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Study of heat and mass transport in

temperature-dependent-viscous fluid under gravity modulation

B.S. Bhadauria

a

and P. Kiran

b,∗

a,bDepartment of Applied Mathematics, School for Physical Sciences, Babasaheb Bhimrao Ambedkar University, Lucknow, India.

Abstract

In this paper, we study the thermosolutal convection in a horizontal temperature dependent viscous fluid layer. The considered gravity field consists of two parts: a steady part and a time-dependent periodic part that oscillates with time. The time periodic gravity modulation, can be realized by vertically oscillating the fluid layer. A weak non-linear stability analysis has been performed by using power series expansion in terms of the amplitude of gravity modulation, which is assumed to be small. The Nusselt and Sherwood numbers have been obtained in terms of the amplitude of convection which is governed by the non-autonomous Ginzburg-Landau equation derived for the stationary mode of convection. Effects of various parameters such as frequency and amplitude of modulation, Prandtl number, diffusivity ratio and solute Rayleigh number, have been analyzed on heat and mass transfer. It is found that heat and mass transport can be controlled by suitably adjusting the external parameters of the system. It is also found that the thermo-rheological parameter is to destabilize the system.

Keywords: Heat and mass transfer, Ginzburg-Landau equation, Temperature-dependant viscosity, Gravity modulation.

2010 MSC:34B18, 39A13. 2012 MJM. All rights reserved.c

1

Introduction

Double diffusive convection is an important fluid dynamics phenomenon. It is a type of instability that occurs in a fluid that possesses two opposing density altering components with differing molecular diffusivity, such as heat and salt or any two solute concentrations. The marked difference between single and double dif-fusive systems lies in the verity that in double difdif-fusive systems convection can occur even when the system is hydrostatically stable if the diffusivities of the two diffusing fields are widely different. The study of the double diffusive convection has received much attention over the years due to its numerous fundamental and industrial applications. Some examples of double diffusive convection can be found in oceanography Stommel [1], lakes and under ground water, atmospheric pollution, chemical processes, laboratory experiments, modeling of solar ponds, astrophysics, geophysics, geology and engineering Chen and Johnson [2], magma chambers and sparks, formation of microstructure during the cooling of molten metals, fluid flows around shrouded heat-dissipation fins, migration of moisture through air contained in fibrous insulations, grain storage system, the dispersion of contaminants through water saturated soil, crystal growth, solidification of binary mixtures, and the under-ground disposal of nuclear wastes. The early work on this problem is summarized in several reviews Turner [3], Turner and Chen [4], Huppert and Turner [5], Bhadauria [6].

Stommel et al. [1] were the first to notice some properties of double diffusive convection with the discovery of the phenomenon of the salt fountain, which occurs when hot salty water lies above cold fresh

Corresponding author.

