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Page 1: Modelling of Coupling between Mechanics and Water ... · PDF fileModelling of Coupling between ... where ρ is mixture density and is vector of mass flux ... (μw − μp) and thermodynamical

Oil & Gas Science and Technology – Rev. IFP, Vol. 61 (2006), No. 6, pp. 759-764Copyright © 2006, Institut français du pétroleDOI: 10.2516/ogst:2006014

Modelling of Coupling between Mechanics andWater Diffusion in Bonded Assemblies

C. Valançon1, A. Roy2 and J.C. Grandidier1

1 LMPM-UMR 6617 ENSMA, Téléport 2, 1, avenue Clément Ader, B.P. 40109, F-86961 Futuroscope - France

2 CRITT Matériaux, B.P. 115, avenue Marcel Dassault, 17303 Rochefort Cedex - France

e-mail: [email protected] - [email protected] - [email protected]

Résumé — Modélisation du couplage entre la mécanique et la diffusion de l’eau dans lesassemblages collés — Les adhésifs structuraux sont des polymères amorphes exhibant uncomportement viscoélastique. Ces colles étant utilisées dans des conditions très proches de leurtempérature de transition vitreuse, leur comportement est alors piloté par l’évolution du volume libre.Les équations régissant le problème thermo-diffuso-mécanique dérivent des principes fondamentauxde la mécanique des milieux continus et de la thermodynamique des processus irréversibles. Laviscoélasticité et les variations de volume libre seront traitées à l’aide du modèle de viscoélasticiténon linéaire de Knauss et Emri [Polym. Eng. Sci., 27, 86-100]. Les hypothèses de matériau isotrope etde petites déformations seront faites.

Abstract — Modelling of Coupling between Mechanics and Water Diffusion in Bonded Assemblies —Structural adhesives are essentially amorphous polymers exhibiting viscoelastic behaviour. Theseglues are used near their glassy transition temperature. In this temperature range, their behaviour isdriven by free volume evolutions. Equations governing thermo-diffuso-mechanical problem derivefrom the fundamental principles of continuum mechanics and thermodynamics of irreversibleprocesses. Viscoelasticity and free volume variations are treated by the non linear viscoelasticmodelling of Knauss and Emri [Polym. Eng. Sci., 27, 86-100] in an isotropic and small strainframework.

Deformation of Solid PolymersDéformation des polymères solides

D o s s i e r

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Oil & Gas Science and Technology – Rev. IFP, Vol. 61 (2006), No. 6

INTRODUCTION

In several sectors of industry, structural bonding is ofgreat interest. It is more and more used to assemblepieces participating to structural resistance. This processis, for example, widely exploited by nautical sector.Indeed, the bulkheads and the hull of a boat are bondedand the assembly is submitted to many solicitationswhich can be harmful. During its life, a joint must sup-port cycles of mechanical and environmental loadings.Sudden temperature variations but also humidity varia-tions accelerate adhesive aging and reduce its resistance.

In a previous study [1], an assembly bonded joint washeld in water at a temperature near the Tg of the adhesiveand a mechanical load was applied. First, water diffusesthrough free surfaces and interfaces. The adhesive gradu-ally absorbs water and swells until failure occurs. It hasbeen suggested that stress gradient accelerates water dif-fusion but also that diffusion is driven by this gradient.Thus it seems paramount to consider the couplingbetween mechanics and diffusion with the aim of predict-ing assembly bonded joint rupture.

Water presence has already been modelled consideringa diffusion coefficient depending on temperature andwater concentration [2] or on temperature and free vol-ume [3]. These studies are able to give mechanical behav-iour of resins. However, they are unable to describe thecoupling phenomenon shown earlier. To describe com-pletely the problem of water diffusion in an adhesive, onemust elaborate a model considering all phenomena: diffu-sion, thermics and mechanics. In this paper, we present afirst model considering all couplings. These couplingswill be separated here in to two families:

– Couplings refered to as direct, such as the influence ofstress gradient on the diffusion path, thermal dilatationand expansion generated by diffusion on volume strain.

