertical diffusion and artificial flow in case
large bottom gradients exist in the model
16
Delft3D-Slurry
• Example of .slu file
17
Validation: beach deposition
18
z [m]
c0
Fines remain
homogenous
Sand settles by
shear
Analytical 1D versus
CFD-2D (Delft3Ds)
Showcase 1: deposition and channelization
19
big lobe
long channel
eroded deposit
Pirouz B.,Javadi S., Williams P., Pavissich C., Caro G. 2015,
Chuquicamata full-scale field deposition trial, Paste 2015, Cairns
Mine tailings, Marine mud deposits,
Volcano, Dam breaks
Flow pattern/regime:
Lobes, channels, plunge pool
Showcase 1: deposition and channelization
20
Showcase 1: deposition and channelization
21
Beach: 100m * 400m, top view, channelization!
Showcase 1: deposition and channelization
22
top view 100m * 400m, sand in lowest layer
Showcase 2: beach deposition and mixing in ponds
Open pit mining Tailings ponds
On path to restoration
beaching
Showcase 2: automated model generation
• Python toolbox for model generation, flow curve calculation, postprocessing
24
Input parameter range
Parameter space
Model 2
Model 1 Model n
…
Translate into model inputs
generate submission file
slope, discharge, SFR, rheology, bulk density, yield stress, …
bathymetry, initial and boundary conditions,
rheological parameters, etc.
running batch simulations on cluster
Showcase 2: beach deposition
25
SFR=0,5 SFR=2,75 SFR=5
FoFW=21%
FoFW=27%
FoFW=33%
increase
of
equilibrium
depth
Increase of sand deposition at bottom
Sand concentrations
Other parameters:
• Slope = 0,004
• Velocity = 0,75 m/s
• 𝜏𝑦𝑖𝑒𝑙𝑑 = 𝜌𝑚𝑖𝑥𝑔𝐻𝑖𝑛𝑖𝑡 ∙ sin(𝜃)
• Rheology= medium
Showcase 2: mixing in tailing ponds
26
SFR_t1=0,5 SFR_t1=2,75 SFR_t1=5,0
density_t1
= 1200 kg/m3
density_t1
= 1525 kg/m3
density_t1
= 1850 kg/m3
Sand concentrations
Other parameters:
• Slope = 0,07
• Depth = 30 m
• Discharge_t1 = 1.65 m3/s
• Density_t2 = 1475 kg/m3
• SFR_t2 = 0,55
• Rheology = strong
Conclusions
• Idea seemed so simple…, all steps needed to be taken from 1D to 3D.
• A research branch Delft3D-Slurry tested and used in various projects.
• Further:
− Application to protective natural dike covering with fluid muds.
− Application to dredge spoil depositions, to predict where and which segregated
materials deposits.
− Run-out studies of tailings dam breaks and of stilling basins dams.
27
Acknowledgement
28
Many people worked on it, in different degree:
Jill Hansen, Luca Sittoni, Walther van Kesteren, Mike Costello, Cees van Rhee, Tom van de Ree, Hugo van Es, Etienne Parent,
Paul Simms, Vincent van Zelst, Miguel de Lucas Pardo, Ben Sheets, Eric Hedblom, Elco Hollander, Geert Keetels, Peter Dobbe,
Rob Uittenbogaard, Jan van Kester, Han Winterwerp, Bas van Maren, Ebi Meshkati, John Cornelissen, Wim Taal, Kees Koree,
Marcel Grootenboer, Marcel Busink, Saskia Huisman, Johan Pennekamp, Maria Ibanez, Maria Louisa Taccari.
Thanks, and thanks for listening !
Reference
30
Deltares applied industry track
Bi Q. and A.M. Talmon, 2025, Calculation of channel pattern in TSF surface disposal, Poster at IHA Hydrotransport, Prague.
Pennekamp Joh.G.S., Talmon A.M. and W.G.M. van Kesteren, 2010, Determination of non-segregating tailings conditions, Wodcon XIX,
Beijing, pp.848-858.