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water. Such a system was later analyzed by Stern [7], who noted the general properties of the motion now commonly known as salt fingers. The situation with reversed gradients has been studied by Veronis [8], and stability criteria for horizontal boundaries of various kinds have been presented by Nield [9] by means of a linear stability analysis. Lortz [10] studied the effect of magnetic field on double-diffusive convection. His object was to clarify some of the mathematical aspects of stability criterion (Malkus and Veronis [11]) but, his analysis is silent about the detailed study of stability analysis. Considering linear gradients, Baines and Gill [12] investigated the thermohaline convection in a fluid layer confined between two horizontal boundaries, which are dynamically free and conducting to both heat and salt. Chen [13] considered a two-dimensional problem of a linearly stratified salt solution contained between two infinite vertical plates, and studied the onset of cellular convection due to a lateral temperature gradient. Proctor [14] studied the thermohaline con-vection in a horizontal fluid layer using rigid-rigid and free-free boundaries. Double diffusive concon-vection in an inclined plane was investigated by Thangam et al. [15] for rigid-rigid boundaries. Later on many other inves-tigators studied this problem of double diffusive convection under various physical and boundary conditions. Sodha and Kumar [16] studied the stability of double diffusive convection in solar ponds with non-constant temperature and salinity gradients. Using linear stability analysis, Saunders et al. [17] studied the effect of gravity modulation on thermosolutal convection in an infinite layer of fluid using free-free boundaries. Gobin and Bennacer [18] investigated the problem of thermohaline convection in a vertical layer of a binary fluid, and studied the onset of convection. Sezai and Mohamad [19] have performed a three-dimensional numerical study to investigate double diffusive, natural convection in a cubic enclosure subject to opposing and horizontal gradients of heat and solute imposed along the two vertical side walls. Ryskin et al. [20] have studied thermod-iffusive convection in ferrofluids. Bajaj [21] considered the thermosolutal magnetic convection in an infinite layer of ferrofluid heated from below, in the presence of vertical magnetic field and the vertical acceleration is modulated by two-frequency modulation. Bhadauria [6] analyzed this problem by considering rigid boundaries under temperature modulation. Starchenko [22] discussed double diffusion magneto-convection for Earths type planets. Siddheshwar et al. [23] performed a local non-linear stability analysis of Rayleigh−B´enard magneto-convection using Ginzburg-Landau equation. Magnetohydrodynamic natural magneto-convection boundary layer flow of an electrically conducting and viscous incompressible fluid along a heated vertical flat plate with uniform heat and mass flux in the presence of strong cross magnetic field has been investigated by Sadia [24].

The classical Rayleigh-B´enard convection due to bottom heating is well known and highly explored phenomenon given by Chandrasekhar [25], Drazin and Reid [26]. Gershuni and Zhukhovitskii [27] and Gresho and Sani [28] were the first to study the effect of gravity modulation in a fluid layer. Biringen and Peltier [29] investigated, numerically, the non-linear three dimensional Rayleigh-B´enard problem under gravity modulation, and confirmed the result of Gresho and Sani [28]. Wadih and Roux [30] presented a study on instability of the convection in an infinitely long cylinder with gravity modulation oscillating along the vertical axis. Saunders et al. [17] have discussed the effect of gravity modulation on thermosolutal convection in an infinite layer of fluid. Clever et al. [31] performed a detailed non-linear analysis of Rayleigh−B´enard convection under g-jitter and presented the stability limits to a much wider region of parameter space. Chen and Chen [32] have studied the effect of gravity modulation on the stability of convection in a vertical slot. They have examined the stability for fluids of different Prandtl numbers. Rogers et al. [33] have observed superlattice patterns in vertically oscillated Rayleigh B´enard convection. Rogers et al. [34], Bhadauria et al. [35] showed that the gravitational modulation, which can be realized by vertically oscillating a horizontal liquid layer, acts on the entire volume of liquid and may have a stabilizing or destabilizing effect depending on the amplitude and frequency of the forcing. Shu et al [36] examined the effects of modulation of gravity and thermal gradients on natural convection in a cavity, numerically as well as experimentally. They found that for low Prandtl number fluids, modulations in gravity and temperature produce the same flow field both in structure and in magnitude. Boulal et al. [37] focused attention on the influence of a quasi-periodic gravitational modulation on the convective instability threshold. They predicted that the threshold of convection corresponds precisely to quasi-periodic solutions. Bhadauria et al. [38] studied thermally or gravity modulated non-linear stability problem in a rotating viscous fluid layer, using Ginzburg-Landau equation for stationary mode of convection. Bhadauria et al. [39] studied internal heating effects on weak non-linear Rayleigh−B´enard convection under gravity modulated, using Ginzburg-Landau equation for stationary mode of convection.

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problems of convective flow, viscosity of many fluids varies with temperature. Therefore, the results drawn from the flow of fluids with constant viscosity are not applicable for the fluid that flows with temperature dependent viscosity, particularly at high temperature. The fluids that flow with variable viscosity are useful in chemical, bio-chemical and process industries as well as in physics of fluid flows, wherein the flow of fluids is governed by different temperatures. Therefore, objective of our study is to investigate the effect of gravity modulation on double diffusive convection in a horizontal temperature dependant fluid layer.

