Research ArticleEffects of Heat and Mass Transfer on the PeristalticTransport of MHD Couple Stress Fluid through PorousMedium in a Vertical Asymmetric Channel
K. Ramesh and M. Devakar
Department of Mathematics, Visvesvaraya National Institute of Technology, Nagpur 440010, India
Correspondence should be addressed to M. Devakar; m [email protected]
Received 30 September 2014; Accepted 10 February 2015
Academic Editor: Jamshid M. Nouri
Copyright Β© 2015 K. Ramesh and M. Devakar. This is an open access article distributed under the Creative Commons AttributionLicense, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properlycited.
The intrauterine fluid flow due to myometrial contractions is peristaltic type motion and the myometrial contractions may occurin both symmetric and asymmetric directions. The channel asymmetry is produced by choosing the peristaltic wave train on thewalls to have different amplitude, and phase due to the variation of channel width, wave amplitudes and phase differences. Inthis paper, we study the effects of heat and mass transfer on the peristaltic transport of magnetohydrodynamic couple stress fluidthrough homogeneous porous medium in a vertical asymmetric channel. The flow is investigated in the wave frame of referencemoving with constant velocity with the wave. The governing equations of couple stress fluid have been simplified under the longwave length approximation. The exact solutions of the resultant governing equations have been derived for the stream function,temperature, concentration, pressure gradient, and heat transfer coefficients.Thepressure difference and frictional forces at both thewalls are calculated using numerical integration. The influence of diverse flow parameters on the fluid velocity, pressure gradient,temperature, concentration, pressure difference, frictional forces, heat transfer coefficients, and trapping has been discussed. Thegraphical results are also discussed for four different wave shapes. It is noticed that increasing of couple stresses and heat generationparameter increases the size of the trapped bolus.The heat generation parameter increases the peristaltic pumping and temperature.
1. Introduction
In recent years, the flow of non-Newtonian fluids has receivedmuch attention due to the increasing industrial, medical,and technological applications. Various researchers haveattempted diverse flow problems related to several non-Newtonian fluids and couple stress fluid is one of them. Thetheory of couple stress fluids originated by Stokes [1] hasmany biomedical, industrial, and scientific applications andwas used to model synthetic fluids, polymer thickened oils,liquid crystals, animal blood, and synovial fluid. Some earlierdevelopments in couple stress fluid theory with some basicflows can be found in the book by Stokes [2]. Recently, fewresearchers have studied some couple stress fluid flows fordifferent flow geometries [3β8].
Nowadays, peristaltic flows have gained much attentionbecause of their applications in physiology and industry.
Peristaltic transport is a form of fluid transport induced bya progressive wave of area contraction or expansion alongthe length of a distensible tube/channel and transportingthe fluid in the direction of the wave propagation. Thisphenomenon is known as peristalsis. In physiology this playsan important role in various situations such as the foodmovement in the digestive tract, urine transport from kidneyto bladder through ureter, movement of lymphatic fluids inlymphatic vessels, bile flow from the gall bladder into theduodenum, spermatozoa in the ductus efferentes of the malereproductive tract, ovum movement in the fallopian tube,blood circulation in the small blood vessels, the movementof the chyme in the gastrointestinal tract, intrauterine fluidmotion, swallowing food bolus through esophagus, andtransport of cilia. Many industrial and biological instrumentssuch as roller pumps, finger pumps, heart-lung machines,blood pumpmachines, and dialysis machines are engineered
Hindawi Publishing CorporationJournal of FluidsVolume 2015, Article ID 163832, 19 pageshttp://dx.doi.org/10.1155/2015/163832
2 Journal of Fluids
based on the peristaltic mechanism [9]. The intrauterinefluid flow due to myometrial contractions is peristaltic innature and these myometrial contractions occur in bothsymmetric and asymmetric directions and also when embryoenters the uterus for implantation there start the asymmetriccontractions.The contractions inside the nonpregnant uterusare very complicated because they are composed of variableamplitudes and different wave lengths [10]. In view of this,Pandey and Chaube [11] have investigated the peristaltictransport of a couple stress fluid in a symmetrical channelusing perturbationmethod in terms of small amplitude ratio.Ali and Hayat [12] have studied the peristaltic motion ofmicropolar fluid in an asymmetric channel. Naga Rani andSarojamma [13] have analyzed the peristaltic transport of aCasson fluid in an asymmetric channel. Hayat et al. [14] havediscussed the peristaltic flow of a Johnson-Segalman fluid inan asymmetric channel. Hayat and Javed [15] have studiedthe peristaltic transport of power-law fluid in asymmetricchannel.
The porous medium plays an important role in thestudy of transport process in biofluid mechanics, indus-trial mechanics, and engineering fields. The fluid transportthrough porous medium is widely applicable in the vascularbeds, lungs, kidneys, tumorous vessels, bile duct, gall bladderwith stones, and small blood vessels. In the pathological situ-ations, the distribution of fatty cholesterol, artery clogging,blood clots in the lumen of coronary artery, transport ofdrugs and nutrients to brain cells, and functions of organsare modeled as porous medium [16]. Recently, Tripathi [17]studied the peristaltic hemodynamic flow of couple stressfluids through a porous medium. Tripathi and BeΜg [18] haveinvestigated the peristaltic flow of generalized Maxwell fluidthrough a porous medium using homotopy perturbationmethod. Abd elmaboud and Mekheimer [19] have discussedperistaltic transport of a second-order fluid through a porousmedium using regular perturbation method. The magneto-hydrodynamic flows also gained much attention due to thewidespread applications in biofluid mechanics and industry.It is the fact that many fluids like blood are conductive innature and gave a new direction for research. The indispens-able role of biomagnetic fluid dynamics in medical sciencehas been very helpful with many problems of physiology.It has wide range of applications, such as magnetic woundor cancer tumour treatment, bleeding reduction duringsurgeries, provocation of occlusion of feeding vessels ofcancer tumor, cell separation, transport of drugs, blood pumpmachines, and magnetic resonance imaging to diagnose thedisease and the influence of magnetic field which may beutilized as a blood pump in carrying out cardiac operationsfor the blood flow in arteries with arterial disease like arterialstenosis or arteriosclerosis. Specifically, the magnetohydro-dynamic flows of non-Newtonian fluids are of great interestin magnetotherapy. The noninvasive radiological tests usethe magnetic field to evaluate organs in abdomen [20].Hayat et al. [21] have studied the peristaltic transport ofmagnetohydrodynamic Johnson-Segalman fluid for the caseof a planar channel. Wang et al. [22] have investigated theperistaltic motion of a magnetohydrodynamic generalizedsecond-order fluid in an asymmetric channel. Nadeem and
Akram [23, 24] have discussed the peristaltic transport of acouple stress fluid and Williamson fluid in an asymmetricchannel with the effect of the magnetic field.
