The mechanics of pyroclastic density currents Montserrat, British - - PowerPoint PPT Presentation
The mechanics of pyroclastic density currents Montserrat, British - - PowerPoint PPT Presentation
The mechanics of pyroclastic density currents Montserrat, British Geological Survey Transport processes (not deposits) The role of particle-scale processes on the large scale dynamics of pyroclastic density currents Michael Manga Interrupt
The role of particle-scale processes
- n the large scale dynamics of
pyroclastic density currents
Michael Manga
Interrupt and ask questions anytime
Mutiphase flows in explosive eruptions
Pyroclastic Flow
- Particulate gravity current
- Particle+Gas Flow
- Interaction with water
Plinian Column
- Buoyant plume
- Particle+Gas Flow
Montserrat Univ West Indies St Helens D Swanson, USGS
Multiphase flows in explosive eruptions
- Controls of particle size?
- How fast?
- How far?
- Internal structure?
- Connect processes
to deposits
Montserrat, Univ West Indies St Helens, USGS
Challenge
- Wide range of length and time scales
- Many critical processes occur at the scale of
particles
- How to integrate the micro- and macro-scale
mass, momentum and heat transfer?
Challenge
- Wide range of length and time scales
- Many critical processes occur at the scale of
particles
- How to integrate the micro- and macro-scale
mass, momentum and heat transfer?
Multiple levels of coupling between discrete and continuous phases
Multiple levels of coupling between discrete and continuous phases Prolonged Frictional Contact
Multiple levels of coupling between discrete and continuous phases Instantaneous Collisions
Multiple levels of coupling between discrete and continuous phases
St= p/f
Mean field multifluid equations
Details of constitutive models, equations of state, turbulence models, in Dufek and Bergantz (2007) Key: determining closure models
Continuity Momentum Thermal Energy
(1 1 1ui) t + (1 1 1ui
1uj)
xi = N(,e)
pM0 2
- (1P)
xi + 1 Re
- xi
1 ij
- + 1
St
- (1ui 2ui)+
1 Frd
2
- ˆ
eg
1 1cp
1T t + 1Ui 1T xi
- =
1 Pe
- 1q
1xi + 1
ThSt
- 2T - 1T
( )
- t
1 1
( )+
x
1 1 1ui
( ) = 0
Sub-grid scale thermo-mechanical processes
1) Collisions between particles within pyroclastic flows (and in volcanic conduits in the afternoon) 2) Role of boundary conditions (over water vs
- ver land)
3) Heat transfer from particles to water
- 1. How much of this ash is made
WITHIN the flow?
Influence on flow mechanics, deposits?
Augustine, 1986 Maurice and Katia Krafft
Frictional ash production experiment
Cagnoli and Manga, JGR (2004)
24R = 1
y(u)
Collisional ash production experiment
Ash, not fractal size distribution (collision energy not large enough)
23R = 24 2
( )
2 3/ 2 2
( )g0
3/ 2
2d
( )
- 1. Generating ash within flows
- t(g g
) + xi (g g gUi ) = 0
- t(2 2
) + xi (2 2 2Ui ) = 23R
Mass loss due to collisional ash prodution
- 24R
Mass loss due to frictional ash prodution
- t(3 3
) + xi (3 3 3Ui ) = + 23R
Mass gain due to collisional ash prodution
- t(4 4
) + xi (4 4 4Ui ) = + 24R
Mass gain due to frictional ash prodution
- Continuity
- t(g g
Ui ) + xi (g g gUi
gUj ) = g
P xi ij + g ij xj + gIi + g g gi
- t(2 2
Ui ) + xi (2 2 2Ui
2Uj ) = 2
P xi ij + 2 ij xj + 2Ii + 2 2 gi 23R2Ui 24R2Ui
- t(3 3
Ui ) + xi (3 3 3Ui
3Uj ) = 3
P xi ij + 3 ij xj + 3Ii + 3 3 gi + 23R3Ui
- t(4 4
Ui ) + xi (4 4 4Ui
4Uj ) = 4
P xi ij + 4 ij xj + 4Ii + 4 4 gi + 24R4Ui
Momentum
g g
gcp g T t + gUi g T xi
- = g
q xi H g2 H g3 H g4
2 2
2cp 2 T t + 2Ui 2 T xi
- = 2
q xi + H g2
3 3
3cp 3 T t + 3Ui 3 T xi
- = 3
q xi + H g3
4 4
4cp 4 T t + 4Ui 4 T xi
- = 4
q xi + H g4
Thermal
Model problem
grid 1m x 5 m; time step < 0.1s initial velocity 50 m/s initial concentration 0.025 initial size 1 cm temperature 650 C
Flow over level terrain
1 cm pumice Collisional ash Frictional ash
Collisional and frictional ash are well mixed Travels far beyond pumice Total ash produced: 7%
Downslope Accelerating
1 cm pumice Collisional ash Frictional ash
1 cm pumice Collisional ash Frictional ash
Ash production rate
Ash generated in more energetic part of flow
1 cm pumice Collisional ash Frictional ash
Ash production rate
Conclusions
- A few to a few 10s of % of
flow is converted to ash
- Ash generation increases
runout distance
- Ash generated within flow
separates from larger particles (travels faster, higher, farther)
- Origin of rounding of larger
clasts
- St. Helens, USGS
rounded Lacroix 1902
- 2. Transport capacity of pyroclastic flows:
substrate-flow interactions
Kos Plateau tuff
Role of boundary condition
Particle-substrate interactions
Measure velocity before and after collision; whether particle bounces Variables: angle , velocity, mass, substrate
Air gun
Example (water substrate)
- Extract quantitative information . . .
