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Jurnal Teknologi, 34(B) Jun 2001: 31–44 © Universiti Teknologi Malaysia NUMERICAL MODELLING OF THERMO-HYDRO- MECHANICAL (THM) IN DEFORMING POROUS MEDIA FOR SUBSURFACE SYSTEMS NORHAN ABD. RAHMAN 1 , SAMIRA ALBATI KAMARUDDIN 2 & BERNHARD A. SCHREFLER 3 Abstract. The study of multiphase flow and heat flow in partially saturated porous media is important in environmental geomechanics engineering because of its relevance to consolidation of porous media in unsaturated zone. A numerical model which describes the thermo-hydro-me- chanical (THM) coupled problems in deformable porous material with two-phase flow has been developed. The relationships between capillary pressure, saturation of water and relative permeabilities of water and gas, proposed by Brooks and Corey was used. An extended study of the numerical model, based on the COMES-GEO code was conducted recently to solve unsa- turated problems in local condition of Kg. Puteh wellfield, Kota Bharu. This site is a potential shallow aquifer which contribute to the largest groundwater supply in Kota Bharu, Kelantan. Some numerical investigation on the proposed formulation is discussed with illustrative example prob- lems to demonstrate solution procedures and validating of the model. Key words: Multiphase flow; heat flow; deforming porous media; numerical model; unsaturated zone; thermo-hydro-mechanical. Abstrak. Kajian aliran berbilang-fasa dan aliran haba dalam bahantara berliang separa tepu menjadi semakin penting dalam kejuruteraan geomekanik persekitaran kerana ia berkait rapat dengan pengukuhan bahantara berliang itu di dalam zon tidak tepu. Satu model berangka telah dikembangkan untuk menghuraikan masalah terganding haba-hidro-mekanikal (THM) dalam bahan berliang boleh ubah bentuk dengan aliran dua-fasa. Hubungan yang disarankan oleh Brooks dan Corey telah digunakan kepada tekanan rerambut, ketepuan air dan kebolehtelapan air serta gas. Satu kajian lanjutan dibuat ke atas model berangka tersebut berasaskan kod COMES-GEO untuk menyelesaikan masalah yang berlaku dalam zon tak tepu di medan telaga Kg. Puteh, Kota Bharu, Kelantan iaitu sebuah akuifer cetek yang berpotensi untuk mengeluarkan bekalan air bumi terbanyak di daerah Kota Bharu. Untuk menunjukkan model dan prosedur penyelesaiannya, rumusan pelaksanaan berangka dan contoh-contoh masalah dibincangkan di dalam kajian ini. Kata kunci: Aliran berbilang-fasa, aliran haba, bahan berliang boleh ubah bentuk, model berangka, zon tidak tepu, haba-hidro-mekanikal. 1&2 Faculty of Civil Engineering, Universiti Teknologi Malaysia, 81310 Skudai, Johor Darul Takzim, Malaysia. Tel: 07-5503023, Fax: 07-5566157, e-mail: [email protected]; e-mail: [email protected] 3 Department of Structural and Transportation Engineering, University of Padua, Via Marzolo 9, 35131 Padova, Italy. e-mail: [email protected] i pd.it Untitled-10 02/16/2007, 17:01 31

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Page 1: NUMERICAL MODELLING OF THERMO-HYDRO- MECHANICAL … · NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 33 Stress is defined as tension positive for solid phase and pore pressure

NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 31

Jurnal Teknologi, 34(B) Jun 2001: 31–44© Universiti Teknologi Malaysia

NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) IN DEFORMING POROUS MEDIA FOR

SUBSURFACE SYSTEMS

NORHAN ABD. RAHMAN1, SAMIRA ALBATI KAMARUDDIN2 & BERNHARDA. SCHREFLER3

Abstract. The study of multiphase flow and heat flow in partially saturated porous media isimportant in environmental geomechanics engineering because of its relevance to consolidation ofporous media in unsaturated zone. A numerical model which describes the thermo-hydro-me-chanical (THM) coupled problems in deformable porous material with two-phase flow has beendeveloped. The relationships between capillary pressure, saturation of water and relativepermeabilities of water and gas, proposed by Brooks and Corey was used. An extended study ofthe numerical model, based on the COMES-GEO code was conducted recently to solve unsa-turated problems in local condition of Kg. Puteh wellfield, Kota Bharu. This site is a potentialshallow aquifer which contribute to the largest groundwater supply in Kota Bharu, Kelantan. Somenumerical investigation on the proposed formulation is discussed with illustrative example prob-lems to demonstrate solution procedures and validating of the model.