Heat transfer plays a significant role in the cooling pro-cesses of industrial and medical applications. Such consider-ation is very important since heat transfer in the human bodyis currently considered as an important area of research. Inview of the thermotherapy and the human thermoregulationsystem, the model of bioheat transfer in tissues has beenattracted by the biomedical engineers. In fact the heat transferin human tissues involves complicated processes such asheat conduction in tissues, heat transfer due to perfusion ofthe arterial-venous blood through the pores of the tissue,metabolic heat generation, and external interactions suchas electromagnetic radiation emitted from cell phones [25].Heat transfer also involves many complicated processessuch as evaluating skin burns, destruction of undesirablecancer tissues, dilution technique in examining blood flow,paper making, food processing, vasodilation, and radiationbetween surface and its environment [26]. Mustafa et al.[27] have studied the peristaltic transport of nanofluid in achannel. The heat transfer characteristics of a couple stressfluid in an asymmetric channel have been analyzed by Abdelmaboud et al. [28]. Nadeem and Akbar [29] have discussedthe influence of heat transfer andmagnetic field on peristalticflow of a Johnson-Segalman fluid in a vertical symmetricchannel. Some more works regarding peristaltic flows withthe effect of heat transfer and magnetic field can be seenin [30β33]. Srinivas et al. [34] have studied the effects ofboth wall slip conditions and heat transfer on peristalticflow of MHD Newtonian fluid in a porous channel withelastic wall properties. Mass transfer is another importantphenomenon in physiology and industry. This phenomenonhas great applications such as nutrientsβ diffusion out from theblood to neighboring tissues, membrane separation process,reverse osmosis, distillation process, combustion process, anddiffusion of chemical impurities [35]. Recently, Noreen [36]studied the problem of mixed convection peristaltic flow ofthird-order nanofluidwith an inducedmagnetic field. Saleemand Haider [37] have discussed the peristaltic transport ofMaxwell fluid with heat and mass transfer in an asymmetricchannel. Some more relevant works on the peristaltic trans-port with heat and mass transfer can be seen in [38β42].
The aim of the present study is to investigate the influenceof heat and mass transfer on the peristaltic flow of magne-tohydrodynamic couple stress fluid through homogeneousporous medium in a vertical asymmetric channel. This paperis arranged as follows. Section 2 presents the mathematicalformulation for the problem. The solution of the problemis obtained in Section 3. The four different wave forms arepresented in Section 4 while the computational results arediscussed in Section 5. The last section, Section 6, presentsthe conclusions of the present study.
2. Formulation of the Problem
Let us consider magnetohydrodynamic couple stress fluid ina vertical asymmetric channel through the porous medium
Journal of Fluids 3
B0
g
Y
X
T0
πa1
H1C1 C0
c
H2
T1
a2
π
d1
d2
o
Figure 1: Physical model of the problem.
with the width of π1+ π2. The surfaces π»
1and π»
2of the
asymmetric channel are maintained at constant temperaturesπ0and π
1and the constant concentrations πΆ
0and πΆ
1,
respectively (see Figure 1).The porous medium is assumed tobe homogeneous. The motion is induced by sinusoidal wavetrains propagating with constant speed π along the channelwalls as defined by the following:
π»1= π1+ π1cos(2π
π(π β ππ‘)) (right side wall) ,
π»2= βπ2β π2cos(2π
π(π β ππ‘) + π) (left side wall) ,
(1)
where π1and π2are the wave amplitudes, π is the wave length,
π1+ π2is the channel width, π is the velocity of propagation,
π‘ is the time, andπ is the direction of wave propagation. Thephase difference π varies in the range 0 β€ π β€ π, in which π =0 corresponds to symmetric channel with waves out of phaseand π = π corresponds to waves in phase, and further π
1, π2,
π1,π2, andπmeet the following relation π2
1+π2
2+2π1π2cosπ β€
(π1+ π2)2.
