FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and...
Transcript of FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and...
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS:
APPLICATION TO SEALING PROBLEMS
D. LASSEUX, C. VALLET
Other contributors C. MARIE, E. PERROY, G. CARILLONCollaboration: LaMCoS, LTDS (Lyon - France)
TREFLE – Université Bordeaux 1Esplanade des Arts et Métiers - 33405 TALENCE Cedex – France
Acknowledgements: CNRS, EDF, SNECMA, CNES
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
ContextContext
Flow through the contact between rough deformable surfaces
Static seal under severe thermodynamic conditionsDirect metal/metal tight contactApplications: spatial and nuclear industry, etc.
General problem:General problem:
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
DifficultiesDifficulties
Many parameters controlling the leak(some not controlled by the designer!):
- type of surfaces (texture, dimensions, … local defaults)- contrast of scales (from material grain size to contact scale)- surface materials- tightening (level, uniform, localized,
micro & macro deformations…)- type of fluid (gas, liquid, SC)- thermodynamic conditions (T, P, phase change)- operating conditions (tightening relaxation, vibrations,cycling etc.) - …
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Literature is relatively poor:
* Gas flow in the rarefied regime(Armand et al., 1964; Lejay, 1967; Polycarpou and Etsion, 2000)
* Experiments in particular situations(Matsuzaki and Kazamaki, 1988; Yanagisawa et al., 1990, 1991)
* Contact models(Greenwood and Williamson, 1966; Nayak, 1973; Bush et al., 1975;McCool, 1985; Bushan, 1988; Kogut and Etsion, 2003)
Literature surveyLiterature survey
To be completed:Gas versus liquid? (Amesz, 1966)General approach (comparisons predictions-experiments)Analysis in terms of scales of surface defaults
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
GoalsGoals
… in the short term:- perform careful experiments under "well controlled" conditions- try to derive "complete" models- perform direct comparison between predictions and experiments- identify relevant parameters - how they can be controlled
… in the long term:- diagnose the expected leak on an existing configuration- improve the design for more efficient contact seals
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
- 1 rough surface, 1 "perfectly" flat(surface-sum, O'Callaghan and Probert, 1987)
- Deterministic and random textures(turned, sand-blasted and lapped surfaces)
RestrictionsRestrictions
- Fluid: liquid- T and P constant- Uniform load
Sand-blasted LappedTurned
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
OutlineOutline
1. ExperimentExperimental set-upResults
2. Physical models (transport)Micro-scaleMacro-scale
3. ComparisonsImportance of macro-scale defaults
4. Some more analysisImpact of some large scale defaults
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
ExperimentExperiment
Temperatureregulated water N2
Gas Phase Chromatography(GPC)
Sapphire
Load cell
P
Leaking fluid underpressure(Solute)
Solvent loop
Sample(metallic surface)
Hydraulic pump
Hydraulicjack
Reservoir
F
Peristaltic pump
Pressure transducer
Viscous conditionViscous condition
Temperatureregulated water
Gas Phase Chromatography(GPC)
Sapphire
Load cell
Solvent loop
