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Effect of Finite Grain Size on the Simulation of Fluid Flow in Porous Media

G. Kohring

To cite this version:

G. Kohring. Effect of Finite Grain Size on the Simulation of Fluid Flow in Porous Media. Journal de

Physique II, EDP Sciences, 1991, 1 (2), pp.87-90. �10.1051/jp2:1991148�. �jpa-00247511�

(2)

J 1fi~s. II ~1

(1991)

87-90

FtvRIER1991,

PAGE 87

Classification

1fi~sksAbstnwts

05.50~7.55M

Shom Communication

Effect of Finite Grain Size

on

the Simulation of Fluid Flow in Porousmedia

GAKohring

Institut far Theoretische

Physik,

Universit3t zu

Knin, 2illpicherstra6e 77,

D15~K©

KoIn,

ERG

(Received13 Lkcember199« accepted19 Lkcember1990)

Abstract. Effects caused

by

the

necessarily

finite grain size used in simulations of flew m porous media are

systematically

Studied in Dvo dimensional

hydrodynamic

cellular automata vnth systems of up to 88 million sites, The

permeability

of the media,

K,

18 found to be a function of the grain size, R, and an

extrapolatiqn

to

physically

realistic grain sizes is given,

The last few years have seen renewed interest in the

problem

of fluid flow in

porous mjdia

[1

5J.

Thin is due in

part

to the

importance

attached to various

physical applications,

e,g., esti-

mating

the

properties

of oil and gas

flowing through

porous rocks in

underground reservpirs;

and in

part

to

thp emergence

of a new numerical

technique, namely,

the

lattice-gas (or hydrodynamic)

cellular automata

[6].

As noted

by

many

researchers,

the

lattice-gas

cellular automata

approach

is

particularly

well suited for the

problem

of flow in porous media because of the ease at which

complicated pore geometries

can be introduced ~[3].

Previous work in this field has concentrated on

proof-of-principle

studies

(e,g., demonsjrating

the emergence of

Darcy's

law at low flow velocities

[1, 2])

and on

qualitative

calculations of the

permeability [4, 5].

Given the

relatively

low accuracy of the

lattice-gas technique

on

present

com-

puters,

there is

justification

in not

pressing

such calculations any further

[7j. However,

a moment's consideration leads one to the conclusion that

systematic

errors in these calculations are not

yet

under control.

For a real fluid

flowing

in a porous

medium,

the size of the individual

grains,

which at fixed

porosity

is related to the size of the rock pores, are several orders of

magnitude larger

than the

mean free

path

of a

jypical

fluid molecule.

By

contrast, the

lattice-gas

simulations

typically

use

grain

sizes

which

are of the same order of

magnitude

as the

particle

mean free

path.

In

principle,

this can lead to

spurious, unphysical

effects since true

hydrodynamic

flow

through

the pores, does not have a chhnce to

develop-

in such small confines

[11].

This paper addresses this

problem,

which

was first

pointed

out

by

Rothman

[2], by systematically examining

the effect of different

grain

sizes

at fixed

porosity.

The lattice gas model used in the

present

simulations is a variant of the six bit FHP model on a

triangular

lattice

[6].

An efficient

implementa,tion

of this model for scalar and vector

computers

(3)

88 JOiJRNALDEPHYSIQUEII N°2

has been discussed in a

previous publication [5].

For

studying

the flow

properties media,

obstacles are

placed randomly

in the center half of a

pipe

of

length

L and the

particles

flow from left to

right. (Such

a simulation mimics the way in which

experiments

are

performed.)

In order to insure that the flow has the

property expected

of a very

long pipe,

the first column of the lattice is con-

stantly replaced by particles having

a

velocity

distrAution

corresponding

to that of

fully developed

Poiseuule flow

[4].

The

particle density

in all the simulations

presented

here was, d m 0.15

parti-

cles

per

link at the

inlet,

or p m 0.9

particles per

site. The maximum

particle velocity

at the inlet is about 0,15 sites per unit

time, I-e-,

small

enough

for nonlinear

velocity

effects to be

neglected.