The continuity, momentum, energy, and concentrationequations for an MHD incompressible couple stress fluid, inthe absence of body couples, are [8, 16]
β β π = 0,
ππ·π
π·π‘= ββπ β πβ
2π β πβ
4π + π½ Γ π΅ + π
+ πππ½π(π β π
0) + πππ½
πΆ(πΆ β πΆ
0) ,
πππ
π·π
π·π‘= πββ2π + π
0,
π·πΆ
π·π‘= π·β
2πΆ +
π·πΎπ
ππ
β2π,
(2)
in which π·/π·π‘ represents the material derivative and π isDarcyβs resistance in the porous medium which are given by
π·
π·π‘=π
ππ‘+ π’
π
ππ₯+ V
π
ππ¦, π = β
π
π0
π, (3)
where π is the velocity vector, π is the density, π is thepressure, π is the viscosity, π is material constant associatedwith couple stress, π½ is the electric current density, π΅ isthe total magnetic field, π is the acceleration due to thegravity, π½
πis the coefficient of thermal expansion, π½
πΆis the
coefficient of expansion with concentration, ππis the specific
heat at constant pressure, π is the temperature, πΆ is themass concentration, πβ is the thermal conductivity, π
0is the
constant heat generation parameter, π· is the coefficient ofmass diffusivity, πΎ
πis the thermal diffusion ratio, π
πis the
mean temperature, and π0is the permeability parameter. The
viscous dissipation is neglected in the energy equation.In the fixed frame, governing equations for the peristaltic
motion of an incompressible magnetohydrodynamic couplestress fluid through homogeneous porous medium in thetwo-dimensional vertical channel are
ππ
ππ+ππ
ππ= 0,
π (ππ
ππ‘+ π
ππ
ππ+ π
ππ
ππ)
= βππ
ππ+ π(
π2π
ππ2+π2π
ππ2)
4 Journal of Fluids
β π(π4π
ππ4+ 2
π4π
ππ2ππ2+π4π
ππ4)
β ππ΅2
0π β
π
π0
π + πππ½π(π β π
0) + πππ½
πΆ(πΆ β πΆ
0) ,
π (ππ
ππ‘+ π
ππ
ππ+ π
ππ
ππ)
= βππ
ππ+ π(
π2π
ππ2+π2π
ππ2)
β π(π4π
ππ4+ 2
π4π
ππ2ππ2+π4π
ππ4) β
π
π0
π,
πππ(ππ
ππ‘+ π
ππ
ππ+ π
ππ
ππ) = π
β(π2π
ππ2+π2π
ππ2) + π
0,
(ππΆ
ππ‘+ π
ππΆ
ππ+ π
ππΆ
ππ)
= π·(π2πΆ
ππ2+π2πΆ
ππ2) +
π·πΎπ
ππ
(π2π
ππ2+π2π
ππ2) ,
(4)
in whichπ andπ are the respective velocity components,π isthe pressure, π is the temperature and πΆ is the concentrationin the reference to fixed frame system, π is the electricalconductivity of the fluid, and π΅
0is the applied magnetic field.
In the above, the inducedmagnetic field is neglected since themagnetic Reynolds number is assumed to be small.
The coordinates, velocities, pressure, temperature, andconcentration in the fixed frame (π, π) and wave frame (π₯, π¦)are related by the following expressions:
π₯ = π β ππ‘, π¦ = π, π’ = π β π, V = π,
π (π₯, π¦) = π (π, π, π‘) , π (π₯, π¦) = π (π, π, π‘) ,
πΆ (π₯, π¦) = πΆ (π, π, π‘) ,
(5)
in which π’, V, π, π, and πΆ are velocity components, pressure,temperature, and concentration in the wave frame, respec-tively.
Using (5), the governing equations in the wave frame aregiven as follows:
ππ’
ππ₯+πVππ¦= 0,
π (π’ππ’
ππ₯+ Vππ’
ππ¦)
= βππ
ππ₯+ π(
π2π’
ππ₯2+π2π’
ππ¦2)
β π(π4π’
ππ₯4+ 2
π4π’
ππ₯2ππ¦2+π4π’
ππ¦4)
β ππ΅2
0(π’ + π) β
π
π0
(π’ + π) + πππ½π(π β π
0)
+ πππ½πΆ(πΆ β πΆ
0) ,
π (π’πVππ₯+ VπVππ¦)
= βππ
ππ¦+ π(
π2Vππ₯2
+π2Vππ¦2
)
β π(π4Vππ₯4
+ 2π4V
ππ₯2ππ¦2+π4Vππ¦4
) βπ
π0
V,
πππ(π’ππ
ππ₯+ Vππ
ππ¦) = π
β(π2π
ππ₯2+π2π
ππ¦2) + π
0,
(π’ππΆ
ππ₯+ VππΆ
ππ¦)
= π·(π2πΆ
ππ₯2+π2πΆ
ππ¦2) +
π·πΎπ
ππ
(π2π
ππ₯2+π2π
ππ¦2) .
(6)
We introduce the following dimensionless parameters:
π₯ =π₯
π, π¦ =
π¦
π1
, π’ =π’
π, V =
Vπ,
β1=π»1
π1
, β2=π»2
π1
, π‘ =ππ‘
π,
π =π2
1
ππππ,
πΏ =π1
π, π =
π2
π1
, π =π1
π1
, π =π2
π1
,
Re =πππ1
π, π = β
π
ππ΅0π1, π·
π=π0
π21
,
πΎ = βπ
ππ1, Gr =
πππ2
1π½π(π1β π0)
ππ,
Gc =πππ2
1π½πΆ(πΆ1β πΆ0)
ππ, π =
π
ππ1
, Pr =πππ
πβ,
π =π β π
0
π1β π0
, Ξ¦ =πΆ β πΆ
0
πΆ1β πΆ0
, π½ =π0π2
1
πβ (π1β π0),
Sc =π
ππ·, Sr =
ππ·πΎπ(π1β π0)
πππ(πΆ1β πΆ0),
(7)
where πΏ is the dimensionlesswave number, Re is the Reynoldsnumber, π is the Hartmann number, π·
πis the Darcy
number, πΎ is the couple stress parameter, Gr is the localtemperature Grashof number, Gc is the local concentration
Journal of Fluids 5
Grashof number, Pr is the Prandtl number, π is the dimen-sionless temperature, Ξ¦ is the dimensionless concentration,π½ is the heat generation parameter, Sc is the Schmidt number,and Sr is the Soret number.