Sample(metallic surface)
Hydraulic pump
HydraulicjackF
Peristaltic pump
Diffusive conditionDiffusive condition
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment (cont'd)Experiment (cont'd)
Patent CNES (France : N°02.01930 – Europe : N° 03.290358.5)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment (cont'd)Experiment (cont'd)
Ra =0.5; 1 µm
20
1.0
φ 50
φ 40 0.3
Ra =0.5; 1 µm
20
1.0
φ 50
φ 40 0.3
Ra =0.5; 1 µm
20
1.0
φ 50
φ 40 0.3
1.0
φ 40 0.3
1.0
φ 40 0.3
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment: Results (viscous condition)Experiment: Results (viscous condition)
Eprouvette A
y = 0.50x + 2.49R2 = 0.999
y = 1.18x + 8.83R2 = 0.999
y = 1.86x + 13.63R2 = 0.998
0
50
100
150
200
250
0 20 40 60 80 100 120 140 160
t (min)
mas
s (m
g)
P=9bar P=9bar P=9bar P=20bar P=20bar P=30bar
Δ
Δ
Δ
ΔΔ
Δ
Turned 316L surface - Contact pressure: Pca = 265 MPaApparent contact area: 38 mm2 - Loadoad: 10 000 N: 10 000 N
Mass of solute versus time (GPC)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Contact pressure:Pca = 700 MPa
m = 1.8 10- 4 t + 9.46R2 = 0.5
9
9.5
10
10.5
0 500 1000 1500
t (min)
mas
s (m
g)ΔP=30bar
m = 5.6 10 - 5 t+ 9.89R2 = 0.10
9
9.5
10
10.5
11
0 500 1000 1500 2000 2500 3000t (min)
mas
s (m
g)
ΔP=10bar m = 1.2 10 - 4 t + 9.71R2 = 0.18
9
9.5
10
10.5
0 500 1000 1500t (min)
mas
s (m
g)
ΔP=20bar
Mass of solute versus time (GPC)Experiment: Results (viscous condition)Experiment: Results (viscous condition)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Mass flow-rate versus pressure drop
y = 0.3059x + 0.0119R2 = 0.9893
y = 0.1104x - 0.0021R2 = 0.9999
y = 0.0516x - 0.0025R2 = 0.9995
y = 0.0397x - 0.0113R2 = 0.9942
y = 0.0108x + 0.0012R2 = 0.9984
y = 0.004x + 0.0005R2 = 0.9992
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0 5 10 15ΔP (bar)
Q (m
g/m
in)
50Mpa75Mpa100Mpa125Mpa150Mpa300Mpa
Experiment: Results (viscous condition)Experiment: Results (viscous condition)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment: Results (viscous condition)Experiment: Results (viscous condition)Q is linear versus ΔP at a given load
( ) ieieii rrµ/rrrµrπ −≈=
ΔPKlnΔPK
2Q ρρ K: transmissivity (m3)
1.0E-091.0E-081.0E-071.0E-061.0E-051.0E-041.0E-031.0E-021.0E-01
0 200 400 600 800Apparent contact pressure Pca (MPa)
K (µ
m3 )
Sample B1Sample B2
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
1.0E-09
1.0E-07
1.0E-05
1.0E-03
1.0E-010 200 400 600 800
Pca (M Pa)
K (µ
m3 )
Sample ASample B1Sample B2
B A
Experiment: Results (viscous condition)Experiment: Results (viscous condition)
Unload
Ra=0.5µmRa=1.1µm
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment: Results (viscous condition)Experiment: Results (viscous condition)
1.0E-091.0E-081.0E-071.0E-061.0E-051.0E-041.0E-031.0E-021.0E-01
0 200 400 600Pca (MPa)
K (µ
m3 )
Turned B1Turned B2Sand-BlastedLapped
Ra=1.1µm
Ra=1µm
Ra=0.4µm
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment: Results (diffusive condition)Experiment: Results (diffusive condition)
ie
ei
iei
ei
i rrcc
rrrcc
r −−
≈−
=)(D
ln)(D
2πQ effeff Deff: effective "diffusivity" (m3/s)
1.E-12
1.E-10
1.E-08
1.E-060 100 200 300 400 500
Pca (MPa)
Def
f (m
3 /s) Turned B1
Turned B2
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Experiment: error estimationExperiment: error estimation
* K estimated fromQ(ΔP) estimations
0
0.05
0.1
0.15
0.2
0.25
0 10 20 30ΔP (bar)