Sheets B., Wagner T., Swenson J.B., Horton J., Langseth J., Sittoni L., Walstra D.J., Winterwerp H., Uittenbogaard R., Kester J. van and
A.M. Talmon, 2014, Muddy river deltas as analogues for oil sand tailings beaches: improving fines capture and operational efficiency with
tailings beach modelling, in proc. 4th Int. Oil Sand Tailings Conference, IOSTC (eds. D. Sego, G.W. Wilson and N. Beier), Lake Louise,
Canada, pp.397-405.
Sisson R., Lacoste-Bouchet P., Vera M., Costello M., Hedblom E., Sheets B. Nesler D. Solseng P., Fandrey A., Van Kesteren W., Talmon
A.M and L. Sittoni, 2012, An analytical model for tailings deposition developed from pilot-scale testing, in: D. Sego, G.W. Wilson and N.
Beier (eds.) proc. 3rd International Oil Sands Tailings Conference, Edmonton, Alberta, Canada, December 2-5, 2012, pp 53-63.
Sittoni L, Talmon A.M., van Kester J.A.T.M., Uittenbogaard R.E. (2015) Latest numerical developments for the prediction of beaching flow
and segregating behaviour of thick non-Newtonian mixtures, in Proceedings 17th International Conference on Transport and
Sedimentation of Solid Particles, 22-25 Sept. 2015, Delft, Wroclaw University and Delft University of Technology, pp.309–316.
Sittoni L., Talmon A., Hanssen J., Van Es H., Van Kester J., Uittenbogaard R., Winterwerp J.C. and C. van Rhee, 2016, Optimizing tailings
deposition to maximize fines capture: latest advance in predictive modeling tools, in: D.C. Sego, G.W. Wilson, N.A. Beier (eds). Proc. 5th
Int. Oil Sand Tailings Conference, IOSTC, Lake Louise, Canada.
Talmon A.M., 2017, Channel width calculation for tailings beaching, proc. 18th int conference on Transport and sedimentation of solid
particles, Prague, Czech Republic, pp 351-358.
31
Talmon A.M., 2018, Rheology and segregation of sand-water-clay mixtures in deposition flow modelling, in: proc. 7th South African Conference on
Rheology (SASOR 2018), 27-28 September 2018; Stellenbosch, South Africa. p. 35-39.
Talmon A.M., 2019, Mathematical Analysis of channelisation in non-Newtonian deposition flow, 19th International Conference on Transport
and Sedimentation of Solid Particles, 24-27 September 2019, Cape Town, South Africa, pp245-252.
Talmon A.M., 2021, Analytical Approach for Channel formation in Hyperconcentrated flows, Book of abstracts 16th International Conference
on Cohesive Sediment Transport Processes, 13-17 September, Delft, The Netherlands
Talmon A.M., 2023, Bed pattern initiation in non-Newtonian laminar deposition flow, IHA 21st Hydrotransport conference, Edmonton, Canada.
Talmon A.M., Hanssen J.L.J., Winterwerp J.C., Sittoni L. and C. Van Rhee, 2016, Implementation of Tailings Rheology in a Predictive Open-
Channel Beaching Model, Paste 2016, Santiago, Chile, ISBN 978.956.9393-47-1.
Talmon A.M., Hanssen J.L.J., Van Maren D.S., Simms P.H., Sittoni L., Van Kester J., Uittenbogaard R., Winterwerp J.C. and C. van Rhee,
2018, Numerical modelling of tailings flow, sand segregation and sand co-deposition: latest developments and applications, in: NA Beier,
Wilson GW & DC Sego (eds), Proc. 6th Int. Oil Sand Tailings Conference, IOSTC, Edmonton, Canada.
Talmon A.M. and M. Huisman, 2005, Fall velocity of particles in shear flow of drilling fluids, J. Tunnelling and Underground Space Technology,
including Horizontal Directional Drilling, vol. 20, no2, pp193-201.
Talmon A.M., Sittoni L., Meshkati Shahmirzadi E. and J.L.J. Hanssen, 2018, Shear settling in laminar open channel flow: analytical solution,
measurements and numerical simulation, in: proc. Paste 2018 conf., Perth.