In terms of these nondimensional variables, the govern-ing equations (6), after dropping the bars, become
πΏππ’
ππ₯+πVππ¦= 0, (8)
Re πΏ(π’ππ’ππ₯+1
πΏVππ’
ππ¦)
= βππ
ππ₯+ (πΏ2 π2π’
ππ₯2+π2π’
ππ¦2)
β1
πΎ2(πΏ4 π4π’
ππ₯4+ 2πΏ2 π4π’
ππ₯2ππ¦2+π4π’
ππ¦4)
β (π2+1
π·π
) (π’ + 1) + Grπ + GcΞ¦,
(9)
Re πΏ2 (π’ πVππ₯+1
πΏVπVππ¦)
= βππ
ππ¦+ (πΏ3 π2Vππ₯2
+ πΏπ2Vππ¦2
)
β1
πΎ2(πΏ5 π4Vππ₯4
+ 2πΏ3 π4V
ππ₯2ππ¦2+ πΏ
π4Vππ¦4
) β1
π·π
πΏV,
(10)
RePrπΏ(π’ππππ₯+ Vππ
ππ¦) = (πΏ
2 π2π
ππ₯2+π2π
ππ¦2) + π½, (11)
Re πΏ(π’πΞ¦ππ₯
+ VπΞ¦
ππ¦)
=1
Sc(π2Ξ¦
ππ₯2+π2Ξ¦
ππ¦2) + Sr(πΏ2 π
2π
ππ₯2+π2π
ππ¦2) .
(12)
The dimensionless velocity components (π’, V) in terms ofstream function π are related by the following relations:
π’ =ππ
ππ¦, V = βπΏ
ππ
ππ₯. (13)
Using (13), the governing equations (9)β(12) reduced to
Re πΏ [(ππ
ππ¦
π
ππ₯βππ
ππ₯
π
ππ¦)ππ
ππ¦]
= βππ
ππ₯+ (πΏ2 π3π
ππ₯2ππ¦+π3π
ππ¦3)
β1
πΎ2(πΏ4 π5π
ππ₯4ππ¦+ 2πΏ2 π5π
ππ₯2ππ¦3+π5π
ππ¦5)
β (π2+1
π·π
)(ππ
ππ¦+ 1) + Grπ + GcΞ¦,
β Re πΏ3 [(ππ
ππ¦
π
ππ₯βππ
ππ₯
π
ππ¦)ππ
ππ₯]
= βππ
ππ¦β (πΏ4 π3π
ππ₯3+ πΏ2 π3π
ππ₯ππ¦2)
+1
πΎ2(πΏ6 π5π
ππ₯5+ 2πΏ4 π5π
ππ₯3ππ¦2+ πΏ2 π5π
ππ₯ππ¦4)
+1
π·π
πΏ2 ππ
ππ₯,
RePrπΏ(ππ
ππ¦
ππ
ππ₯βππ
ππ₯
ππ
ππ¦) = (πΏ
2 π2π
ππ₯2+π2π
ππ¦2) + π½,
Re πΏ(ππ
ππ¦
πΞ¦
ππ₯βππ
ππ₯
πΞ¦
ππ¦)
=1
Sc(πΏ2 π2Ξ¦
ππ₯2+π2Ξ¦
ππ¦2) + Sr(πΏ2 π
2π
ππ₯2+π2π
ππ¦2) .
(14)
The dimensionless boundary conditions can be put in theforms
π =πΉ
2,
ππ
ππ¦= β1,
π3π
ππ¦3= 0,
π = 0, Ξ¦ = 0
at π¦ = β1= 1 + π cos (2ππ₯) ,
π = βπΉ
2,
ππ
ππ¦= β1,
π3π
ππ¦3= 0,
π = 1, Ξ¦ = 1
at π¦ = β2= βπ β π cos (2ππ₯ + π) .
(15)
The dimensionless mean flow rate Ξ in fixed frame is relatedto the nondimensional mean flow rate πΉ in wave frame by
Ξ = πΉ + 1 + π, (16)
in which
πΉ = β«
β1
β2
ππ
ππ¦ππ¦ = π (β
1(π₯)) β π (β
2(π₯)) . (17)
We note that β1and β
2represent the dimensionless forms of
the peristaltic walls
β1(π₯) = 1 + π cos (2ππ₯) ,
β2(π₯) = βπ β π cos (2ππ₯ + π) ,
(18)
where π, π, π, and π satisfy the relation π2 + π2 + 2ππ cosπ β€(1 + π)
2.
3. Solution of the Problem
Assuming that the wave length of the peristaltic wave is verylarge compared to the width of the channel, the wave number
6 Journal of Fluids
πΏ becomes very small.This assumption is known as longwavelength approximation. Since πΏ is very small, all the higherpowers of πΏ are also very small. Therefore, neglecting termscontaining πΏ and its higher powers from (14), we get
ππ
ππ₯=π3π
ππ¦3β1
πΎ2
π5π
ππ¦5
β (π2+1
π·π
)(ππ
ππ¦+ 1) + Grπ + GcΞ¦,
(19)
ππ
ππ¦= 0, (20)
π2π
ππ¦2+ π½ = 0, (21)
1
Scπ2Ξ¦
ππ¦2+ Srπ
2π
ππ¦2= 0. (22)
Elimination of pressure form from (19) and (20) yields
π4π
ππ¦4β1
πΎ2
π6π
ππ¦6β (π
2+1
π·π
)π2π
ππ¦2+ Grππ
ππ¦+ GcπΞ¦
ππ¦= 0.
(23)
Solving (21) and (22) with the boundary conditions (15), thetemperature and concentration are obtained as
π = βπ½π¦2
2+ π΄1π¦ + π΄
2,
Ξ¦ = SrScπ½π¦2
2+ π΅1π¦ + π΅2,
(24)
where
π΄1=π½ (β2
1β β2
2) β 2
2 (β1β β2); π΄
2=π½β2
1β 2π΄1β1
2;
π΅1= β
ScSrπ½ (β21β β2
2) + 2
2 (β1β β2)
; π΅2= β
ScSrπ½β21+ 2π΅1β1
2.