Q (m
g/m
in)
* Q estimated fromm(t) measurement
y = 9.0789x + 413.33R2 = 0.9938
0500
100015002000
0 50 100 150t (min)
m (m
g)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
m(t) is determined form the GPC calibration curve
0
5
10
15
0 5 10mass ratio
Pic
area
ratio
Estimation of Q, K, calibration coefficient etc.and their associated uncertainties
Gauss Markov parameter estimation method
Experiment: error estimationExperiment: error estimation
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Illustration on the flow-rate Q ctM jbj += Q
⎟⎠⎞
⎜⎝⎛
⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛=
⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛= Q
1
1 11 c
t
t
M
MM
X
mbm
b
321
MMM
Optimal estimation with minimal variance
( ) MXPXXPc tt 111
Q−−−=⎟
⎠
⎞⎜⎝
⎛ with ( )
⎟⎟⎟⎟⎟
⎠
⎞
⎜⎜⎜⎜⎜
⎝
⎛
==
2
22
21
0
0
cov
m
MP
σ
σσ
O
andif mass measurement errorsare uncorrelated
( ) 11
Qcov
−−=⎟⎠
⎞⎜⎝
⎛ XXPc t
Experiment: error estimationExperiment: error estimation
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
⎟⎟⎟⎟
⎠
⎞
⎜⎜⎜⎜
⎝
⎛ +−
⎟⎟⎠
⎞⎜⎜⎝
⎛−
=
∑ ∑
∑∑
∑ ∑∑= =
−−
=
−
=
−
= =
−
=
−−m
j
m
jjbjMM
m
jbjM
m
jjM
m
j
m
jjM
m
jjMM
tM
Mt
tt bjbj
bjbj
bjbjbj 1 1
22
1
2
1
2
1
2
1
2
1
222
1Qσσ
σσ
σσσ
1
1
2
1
2
1
222
1
22
−
= =
−
=
−−
=
−
⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛
⎟⎟⎠
⎞⎜⎜⎝
⎛−= ∑ ∑∑∑
m
j
m
jjM
m
jjMM
m
jMQ tt
bjbjbjbjσσσσσand
Same approach to estimate m(t) from calibrationand to estimate K (and Deff) from Q and ΔP
Result: error on K is less than 10%error on Pca can reach 10%
Experiment: error estimationExperiment: error estimation
Complete determination of optimal parametersand associated errors
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
1. ExperimentExperimental set-upResults
2. Physical models (transport)Micro-scaleMacro-scale
3. ComparisonsImportance of macro-scale defaults
4. Some more analysisImpact of some large scale defaults
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescale1. Viscous flowLow Re, stationary, isothermal flow; rigid surfaces.
Stokes model:
0. =∇ vv20 ∇+−= μp∇
0=v at solid walls
v, p
xyz
α
h 0
l 0
B.C.
Hyp:slope is small everywhereh0/l0=ε <<1
u, v ~ u0 x, y ~ l0
w ~ w0 z ~ h0
v(u,v,w)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescale0*
**
*** =++ zyx wvuMass: with 00 uw ε=
Momentum:
withε
μ0
00
hup =
( ) ***
***
***
2**0 zzyyxxx uuup +++−= ε
( ) ***
***
***
2**0 zzyyxxy vvvp +++−= ε
( ) ***
***
***
2**
20 zzyyxxz wwwp +++−= − εε
( )*** , yxp only integrate x and y momentum eqs over z*
( )**2***
* 21 zhzpu x −=
( )**2***
* 21 zhzpv y −=
0*** =⋅+⋅+⋅ zy wvu enenen x ε at the wallsB.C.
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescale
xphdzu
dydQq
hx
x ∂∂
−=== ∫ μ12
3
0
Integrate over z: dimensional form
yphdzv
dxdQ
qh
yy ∂
∂−=== ∫ μ12
3
0
Reynolds or lubricationapproximation(Zimmerman and Bodvarsson,1996)
Integration of the mass balance equation:
0)(00 =+∂
∂
+∂
∂ ∫∫zw
y
dzv
x
dzuzz
i.e. for z=h 0=∂
∂+
∂∂
yq
xq yx
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescale
2D viscous flow problem: q(qx,qy)
ph∇−=
μ12
3q
0=⋅nq
0=⋅∇ q
in β
in β
on Cβσ
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescale1. Diffusive flowFickian, stationary, isothermal; rigid surfaces
0. =∇ jcD∇−=j
0=⋅nj at solid walls
c
xyz
α
h 0
l 0
Hyp: slope is small everywhere h0/l0=ε <<1
jx, jy ~ j0 x, y ~ l0
jz ~ j1 z ~ h0
B.C.