Van Kesteren, W.G.M., van de Ree T., Talmon, A.M., de Lucas Pardo M., Luger D., Sittoni L. (2015) A large-scale experimental study of high
density slurries deposition on beaches, in Proceedings 17th International Conference on Transport and Sedimentation of Solid Particles, 22-
25 Sept. 2015, Delft, Wroclaw University and Delft University of Technology, pp.147–154.
32
Delft Univ. academic track
Dobbe P., 2021, Simulation of multiphase flow using non-Newtonian fluids and sand segregation in OpenFOAM, MSc-thesis, Delft
University of Technology, Delft, The Netherlands.
Hanssen J.L.J., 2016, Towards improving predictions of non-Newtonian settling slurries with Delft3D: theoretical development and
validation in 1DV , MSc-thesis, Delft University of Technology, Delft, The Netherlands.
Van de Ree T.H.B., 2015, Deposition of high density tailings on beaches, MSc-thesis, Delft University of Technology, Delft, The Netherlands.
Van Es H.E., 2017, Development of a numerical model for dynamic depositioning of non-Newtonian slurries, MSc-thesis, Delft University of
Technology, Delft, The Netherlands.
Van Rhee C., 2017, Simulation of the Settling of solids in a non-Newtonian fluid, proc. 18th int conference on Transport and sedimentation
of solid particles, Prague, Czech Republic, pp.265-270.
Contact
www.deltares.nl
info@deltares.nl
@deltares
@deltares
linkedin.com/company/deltares
facebook.com/deltaresNL

DSD-INT 2025 Modelling Non-Newtonian Slurry Beaching with Delft3D-Slurry - Bi

  • 1.
    1 Qilong Biand 2 Arno Talmon 1 Department of Ecosystem and Sediment Dynamics, Deltares 2 Department of mechanical engineering, TU Delft 11 November 2025 ∙ Delft, The Netherlands Modelling Non-Newtonian Slurry Beaching with Delft3D-Slurry
  • 2.
    What is non-Newtonianflow • Newtonian fluids: Viscosity is constant (independent of shear rate) − Examples: water, air • Non-Newtonian fluids: Viscosity changes with shear rate or time − Examples: mud, sludge, tailings, blood, polymer solutions • Common Behaviors: − Shear-thinning (pseudoplastic): Viscosity ↓ with shear (e.g., mud) − Shear-thickening (dilatant): Viscosity ↑ with shear (e.g., cornstarch-water) − Bingham plastic: Acts solid until yield stress is exceeded − Thixotropic / Rheopectic: Time-dependent viscosity 2
  • 3.
    Why we wantto model it • Non-Newtonian flow is common • Environmental and Engineering Contexts: − Tailings management − Beneficial sediment re-use − Pipeline transport of slurries and dredged materials − Drilling fluids in drilling operations − Fluid mud in natural water systems 3 Rijpdijk project
  • 4.
    Theorical background ofDelft3D-Slurry Rheology, sand mobility in non-Newtonian flow, gelled bed, etc.
  • 5.
    Carrier fluid &sand 5 • Rheology carrier fluid is a • function of water content to the fines. • Settling sand leads to inhomogeneous mixture: mixture rheology varies spatially: a CFD model has to capture that. clays fines=clay + silt sand carrier fluid 0.044 mm 0.002 mm Sand: increases mixture rheology Sand settling: is governed by rheology of interstitial carrier fluid Particle size distribution
  • 6.
    Rheology: Carrier fluid 6 Claycolloids form flocs. Flocs determine the rheological properties. Skip the colloid science: we start from flow curves No sand yet Wf= water content to fines water HE LO Y
  • 7.
    Rheology: Sand influence 7 Sandvia linear Bagnold sand concentration effect Similar: Gillies, Thomas Sand can be difficult (jamming, sand settling): vane fissure is applied. Base rheology (clay and silt) in well defined element (bob-cup) SFR= sand-to-fines ratio water content w.r.t. the clay yield stress
  • 8.