(25)
Inserting (24) in (23), with the help of boundary conditions(15), we obtain the stream function as
π = π·1π¦3+ π·2π¦2+ πΆ3π¦ + πΆ
4+ πΆ5cosh (π
1π¦)
+ πΆ6sinh (π
1π¦) + πΆ
7cosh (π
2π¦) + πΆ
8sinh (π
2π¦) .
(26)
in which
π1= βπ2 +
1
π·π
; π1=βπΎ2+ πΎβπΎ2 β 4π2
1
2;
π2=βπΎ2β πΎβπΎ2 β 4π2
1
2;
πΆ1= π½πΎ2(GcScSr β Gr) ; πΆ
2= πΎ2(Grπ΄
1+ Gcπ΅
1) ;
πΆ3= π·19+ πΆ8π·20;
πΆ4=πΉ
2β π·1β3
1β π·2β2
1β πΆ3β1β πΆ5cosh (π
1β1)
β πΆ6sinh (π
1β1) β πΆ7cosh (π
2β1) β πΆ8sinh (π
2β1) ;
πΆ5= π·13+ πΆ8π·14; πΆ
6= π·15+ πΆ8π·16;
πΆ7= π·17+ πΆ8π·18; πΆ
8=π·21
π·22
;
π·1=
πΆ1
6π21πΎ2; π·
2=
πΆ2
2π21πΎ2;
π·3= sinh (π
1β1) β sinh (π
1β2) ;
π·4= cosh (π
1β1) β cosh (π
1β2) ;
π·5= sinh (π
2β1) β sinh (π
2β2) ;
π·6= cosh (π
2β1) β cosh (π
2β2) ;
π·7= π3
1(sinh (π
1β1) β
π·3sinh (π
2β1)
π·5
) ;
π·8= π3
1(β cosh (π
1β1) +
π·4sinh (π
2β1)
π·5
) ;
π·9= π3
2(cosh (π
2β1) +
π·6sinh (π
2β1)
π·5
) ;
π·10= 3π·1(β2
2β β2
1) + 2π·
2(β2β β1)
β6π1π·1π·4
π·8
+6π3
1π·1π·4
π22π·8
;
π·11= π1π·3+π1π·4π·7
π·8
βπ3
1π·3
π22
βπ3
1π·4π·7
π22π·8
;
π·12=π1π·4π·9
π·8
βπ3
1π·4π·9
π22π·8
;
π·13=π·10
π·11
; π·14=π·12
π·11
;
π·15=π·7π·13+ 6π·1
π·8
; π·16=π·7π·14β π·9
π·8
;
π·17= β
π3
1(π·3π·13+ π·4π·15)
π32π·5
;
π·18= β
π3
1(π·3π·14+ π·4π·16) + π3
2π·6
π32π·5
;
π·19= β 1 β 3π·
1β2
1β 2π·2β1β π1π·13sinh (π
1β1)
β π1π·15cosh (π
1β1) β π2π·17sinh (π
2β1) ;
π·20= β π
1π·14sinh (π
1β1) β π1π·16cosh (π
1β1)
β π2π·18sinh (π
2β1) β π2cosh (π
2β1) ;
π·21= πΉ β π·
1(β3
1β β3
2) β π·2(β2
1β β2
2) β π·19(β1β β2)
β π·4π·13β π·3π·15β π·6π·17;
π·22= π·20(β1β β2) + π·4π·14+ π·3π·16+ π·6π·18+ π·5.
(27)
Journal of Fluids 7
0 0.5 1 1.5
0
0.5
β1β1
β0.5
β0.5
u
y
M = 0.0
M = 1.0
M = 1.5
M = 2.0
(a)
0 0.5 1 1.5
00.20.40.6
β1 β0.5
u
y
β0.2
β0.4
β0.6
β0.8
β1
Sc = 0Sc = 1
Sc = 2Sc = 3
(b)
0 0.5 1 1.5
0
0.5
β1β1
β0.5
β0.5
u
y
πΎ = 4
πΎ = 5
πΎ = 7πΎ = 11
(c)
0 0.5 1 1.5
0
0.5
β1β1
β0.5
β0.5
u
y
Da = 0.2
Da = 0.3
Da = 0.4
Da = 0.6
(d)
0 0.5 1 1.5
00.20.40.6
β1 β0.5
u
y
β0.2
β0.4
β0.6
β0.8
β1
π½ = 0π½ = 3
π½ = 6
π½ = 9
(e)
0 0.5 1 1.5
0
0.5
β1β1
β0.5
β0.5
u
y
Gr = 0Gr = 1
Gr = 2Gr = 3
(f)
Figure 2: Velocity profile for (a) π₯ = 1, π = 0.7, π = 0.5, π = 1, π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and
π½ = 0.2; (b) π₯ = 1, π = 0.7, π = 0.5, π = 1,π = 1,π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Ξ = 2, and π½ = 7; (c) π₯ = 1, π = 0.7,
π = 0.5, π = 1,π = 1,π·π= 0.5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4,Ξ = 2, and π½ = 0.2; (d) π₯ = 1, π = 0.7, π = 0.5, π = 1,π = 1,
πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2; (e) π₯ = 1, π = 0.7, π = 0.5, π = 1,π = 1,π·π= 0.5, πΎ = 5, π = π/3,
Gr = 0.5, Gc = 0.5, Sr = 0.8, Sc = 0.8, and Ξ = 2; (f) π₯ = 1, π = 0.7, π = 0.5, π = 1,π = 1, π·π= 0.5, πΎ = 5, π = π/3, Gc = 0.5, Sr = 0.4,
Sc = 0.4, Ξ = 2, and π½ = 0.2.