Key words: Multiphase flow; heat flow; deforming porous media; numerical model; unsaturatedzone; thermo-hydro-mechanical.

Abstrak. Kajian aliran berbilang-fasa dan aliran haba dalam bahantara berliang separa tepumenjadi semakin penting dalam kejuruteraan geomekanik persekitaran kerana ia berkait rapatdengan pengukuhan bahantara berliang itu di dalam zon tidak tepu. Satu model berangka telahdikembangkan untuk menghuraikan masalah terganding haba-hidro-mekanikal (THM) dalam bahanberliang boleh ubah bentuk dengan aliran dua-fasa. Hubungan yang disarankan oleh Brooks danCorey telah digunakan kepada tekanan rerambut, ketepuan air dan kebolehtelapan air serta gas.Satu kajian lanjutan dibuat ke atas model berangka tersebut berasaskan kod COMES-GEO untukmenyelesaikan masalah yang berlaku dalam zon tak tepu di medan telaga Kg. Puteh, Kota Bharu,Kelantan iaitu sebuah akuifer cetek yang berpotensi untuk mengeluarkan bekalan air bumi terbanyakdi daerah Kota Bharu. Untuk menunjukkan model dan prosedur penyelesaiannya, rumusanpelaksanaan berangka dan contoh-contoh masalah dibincangkan di dalam kajian ini.

Kata kunci: Aliran berbilang-fasa, aliran haba, bahan berliang boleh ubah bentuk, model berangka,zon tidak tepu, haba-hidro-mekanikal.

1&2 Faculty of Civil Engineering, Universiti Teknologi Malaysia, 81310 Skudai, Johor Darul Takzim,Malaysia. Tel: 07-5503023, Fax: 07-5566157, e-mail: [email protected]; e-mail:[email protected]

3 Department of Structural and Transportation Engineering, University of Padua, Via Marzolo 9,35131 Padova, Italy. e-mail: [email protected]

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER32

1.0 INTRODUCTION

In recent years there have been an increased interest in thermo-hydro-mechanics ofpartially saturated porous materials. Several mathematical models of transport pro-cesses were proposed in [1–5]. The studies on multiphase flow and heat flow inpartially saturated porous media is significant in environmental geomechanics engi-neering because of its relevance to consolidation of porous media in unsaturatedzone. The description of multiphase systems in porous media may be based eitheron the mixture theory integrated by the concept of volume fractions or on averagingtheories and from a classical viewpoint on Biot's theory. For this study, the averagingtheories developed by Hassanizadeh and Gray [6], based on spatial averaging ope-rators were applied as it gives a better understanding on the microscopic situationand macroscopic relations. Recent studies by Chauteau and Dormieux [7] discussedthe behaviour of unsaturated porous media in the light of a micromechanical ap-proach based on the macroscopic and microscopic level.

The work described herein is a development of a numerical model for thermo-hydro-mechanical (THM) coupled problems in deformable porous material withtwo-phase flow. The model will be applied to the local condition of Kg. Puteh wellfield,one of the major shallow aquifers contributing to the groundwater sources to KotaBharu water supply demand. It is an extension of a study on the existing codeknown as the Computational Solid Mechanics (COMES-GEO) written by Baggioand Gawin, [8]. The code is developed along the lines of the theory outlined byLewis and Schrefler [5] using finite element method. It is usually used in solving theproblems of unsaturated zone of the subsurface systems. The primary function ofthe model is to provide prediction of future performance of selected site/situation.This includes the development of mathematical models to study the phenomenarelated to heat, and mass transfer in partially saturated deforming porous media.