    Sand mobility: settlingin non-Newtonian shear flow 8 Diagrams for different direction of shear (horizontal/vertical) Talmon Huisman 2005, J Tunnelling and Underground Space Technology Ha ha superposition principle
  • 9.
    Sand mobility: settlingin non-Newtonian shear flow • Fundamental of shear settling visualised 9 CSIRO, Dr Lionel Pullum, 2010, 2017 Before shearing After shearing
  • 10.
    Sand mobility: shearsettling 10 Solids settling in laponite: Shearing in Caroussel, and Bob shearing in graduated glass. Caroussel: endless horizontal channel driven by rigid lid. 2 m Talmon A.M. and M. Huisman, 2005, Fall velocity of particles in shear flow of drilling fluids, J. Tunnelling and Underground Space Technology, including Horizontal Directional Drilling, vol. 20, no2, pp193-201.
  • 11.
    Settling of concentrationsof sand: shear cell 11 level 1 level 2 level 3 level 4 electrodes broad PSD Pennekamp Joh.G.S., Talmon A.M. and W.G.M. van Kesteren, 2010, Determination of non-segregating tailings conditions, Wodcon XIX, Beijing
  • 12.
    Gelled bed 12 low concentration ofclays high concentration of clays Gelled bed Granular bed Gel: frozen, immobile. We can keep this in fluid domain We need separate stagnant bed layer (classic morphology)
  • 13.
    Gelled bed 13 SFR= sand-to-finesratio water content w.r.t. clay yield stress Gelled bed by settling sand: settling continues until yield stress equals fluid shear stress of the flow
  • 14.
    Modelling non-Newtonian flowusing Delft3D-Slurry Assumptions, model set-ups, limitations and showcases
  • 15.
    Delft3D-Slurry • Laminar flow+ non-Newtonian rheology • Shear-induced sand settling, no settling of carrier fluid • No-slip boundary + gelled bed condition • Baroclinicity (density driven transport) • Doesn’t include thixotropy, dewatering, consolidation 15 Constitutive law of non- Newtonian sand-mud mixture Shear-induced sand settling Papanastasiou regularization (red) of Bingham model (blue)
  • 16.
    Delft3D-Slurry Model set-ups: • A.slu file for rheological model configuration • Zero turbulence (Tkemod = Constant, Vicouv, Vicoww, Dicoww, and Dicouv = 0) – laminar flow • Effect of sediment concentration on fluid density (DensIn = true) – baroclinic forcing • Low Chezy coefficient (Ccofu and Ccofv = 0.5) - requested by no-slip bottom for achieving gelled bed condition • No bed level update in the calculation (MorUpd = false) - gelled bed condition • Activate anti-creep (Sigcor = Y) - for minimizing artificial vertical diffusion and artificial flow in case large bottom gradients exist in the model 16
  • 17.
  • 18.
    Validation: beach deposition 18 z[m] c0 Fines remain homogenous Sand settles by shear Analytical 1D versus CFD-2D (Delft3Ds)
  • 19.
    Showcase 1: depositionand channelization 19 big lobe long channel eroded deposit Pirouz B.,Javadi S., Williams P., Pavissich C., Caro G. 2015, Chuquicamata full-scale field deposition trial, Paste 2015, Cairns Mine tailings, Marine mud deposits, Volcano, Dam breaks Flow pattern/regime: Lobes, channels, plunge pool
  • 20.
    Showcase 1: depositionand channelization 20
  • 21.
    Showcase 1: depositionand channelization 21 Beach: 100m * 400m, top view, channelization!
  • 22.
    Showcase 1: depositionand channelization 22 top view 100m * 400m, sand in lowest layer
  • 23.
    Showcase 2: beachdeposition and mixing in ponds Open pit mining Tailings ponds On path to restoration beaching
  • 24.
    Showcase 2: automatedmodel generation • Python toolbox for model generation, flow curve calculation, postprocessing 24 Input parameter range Parameter space Model 2 Model 1 Model n … Translate into model inputs generate submission file slope, discharge, SFR, rheology, bulk density, yield stress, … bathymetry, initial and boundary conditions, rheological parameters, etc. running batch simulations on cluster
  • 25.