Using (24) and (26) in (19), the pressure gradient is given by
ππ
ππ₯= πΈ1π¦2+ πΈ2π¦ + πΈ3+ πΈ4cosh (π
1π¦) + πΈ
5sinh (π
1π¦)
+ πΈ6cosh (π
2π¦) + πΈ
7sinh (π
2π¦) ,
(28)
where
πΈ1=GcScSrπ½ β Grπ½ β 6π2
1π·1
2;
πΈ2= Grπ΄
1+ Gcπ΅
1β 2π2
1π·2;
πΈ3= Grπ΄
2+ Gcπ΅
2+ 6π·1β π2
1(1 + πΆ
3) ;
8 Journal of Fluids
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
10
20
30
40
50
60
x
dp/dx
M = 0.0
M = 1.0
M = 1.5
M = 2.0
(a)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
5
10
15
20
25
30
x
dp/dx
π½ = 0π½ = 3
π½ = 6
π½ = 9
(b)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 105
10152025303540455055
x
dp/dx
Gr = 0Gr = 2
Gr = 4Gr = 6
(c)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
10
20
30
40
50
60
Da = 0.2
Da = 0.3
Da = 0.4
Da = 0.6
x
dp/dx
(d)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
5
10
15
20
25
x
dp/dx
Sc = 0Sc = 1
Sc = 2Sc = 3
(e)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
10
20
30
40
50
60
x
dp/dx
πΎ = 4
πΎ = 5
πΎ = 7πΎ = 11
(f)
Figure 3: Pressure gradient for (a) π¦ = 0, π = 0.7, π = 0.5, π = 1, π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = β1,
and π½ = 0.2; (b) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1,π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, and Ξ = β1; (c) π¦ = 0,
π = 0.7, π = 0.5, π = 1,π = 1, π·π= 0.5, πΎ = 5, π = π/2, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = β1, and π½ = 0.2; (d) π¦ = 0, π = 0.7, π = 0.5, π = 1,
π = 1, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = β1, and π½ = 0.2; (e) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1,π·π= 0.5, πΎ = 5,
π = π/2, Gr = 0.5, Gc = 0.5, Sr = 0.4, Ξ = β1, and π½ = 0.2; (f) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1, π·π= 0.5, π = π/3, Gr = 0.5, Gc = 0.5,
Sr = 0.4, Sc = 0.4, Ξ = β1, and π½ = 0.2.
πΈ4= πΆ6(π3
1β π2
1π1βπ5
1
πΎ2) ;
πΈ5= πΆ5(π3
1β π2
1π1βπ5
1
πΎ2) ;
πΈ6= πΆ8(π3
2β π2
1π2βπ5
2
πΎ2) ;
πΈ7= πΆ7(π3
2β π2
1π2βπ5
2
πΎ2) .
(29)
Journal of Fluids 9
0 0.5 1 1.51.5
22.5
33.5
44.5
55.5
6
x
dp/dx
d = 1.0d = 1.1
d = 1.2
d = 1.3
(a) Sinusoidal wave
0 0.5 1 1.52
2.5
3
3.5
4
4.5
x
dp/dx
d = 1.0d = 1.1
d = 1.2
d = 1.3
(b) Triangular wave
0 0.2 0.4 0.6 0.8 1 1.21.5
22.5
33.5
44.5
55.5
6
x
dp/dx
β0.2
d = 1.0d = 1.1
d = 1.2
d = 1.3
(c) Square wave
0 0.5 1 1.51.5
22.5
33.5
44.5
55.5
6
x
dp/dx
d = 1.0d = 1.1
d = 1.2
d = 1.3
(d) Trapezoidal wave
Figure 4: Pressure gradient for various wave forms for fixed values of π¦ = 0, π = 0.7, π = 0.5, π·π= 0.5,π = 1, πΎ = 5, π = 0, Gr = 0.5,
Gc = 0.5, Sr = 0.4, Sc = 0.4, and π½ = 0.2.
The nondimensional expressions for the pressure differencefor one wave lengthΞ
ππ
, the frictional forces at both wallsπΉπ1
at π¦ = β1and πΉ
π2
at π¦ = β2, and the heat transfer coefficients
πβ1
and πβ2
at the right and left walls are defined as follows[32]:
Ξππ= β«
1
0
(ππ
ππ₯)ππ₯, πΉ
π1
= β«
1
0
β2
1(βππ
ππ₯)ππ₯,
πΉπ2
= β«
1
0
β2
2(βππ
ππ₯)ππ₯,
πβ1
=πβ1
ππ₯
ππ
ππ¦, π
β2
=πβ2
ππ₯
ππ
ππ¦.
(30)
Using (30), the heat transfer coefficients at the right and leftwalls, respectively, are obtained as
πβ1
= 2ππ (π½π¦ β π΄1) sin (2ππ₯) ,
πβ2
= β2ππ (π½π¦ β π΄1) sin (2ππ₯ + π) .
(31)
The expressions for pressure rise Ξππand frictional forces
at both walls πΉπ1
at π¦ = β1and πΉ
π2
at π¦ = β2involve the
integration of ππ/ππ₯. Due to the complexity of ππ/ππ₯, theanalytical integration of integrals of (30) is not possible. Inview of this, a numerical integration scheme is used for theevaluation of the integrals.
4. Expressions for Wave Shapes
The nondimensional expressions for the four consideredwave forms are given in the following.
(1) Sinusoidal wave:β1(π₯) = 1 + π sin (2ππ₯) ,
β2(π₯) = βπ β π sin (2ππ₯ + π) .
(32)
(2) Triangular wave:
β1(π₯) = 1 + π(
8
π3
β
β
π=1
(β1)π+1
(2π β 1)2sin (2π (2π β 1) π₯)) ,
β2(π₯) = βπ β π(
8
π3
β
β
π=1
(β1)π+1
(2π β 1)2sin (2π (2π β 1) π₯ + π)) .