2.0 PHYSICAL MODEL

The Biot’s theory is derived and extended for the case of non-isothermal two-phaseflow in deforming porous media. Schrefler, Zhan and Simoni [4, 9] made this exten-sion for the case of slow phenomena. For isothermal case with the air phase atatmospheric pressure, inertia forces are considered, as done by Zienkiewicz et al.,[1]. For simplicity, and dealing with macroscopic variables small displacements areassumed for the solid phase.

The void of the skeleton is partly filled with water and partly with moist air (dryair + water vapour) where the summation of the degree of water saturation, Sw anddegree of gas saturation, Sg is equal to one, i.e.

w gS S+ = 1 (2.1)

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NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 33

Stress is defined as tension positive for solid phase and pore pressure is defined ascompressive positive for fluids. The water pressure, pw and gas pressure, pg arerelated through the capillary pressure, pc: pg − pw = pc where, pc is the function of Swand T (temperature): pc = pc (Sw, T). The constitutive law of the solid is introducedthrough the concept of effective stress, σ' = σ + Ips, which stipulates that the maincharacteristics of the solid-phase constitutive relation can be written in terms of σ'(also known as Bishop stress) where σ is the total stress tensor, I the second-orderunit tensor and ps is the average pressure of both water and air surrounding thegrains.

3.0 MATHEMATICAL MODEL

The model is based on strong physical background aimed at handling situationswhich span from fully saturated to almost dry conditions. It consists of balanceequations of mass, linear momentum and energy, as well as appropriateness of theconstitutive equations. The macroscopic balance equations applied in the modelwere obtained from balance equations at macroscopic level by use of spatial averag-ing operators. The gas phase is modelled as an ideal gas composed of dry air andwater vapour, which are considered as two miscible species. Phase changes of water(evaporation-condensation) and heat transfer through conduction and convection,as well as latent heat transfer are considered. This model is an extension of the heatand mass transfer formulation to the case of deformable porous media by Baggio et.al., [10], based on Whitaker’s approach [11–12]. The model makes use of a modi-fied effective stress concept together with the capillary pressure relationship. Theselected primary variables are gas pressure, capillary pressure, temperature anddisplacements which correspond to the measured quantities in the laboratory. Thisis an important aspect when selecting the appropriate constitutive equations. Thegoverning equations and discretized equations are solved by Newton-Raphson pro-cedure.

3.1 Conservation Equation

Only slow phenomena and small displacements are considered in the followingequations. The assumption is based on thermal equilibrium between solid matrix,gas and liquid, given the same temperature for the three constituents. The laws ofcontinuum are used to formulate heat and mass transfer in porous media comprisedof four equations which takes into consideration the mass of the dry air, mass of thewater species (liquid water + vapour), enthalpy of the whole medium (latent heat)and linear momentum of the multiphase medium. The governing equations of themodel, expressed in terms of the chosen state variables, gas pressure, pg, capillarypressure, pc, temperature, T and displacements vector, u, are stated as follows:

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER34

(a) Dry air conservation equation:

( ) ( ) ( ) ( ) ( )( )

hydrga ga ga ga g

dgag

S S S . .t t t

.

φφ ρ ρ α ρ ρ

ρ

∂∂ ∂ − + − + − ∇ + ∇ ∂ ∂ ∂+ ∇ =

1 1 1

0v

u v

(3.1)

(b) Water species (liquid-vapour) conservation equation:

( ) ( ) ( ) ( ) ( )

( ) ( )

( ) ( ) ( )

hydrgw gw gw gw g

hydrdgwg w w

w gw l hydr

S S S . .t t t

. S St t

S . .t t

φφ ρ ρ α ρ ρ

φρ φ ρ ρ

α ρ ρ

∂∂ ∂ − + − + − ∇ + ∇ ∂ ∂ ∂∂∂+∇ == − −

∂ ∂∂ ∂− ∇ − ∇ − ∆∂ ∂

1 1 1 u v

v

u v m (3.2)

(c) Energy conservation (enthalpy balance):

( )( ) ( ) ( )

( )

p pw w l pg g g eff

hydrphase w w w w l

hydr hydr

TC C C T . T

t

h S S S . .t t t

ht

ρ ρ ρ λ

φφ ρ ρ α ρ ρ

∂ + + ∇ − ∇ ∇ = ∂∂ ∂ ∂= ∆ + + ∇ + ∇ ∂ ∂ ∂

∂+∆ ∆∂

v v

u v

m (3.3)