These

parameters yield

a mean free

path

of several lattice sites in the free fluid case

[2].

The

shape

of the obstacles are, for

convenience,

chosen to be rhombi with sides of

length, R,

but the exact

shape

does not appear to make any difference in the results [8~

4, 5J.

In

particular

for our lattice structure, circular obstacles would have

quite rough boundaries,

should therefore be avoided. lvhen

placing

the rhombi on the lattice

they

were allowed to

overlap, creating

very

irregular

structures. After the rhombi are all in

place,

the

porosity

of the medium is calculated

as the ratio of

unoccupied

sites to the total number of sites in the middle half of the

pipe.

For a

random medium this affords a

good

definition of

porosity, #.

In the first

part

of the simulations the size of the rhombi varied while the

porosity

was held fixed.

Figure

I shows

typical

results for the variation of the reduced

permeability

as a function of

grain

size at constant

porosity,

in this case

#

= 0 8 IS + 0 0 IS. The

figure

shows data for

system sizes,

2048 x

640,

4096 x

1344,

8192 x 2688 an16384 x 5376. The small

systems

were run on

the HLRZ'S

Cray-YMP/832 using

the

single pro~essor program

dhcussed

previously.

The

largest system

size

required

I.4

Giga-bits,

or most of the machines shared memory, and was therefore

run in the

autotasking

mode

using up

to 8

processors.

In this

mode,

the

program

achieves a

peak speed

of over 1 000 million site

updates

per second.

The

permeability

of the

sample,

~, was determined

by dividing

the average

velocity

over the last

I/4

of the

pipe by

the

pressure

difference across the

sample.

Note that there are no clear indications of

systematic

effects due to the finite

system sizes,

but there is reasonable evidence for

believing

that the

permeability

scales

linearly

with

grain

size over a

large

range of sizes.

Only

for the

largest grain

sizes do we see indications of the

theoretically expected

Jc «

R~

behavior 11

0, 12].

This effect may be due to the

development

of Poiseuille flow inside the

larger

pores

ill].

Figure

I also

provides

evidence that it may be

posskle

to

extrapolate

to the

physically

inter-

esting region

of

large pore

size

by scaling

~

/R

as a linear function of

I/R.

The data indicate that this linear

extrapolation

should be carried out to the

regime

of I

/R

~

10~~

where a cross over behavior appears to set

in,

and

~/R~

- coast. Note the results obtained for R =

I,

where the

system

is

just

a collectibn of

point

obstacles or a

"dusty"

medium.

Although

such dust has been used in other work

[1, 9],

the

present

data indicate that the dust

regime

is far from the

physical regime.

Figure

2

presents

a

plot

of the

extrapolated permeabilities

as a function of the

porosity using

a linear I

/R extrapolation

of the data.

(Since only

for the

porosity

of

figure

I did we have

enough computer

time to simulate lattices

large enough

to see a

crossover.)

From this

figure

it can be seen hat a

good

fit to the reduced

permeability

is

given by:

~

/R

«

e6

5 *

/(1 #).

Such a functional form

appears

to hold over a

large

range of

porosities, although

we avoid here the

complications

which arise when

studying porosities

near the

percolation

threshold. The functional form of the

permeability

obtained here in the limit of

large grain

sizes is not inconsistent with that of

previous

work

[3, 4],

but the

quantitative

results we obtain are very differenL These new data should be closer to real

experimental

numbers and it would be of interest to see how well the lattice gas

simulations

compare

to

experiments

for this

problem.

In summary, we have studied the effects which are due to the finite

grain

size used in lattice gas simulations of flow in porous

media,

and we find evidence for a crossover behavior as the

grain

size

(4)

N°2 SIMULA3TONOFFLIJIDFLOWINPOROUSMEDIA 89

10~ "

Ol 10°

Ct ~

~ 53 ,

O X o

[

10~~

o

~ CP

10'~

lo' ~ 10~~ 10~~ 10°

~-i

Fig,

I. Plot of the reduced

permeability, ~/R~ wnusl/R

at porosity, #

= 0 815 + o 015. The open

squares are for 2048 x 640, the solid circles for 4096 x 1344, the crosses for 8192 x 2688 and the open

tnangle

for 16384 x 5376. Jlecause of the

crowding

of the data

only

a

single typical

error bar is shown. The

units of

~/R~

are: unit time/ unit mass.

lo'

cr~'

~ s-

1

§2

Fig.

