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JCT1 Benchmarking exercise
Depth-averaged Two-phase Debris-flow Model with a Shear-rate Dependent
Internal Friction
Xie Y.X., Cui, K.F., Zhou G.D., Song D.R., Zhou M.J.
a Key Laboratory of Mountain Hazards and Earth Surface Process, Chinese Academy of Sciences, Chengdu, China
b Institute of Mountain Hazards and Environment, Chinese Academy of Sciences & Ministry of Water Conservancy, Chengdu, China
Introduction
The interaction between the solid and fluid phases play an important role
in the dynamics of the system and on the flow mobility.
Fixed rheology debris flow models cannot accurately represent its
complex evolving behavior – from nearly static to liquefied.
Iverson, R.M., The Physics of Debris Flows, Reviews of Geophysics, 35, 3, August 1997Iverson, R.M., The Debris Flow Rheology Myth, Debris-Flow Hazards Mitigation: Mechanics, Prediction, and Assessment, Rickenmann & Chen, 2003
USGS Flume experiments
Natural debris flow
Granular
System
SlurryWater + Fines
Coarse debris
Pebbles
Boulders
Two-phase debris flow model
Mass and Momentum Balance Equations
Flow of a mixture composed of solids and fluids. Based on the dynamics of an assemblyof solid particles immersed in a Newtonian fluid.
𝜌𝑠 𝜕𝑡𝐶𝑠 + 𝛻 ∙ 𝐶𝑠𝑣𝑠 = 0
𝜌𝑓 𝜕𝑡(1 − 𝐶𝑠) + 𝛻 ∙ (1 − 𝐶𝑠)𝑣𝑓 = 0
𝜌𝑠𝐶𝑠 𝜕𝑡𝑣𝑠 + 𝛻(𝑣𝑠 ∙ 𝑣𝑠 = −𝛻 ∙ 𝜏𝑠 + 𝑓𝑖 + 𝜌𝑠𝐶𝑠g
𝜌𝑓(1 − 𝐶𝑠) 𝜕𝑡𝑣𝑓 + 𝛻(𝑣𝑓 ∙ 𝑣𝑓 ) = −𝛻 ∙ 𝜏𝑓 − 𝑓𝑖 + 𝜌𝑓(1 − 𝐶𝑠)g
Solid phase
Fluid phase
Solid-fluid interaction term
Shear stress in granular flows
Viscosity of Newtonian Fluid Bouchut F., Fernandez-Nieto E.D., Mangeney A., Narbona –Reina G. 2015. A Two-phase debris flow model with energy balance. ESAIM: M2AN 49:101-140, doi: 10.1051/m2an/2014026
𝐶𝑠 =ℎ𝑠
ℎ𝑓 + ℎ𝑠
𝜌𝑚 = 𝜌𝑠𝐶𝑠 + 𝜌𝑓(1 − 𝐶𝑠)
𝑣𝑚 =𝜌𝑠𝐶𝑠𝑣𝑠 + 𝜌𝑓(1 − 𝐶𝑠)𝑣𝑓
𝜌𝑠𝐶𝑠 + 𝜌𝑓(1 − 𝐶𝑠)
Mixture Properties
Two-phase debris flow model
Depth- averaged forms
𝜌𝑠𝜕ℎ𝑠𝜕𝑡
+𝜕(ℎ𝑠𝑢𝑠)
𝜕𝑥+𝜕(ℎ𝑠𝑣𝑠)
𝜕𝑦= 0
𝜌𝑓𝜕ℎ𝑓
𝜕𝑡+𝜕(ℎ𝑓𝑢𝑓)
𝜕𝑥+𝜕(ℎ𝑓𝑣𝑓)
𝜕𝑦= 0
𝜌𝑠𝜕(ℎ𝑠𝑢𝑠)
𝜕𝑡+𝜕 ℎ𝑠𝑢𝑠
2 + ൗ𝑘𝑠𝑔ℎ𝑠2
2𝜕𝑥
+𝜕(ℎ𝑠𝑢𝑠𝑣𝑠)
𝜕𝑦= 𝜌𝑠𝑔𝑧ℎ𝑠
𝜕𝑧
𝜕𝑥− 𝜏𝑠𝑥 + 𝑓𝑖𝑥
𝜌𝑠𝜕(ℎ𝑠𝑣𝑠)
𝜕𝑡+𝜕(ℎ𝑠𝑣𝑠𝑢𝑠)
𝜕𝑥+𝜕 ℎ𝑠𝑢𝑠
2 + ൗ𝑘𝑠𝑔ℎ𝑠2
2𝜕𝑦
= 𝜌𝑠𝑔𝑧ℎ𝑠𝜕𝑧
𝜕𝑦− 𝜏𝑠𝑦 + 𝑓𝑖𝑦
𝜌𝑓𝜕(ℎ𝑓𝑣𝑓)
𝜕𝑡+𝜕(ℎ𝑓𝑣𝑓𝑢𝑓)
𝜕𝑥+𝜕 ℎ𝑓𝑢𝑓
2 + ൘𝑘𝑓𝑔ℎ𝑓2
2𝜕𝑦
= 𝜌𝑓𝑔𝑧ℎ𝑓𝜕𝑧
𝜕𝑦− 𝜏𝑓𝑦 + 𝑓𝑖𝑦
𝜌𝑓𝜕(ℎ𝑓𝑢𝑓)