– Couplings refered to as indirect, such as the influenceof absorbed water on creep response taken into accountthrough functions of material parameters such as statevariables and internal variables.

This modelling is essentially phenomenological, but itis based on some physical considerations which areessential. Most adhesives used in industry are thermoset-ting amorphous polymers. Generally, they are used in thevicinity of their glassy transition temperature. Theirbehaviour is then driven by the free volume [4]. In the lit-erature, it is proposed that this free volume is sensitive totemperature, mechanical solicitations and water absorbedby the material [5]. On these physical assumptions, weintroduce indirect couplings in the formulation. Free vol-ume evolution influences viscous behaviour of polymerin modifying relaxation times. Water and polymer areconsidered as a perfect and homogeneous mixture [6]. To

describe direct couplings, the model is built in the frame-work of thermodynamics of irreversible processes [7].

This article presents balance equations and a “diffuso-thermo-mechanical” constitutive law, describing princi-pally the behaviour of bonded joints of thermosettingresins on a moist environment. First numerical results onthe structural relaxation will be compared to literaturedata.

1 BALANCE EQUATIONS

1.1 Mass Balance

Consider a polymer absorbing water. These two speciesform a perfect, homogeneous and continuous mixture [6]where chemical reactions are neglected. The followingrelationship is then respected:

Yw + Yp = 1 (1)where Yw and Yp are respectively specific fraction of waterand polymer. Equations will in the following be expressedonly as a function of water fraction. Polymer behaviourcan then be deduced through Equation (1). Studied materi-als are rather sensitive to hydrolysis phenomena.Nevertheless, to simplify the problem, we assume there isno chemical reaction between water and polymer.

Consider a representative volume of this mixture. Themass contained in this volume varies only by matter trans-fer through its walls. This phenomenon is described by theequation of mass balance:

(2)

where ρ is mixture density and is vector of mass fluxrelating to water. In the following, we use the notation ‘ . ’for all time derivatives.

1.2 Momentum Balance

Balance equations derived from fundamental principle ofmechanics are written in their local form:

(3)

where is stress tensor of Cauchy applied to the mixture,represents specific density of forces exerted identically oneach volume point. Adhesive ageing is our primary interesthere. Therefore, acceleration exerted on each particle ofthe mixture is neglected.

1.3 Energy Conservation – First Principle

Total energy conservation of the volume (first principle ofthermodynamics) is expressed classically in its local form by:

σ

div f� �� �� �

σ ρ ργ+ =

J mw� ��� ρ

�� ���

Y div Jw mw= −

760

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C Valançon et al. / Modelling of Coupling Between Mechanics and Water Diffusion in Bonded Assemblies

(4)

where u is specific internal energy of the mixture,

linearised strain tensor, heat flux vector relating toheat given by conduction and r volume density of heat dueto external sources.

1.4 Second Principle of Thermodynamics

The main point in this modelling is to introduce and define aset of internal variables. First, it seems important to note that,after a fast quench below Tg, when temperature equilibrium isreached, material volume evolves slowly towards its stablestate [8]. The same phenomenon is found when pressure isconsidered. An isopiestic volume evolution is found [4]. Thisis the consequence of free volume relaxation. One can thenextend structural relaxation to water diffusion. More precisely,a sudden jump in water concentration below Tg takes thematerial out of equilibrium. When macroscopic equilibrium isreached and maintained, the material continues to evolvetowards a stable state. Relaxation of each process is treatedthrough distinct internal variables characterising the evolutionof all the different microscopic processes. For homogeneity innotations, mathematical representation of internal variables ischosen with respect to the corresponding state variables.