2

Governing Equations

We consider an infinite horizontal layer of temperature dependent viscous fluid mixture subjected to a vertical gravity field, confined between two free-free boundaries at z = 0 andz =d. To maintain a constant temperature difference ∆T and a constant solutal difference ∆S, across the layer, the layer is heated and salted from below. A Cartesian frame of reference is chosen with origin in the lower boundary and the z-axis vertically which is given in Fig.1. given bellow.

The fluid layer is considered to be Boussinesq, and thus the basic governing equations are

∇.~q = 0, (2.1)

ρ0

∂~q

∂t + (~q.∇)~q

= −∇p+ρ~g(t)k~+µ(T)∇2~q, (2.2)

γ∂T

∂t + (~q.∇)T = κT∇

2T, (2.3)

∂S

∂t + (~q.∇)S = κS∇

2S, (2.4)

~g(t) = g0

1 +2δcos(Ωt)~k, (2.5)

ρ = ρ0[1−βT(T−T0) +βS(S−S0)], (2.6)

µ(T) = µ0

1 +2δ

0(T−T0)

, (2.7)

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The thermo-rheological relationship in Eq.(2.7) is guided by Nield[9]. The thermal boundary conditions are

T =T0+ ∆T at z= 0 T =T0 at z=d. (2.8)

Since an uniform concentration gradient∆dS, has been maintained between the walls of the liquid layer, therefore the boundary conditions onS are

S=S0+ ∆S atz= 0 S=S0 atz=d. (2.9)

The basic state of liquid is quiescent and given by

~

qb = 0, p=pb(z), T =Tb(z), S=Sb(z), ρ=ρb(z). (2.10)

The basic state temperatures and concentration satisfy the equations

d2S

b

dz2 = 0,

d2T

b

dz2 = 0. (2.11)

The conduction state solutions of the Eq.(2.11), subject to the boundary conditions Eqs.(2.8-2.9) are given by

Sb(z) =S0+ ∆S

1−z

d

, (2.12)

Tb(z) =T0+ ∆T

1−z

d

. (2.13)

We assume finite amplitude perturbations to the basic state in the form

~

q=~qb+~q

0

, T =Tb+T

0

, S=Sb+S

0

, p=pb+p0, ρ=ρb+ρ0. (2.14)

Substituting Eq.(2.14) in the set of Eqs.(2.1)-(2.7), we get the following equations

∇.~q0

= 0, (2.15)

ρ0

∂ ~q0

∂t + ( ~ q0

.∇)q~0

!

= −∇p0+ρ0~g(t)~k+µ(T)∇2q~0

, (2.16) γ∂T 0 ∂t + ~ q0

.∇T0+w0∂Tb

∂z = κT∇

2T0, (2.17)

φ∂S

0

∂t +

~

q0

.∇S0+w0dSb

dz = κS∇

2S0

, (2.18)

ρ0 = −ρ0

h βTT

0 −βSS

0i

. (2.19)

We consider only two-dimensional disturbances in our study, and hence the stream functionψis introduced as

u0 =∂ψ

∂z, w

0=∂ψ

∂x. (2.20)

By operating curl twice on Eq.(2.16), we eliminatep0 from it, and use Eq.(2.19) to eliminateρ0, and then render the resulting equation and Eqs.(2.17), (2.18) and (2.20) dimensionless using the following transformations

ψ=κTψ∗,(x, y, z) =d(x∗, y∗, z∗), T = ∆T T∗, S= ∆S S∗, t= d 2 κTt

.