(d) Linear momentum balance equation for the whole mixture of terms of totalstresses (in incremental form):-

σ ρ∂ ∂∇ + =∂ ∂

0.t t

b (3.4)

where ρ is the averaged density of the multi-phase medium, given by

( ) ( )ρ φ ρ φ ρ φ ρ= − + + −1 1s l gS S (3.5)

and φ is the total porosity, S is saturation of water, α is known as Biot’s con-stant, σ represents total stress tensor, T is temperature, u means displacementvector of solid matrix, b indicates vector of the specific body term (normally

corresponding to the acceleration of gravity) and kkx

∂∇ =∂

i , Nabla operator,

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NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 35

where ik is versor of the xk axis. Meanwhile vg and vl is the velocity of gaseousand liquid phase; Cp, Cpg and Cpw are effective specific heat of porous medium,specific heat of gas mixture and water; λeff is the effective thermal conductivity;φhydr as part of porosity resulting from dehydration process; ∆mhydr, mass sourceterm related to hydration-dehydration process and finally ∆hphase is the enthalpybalance of the phase per unit mass.

For fluid phases the multiphase Darcy’s law has been applied as constitutiveequation, thus for capillary water we have:

( )rww w w

w

Kp ρ

µ= − ∇ −K

v b pc < pb (3.6a)

( )rww g c w

w

Kp p ρ

µ= − ∇ − ∇ −K

v b cr c bp p p> ≥ (3.6b)

w = 0v c crp p≥ (3.6c)

while for the gas phase holds:

rgg g

g

Kp

µ= − ∇

Kv c bp p≥ (3.7a)

vg = 0 pc < pb (3.7b)

where K is intrinsic permeability tensor, Krg and Krw are relative permeabilities ofthe gaseous and liquid phases, vw and vg are volume averaged velocities of capillarywater and gaseous phase relative to the solid phase and b indicates the specific bodyforce term. For the description of the diffusion process of the binary gas speciesmixture (dry air and water vapour) Fick's law is applied:

ga gwd da w a wga gweff eff2 2

g gg g

p pM M M MD D

p pM M

= − ∇ = ∇ = −

v v (3.8)

where gw ga

g g w g aM M M

ρ ρρ ρ

= +1 1 1(3.9)

and Deff is the effective diffusion coefficient of vapour species in the porous me-dium, and Ma, Mg and Mw are the molar mass of dry air, gas moisture and watervapour. For all the gaseous constituents, i.e. dry air (ga), water vapour (gw) andmoist air (g), the equation of state of perfect gases: pga = ρgaTR/Ma, pgw = ρgwTR/Mw,pg = ρgTR/Mg, and Dalton's law is pg = pga + pgw are assumed as constitutive equa-tions.

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER36

The constitutive relationship for the solid skeleton is assumed in the form: dσ′ =KT(dε−dεT−dεo) together with the definition of the strain matrix B relating strain and

displacement: ε = Bu, where KT is a tangent matrix and T sd dTβε =3

I defined as

the strain increment caused by thermo-elastic expansion, βs is the cubic thermalexpansion coefficient of the solid and dεo is the autogeneous strain increments.

3.2 Initial and Boundary Conditions

The initial conditions specify the full fields of gas pressure, capillary pressure, tem-perature and displacements:

pg = pog, pc = po

c, T = To, u = uo at t = 0 (3.6)

The boundary conditions can be of the first kind or Dirichlet's boundary conditionson Γi

1:

g g c c Tp p , p p , T T ,= Γ = Γ = Γ = Γ1 1 1 1on on on on uu u (3.7)

of the second kind or Neumann's boundary conditions on Γi2:

( )dgwga a g ga. qρ ρ− − =v v n on Γg

2,

( )dgwgw g w l g gw l. q qρ ρ ρ− + + = +v v v n on Γc

2,

( )w l phase eff Th T . qρ λ− ∆ − ∇ =v n on ΓT2,

ga. qσ =n on Γu2, (3.8)

and of the third kind or Cauchy’s (mixed) boundary conditions on Γi3:

( ) ( )dgwgw g l g c gw gwρ ρ ρ β ρ ρ ∞+ + = −v v vw .n on Γc

3

( ) ( ) ( )w l phase eff ch T T T e T Tρ λ α σ∞ ∞∆ − ∇ = − + −4 4v o.n on ΓT3, (3.9)

where the boundary i i iΓ = Γ ∪ Γ ∪ Γ1 2 3 , n is the unit normal vector, for the sur-

rounding gas, qga, qgw, ql and qT corresponding to the imposed dry air flux, imposedvapour flux, imposed liquid flux and imposed heat flux.

t is the imposed traction, ρgw∞ is the mass concentration of water vapour and toois the temperature in the far field of undisturbed gas phase, e is the emmisivity of theinterface, σo is the Stefan-Boltzmann constant, while αc and βc are convective heatand mass transfer coefficients.

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NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 37

4.0 NUMERICAL MODEL

The Galerkin form of the method of weighted residuals (MWR) was selected toproduce an integral representation of the basic conservation laws. Within each ele-ment, a set of nodal points is established at which the dependent variables Pg, Pc, T,ux and uy are evaluated. For the purpose of developing the equations of the nodalpoint unknowns, an individual element is discretised from the assemblage. Withineach element, it is assumed that the dependent variables can be expressed in termsof approximating function (shape functions) by:

( ) ( )g g p gp p t t ,= = N p ( ) ( )c c p cp p t t ,= = N p

( ) ( )tT T t t ,= = N T ( ) ( )ut t .= =u u N u (4.1)

The integral or weak form of the heat and mass transfer equations (and othersrequired to complete the model), was obtained by means of the Galerkin procedure(weighted residuals) and expressed in matrix form as follows:

+ + + + + + + ∞

+ + + + + + +

+ + + + + + +

+ + + +

gg gc gt gu gg g gc c gt gg c

cg cc ct cu cg g cc c ct cg c

tg tc tt tu tg g tc c tt tg c

uu ug uc ut ug c

C p C p C T C u K p K p K T f = 0,

C p C p C T C u K p K p K T f = 0,

C p C p C T C u K p K p K T f = 0,

C u C p C p C T f = 0, (4.2)

The above non-symmetric, non-linear and coupled system of ordinary differential

equations can be written as: ( ) ( ) ( )+ +C x x K x x f x = 0 where

{ }=Tg cx p ,p , T,u and the non-linear (matrix) coefficients C(x), K(x) and f(x)

are obtained by assembling the sub-matrices indicated in (4.2).

5.0 NUMERICAL EXAMPLES

In this particular example, partially saturated flow in deforming porous media isinvestigated under the assumption that, either air remains at atmospheric pressure inthe unsaturated zone, or there is flow of both water and air. For partially saturatedconditions we have one for water and one for air. The equations for the saturation-capillary pressure and relative permeability-saturation relationships as was used byLiakopoulos [13] are valid for saturation S ≥ 0.91 and have in the following form:

cS p= − × 11 2.42791 1.9722 10 (5.1)

( )rlK S= − − 1.01211 2207 1 (5.2)

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER38

The relative permeability of the gas phase was assumed to be as given by Brooksand Corey [14]:

( ) ( )rg e eK S S= − −2 5 31 1 (5.3)

( ) ( )eS S= − −0.2 1 0.2 (5.4)

For numerical purposes, the examples were solved in one-dimensional, unsatur-ated, consolidation problem and compared with a previous solution by Lewis andSchrefler, [5]. The column of soil samples was simulated by 20 eight-nodeisoparametric finite elements of equal size and within 103 nodes as shown in Figure5.1. At the beginning, and besides uniform flow conditions (i.e. unit vertical gradientof the potential and pc = 0 on the top surface), a mechanical equilibrium state wasassumed. The boundary conditions used: for the lateral surface are: qT = 0, uh = 0,where uh is the horizontal displacement of the soil; for the top surface: pg = patm,where patm is the atmospheric pressure, T = 293.15K. For the bottom surface: pg =patm, pc = 0 for t > 0, T = 293.15K, uh = uv = 0, where uv is the vertical displacementsoil.