Water substrate
sinkers Restitution coefficient: Fraction that sink:
Pumice substrate
Restitution coefficient: No effect of mass, impact velocity
Model problem
initial velocity 80 m/s Initial height 100 m initial concentration 0.025 or 0.40 density 1000 kg/m3 size: 95% are 10 microns, 5% are 0.5 mm temperature 700 K; air 300 K
Effect of boundary type
water pumice
Over land flows develop a dense bed-load region because particles are not lost from the flow
10 microns 10 microns 0.5 mm 0.5 mm
Add Lagrangian tracers
Interact with the flow, but do not affect the flow Introduced near inlet Size from 1 micron to 10 m
Over water
No concentrated bedload Concentration has little effect of large clast transport
concentration 0.025 concentration 0.40 > 1cm > 1cm < 1cm < 1cm furthest transport
- f 1 cm clast
Over land
With concentrated bedload, large clasts transported to the end of the flow! Flows travel further than over water concentration 0.025 concentration 0.40 > 1cm > 1cm < 1cm < 1cm furthest transport
- f 1 cm clast
Over water
1) Boundary condition has a small effect for dilute flows 2) Dense flows over land develop a particle-rich bedload which transports large clasts (over water, particles sink and no particle-rich bedload forms)
> 1cm < 1cm
Over land
0.025 0.025 0.40 0.40
Adding mass back into the current?
Can settling particles “splash” mass back into the current?
Experiments
Experiments
Mass ejected can exceed mass of incident particle
Fauria et al. (2016)
Scaling
New and literature data, new scaling law
Fauria et al. (2016)
Density current model
Compute concentration, velocity, temperature as a function of time (and distance) Assume turbulent gravity current (e.g., Dade and Huppert, 1995) more details in Fauria et al. (2016) Allow big particles to settle
Density current model
Allow small particles to splash Conserve energy more details in Fauria et al. (2016) Currents travel until either all particles settle,
- r they become buoyant
Splash cools flow, increases runout
Fauria et al. (2016)
Fauria et al. (2016)
Splash cools flow, increases runout
Fauria et al. (2016)
What we learned
Large clast transport is . . . 1) dominated by momentum exchange from smaller particles 2) suppressed over water because a dense bedload region does not develop (boundary effect is indirect through the concentration of particles in bedload region) 3) Resuspension can change runnout distance by an order-of-magnitude
- 3. Interaction with water
Hot flows, when they enter water, generate stream
- How much?
- How fast?
- Effects of steam generation?
Montserrat, Univ West Indies
Measurement of steam production rate
1) Measure mass of stream released 2) Measure time clasts float
(results in Dufek, Manga Staedter, J Geophys Res 2007)
100-700 oC Pumice, glass beads 3 mm - 2 cm
Stroberg, Manga and Dufek, JVGR 2010
Measurement of steam production rate
Rv =
p
( )
( ) p
( )
pcp
( )(pT wT )
mp[wcp(bT wT ) + L] = 6 p
( )
( ) pcp
( )(pT wT )
d3[wcp(bT wT ) + L]
Multiphase equations
- t(w w
) + xi (w w wUi ) = Rv
Mass loss due to phase change
- t(g g
) + xi (g g gUi ) = +Rv
Mass gain due to phase change
- t(p p
) + xi (p p pUi ) = 0
- t(g g
Ui ) + xi (g g gUi
gUj ) = g
P xi ij + g ij xj + gIi + g g gi + Rv
gUi Momentum gain to phase change
- t(w w
Ui ) + xi (w w wUi
wUj ) = w
P xi ij + w ij xj + wIi + w w gi Rv
wUi Momentum loss due to phase change
- t(p p
Ui ) + xi (p p pUi
pUj ) = p
P xi ij + p ij xj + pIi + p p gi
w
w wcp w T t + wUi w T xi
- = w
q xi + H wg H wp
Mean interphase heat transfer (particle-water)
- H s
wp Subgrid interphase heat transfer (particlewater)
- +
S
Mean field latent heat of vaporization
- +
Ss
Subgrid latent heat of vaporization
- g g
gcp g T t + gUi g T xi
- = g
q xi H gp H gw S
Mean latent heat of vaporization
- Ss
Subgrid latent heat of vaporization
- p p
pcp p T t + pUi p T xi
- = p
q xi + H gp + H wp
Mean interphase heat transfer (particlewater)
- +
H s
wp Subgrid interphase heat transfer (particlewater)
- Continuity
Momentum Thermal Energy
Application to July 12-13, 2003 littoral blast, Montserrat
grid 2 m x 10 m; time step , 0.1 s initial velocity 50 m/s initial concentration 0.1 initial sizes: 50% is 1 cm, 50% is 0.1 mm temperature 650 C
Landward directed base surge
- 0.6% flow forms landward-directed base surge
(Edmonds et al. (2006) estimate a volume of 0.75%)
- Landward directed flow is dry
Edmonds and Herd, Geology (2005)
steam landward directed blast
Conclusions
- Experimental measurements can be used to
link the micro- and macro-scale
- Particle-scale thermo-mechanical processes
and properties (ash production, vaporization of water, boundary conditions) matter - qualitatively and quantitatively
Suggested reading Dufek, J. (2016) The fluid mechanics of pyroclastic density currents, Annual Reviews of Fluid Mechanics, vol. 48, 459-485