𝜕𝑡+𝜕 ℎ𝑓𝑢𝑓
2 + ൘𝑘𝑓𝑔ℎ𝑓2
2𝜕𝑥
+𝜕(ℎ𝑓𝑢𝑓𝑣𝑓)
𝜕𝑦= 𝜌𝑓𝑔𝑧ℎ𝑓
𝜕𝑧
𝜕𝑥− 𝜏𝑓𝑥 + 𝑓𝑖𝑥
Bouchut F., Fernandez-Nieto E.D., Mangeney A., Narbona –Reina G. 2015. A Two-phase debris flow model with energy balance. ESAIM: M2AN 49:101-140, doi: 10.1051/m2an/2014026
Solid phase
Fluid phase
Solid-fluid coupling
𝑓𝑖 = −𝑣𝑝𝑖𝛻𝑝 +1
2𝐶𝑑𝜌𝑓
𝜋𝑑2
4𝑼− 𝑽 𝑼− 𝑽 𝑛−𝜒+1 +
BuoyancyHydrostatic
Drag ForceHydrodynamic
Virtual Mass ForceBasset ForceStaffman ForceMagnus Force
Drag Coefficient
Porosity Correction Factor
Reynold’s Number (Particle Scale)
Zhao T., 2017. Coupled DEM-CFD Analyses of Landslide-Induced Debris Flows. Singapore, Springer Nature.Zhu H.P., Zhou Z.Y., Yang R.Y., Yu A.B., Discrete particle simulation of particulate systems: Theoretical developments, Chemical Engineering Science 62 (2007) 3378 – 3396
𝐶𝐷 =24
𝑅𝑒𝑝1 + 0.15𝑅𝑒𝑝
0.681 +0.407
1 +8710𝑅𝑒𝑝
𝜒 = 3.7 − 0.65exp −1.5 − log10 𝑅𝑒𝑝
2
2
𝑅𝑒𝑝 = Τ𝜌𝑓𝑑 𝑼 − 𝑽 𝜇
Brown & Lawler 2003
Internal Friction
Shear stress models for granular flows
𝜏𝑠 = 𝜇𝜌𝑔𝑐𝑜𝑠ѲℎCoulomb model
Voellmy model
𝜏𝑠 = 𝜇𝜌𝑔𝑐𝑜𝑠Ѳℎ + 𝑔ℎ𝑢2
𝜌ξℎ2
Non-local 𝝁 𝑰 rheology model
𝜏𝑠 = 𝜌𝑔𝑐𝑜𝑠Ѳℎ 𝜇𝑠 +𝜇2 − 𝜇𝑠 𝑢𝑑50
𝐼0ℎ32 𝐶𝑠𝑔 + 𝑢𝑑50
𝐼0 =5
2
𝑑
𝑙0
𝛽
𝜙𝑐𝑜𝑠𝜃
• Only apply to quasi-static conditions;unable to capture the effects of particle contacts within the granular body.
• Adds a dynamic shear resistance term;turbulence coefficient is not physically well-defined.
• The shear rate dependence enables the frictional model to transition from a quasi-static regime to a rapid shear regime.
Zhou G G D, Ng C W W, Sun Q C. 2014. A new theoretical method for analyzing confined dry granular flows, Landslides, 11(3), 369-384Jop P., Fortrerre Y., Poliquen O. 2006. A Constitutive law for dense granular flows. Nature, 441(8), 727-730
𝜇𝑠 function of bed friction angle 𝜇2 function of internal friction angle
𝛽 and 𝑙0 are material constants𝑑50 is the mean particle diameter𝐶𝑠 is the solid volume concentration
Experiments to determine material bed friction angle (𝜽𝒃𝒆𝒅) and internal friction angle (𝜽𝒊𝒏𝒕).
Numerical Scheme (FDM)
S1 S2
S3S4
Non-oscillatory Central Differencing Scheme
• Based on the NT scheme, natural extension of the Lax first order scheme.
• Scheme viscosity is treated desirably.