We obtain the non-dimensional governing equations in the form (on dropping the asterisks for simplicity)

1

P r ∂ ∂t(∇

2ψ) 1

P r

∂(ψ,∇2ψ)

∂(x, z) = µ(T)(∇

4ψ) +∂µ

∂z

∂(∇2ψ)

∂z −RaT(1 +gm) ∂T ∂x

+RaS(1 +gm)

∂S

∂x, (2.21)

∂ψ

∂x − ∇

2T = ∂T

∂t +

∂(ψ, T)

∂(x, z), (2.22)

∂S

∂x −

1

Le∇

2S =

−∂S

∂t +

∂(ψ, S)

(5)

where gm=2cos(Ωt) andµ(T) = 1+12V T, 2 is a small quantity which indicates that the viscosity variation with temperature is weak, V is the temperature dependent viscosity. The non-dimensionalized parameters in the above equations are P r = ν

κT is the Prandtl number, RaT =

βTg∆T d3

νκT is the thermal Rayleigh number,

RaS =βSg∆Sd 3

νκT is the solute Rayleigh number, and Le= κT

κS is the Lewis number.

To keep the time variation slow, we have re-scaled the timetby using the time scaleτ =2t. Now, to study

the stationary mode of double-diffusive convection, we write the above non-linear system Eqs.(2.21)-(2.23) into the matrix form

  

−µ(T)∇4 Ra

T∂x∂ −RaS∂x

∂x −∇

2 0

∂x 0 −

1 Le∇ 2         ψ T S     =        

−2 P r

∂ ∂τ(∇

2ψ) +∂µ(T)

∂z ∂ψ ∂z

−gm(RaT∂T∂x −RaS∂S∂x) +P r1 ∂(ψ,∇ 2ψ) ∂(x,z)

−2∂T ∂τ +

∂(ψ,T)

∂(x,z)

−2∂S ∂τ +

∂(ψ,S)

∂(x,z)

        . (2.24)

We solve Eq.(2.24) by using µ=µ(Tb) guided by Nield[9] and considering free-free, isothermal and isohaline boundary conditions as given bellow

ψ= 0 =∇2ψ, T =S= 1 on z=0,

ψ= 0 =∇2ψ, T =S= 0 on z=1, (2.25)

3

Heat and mass transport for stationary instability

To solve the system (2.24), we introduce the following asymptotic expansion

RaT =R0c+2R2+4R4+..., (3.26)

ψ=ψ1+2ψ2+3ψ3+..., (3.27)

T =T1+2T2+3T3+..., (3.28)

S=S1+2S2+3S3+..., (3.29)

where R0c is the critical value of the Rayleigh number at which the onset of convection takes place in the absence of temperature modulation.

At the lowest order, we have

−∇4 R

0c∂x∂ −RaS∂x∂ ∂

∂x −∇

2 0

∂x 0 −

1 Le∇ 2     ψ1 T1 S1  =   0 0 0 

. (3.30)

The solution of the lowest order system is

ψ1 = Asin (kcx) sin (πz),

T1 = −

kc

α2Acos (kcx) sin (πz),

S1 = −

kcLe

α2 Acos (kcx) sin (πz). (3.31)

whereα2=k2

c+π2. The system (2.24) gives us the critical value of the Rayleigh number and the corresponding wave number for the onset of stationary convection

R0c=

α6+ Ra

SLekc2

k2

c

(6)

kc=

π

2. (3.32)

which are the results given by Chandrasekhar [25].

At the second orderwe have

−∇4 R

0c∂x∂ −RaS∂x∂ ∂

∂x −∇

2 0

∂x 0 −

1 Le∇ 2     ψ2 T2 S2  =   R21 R22 R23   (3.33) where

R21 = 0, (3.34)

R22 =

∂ψ1 ∂x ∂T1 ∂z − ∂ψ1 ∂z ∂T1

∂x, (3.35)

R23 =

∂ψ1 ∂x ∂S1 ∂z − ∂ψ1 ∂z ∂S1

∂x . (3.36)

The second order solution can be obtained as follows

ψ2 = 0, (3.37)

T2 = −

k2cA2

8πα2sin (2πz), (3.38)