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescale0*
***
** =++ zyx jjjMass: with 01 jj ε=
Fick's law along ez *
***
2zcjz ∂∂
−=ε
),( yxcc = only Integrate over z to get (dimensional form)
xcDhdzjq
h
xx ∂∂
−== ∫0 y
cDhdzjqh
yy ∂∂
−== ∫0
0=∂
∂+
∂∂
yq
xq yx
0=B.C. ⋅+⋅ yyx qq enen x at solid walls
* x and y Fick's law
* mass
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
2D diffusive problem: q(qx,qy)
Physical models: microPhysical models: micro--scalescale
cDh ∇−=q
0=⋅nq
0=⋅∇ q
in β
in β
on Cβσ
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: microPhysical models: micro--scalescaleSame problem for diffusion and viscous flow
ω∇−= kq
0=⋅nq
0=⋅∇ q
in β
in β
on Cβσ
Diffusion: and Dhk = c=ω
Viscous flow: and μ12
3hk = p=ω
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: macroPhysical models: macro--scalescaleUpscaling of the micro-scale model
Method: surface averaging(Whitaker, 1999)
∫=β
ϕϕS
dSS1
∫=β
ϕϕβ
β
SdS
S1
* Averaging theorem:
∫+∇=∇βσ
ϕϕϕC
dCS1
* 2 averages:
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: macroPhysical models: macro--scalescaleResult: model at the RES scale
βω∇⋅−= Hq0=⋅∇ q
( )bIH ∇+= k
b is solution of the closure problem (micro-scale):
( ) kk ~−∇=∇⋅∇ b in βnbn =∇⋅− on Cβσ
0=bb is periodic and
kkk −=~
Diffusion:
Viscous flow:
βcD ∇⋅−= Dq ( )bID ∇+= h
β
μp∇⋅−=
Kq ( )bIK ∇+=12
3h
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Physical models: macroPhysical models: macro--scalescale
Solution of the closureAperture field h(x,y) is known on a regular discrete gridh is constant on each cell
Cell i
Interface ij
Cell j
b is periodic
ijn
0=b
02 =∇ ib( ) ( )IbnIbn +∇⋅=+∇⋅− jjii kk
ji bb =
02 =∇ jb
Numerical scheme: finite volume O(Δx2,Δy2)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
1. ExperimentExperimental set-upResults
2. Physical models (transport)Micro-scaleMacro-scale
3. ComparisonsImportance of macro-scale defaults
4. Some more analysisImpact of some large scale defaults
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionMicro-scale data: surface roughness measurement usingwhite light interferometry (LTDS, Lyon)Resolution : x-y: 0.1 to 1µm z: 2 nm
Turned surface (B1):Computational flow-chart
z(x,y)
Deformation
Percolation
Closure resolution
h(x,y)
h(x,y)h3(x,y)/12
K D
(Flat rigidplane)
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionDeformation: elasto-plastic or purely plastic (erosion) model
Result on turned surface B1
Transmissivity at Pca=200 MPaKyy (µm(µm33))
ElastoElasto plastic plastic ((LaMCoSLaMCoS)) 0.94 0.94
ElastoElasto plasticplastic(LTDS)(LTDS)
1.121.12
PurelyPurely plastic plastic (Erosion)(Erosion) 1.031.03
x
y
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionOn surface B1: no radial flow: leak is along the spiral groove
1.E-06
1.E-05
1.E-04
1.E-03
1.E-02
1.E-01
1.E+00
1.E+010 200 400 600 800
Pca (MPa)
Q (m
g/m
in/b
ar) Computed
Experiment B2Experiment B1
Topological description is uncomplete
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionIdea: larger scale defaults must be taken into account
Default order1 Form default2 Waviness
3 and 4 Roughness
Flatness measurement by fingering (Talyrond) on the rough surface
(Default on sapphire surface < 56nm)
1 div.=0.1µmPeriod ~30° - Amplitude ~1.2µm
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionReconstruction of the complete annular contact
-0.8-0.6-0.4-0.2