Most adhesives used for structural bonding are amor-phous polymers cross-linking under ambient conditions. Atambient temperature, adhesives can be in a temperaturerange near their glassy transition temperature. In thisrange, molecular mobility is making easier by free volumepresence. This latter is a direct function of hydrostaticpressure. Consequently, volume and deviatoric effectsmust be differentiated. These are taken into account considering separately the hydrostatic part (tr ) and thedeviatoric part ( ) of the stress tensor. Thus, by mathematical coherence, strain tensor and internal variables tensor aredecomposed into their traces (tr and ztrε) and their deviators

( and ). For temperature and diffusion phenomena,scalar internal variables are introduced, respectively zT andzc. This choice of separating internal variables means that, whenwater diffusion in the material occurs, physical mechanisms tak-ing place are different from those acting due to mechanical load-ing. This decision can be questioned because in the material, it ismolecular mobility which is the main microscopic mecha-nism. Nevertheless, diffusion phenomenon refers to chemicalconsiderations which have another origin than “crank” mech-anisms (see below for a discussion of “crank” mechanisms).Internal variables introduced here allow us to quantify thedeviation from a diffuso-thermo mechanical equilibrium state.Out theoretical framework is the thermodynamics of irre-versible processes [7] where one considers a medium whichis open and in course of evolution. Based on the second

principle, intensive variables (internal energy u, entropy s,stress tensor of Cauchy , difference of chemical potentialsΔμ = (μw − μp) and thermodynamical affinities associatedwith each elementary process ATj, Acj, Atrεj and ) arerelated to their respective extensive variables (temperatureT, linearised strain tensor , specific fraction of water Yw

and introduced internal variables zTj, zcj, ztrεj and ).

(5)

One distinguishes two contributions in entropy variation:one giving by exchanges with the exterior s·e and anotherdue to internal sources s·i such as: ρs· = ρs·e + ρs·i with s·i ≥ 0.

The variation of internal entropy defines volume dissi-pation ϕ via Equation (6):

(6)

where is vector of entropy flux which is related to heat

flux vector by . Total volumedissipation is divided into three contributions: ϕ1 representingdissipation due to internal processes, ϕ2 volume dissipationdue to thermics and ϕ3 giving by diffusive phenomenon.

(7)

(8)

(9)

2 CONSTITUTIVE EQUATIONS

2.1 Complementary Laws of Evolution

For the sake of simplicity, the principle of Curie is applied.Only a partial coupling is then envisaged for establishingcomplementary laws of evolution (i.e. only couplingbetween diffusive and thermal phenomenon is considered).Direct coupling relating vectors of specific flux of waterand entropy flux to gradients of temperature and differenceof chemical potentials are presented in the following clas-sical form:

(10) J k gradT c grads T

T

��� � ���� � ����= ⋅ + ⋅[ ] [ ]

μμΔ

ϕ μ3 = − ⋅J gradmw� ��� � ����

Δ

ϕ2 = − ⋅J gradTs��� � ����

ϕ ρ ρ ρε ε1

1 1

= + += =

∑ ∑A z A z A ztr j tr j

j

nej ej

j

kTj T� � �: jj

j

ncj cj

j

n

A z= =

∑ ∑+1 1

ρ �

ρ ρ ρ ρε εT s A z A z A zitr j tr j ej ej Tj Tj

j

n

j

� � � �= + +=

∑:1=== =

∑∑ ∑+

− ⋅ −

11 1

k

j

ncj cj

j

n

s

A z

J gradT

ρ �

��� � �����JJ gradmw� ��� � �����

⋅ ≥Δμ 0

T s u tr tr s e Y

A z

w

tr j tr

� � � �

= − − −

+

1 1

ρσ ε

ρμ

ε ε

( )( ) : Δ

jj

j

nej ej

j

kTj Tj cj cj

j

n

j

A z A z A z+ + += = =

∑ ∑ ∑1 1 1

: � � �==

∑1

n

ejz ε

ejA

σ

zee

ε

ε

ρ σ ε�� ��

u div J rq= − +:

761

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Oil & Gas Science and Technology – Rev. IFP, Vol. 61 (2006), No. 6