S2 = −

k2

cLe2A2

8πα2 sin (2πz). (3.39)

The horizontally-averaged Nusselt number, N u, and Sherwood number, Sh, for the stationary mode of double-diffusive convection (the preferred mode in this problem) are given by

N u(τ) = 1 +

" kc 2π R 2π kc 0 ∂T2 ∂z dx # z=0 " kc 2π R 2π kc 0 ∂Tb ∂z dx # z=0 ,

Sh(τ) = 1 +

" kc 2π R 2π kc 0 ∂S2 ∂z dx # z=0 " kc 2π R 2π kc 0 ∂Sb ∂z dx # z=0 ,

N u(τ) = 1 + k

2

c

4α2[A(τ)] 2

, (3.40)

Sh(τ) = 1 +k

2

cLe2 4α2 [A(τ)]

2

. (3.41)

At the third order, we have

−∇4 R

0c∂x∂ −RaS∂x∂ ∂

∂x −∇

2 0

∂x 0 −

1 Le∇ 2     ψ3 T3 S3  =   R31 R32 R33 

, (3.42)

R31 = −

1

P r ∂ ∂τ(∇

2ψ

1)−V Tb(∇2ψ1) +V

∂ ∂z(∇

2ψ

1)−(R0c(2V Tb+gm) +R2)

∂T1

∂x

+RaS(2V Tb+gm)

∂S1

∂x ,

R32 =

∂ψ1 ∂x ∂T2 ∂z − ∂T1 ∂τ ,

R33 =

(7)

Using first and second order solutions we can easily obtain the expression forR31-R33.Now applying solvability

condition for the existence of third order solution, we obtain the Ginzburg-Landau equation for stationary convection with time periodic coefficients in the form

A1

dA(τ)

dτ =A2A(τ)−A3A

3(τ), (3.43)

where

A1=

h

α2 P r+

R0kc2 α4 −

RaSk2cLe2 α4

i ,

A2=

k2 c α2

h

R2+V R0c−V α 4 k2

c −RaSV Le+δcos(Ωτ)(R0c−RaSLe)

i ,

A3=

k4 c

8α4

R0c−RaSLe3

.

The solution of Eq.(3.43), subject to the initial condition A(0) =a0, where a0is a chosen initial amplitude of

convection, can be obtained by using NDSolve, Mathematica 8. In calculations we may assume R2 =R0c, to keep the parameters to the minimum.

4

Analytical solution for Unmodulated case

In the case of unmodulated fluid layer, the above Ginzburg-Landau equation can be written as

A1A0u(τ)−A2Au(τ) +A3Au(τ)3= 0, (4.44)

whereAu(τ) is an amplitude of convection for unmodulated case andA1, A3have the same expression as given

in the Eq.(3.43) , andA2=

k2 c α2

h

R2+V R0c−V α 4 k2

c −RaSV Le

i .

The solution of Eq.(4.44), is given by

Au(τ) =

1

r

A3

2A2 +C1Exp

h

−2A2 A1

i

, (4.45)

whereC1is a parameter, it can be obtained for given suitable initial condition. The horizontal averaged Nusselt

and Sherwood numbers in this case is obtained, respectively from Eq.(3.40) and Eq.(3.41) by using the value of Au(τ) in the place ofA(τ). It can also be done in the case of gravity modulation by the similar process.

5

Results and Discussion

The present paper deals with double-diffusive convection under gravity modulation by using Ginzburg-Landau model. It is necessary to consider a non-linear theory to analyze heat and mass transfer which is not possible by the linear theory. Also, we consider the effect of gravity modulation to be of orderO(2), this leads to small amplitude of modulation. Such an assumption will help us in obtaining the amplitude equation of convection in a rather simple and elegant manner and is much easier to obtain than in the case of the Lorenz model. Also, we have investigated the effect of thermo-rheological parameter on heat and mass transfer.