32

62

82

101 102 103

0.1 m

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����������������������������������������������������������������������������������������

1 m

z

y

Surface

Impermeable

Porous material

Figure 5.1 One-dimensional model and finite element mesh

The first problem example was simulated using two different values of intrinsicpermeability, i.e. K1 = 8.63 × 10–13 m2 and K2 = 9.37 × 10–12 m2. These valuesrepresent the soil permeability for a selected study area at Kg. Puteh wellfield. Theporosity of the soil is estimated as 0.42 and whilst other parameters assumed asfollows:

Young’s modulus E = 1.3 MPa

Poisson’s ratio ν = 0.4

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NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 39

Solid grain density ρs = 2000 kg/m3

Liquid density ρw = 1000 kg/m3

Water viscosity µw = 1 × 10–3 Pas

Air viscosity µg = 1.8 × 10–5 Pas

Gravitational acceleration g = 9.806 m/s2

Atmosphere pressure patm = 101325 Pa

Biot’s constant α = 1

The illustration in Figure 5.2 and 5.3 show no great differences between the tworesults. Figure 5.2 display the results for K1 = 8.63 × 10–13 m2 and porosity = 0.42which illustrates good agreement with previous experimental results of Liakopoulosfor K1 = 4.5 × 10–13 m2 and porosity = 0.2975 as shown in Figure 5.4. There are somedifferences between the K1 and K2 results (Figure 5.2 and 5.3) for gas pressure,capillary pressure and saturation of water, although there are similarities as the pat-

Height of soil sample versus gas pressure for Kg. Puteh w ellf ield problem, w ith k = 8.63 x 10-13 m2 and n = 0.42.

00.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

96000 97000 98000 99000 100000 101000 102000Gas pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus capillary pressure for Kg. Puteh w ellf ield problem, w ith k = 8.63 x 10-13 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0 2000 4000 6000 8000 10000

Capillary pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height soil sample versus vertical displacement for Kg. Puteh w ellf ield problem, w ith k = 8.63 x 10-13 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-0.005 -0.004 -0.003 -0.002 -0.001 0Vertical displacement [m]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus saturation for Kg. Puteh w ellf ield problem, w ith k = 8.63 x 10-13 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0.9 0.92 0.94 0.96 0.98 1 1.02Saturation [-]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

(a) (b)

(c) (d)

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER40

Height of soil sample versus w ater pressure for Kg. Puteh w ellf ield problem, w ith k = 8.63 x 10-13 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-10000 -8000 -6000 -4000 -2000 0Water pressure [Pa]

Hei

ght [

m]

5 min10 min

20 min30 min

60 min120 min

(e)

Figure 5.2 The resulting profiles of (a) gas pressure, (b) capillary pressure, (c) vertical displacement,(d) saturation and (e) water pressure for unsaturated case with K1 = 8.63 × 10–13 m2 andn = 0.42

Height of soil sample versus gas pressure for Kg. Puteh w ellf ield problem, w ith k = 9.37 x 10-12 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

96000 97000 98000 99000 100000 101000 102000Height [m]

Gas

pre

ssur

e [P

a]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus capillary pressure for Kg. Puteh w ellf ield problem, w ith k = 9.37 x 10-12 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0 2000 4000 6000 8000 10000 12000Capillary pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus vertical displacement for Kg. Puteh w ellf ield problem, w ith k = 9.37 x 10-12 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-0.005 -0.004 -0.003 -0.002 -0.001 0

Vertical displacement [m]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus saturation for Kg. Puteh w ellf ield problem, w ith k = 9.37 x 10-12 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0.88 0.9 0.92 0.94 0.96 0.98 1Saturation [-]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

(a) (b)

(c) (d)

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NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 41

(c) (d)

(e)

Figure 5.3 The resulting profiles of (a) gas pressure, (b) capillary pressure, (c) vertical displacement,(d) saturation and (e) water pressure for unsaturated case with K2 = 9.37 × 10–12 m2 andn = 0.42

Height of soil sample versus w ater pressure for Kg. Puteh w ellf ield problem, w ith k = 9.37 x 10-12 m2 and n = 0.42.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-10000 -8000 -6000 -4000 -2000 0