(11)

where , and are coupling coefficients of

Onsager.Concerning internal variables, they translate viscoelastic

characteristics of amorphous polymers. As has often beenemphasized before, adhesives are used in a temperaturerange near their glassy transition temperature. In thisrange, polymers behaviour is driven by free volume. Thelatter influences relaxation times in the matter. In the nonlinear viscoelastic model realised by Knauss and Emri [5],evolution laws of relaxation times are proposed and seemto be efficient. Based on these developments we propose afamily of evolution laws of internal variables. These lawsgeneralize the model of Knauss and give a thermodynami-cal justification based on mechanics to extend this conceptto a case of diffusion, thermics and mechanics:

(12)

(13)

(14)

(15)

where indices ∞ and j refer respectively to equilibriumstate and different state in the course of evolution,

τ is characteristic relaxation time at each internal state, a is time shift function,

αTj coefficient of thermal dilation,

αcj coefficient of dilation produced by solvent diffusion,

To is initial temperature, kj is bulk modulus of the j-th internal state,

Cpj specific heat of the j-th internal state,

dTj diffusion coefficient relating to thermics,

dcj diffusion coefficient relating only to water presence

in the polymer.

From internal point of view, one knows that molecularsegments move essentially by jumps called “cranks”. Fora jump to take place, the intermolecular space, named alsofree volume, must be sufficient. Jump activation is gener-ally the result of thermal vibrations. Imagine now thatinternal variable zT represents the thermal vibration of amolecular jump, Equation (13) tells us that this vibrationdepends on a thermal part necessary to reach an equilib-rium state but is also disrupted by relaxation phenomenonprovided by mechanical and diffusive loadings. Internalvariables relating to mechanics must be associated to freevolume fraction or excess of entropy. The evolution ofthis latter is indeed the consequence of internal relax-ations. When macroscopic equilibrium is reached, thematerial continues to evolve. Equation (12) describes thisphenomenon.

2.2 Relaxed State

The evolutions of dissipative internal processes can beunderstood by the differential equations presented above.Internal variables translating the deviation from equilib-rium tend to this state when they are not excited.Equilibrium definition is not easy because it is hypotheti-cal. Relaxation times of considered materials can be suchthat the relaxed state is reached in a time scale above rea-sonable experimental time scale. In a first approach, wehave chosen tangential linear laws for each family of inter-nal variables.

(16)

where coefficients β are rigidities of relaxed state.

2.3 State Laws

The thermodynamical potential chosen to define state lawsis specific free energy. This is taken as a simple quadraticand isotropic function of macroscopic data and internalvariables. One presents only state laws, which are thederivatives of the thermodynamical potential, introducingthe rigidities of relaxed states by the use of the equilibriumdefinition of internal variables (16). Coupling betweeneach phenomenon is taken into account in a relatively com-plete manner. However, indirect coupling of constitutivelaws is done through free volume. Its evolution is essen-tially influenced by volume changes. In this framework,we have chosen not to describe direct coupling betweenshear behaviour and others phenomena. On the other hand,relaxation times in shear are affected by these latter. Onlyconstitutive laws concerning stresses and chemical poten-tials are presented.

dz d tr dz dT

dz dY

tr j tr j Tj Tj

cj cj

∞ ∞

= = −

= −

ε εβ ε β

β

( )ww ej ejdz de

∞= β

�z

a tr T Yz zej

shearej ej w

ej ej= − −( )∞

1

τ ε( , , )

�za tr T Y

z zd

cj

volumecj cj w

cj cj j

= − ×

−( ) +∞

1

τ ε( , , )TT

jc

Tj Tj j jc

jc

tr j tr j

dz z

k

dz z−( ) + −( )⎧

⎨⎪

⎩⎪∞ ∞

α ε ε ⎫⎫⎬⎪

⎭⎪

�za tr T Y

z zT

Tj

volumeTj Tj w

Tj Tj o

= − ×

−( ) +∞

1

τ ε( , , )

kk

Cz z

T k

Cz zj j

T

jp

tr j tr j o j jc

jp

cj cαρ

αρ

ε ε−( ) + −∞ ∞jj( )⎧

⎨⎪

⎩⎪

⎫⎬⎪

⎭⎪

�za tr T Y

z z

tr j

volumetr j tr w

tr j

j

εε ε

ε

τ ε= − ×

1

( , , )