The parameters that arise in the problem areP r, V, Le, RaS, δ,Ω, these parameters influence the con-vective heat and mass transfer. The first four parameters related to the fluid layer, and the last two concern the external mechanisms of controlling convection. Also the fluid layer is not considered to be highly viscous, therefore only moderate values ofP rare taken for calculations. The effect of gravity modulation is represented by an amplitude δ, which takes the values around 0.3, since we are studying the effect of small amplitude modulation on the heat and mass transport.

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i. The effect of Prandtl numberP r for small values of timeτis to advances the convection and hence heat and mass transfer, given in Figs. [2a], [3a], however for large values of time it shows oscillatory behaviour.

ii. The effects of thermo-rheological parameterV and Lewis Le number is to advances the convection and hence heat and mass transfer. Thus, bothV andLehave destabilizing effect on the system, given in Figs [2b,2c]N uand [3b,3c]Sh.

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gradient of solute will prevent the onset of convection, the strong finite-amplitude motions, which exist for large Rayleigh numbers, tend to mix the solute and redistribute it so that the interior layers of the fluid are more neutrally stratified. As a consequence, the inhibiting effect of the solute gradient is greatly reduced and hence fluid will convect more and more heat and mass, whenRaS is increased.

iv. An increment in amplitude of g-jitterδleads to increment inN u andSh, hence heat and mass transfer as given in Figs. [2e]N u, [3e]Sh.

v. An increment in frequency of modulation shortens the wavelength and decreases the magnitude ofN u,

Sh, and hence heat and mass transfer as given in Figs [2f]N u, [3f]Sh.

vi. The comparison between modulated and unmodulated system is shown in Fig.[4a,b], unmodulated case has no effect on heat and mass transfer except for small values of time. But, modulated case has an oscillatory behaviour of heat and mass transfer.

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viii. The results of this work can be summarized as follows from the Figs. [2, 3]. 1. [N u/Sh]P r=0.5<[N u/Sh]P r=1.0<[N u/Sh]P r=1.5

2. [N u/Sh]V=0.2<[N u/Sh]V=0.4<[N u/Sh]V=0.7

3. [N u]Le=1.2<[N u]Le=1.6<[N u]Le=2.2

4. [Sh]Le=1.2<[Sh]Le=1.3<[Sh]Le=1.4

5. [N u/Sh]RaS=20<[N u/Sh]RaS=50<[N u/Sh]RaS=100

6. [N u/Sh]δ=0.3<[N u/Sh]δ=0.5<[N u/Sh]δ=0.7

7. [N u/Sh]Ω=100<[N u/Sh]Ω=50<[N u/Sh]Ω=30<[N u/Sh]Ω=2.

6

Conclusions

We performed the weak nonlinear analysis, using the Ginzburg-Landau equation for double diffusive convec-tion, in a temperature sensitive horizontal fluid layer, in the presence of gravity modulation. The following conclusions have been made from our analysis.

i. Prandtl numberP r has an effect for small values of time, further increasing time no effect on heat and mass transfer.

ii. Thermo-rheological parameterV: both heat and mass transfer increase.

iii. Lewis number Le : heat and mass transfer increase.

iv. Solute Rayleigh number RaS: heat and mass transfer increase.

v. amplitude of modulationδ: heat and mass transfer increase.

vi. The frequency of modulation Ω: heat and mass transfer decrease.

vii. The unmodulated system has no effect on heat and mass transfer but modulated system affect the system.

ACKNOWLEDGMENT

This work was done during the lien sanctioned to the author by Banaras Hindu University, Varanasi, India to work as Professor of Mathematics at Department of Applied Mathematics, School for Physical Sciences, Babasaheb Bhimrao Ambedkar Central University, Lucknow, India. The author B.S Bhadauria gratefully acknowledges Banaras Hindu University, Varanasi for the same. Further, the author Palle Kiran gratefully acknowledges the financial assistance from Babasaheb Bhimrao Ambedkar University as a research fellowship.

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Received: August 19, 2013;Accepted: September 1, 2013

References

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