• Offers the advantage of avoiding the costly Riemann characteristic decomposition while retaining high
resolution.First-order Lax central
differencing scheme
Second-order central
differencing scheme
under staggered grid
Second or higher-order
central differencing under
non-staggered grid
Van-Leer
interpolation
Re-averaged,
reconstructed
value of staggered
form
Nessyahu H, Tadmor E. 1990. Non-oscillatory central differencing for hyperbolic conservation laws, Journal of computational physics, 87(2), 408-463
Model Validation
Solid Parameters Values
Solid Volume Concentration
𝐶𝑠 0.4
𝜇𝑠 0.25
𝜇2 0.32
𝐼0 0.28
Mean Particle Diameter
𝑑50 (𝑚) 0.0005
Fluid Parameters Values
Fluid Viscosity (𝑃𝑎 ⋅ 𝑠) 0.01
Two-phase flume experiment is compared with model.
Flume experiment using mono-sized glass beads mixed with glycerol
Mixture of glass beads and glycerol
solution
0.4
Model Validation
Numerical result
Flume test
Point B
Height
Shear and normal forces obtained from flume experiments are validated
against model calculated values.
Numerical result
Flume testPoint A
Height
𝑃 = 𝜌𝑠𝑔ℎ 𝑠 + 𝜌𝑓𝑔ℎ 𝑓
𝜏 = 𝐶𝑠𝜏𝑠 + (1 − 𝐶s)𝜏𝑓
Case study I
Source location
Disruption to traffic
A
B
C
D
E
General Features:The Yu Tung Debris Flow of Hong Kong is a series of 19 landslides that occurred at the hillside area adjacent the Yu Tung
road. The largest debris flow had a total detached mass of 2,350 m3 and a total run-out distance of 600 m. The velocity at 100
m from the source location was estimated to be about 12 m/s which reduced to about 10m/s at 400 m.
Yu Tung debris flow, Hong Kong Solid Parameters Values
Solid Volume Concentration
𝐶𝑠 0.2~ 0.5
𝜇𝑠 0.23
𝜇2 0.3
𝐼0 0.28
Mean Particle Diameter
𝑑50 (𝑚) 0.001
Fluid Parameters Values
Fluid Viscosity (𝑃𝑎 ⋅ 𝑠) 0.005
*Parameter values are based on Zhou et al. 2014
Zhou G G D, Ng C W W, Sun Q C. 2014. A new theoretical method for analyzing confined dry granular flows, Landslides, 11(3), 369-384
Flow Velocities
Velocities calculated two-phase model against field-estimated velocities.
• The higher the solid concentration the lower the velocity.
• Best predictions come at a relatively low solid concentration (i.e. 0.4)
• Highest velocities correspond to the sudden bend in the flow path at ~300 m.
• Total run-out distance is ~600 m.
Two - phase
Evolution of Solid Concentration
• The model shows a constant re-distribution of the solid concentration during the
course of the flow.
Initial state is assumed to be well-mixed.
Volume= 2350 m3
Mixture Cs= 0.3
Runout= 530 m
Grid: 325× 88
Space gridding: 2 m
Comp. time=10 min. Actual footage
Flow is highly saturated. Head
region is watery/highly fluidized
followed by a more solid-rich region.Time= 0 s Time= 20 s Time= 50 s Time= 100 s
Cs
Conclusions
• A two-phase depth-averaged model was presented which incorporates solid-
fluid interaction and shear-stress dependent internal friction for the flow of the
solid mixture.
• Validation results show over-prediction of shear and normal stresses, and flow
height.
• Benchmark results for the Yu Tung debris flow show reasonable agreement
with known velocities. Fluctuations in the velocities arise due to the re-
arrangement of phases during flow.
• The model features a separation of the solid and fluid phases during the course
of the flow as marked by sharp transitions in the solid volume fractions.
Thank you.That’s all for now
DEM of landInformation of
material in source area
Basal parameters
Initial condition
Begin
Data initializtion
Model of single phase
Shallow water equations
frictional
equations
Discrete equationsusing high resolution scheme
over
( ) ( ) ( ) ( )2 2 2
t dt t dt tU t t U t F t G t S t
dx dy
Current time=total time
( ) ( ) ( ) ( )2
t dt dtU t U t F t G t
dx dy
crt crt dt
2 2
2 2
1( )
( ) ( )2r
hu kghhu huv u Z
f ght x y xu v
( ) ( ) ( )h hu hvE
t x y
2 2
2 2
1( )
( ) ( ) 2r
hv kghhv huv v Z
f ght x y yu v
Grid mesh
Difinite function
Current time<total time
Aftertreatment(animation)
Data analysis
Erosion block
Pre processing: Mesh grid, read terrain info…What you need to do:
1. Get the Dem(digital elevation map) of terrain and source material2. Define the basal friction ( basal friction parameters)
Main processing: 1. Discrete the governing equations using specific math schemes
2. Iterate the variables
Post processing: 1. Data analysis2. Animation and figures (Tecplot, Gmesh, Google
earth, and Arcgis, surfer)
Appendix 1: Program setting