~

Semi-log plot

of the scaled and

extrapolated

reduced

permeability (in

un lattice constant x unit time

/

unit

mass),

(1

#) (~ /R),

wnus #. The solid line is a least squares fit to the data.

increases.

Figure

I has shown

however,

that it is still

possible

to extract

meaningful

information about the limit of

physical grain

sizes

by

a

proper

finite size

scaling analysh

of

systems having

small

grains.

For future

work,

it would be very

interesting

to carry out these calculations near the

percolation

threshold and for a fluid

moving

at nonlinear velocities.

(5)

9o

'JOURNAL

DE PHYSIQUE II ' N°2

Acknowledgements.

It b a

pleasure

to thank D. Stouffer and S. Zaleski for useful discussions. A

grant

bom tile BMFT

(# 0326657D)

for

partial support

of tllh

project

is

gratefully acknowledged

as well as a

grant

of

about 100 hours of

computer

time on tile HLRZ'S

Cray-YMP/832

at the EEA Julich.

References

[ii

BALASUBRAMANIAN

K.,

HAYOT F and SAAM

WE, Phys.

Rev A36

(1987)

2248.

[2] ROTHMAN

D-H-, Geophysics

53,

(1988)

509~

CHEN

S.,

DIEMER K., DOOLEN

G-D-,

EGGERr

K.,

Fu C., GUTMAN S. and TRAvls B., in the

"Proceedings

of the NATO Advanced

Workshop

on Lattice Gas Methods for

PDE'S", Physica

D to be

published;

SucI

S.,

CANCELLIERE A., CHANG C., FOTI E., GRAMIGNANI M. and ROTHMAN D., m

Computational

Methods m Subsurface

Hydrology,

G.

Gambalati,

A. Rinaldo, C.A~ Brebbia, WG.

Gray

and G F

Pinder Eds.

(Spinger-Verlag, Berlin)

1990. ,

[3] DOOLEN G-D-, First

lbpical

Conference

"Computational Physics"

of the Arn.

Phys.

Sac.

(Boston)

June 1989.

[4] BROSA U, and STAUFFER

D.,

I Stat.

Phys.

63

(1991)

to be

published.

,

[5j KOHRING G-A-, f Stat.

Phys.

63

(1991)

to be

published.

[6j FRlscH

U.,

HASSLACHER B, and POMEAU

Y., Phys.

Rev Lett. 56

(1986) 1505;

M.

H#NON, Complex Systems

1

(1987) 763;

RENET

J.-P,

HtNON M., FRlscH U. and D'HUMItRES

D., Eumphys.

Lett 7

(1988)

231;

LIM

H-A-, Pfiys.

Rev A40

(1989) 968;

KADANOFF

P,

MCNAMARA G-R- and ZANETTI G

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Phys.

Rev A40

(1989)

4527.

[7j BROSA

U.,

I

Phys.

France 51

(1990) 1051;

BROSA U., KCIINER C, and WERNER U., Istat.

Phys.

60

(1990)

875.

[8] DUARrE J.A.M.S, and BROSA U., I Stat.

Phys.

59

(1990)

501.

[9] BOON

J.P,

m Correlations and

Connectivity Geometry Aspects

of

Physics, Chemistry

and

Biology,

H-E

Stanley

and N.

Ostrowsky

Eds.

(Academic Press, Dordrecht)

1990.

[10] LI W-H and LAM

S.-H., Principles

of Fluid Mechanics

(Addison-Wesley, Reading)

1976 [11] D'HUMItRES D. and LALLEMAND

P,

C.R-4.S. Paris 302

(1986)

983

[12] WEISSBERG Hi. and PRAGER S.,

Phys.

Fluids 13

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2958.

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