00.20.40.60.8
0 20 40 60 80 100 120 140
Circonférence (mm)
Déf
auts
de
plan
éité
s (µ
m)
+
-3-2-10123
0 50 100 150 200 250 300(µm)
(µm
)
Circumference (mm)Wav
ines
s (µm
)
µm
µm
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
0
100
200
300
4000
25
50
75
100
125
150
175
-2.50-1.250.001.252.50
-2.50 -1.25 0.00 1.25 2.50
(µm)
125 mm
0.3 mm
0
100
200
300
4000
25
50
75
100
125
150
175
-2.50-1.250.001.252.50
-2.50 -1.25 0.00 1.25 2.50
(µm)
125 mm
0.3 mm
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionΔr
Q
L
X
Δr
x
QY
Δr
Q
L
X
Δr
x
QY
Q
L
X
Δr
x
QY
YX
C.L.* Y periodic* X: Dirichlet
(on p or c)
![Page 41: FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and Transport in Industrial Porous Media – Utrecht – 12-16/11/07 FLOW IN FRACTURES COUPLED](https://reader033.fdocuments.in/reader033/viewer/2022041518/5e2ca3de68c35c3c4d0abd66/html5/thumbnails/41.jpg)
______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionLocal velocity map
0 25 50 75 100 125 150 175
0
25
50
75
100
125
0 20000 40000 60000 80000 100000
(µm/s)
Pca=200 Mpa – Local radial flow
![Page 42: FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and Transport in Industrial Porous Media – Utrecht – 12-16/11/07 FLOW IN FRACTURES COUPLED](https://reader033.fdocuments.in/reader033/viewer/2022041518/5e2ca3de68c35c3c4d0abd66/html5/thumbnails/42.jpg)
______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
0 25 50 75 100 125 150 175
0
25
50
75
100
125
0 100 200 300 400 500
(µm/s)
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionLocal velocity map
Pca =600 Mpa – Circumferential flow in the spiral groove
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionB1 and B2 surfaces – Viscous flow
1.0E-09
1.0E-07
1.0E-05
1.0E-03
1.0E-010 100 200 300 400 500 600 700 800
Pca (MPa)
K (µ
m3 )
Experiment B1Experiment B2Computed
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Comparisons: experiment Comparisons: experiment vsvs predictionpredictionB1 and B2 surfaces – Diffusion (D=10-9m2/s)
1.E-07
1.E-06
1.E-05
1.E-04
1.E-03
1.E-02
1.E-01
1.E+00
1.E+01100 200 300 400 500
Pca (MPa)D
=Def
f/D
(m)
Experiment B1Experiment B2Computed
![Page 45: FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and Transport in Industrial Porous Media – Utrecht – 12-16/11/07 FLOW IN FRACTURES COUPLED](https://reader033.fdocuments.in/reader033/viewer/2022041518/5e2ca3de68c35c3c4d0abd66/html5/thumbnails/45.jpg)
______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
1. ExperimentExperimental set-upResults
2. Physical models (transport)Micro-scaleMacro-scale
3. ComparisonsImportance of macro-scale defaults
4. Some more analysisImpact of some large scale defaults
![Page 46: FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and Transport in Industrial Porous Media – Utrecht – 12-16/11/07 FLOW IN FRACTURES COUPLED](https://reader033.fdocuments.in/reader033/viewer/2022041518/5e2ca3de68c35c3c4d0abd66/html5/thumbnails/46.jpg)
______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Some more analysis: turned surfacesSome more analysis: turned surfacesLarge effect of 2nd order (waviness) defaults
Analyze 3 types of defaults (viscous flow)
Pure waviness Conical defaultSkew default
Origin: - LF spindle vibrations,- excessive tightening during machining, - remaining stress within the material,- spindle and cutting tool movement axes not perpendicular,- non-uniform chip.