(33)
(3) Square wave:
β1(π₯) = 1 + π(
4
π
β
β
π=1
(β1)π+1
2π β 1cos (2π (2π β 1) π₯)) ,
β2(π₯) = βπ β π(
4
π
β
β
π=1
(β1)π+1
2π β 1cos (2π (2π β 1) π₯ + π)) .
(34)
10 Journal of Fluids
0 0.5 1 1.5 2
05
10152025
Ξ
Ξpπ
β2 β1.5 β1 β0.5
β5
β10
β15
M = 0.0
M = 1.0
M = 1.5
M = 2.0
(a)
0 0.5 1 1.5 2
05
10152025
Ξ
Ξpπ
β2 β1.5 β1 β0.5
β5
β10
β15
Da = 0.2
Da = 0.3
Da = 0.4
Da = 0.6
(b)
0 0.5 1 1.5 2
0
5
10
15
20
Ξ
Ξpπ
β2 β1.5 β1 β0.5
β5
β10
πΎ = 4πΎ = 5 πΎ = 9
πΎ = 6
(c)
0
0 0.5 1 1.5 2
5
10
15
20
Ξ
Ξpπ
β5
β2 β1.5 β1 β0.5β10
Sr = 0Sr = 1
Sr = 2Sr = 3
(d)
0
0 0.5 1 1.5 2
5
10
15
20
Ξ
Ξpπ
β5
β2 β1.5 β1 β0.5β10
π½ = 0π½ = 3
π½ = 6
π½ = 9
(e)
0
0 0.5 1 1.5 2
5
10
15
20
Ξ
Ξpπ
β5
β2 β1.5 β1 β0.5β10
Gc = 0Gc = 1
Gc = 2Gc = 3
(f)
Figure 5: Pressure difference for (a) π¦ = 0, π = 0.7, π = 0.5, π = 1, π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2,
and π½ = 0.2; (b) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2; (c) π¦ = 0,π = 0.7, π = 0.5, π = 1,π = 1,π·
π= 0.5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4,Ξ = 2, and π½ = 0.2; (d) π¦ = 0, π = 0.7, π = 0.5, π = 1,
π = 1, π·π= 0.5, πΎ = 5, π = π/2, Gr = 0.5, Gc = 0.5, Sc = 0.4, Ξ = 2, and π½ = 0.2; (e) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1, π·
π= 0.5, πΎ = 5,
π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, and Ξ = 2; (f) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1, π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5,
Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2.
(4) Trapezoidal wave:
β1(π₯)
= 1 + π(32
π2
β
β
π=1
sin ((π/8) (2π β 1))(2π β 1)
2sin (2π (2π β 1) π₯)) ,
β2(π₯)
= βπ
β π(32
π2
β
β
π=1
sin ((π/8) (2π β 1))(2π β 1)
2sin (2π (2π β 1) π₯ + π)) .
(35)
Journal of Fluids 11
0 0.5 1 1.5 2
0
5
10
β5
β10
β2 β1.5 β1 β0.5
Ξ
Fπ1
M = 0.0
M = 1.0
M = 1.5
M = 2.0
(a)
0 0.5 1 1.5 2
0
5
10
β5
β10
β2 β1.5 β1 β0.5
Ξ
Fπ1
Da = 0.2
Da = 0.3
Da = 0.4
Da = 0.6
(b)
0 0.5 1 1.5 2
0246
β2
β4
β6
β8
β10β2 β1.5 β1 β0.5
Ξ
Fπ1
πΎ = 4πΎ = 5 πΎ = 9
πΎ = 6
(c)
0 0.5 1 1.5 2β2 β1.5 β1 β0.5Ξ
02468
β2
β4
β6
β8
β10
Fπ1
Sr = 0Sr = 1
Sr = 2Sr = 3
(d)
0 0.5 1 1.5 2β2 β1.5 β1 β0.5Ξ
0246
β2
β4
β6
β8
β10
Fπ1
π½ = 0π½ = 3
π½ = 6
π½ = 9
(e)
0 0.5 1 1.5 2β2 β1.5 β1 β0.5Ξ
02468
β2β4β6β8β10β12
Fπ1
Gc = 0Gc = 1
Gc = 2Gc = 3
(f)
Figure 6: Frictional force at the right wall for (a) π¦ = 0, π = 0.7, π = 0.5, π = 1, π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4,
Sc = 0.4, Ξ = 2, and π½ = 0.2; (b) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, andπ½ = 0.2; (c) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1, π·
π= 0.5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2; (d) π¦ = 0,
π = 0.7, π = 0.5, π = 1,π = 1, π·π= 0.5, πΎ = 5, π = π/2, Gr = 0.5, Gc = 0.5, Sc = 0.4, Ξ = 2, and π½ = 0.2; (e) π¦ = 0, π = 0.7, π = 0.5, π = 1,
π = 1,π·π= 0.5, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, and Ξ = 2; (f) π¦ = 0, π = 0.7, π = 0.5, π = 1,π = 1,π·
π= 0.5, πΎ = 5,
π = π/3, Gr = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2.
5. Results and Discussion
This section is dedicated to discussion and analysis of thevelocity distribution, pumping characteristics, heat and masscharacteristics, and trapping phenomena for different flowparameters.