    Showcase 2: beachdeposition 25 SFR=0,5 SFR=2,75 SFR=5 FoFW=21% FoFW=27% FoFW=33% increase of equilibrium depth Increase of sand deposition at bottom Sand concentrations Other parameters: • Slope = 0,004 • Velocity = 0,75 m/s • 𝜏𝑦𝑖𝑒𝑙𝑑 = 𝜌𝑚𝑖𝑥𝑔𝐻𝑖𝑛𝑖𝑡 ∙ sin(𝜃) • Rheology= medium
  • 26.
    Showcase 2: mixingin tailing ponds 26 SFR_t1=0,5 SFR_t1=2,75 SFR_t1=5,0 density_t1 = 1200 kg/m3 density_t1 = 1525 kg/m3 density_t1 = 1850 kg/m3 Sand concentrations Other parameters: • Slope = 0,07 • Depth = 30 m • Discharge_t1 = 1.65 m3/s • Density_t2 = 1475 kg/m3 • SFR_t2 = 0,55 • Rheology = strong
  • 27.
    Conclusions • Idea seemedso simple…, all steps needed to be taken from 1D to 3D. • A research branch Delft3D-Slurry tested and used in various projects. • Further: − Application to protective natural dike covering with fluid muds. − Application to dredge spoil depositions, to predict where and which segregated materials deposits. − Run-out studies of tailings dam breaks and of stilling basins dams. 27
  • 28.
    Acknowledgement 28 Many people workedon it, in different degree: Jill Hansen, Luca Sittoni, Walther van Kesteren, Mike Costello, Cees van Rhee, Tom van de Ree, Hugo van Es, Etienne Parent, Paul Simms, Vincent van Zelst, Miguel de Lucas Pardo, Ben Sheets, Eric Hedblom, Elco Hollander, Geert Keetels, Peter Dobbe, Rob Uittenbogaard, Jan van Kester, Han Winterwerp, Bas van Maren, Ebi Meshkati, John Cornelissen, Wim Taal, Kees Koree, Marcel Grootenboer, Marcel Busink, Saskia Huisman, Johan Pennekamp, Maria Ibanez, Maria Louisa Taccari. Thanks, and thanks for listening !
  • 29.
  • 30.
    30 Deltares applied industrytrack Bi Q. and A.M. Talmon, 2025, Calculation of channel pattern in TSF surface disposal, Poster at IHA Hydrotransport, Prague. Pennekamp Joh.G.S., Talmon A.M. and W.G.M. van Kesteren, 2010, Determination of non-segregating tailings conditions, Wodcon XIX, Beijing, pp.848-858. Sheets B., Wagner T., Swenson J.B., Horton J., Langseth J., Sittoni L., Walstra D.J., Winterwerp H., Uittenbogaard R., Kester J. van and A.M. Talmon, 2014, Muddy river deltas as analogues for oil sand tailings beaches: improving fines capture and operational efficiency with tailings beach modelling, in proc. 4th Int. Oil Sand Tailings Conference, IOSTC (eds. D. Sego, G.W. Wilson and N. Beier), Lake Louise, Canada, pp.397-405. Sisson R., Lacoste-Bouchet P., Vera M., Costello M., Hedblom E., Sheets B. Nesler D. Solseng P., Fandrey A., Van Kesteren W., Talmon A.M and L. Sittoni, 2012, An analytical model for tailings deposition developed from pilot-scale testing, in: D. Sego, G.W. Wilson and N. Beier (eds.) proc. 3rd International Oil Sands Tailings Conference, Edmonton, Alberta, Canada, December 2-5, 2012, pp 53-63. Sittoni L, Talmon A.M., van Kester J.A.T.M., Uittenbogaard R.E. (2015) Latest numerical developments for the prediction of beaching flow and segregating behaviour of thick non-Newtonian mixtures, in Proceedings 17th International Conference on Transport and Sedimentation of Solid Particles, 22-25 Sept. 2015, Delft, Wroclaw University and Delft University of Technology, pp.309–316. Sittoni L., Talmon A., Hanssen J., Van Es H., Van Kester J., Uittenbogaard R., Winterwerp J.C. and C. van Rhee, 2016, Optimizing tailings deposition to maximize fines capture: latest advance in predictive modeling tools, in: D.C. Sego, G.W. Wilson, N.A. Beier (eds). Proc. 5th Int. Oil Sand Tailings Conference, IOSTC, Lake Louise, Canada. Talmon A.M., 2017, Channel width calculation for tailings beaching, proc. 18th int conference on Transport and sedimentation of solid particles, Prague, Czech Republic, pp 351-358.