∞∞ ∞ ∞( ) + −( ) + −( ){ }tr jjT Tj Tj

jc cj cjz z z zε α α

J k grad c gradTmw

T

� ��� � ���� � ����= ⋅ + ⋅

μ μμ[ ] [ ]Δ

762

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C Valançon et al. / Modelling of Coupling Between Mechanics and Water Diffusion in Bonded Assemblies

(17)

(18)

(19)

where and are shear moduli respectively of equi-

librium state and j-th state in course of evolution.

One notes that, in the expression for stress, usual termsare found such as strain and temperature but now diffu-sion occurs through specific inclusion of the fraction ofwater and diffusion processes in the course of evolution.One finds also the fact that the material changes instanta-neously in volume but also with retardation effects. In thesame way, the difference of chemical potentials whichrepresents the driving force for diffusion depends on thequantity of absorbed water but also on the repercussionsof mechanics and thermics on rearrangement of molecu-lar segments.

2.4 Equation of Diffusion

Finally, in considering Equations (2), (11) and (19) thevector of specific flux of water is presented in the follow-ing form:

(20)

where se is water solubility and c is water concentration.

The first term of specific flux matches the classical lawof Fick. The second term is not classical but correspondsto internal phenomenon of relaxation relating to water dif-fusion. The third and fourth terms represent the influenceof material volume variation on flux of mass. More pre-cisely, these terms represent the effect of spatial reparti-

tion of hydrostatic stress (bulk modulus in product withvolume strain) on the diffusion and on the direction of dif-fusion. This permits to explain through couplings theobservations of Roy et al. [1], which suggest that stressgradient accelerates water diffusion but also that diffusionis driven by this gradient. The fourth term represents thevolume relaxation effect producing by mechanics on spe-cific flux. In the same way, the last terms of the specificflux translate the effect of thermal gradient on the diffu-sion path. It is clearly established that temperature influ-ences diffusion kinetics. Nevertheless, here, it is the tem-perature gradient which directly influences diffusion path.This point needs thus to be verified experimentally.

Following observations made during earlier works [1],one can hope that this modelling contains all ingredientsto represent quantitatively experimental phenomenon.

3 NUMERICAL RESULTS

To first improve this modelling, a software has been devel-oped in Fortran and only considering the constitutive lawsfor the stress (17, 18). Therefore, numerical test can beonly about volume variations and the phenomenon ofstructural relaxation is chosen. More precisely, the relax-ation after relative humidity jumps is studied and com-pared to the experimental results of Zheng and McKenna[9]. Specimens used in their experiments are epoxy mem-branes which are put in a controlled humidity room at aconstant temperature. Jumps are done from a relativehumidity (90%) above RHg (60%) to relative humiditybelow (reported in Fig. 1) at a rate of 1.5%/min. In Figure 1is represented the evolution of the departure δ from theequilibrium during the soaking. This quantity is defined asfollows:

(21)

and in the presented model as a function of tr :

(22)with

where V denotes the specific volume, V∞ the equilibriumvolume and RH the relative humidity rate.

A comparison between numerical results and literature data[9] is illustrated in Figure 1. First, the model gives a goodapproximation of the phenomenon of the structural relaxationprovoked by a RH-jump. The departure at the beginning ofthe soaking is not very well estimate and the evolution of thevolume for the smallest jump is overestimated. Nevertheless,these results show the ability of the presented model to repre-sent physical phenomenon such as structural relaxation. Othersimulations must be realised to validate the model entirely.