Water pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus gas pressure based on experimental results of Liakopoulos (k = 4.5 x 10-13 m2 and n =0.2975)

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

96000 97000 98000 99000 100000 101000 102000

Gas pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus capillary pressure based on experimental results of Liakopoulos (k = 4.5 x 10-13 m2 and n =0.2975)

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0 2000 4000 6000 8000 10000Capillary pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

(c) (b)

Height of soil sample versus vertical displacement based on experimental

results of Liakopoulos (k = 4.5 x 10-13 m2 and n =0.2975)

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-0.005 -0.004 -0.003 -0.002 -0.001 0Vertical displacement [m]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

Height of soil sample versus saturation based on experimental results of Liakopoulos (k = 4.5 x 10-13 m2 and n =0.2975)

00.10.20.30.40.50.60.70.80.9

1

0.9 0.92 0.94 0.96 0.98 1

Saturation [-]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

(a) (b)

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER42

tern. Meanwhile Figure 5.5 shows the relationships profiles of capillary pressure andsaturation for K1 and K2. Both curves indicate the same patterns for selected abso-lute time. The capillary pressure decreased gradually until water saturation reacheszerto.

The profiles of vertical displacement are shown in Figure 5.6 (a) and (b). Twodifferent sets of Young's modulus: E1 = 1.0 × 103 Pa and E2 = 1.0 × 109 Pa wereselected to test the deformation of the material with respect to the average intrinsicpermeability of K1 and porosity = 0.42.

Height of soil sample versus water pressure based on experimental results of Liakopoulos (k = 4.5 x 10-13 m2 and n =0.2975)

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-10000 -8000 -6000 -4000 -2000 0Water pressure [Pa]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

(e)

Figure 5.4 The resulting profiles of (a) gas pressure, (b) capillary pressure, (c) vertical displace-ment, (d) saturation and (e) water pressure for unsaturated case with K = 4.5 × 10–13 m2

and n = 0.2975 based on experimental results of Liakopoulos

(a) (b)

Figure 5.5 The resulting profiles of capillary pressure versus saturation of water for unsaturatedcase with (a) K1 = 8.63 × 10–13 m2 and n = 0.42 and (b) K2 = 9.37 × 10–12 m2 and n =0.42

Capillary pressure versus saturation for Kg. Puteh w ellf ield problem, w ith k = 8.63 x 10-13 m2 and n = 0.42.

0

1000

2000

3000

4000

5000

6000

7000

8000

9000

10000

0.9 0.92 0.94 0.96 0.98 1Saturation [-]

Cap

illary

pre

ssur

e [P

a] 5 min

10 min

20 min

30 min

60 min

120 min

Capillary pressure versus saturation for Kg. Puteh wellfield problem, with k = 9.37 x 10-12 m2 and n = 0.42.

0

1000

2000

3000

4000

5000

6000

7000

8000

9000

10000

0.88 0.9 0.92 0.94 0.96 0.98 1Saturation [-]

Cap

illary

pre

ssur

e [P

a] 5 min10 min20 min30 min60 min120 min

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NUMERICAL MODELLING OF THERMO-HYDRO-MECHANICAL (THM) 43

Height of soil sample versus vertical displacement for Kg. Puteh wellfield problem, with k = 8.63 x 10-13 m2, n = 0.42 and E = 1.0 x 109 Pa.

00.10.20.30.40.50.60.70.80.9

1

0.00E+00

2.50E-05

5.00E-05

7.50E-05

1.00E-04

1.25E-04

1.50E-04

Vertical displacement [m]

Hei

ght [

m]

5 min10 min20 min30 min

60 min120 min

Height of soil sample versus vertical displacement for Kg. Puteh wellfield problem, with k = 8.63 x 10-13 m2, n = 0.42 and E = 1000 Pa.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

-2 -1.5 -1 -0.5 0Vertical displacement [m]

Hei

ght [

m]

5 min

10 min

20 min

30 min

60 min

120 min

(a) (b)

Figure 5.6: The resulting profiles of height of soil sample versus vertical displacement for (a) K1 =8.63 × 10–13 m2, n = 0.42 and E1 = 1000 Pa and (b) K2 = 8.63 × 10–13 m2, n = 0.42 andE2 = 1.0 × 109 Pa