  • 31.
    31 Talmon A.M., 2018,Rheology and segregation of sand-water-clay mixtures in deposition flow modelling, in: proc. 7th South African Conference on Rheology (SASOR 2018), 27-28 September 2018; Stellenbosch, South Africa. p. 35-39. Talmon A.M., 2019, Mathematical Analysis of channelisation in non-Newtonian deposition flow, 19th International Conference on Transport and Sedimentation of Solid Particles, 24-27 September 2019, Cape Town, South Africa, pp245-252. Talmon A.M., 2021, Analytical Approach for Channel formation in Hyperconcentrated flows, Book of abstracts 16th International Conference on Cohesive Sediment Transport Processes, 13-17 September, Delft, The Netherlands Talmon A.M., 2023, Bed pattern initiation in non-Newtonian laminar deposition flow, IHA 21st Hydrotransport conference, Edmonton, Canada. Talmon A.M., Hanssen J.L.J., Winterwerp J.C., Sittoni L. and C. Van Rhee, 2016, Implementation of Tailings Rheology in a Predictive Open- Channel Beaching Model, Paste 2016, Santiago, Chile, ISBN 978.956.9393-47-1. Talmon A.M., Hanssen J.L.J., Van Maren D.S., Simms P.H., Sittoni L., Van Kester J., Uittenbogaard R., Winterwerp J.C. and C. van Rhee, 2018, Numerical modelling of tailings flow, sand segregation and sand co-deposition: latest developments and applications, in: NA Beier, Wilson GW & DC Sego (eds), Proc. 6th Int. Oil Sand Tailings Conference, IOSTC, Edmonton, Canada. Talmon A.M. and M. Huisman, 2005, Fall velocity of particles in shear flow of drilling fluids, J. Tunnelling and Underground Space Technology, including Horizontal Directional Drilling, vol. 20, no2, pp193-201. Talmon A.M., Sittoni L., Meshkati Shahmirzadi E. and J.L.J. Hanssen, 2018, Shear settling in laminar open channel flow: analytical solution, measurements and numerical simulation, in: proc. Paste 2018 conf., Perth. Van Kesteren, W.G.M., van de Ree T., Talmon, A.M., de Lucas Pardo M., Luger D., Sittoni L. (2015) A large-scale experimental study of high density slurries deposition on beaches, in Proceedings 17th International Conference on Transport and Sedimentation of Solid Particles, 22- 25 Sept. 2015, Delft, Wroclaw University and Delft University of Technology, pp.147–154.
  • 32.
    32 Delft Univ. academictrack Dobbe P., 2021, Simulation of multiphase flow using non-Newtonian fluids and sand segregation in OpenFOAM, MSc-thesis, Delft University of Technology, Delft, The Netherlands. Hanssen J.L.J., 2016, Towards improving predictions of non-Newtonian settling slurries with Delft3D: theoretical development and validation in 1DV , MSc-thesis, Delft University of Technology, Delft, The Netherlands. Van de Ree T.H.B., 2015, Deposition of high density tailings on beaches, MSc-thesis, Delft University of Technology, Delft, The Netherlands. Van Es H.E., 2017, Development of a numerical model for dynamic depositioning of non-Newtonian slurries, MSc-thesis, Delft University of Technology, Delft, The Netherlands. Van Rhee C., 2017, Simulation of the Settling of solids in a non-Newtonian fluid, proc. 18th int conference on Transport and sedimentation of solid particles, Prague, Czech Republic, pp.265-270.
  • 33.