ε α∞ = ± ∞tr RH RHc( , ) Δ

δ ε ε= − ∞tr RH t tr RH( , ) ( , )

ε

δ = − ∞

V V

V

J k d s gradc d grmw c e cjjc

� ��� � �����= − −∞μ ρ

β[ (1

106 aad z z

k grad tr

cj cj

j

n

c

� �����

� �����

−( )

∞=

∞ ∞

∑1

α ( εε β α

β

ε ε) − −( )

=∞∑ cj

j jc

j

ntr j tr jk grad z z

� �����

1

ccjjT

j

nTj Tj

Td grad z z c

k d� �����

=∞

∞∑ −( ) + −1

)] (μ

μTT

gradTρ

)[ ]−� �����

ρ μ α ε

β

Δ = −( ) − ( ) − −( )

∞ ∞ ∞ ∞d Y Y k tr d T T

d

c wow c T

o

cj cj zz z k z zcj cj

j

ncj

j jc tr j tr j

j

n

−( ) − −( )∞=

∞=

∑1 1

β α ε ε∑∑

∑− −( )∞=

βcj Tj Tj Tj

j

n

d z z1

s G e G z zej

j

k

jej ej= ∗ − −( )∞

=∞∑2 2

1

: :β

tr k tr k T T k Y Y

k

To

c wow

tr jj

σ ε α α

β ε

= − − − −

∞ ∞ ∞ ∞ ∞( ) ( )

(( ) ( )z z k z ztr j tr j

j

ntr j

j jT Tj Tj

j

ε ε εβ α− + −∞=

∞=

∑1 11

1

n

tr jj j

c cj cj

j

n

k z z

∑+ − ∞=

β αε ( )

763

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Oil & Gas Science and Technology – Rev. IFP, Vol. 61 (2006), No. 6

CONCLUSION

In this article, the main equations of a model considering athermo-diffuso-mechanical coupling have been developed.This latter has essentially been built for describing thebehaviour of thermosetting amorphous polymers, and moreprecisely structural adhesive. A first comparison betweennumerical results and experimental results of literature hasbeen presented and gives a good fit, but other investiga-

tions must be done to validate this model. One can imaginethat the application range can be expanded to all amor-phous polymers and to several species in diffusion.

REFERENCES

1 Roy, A., Gontcharova-Bénard, E., Gacougnolle, J.-L. andDavies, P. (2000) Hygrothermal effects on failure mechanismsof composite/steel bonded joints, in Time dependent and non-linear effects in polymers and composites, ASTM STP 1357,Schapery, R.A. and Sun, C.T. (Eds.), American society fortesting and materials, West Conshohocken, PA.

2 Weitsman, Y. (1990) A Continuum diffusion model forviscoelastic materials., J. Phys. Chem., 94, 961-968.

3 Roy, S. and Reddy, J.N. (1988) A finite element analysis ofadhesively bonded composite joints with moisture diffusionand delayed failure, Comput. Struct., 29, 1011-1031.

4 Kovacs, A.J. (1966) Applicability of the free volume concepton relaxation phenomena in the glass transition range, Rheol.Acta, 5, 262-269.

5 Knauss, W.G. and Emri, I. (1987) Volume change and thenonlinearity thermo-viscoelastic constitution of polymers,Polym. Eng. Sci., 27, 86-100.

6 Müller, I. (1975) Thermodynamics of mixtures of fluids,J. Mécanique, 14, 268-303.

7 Münster, A. (1966) Thermodynamique des processusirréversibles, Bibliothèque des Sciences et TechniquesNucléaires.

8 Kovacs, A.J. (1958) La contraction isotherme du volume despolymères amorphes, J. Polym. Sci., 30, 131-147.

9 Zheng, Y. and McKenna, G.B. (2003), Structural recovery in amodel epoxy: Comparison of responses after temperature andrelative humidity jumps, Macromolecules, 36, 1164-1169.

Final Manuscript received in October 2006

764

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Figure 1

Comparison between numerical results and experiments ofZheng and McKenna [9].

RH = 60%RH = 50%RH = 40%RH = 30%Numerical results

2.5

2.0

1.5

1.0

0.5

δ x

1000

0100 1000 10 000 100 000

(t-ti) (s)1000 000