Roughness amplitude (sine): 5µm; contact width: 300µm;contact length: 100mm; default amplitude: 1µm
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Pure waviness
0.000001
0.00001
0.0001
0.001
0.01
0.1
1-2.5 -2 -1.5 -1 -0.5 0 0.5 1
Enfoncement
K
10 périodes5 périodes
0 50 100 150 200 250
0
20
40
60
80
X
Y
0 50 100 150 200 250
0
20
40
60
80
X
Y
0 50 100 150 200 250
0
20
40
60
80
X
Y
0 50 100 150 200 250
0
20
40
60
80
X
Y
Effective contact area contours
Deformation
10 periods5 periods
Some more analysis: turned surfacesSome more analysis: turned surfaces
![Page 48: FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and Transport in Industrial Porous Media – Utrecht – 12-16/11/07 FLOW IN FRACTURES COUPLED](https://reader033.fdocuments.in/reader033/viewer/2022041518/5e2ca3de68c35c3c4d0abd66/html5/thumbnails/48.jpg)
______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Pure waviness
1.E-10
1.E-08
1.E-06
1.E-04
1.E-02
1.E+00
0 500 1000 1500
Pca (Mpa)
K (µ
m3 )
Surface plane Ondulation (5)Ondulation (10)Ondulation (15)
Flat surface Waviness (5)Waviness (10)Waviness (15)
Some more analysis: turned surfacesSome more analysis: turned surfaces
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
0.000001
0.00001
0.0001
0.001
0.01
0.1
1-2.5 -2 -1.5 -1 -0.5 0 0.5 1
Enfoncement
K
0 50 100 150 200 250
0
20
40
60
80
X
Y
0 50 100 150 200 250
0
20
40
60
80
X
Y
0 50 100 150 200 250
0
20
40
60
80
X
Y
0 50 100 150 200 250
0
20
40
60
80
X
Y
Effective contact area contours
Deformation
Conical defaultSome more analysis: turned surfacesSome more analysis: turned surfaces
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Conical default
1.E-10
1.E-08
1.E-06
1.E-04
1.E-02
1.E+00
0 500 1000 1500
Pca (Mpa)
K (µ
m3 )
Surf. PlaneConiqueFlat surfaceConical
Some more analysis: turned surfacesSome more analysis: turned surfaces
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
0.000001
0.00001
0.0001
0.001
0.01
0.1
1-2.5 -2 -1.5 -1 -0.5 0
Enfoncement
K
10 sommets
20 sommets
0 50 100 150 200 250
0
25
50
75
X
Y
enfoncement = -0.9
0 50 100 150 200 250
0
20
40
60
80
X
Y
enfoncement = -1
0 50 100 150 200 250
0
25
50
75
X
Y
enfoncement = -1.3
0 50 100 150 200 250
0
25
50
75
X
Y
enfoncement = -2
Effective contact area contours
Skew default
10 peaks20 peaks
Deformation
Some more analysis: turned surfacesSome more analysis: turned surfaces
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
1.E-10
1.E-08
1.E-06
1.E-04
1.E-02
1.E+00
0 500 1000 1500
Pca (Mpa)
K (µ
m3 )
Surf. PlaneGauche (5)Gauche (10)Gauche (15)
Skew default
Flat surface Skew (5)Skew (10)Skew (15)
Some more analysis: turned surfacesSome more analysis: turned surfaces
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
1.E-07
1.E-06
1.E-05
1.E-04
1.E-03
1.E-02
1.E-01
1.E+00
0 100 200 300 400 500
Pression de Contact (en Mpa)
K (µ
m)
Surf. PlaneConiqueGauche (5)Ondulée (5)
Flat surface ConicalSkew (5)Wavy (5)
Pca (MPa)
Some more analysis: turned surfacesSome more analysis: turned surfaces
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Some conclusionsSome conclusions- Static seal performance of direct metal/metal contactstrongly depends on many parameters.- Texture of both machined surfaces is one the most important.- Many different scales of defaults are usually involved.- The complete structure of the contact might be representedby a simplified two-scale approach.- For turned surfaces, some macro-scale defaults (conical)are preferable.
- Data obtained from very careful experiments are a key supportto assess validity of models that include a complex combinationof mechanisms.-Viscous flow (h3) and diffusion (h) provide two separateddiscriminating tests of aperture description and evolution.
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
Flat non-deformable plane
h
h
- Aperture fields h(x,y) are identical
- Elasticity of the material is acombination of the two original ones
- Hardness of the material is thatof the softer one
SurfaceSurface--sum conceptsum concept
2
22
1
21
*111
EEEνν −
+−
=
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______________________________________________________________________________________________________________________________________________________________________Marie Curie Workshop on Flow and Transport in Industrial Porous Marie Curie Workshop on Flow and Transport in Industrial Porous Media Media –– Utrecht Utrecht –– 1212--16/11/0716/11/07
ErosionErosion
Aperture field under load after erosion
Ai
Position cutting plane
Compute effective contact area
Test:
∑∑ ==i
ii
ii AHApW
Cutting plane
W applied load, H material hardness