6.0 CONCLUSIONS

A fully coupled model for simulating heat and mass transfer in deformable porousmaterials involving phase changes phenomena (evaporation, condensation and la-tent heat transfer) has been presented. The model based on a strong physical back-ground clearly identifies that the constitutive equations and other coefficients areneeded to characterize the analyzed medium. The model results in a set of non-linear and coupled partial differential equations. Which are discretized in spaceusing finite element method and finite differences method to solve for the gas pres-sure, pg, capillary pressure, pc temperature T and displacements u as primary vari-ables. Due to the non-linearity of the equations a Newton-Raphson approach wasused for solving the numerical problems. The validity of the approach was verifiedby agreement between the simulation results and experimental data of Liakopoulos,[13]. Further examples showed that the robustness of the model in dealing withvarious problems and the appreciable influences of proper physical modelling withregards to phase changes and realistic boundary conditions affects the evolution ofthe phenomena. The results indicate that the model can be generalised for manyother problems on deforming porous media specifically those concerning thermo-hydro-mechanical in subsurface systems.

REFERENCES[1] Zienkiewicz O. C., Y. M. Xie, B. A. Schrefler, A. Ledesma, N. Bicanic. 1990. Static and Dynamic Behaviour

of Soils: A Rational Approach to Quantitative Solutions, II, Semi-saturated Problems. Proc. R. S. London.A 429: 311 – 321.

[2] Coussy O. 1991. Mecanique des Milieux Poreux. Paris: Editions Technip.

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NORHAN ABD. RAHMAN, SAMIRA ALBATI & BERNHARD A. SCHREFLER44

[3] Abd. Rahman N. and R. W. Lewis. 1999. Finite Element Modelling of Multiphase Immiscible Flow inDeforming Porous Media for Subsurface Systems. Journal of Computers and Geotechnics. Elsevier Science.24(1): 41 – 63.

[4] Schrefler B. A., Zhan Xiaoyang, L. Simoni. 1995. A Coupled Model for Water Flow, Airflow and HeatFlow in Deformable Porous Media. Int. J. Num. Meth. Heat Fluid Flow. 5: 531 – 547.

[5] Lewis R. W. and B. A. Schrefler. 1998. The Finite Element Method in the Static and Dynamic Deformationand Consolidation of Porous Media. New York: John Wiley.

[6] Hassanizadeh M. and W. G. Gray. 1979. General Conservation Equations for Multiphase Systems: 2.Mass, Momenta, Energy and Entropy Equations. Adv. Water Res. 2: 191 – 203.

[7] Chateau X. and L. Dormieux. 2000. The Behaviour of Unsaturated Porous Media in the Light of aMicromechanical Approach. Proceeding of the Asian Conference on Unsaturated Soils Unsat-Asia 2000/Singapore. Rotterdam: A. A. Belkema.

[8] Schrefler B. A. 1999. COMES GEO. Part I: Theoretical Manual & Part II: User Guide. University ofPadua, Italy.

[9] Schrefler B. A. and Zhan Xiaoyang. 1993. A Fully Coupled Model for Water Flow and Airflow inDeformable Porous Media. Water Resources Research. 29: 155 – 67.

[10] Baggio P., C. Bonacina, and M. Strada. 1993. Trasporto di calore e di massa nel calcestruzzo celulare. LaTermotecnica. 45(12): 53 – 60.

[11] Whitaker S. 1977. Simultaneous Heat, Mass and Momentum Transfer in Porous Media: A Theory ofDrying. Advances in Heat Transfer. 13. Academic, New York.

[12] Whitaker S. 1980. Heat and Mass Transfer in Granular Porous Media. Advances in Drying. 1. Hemisphere,New York.

[13] Liakopoulos A. C. 1965. Transient Flow Through Unsaturated Porous Media. Ph. D. Thesis. University ofCalifornia, Berkeley.

[14] Brooks R. N. and A.T. Corey. 1966. Properties of Porous Media Affecting Fluid Flow. J. Irrig. Drain. Div.Am. Soc. Civ. Eng. 92(IR2): 61 – 68.

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