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 12 12 - - 16/11/07 16/11/07 FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS: APPLICATION TO SEALING PROBLEMS D. LASSEUX , C. VALLET Other contributors C. MARIE, E. PERROY, G. CARILLON Collaboration: LaMCoS, LTDS (Lyon - France) TREFLE – Université Bordeaux 1 Esplanade des Arts et Métiers - 33405 TALENCE Cedex – France Acknowledgements: CNRS, EDF, SNECMA, CNES

Transcript of FLOW IN FRACTURES COUPLED WITH DEFORMATION EFFECTS ... · Marie Curie Workshop on Flow and...

Page 1: 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

______________________________________________________________________________________________________________________________________________________________________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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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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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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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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- 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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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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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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Experiment (cont'd)Experiment (cont'd)

Patent CNES (France : N°02.01930 – Europe : N° 03.290358.5)

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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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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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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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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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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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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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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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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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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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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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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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⎟⎟⎟⎟

⎜⎜⎜⎜

⎛ +−

⎟⎟⎠

⎞⎜⎜⎝

⎛−

=

∑ ∑

∑∑

∑ ∑∑= =

−−

=

=

= =

=

−−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

Page 22: 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

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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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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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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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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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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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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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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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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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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

Page 35: 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

______________________________________________________________________________________________________________________________________________________________________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

Page 38: 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

______________________________________________________________________________________________________________________________________________________________________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)

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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 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

______________________________________________________________________________________________________________________________________________________________________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

Page 44: 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

______________________________________________________________________________________________________________________________________________________________________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

______________________________________________________________________________________________________________________________________________________________________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

______________________________________________________________________________________________________________________________________________________________________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

Page 47: 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

______________________________________________________________________________________________________________________________________________________________________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

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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

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

Page 49: 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

______________________________________________________________________________________________________________________________________________________________________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

Page 52: 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

______________________________________________________________________________________________________________________________________________________________________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

Page 53: 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

______________________________________________________________________________________________________________________________________________________________________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

Page 54: 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

______________________________________________________________________________________________________________________________________________________________________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 −

+−

=

Page 56: 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

______________________________________________________________________________________________________________________________________________________________________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