5.1. Flow Characteristics. Figures 2(a)β2(f) illustrate theinfluence of Hartmann number π, Schmidt number Sc,couple stress parameter πΎ, Darcy numberπ·
π, heat generation
parameter π½, and Grashof number Gr on axial velocity profileacross the channel. From these figures, it is observed thatthe maximum velocities are always located near the centre
12 Journal of Fluids
0 0.5 1 1.5 2
01020304050607080
Trapezoidal waveSquare wave
Sinusoidal waveTriangular wave
β20
β10
β2 β1.5 β1 β0.5
Ξ
Ξpπ
(a)
0 0.5 1 1.5 2
02468
β2
β4
β6
β8
β10β2 β1.5 β1 β0.5
Ξ
Trapezoidal waveSquare wave
Sinusoidal waveTriangular wave
Fπ1
(b)
0
5
10
0 0.5 1 1.5 2β2 β1.5 β1 β0.5Ξ
β5
β10
β15
β20
Trapezoidal waveSquare wave
Sinusoidal waveTriangular wave
Fπ2
(c)
Figure 7: (a) Pressure difference, (b) frictional force at right wall, and (c) frictional force at left wall for different wave forms when π¦ = 0,π = 0.7, π = 0.5, π = 1,π·
π= 0.5,π = 1, πΎ = 5, π = 0, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2.
of the channel and the velocity profiles are nearly parabolicin all cases. It is noted from Figure 2(a) that as Hartmannnumber π increases, the velocity decreases near the centreof the channel and it is increased in the neighborhood of thewalls. This seems realistic because the magnetic field acts inthe transverse direction to the flow andmagnetic force resiststhe flow. The similar behavior is observed in [25]. The samebehavior can be seen with increasing of Schmidt number Scand couple stress parameter πΎ (see Figures 2(b) and 2(c)). It isobserved from Figure 2(d) that increasing of Darcy numberπ·πincreases the velocity near the centre of the channel
and decreases the velocity of the fluid near the peristalticwalls. The same trend is followed with the increasing of heatgeneration parameter π½ (see Figure 2(e)). It is noticed fromFigure 2(f) that, with increasing of Grashof number Gr, thevelocity at the left wall increases while a reverse trend is seenat the right wall.
5.2. Pumping Characteristics. Figure 3 illustrates the varia-tion of pressure gradient over one wave length π₯ β [0, 1].The effects ofπ, π½, and Gr on pressure gradient are displayedin Figures 3(a)β3(c). It can be seen from Figure 3(a) thatincreasing of Hartmann number π increases the pressuregradient. It shows that when strong magnetic field is applied
to the flow field then higher pressure gradient is neededto pass the flow. This result suggests that the fluid pressurecan be controlled by the application of suitable magneticfield strength. This phenomenon is useful during surgeryand critical operation to control excessive bleeding. It is alsoobserved that increasing of π½ and Gr increases the pressuregradient. From Figures 3(d)β3(f), it is noted that with theincreasing of π·
π, Sc, and πΎ the pressure gradient decreases.
It is noticed that, in the wider part of the channels π₯ β[0, 0.2] and π₯ β [0.7, 1], the pressure gradient is small, sothe flow can be easily passed without the imposition of largepressure gradient. However, in the narrow part of the channelπ₯ β [0.2, 0.7] the pressure gradient is large; that is, muchlarger pressure gradient is needed to maintain the same givenvolume flow rate. Figure 4 is prepared to see the behaviour ofpressure gradient for different four wave forms. It is observedfrom Figures 4(a)β4(d) that, in all the wave forms, increase inπ decreases pressure gradient.
The dimensionless pressure difference per unit wavelength versus time mean flow rate Ξ has been plotted inFigure 5. We split the whole region into four segments asfollows: peristaltic pumping region where Ξπ
π> 0 and
Ξ > 0 and augmented pumping region when Ξππ< 0 and
Ξ > 0. There is retrograde pumping region when Ξππ> 0
Journal of Fluids 13
0 0.5 1 1.50123456789
1011
π
y
β0.5β1
π½ = 0π½ = 3
π½ = 6
π½ = 9
(a)
0 0.5 1 1.5
00.20.40.60.8
1
y
β0.5β1
β0.2β0.4β0.6β0.8β1
Ξ¦
π½ = 0π½ = 3
π½ = 6
π½ = 9
(b)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1
010203040
β10
β20
β30
β40
β50
β60
x
Zh1
π½ = 0π½ = 3
π½ = 6
π½ = 9
(c)
Figure 8: (a) Temperature profile, (b) concentration profile, and (c) heat transfer coefficient at the right wall for π = 0.7, π = 0.5, π = 1,π·π= 0.5,π = 1, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, and Ξ = 2.
and Ξ < 0. Free pumping region corresponds to Ξππ=
0. The region where Ξππ> 0 and Ξ > 0 is known as
peristaltic pumping region. In this region, the positive valueof Ξ is entirely due to the peristalsis after overcoming thepressure difference. The region where Ξπ
π< 0 and Ξ > 0
is known as copumping or augmented pumping region. Inthis region, a negative pressure difference assists the flow dueto the peristalsis of the walls. The region where Ξπ
π> 0
and Ξ < 0 is called retrograde pumping region. In thisregion, the flow is opposite to the direction of the peristalticmotion. In the free pumping region, the flow is caused purelyby the peristalsis of the walls. It is evident from Figure 5 thatthere is an inversely linear relation betweenΞπ
πandΞ. From
Figure 5(a), it is clear that with the increasing of π, in theaugmented pumping and free pumping regions, the pumpingdecreases, in the peristaltic pumping region, the pumpingincreases up to a critical value of Ξ and decreases afterthe critical value, and in the retrograde pumping region thepumping increases. It is observed from Figure 5(b) that, withthe increasing ofπ·
π, the behaviour is quite opposite withπ.
It is noticed from Figure 5(c) that in the augmented pumpingregion the pumping increases and in the peristaltic pumpingand retrograde pumping regions the pumping decreases.Figure 5(d) depicts that, in all the pumping regions, the
pumping decreases by increasing Sr. It is noted from Figures5(e)-5(f) that the behaviour is quite opposite with Sr whileincreasing π½ and Gc.
Figure 6 describes the variation of frictional forces againstflow rate Ξ for different values of π, π·
π, πΎ, Sr, π½, and Gc.
It is observed that there is a direct linear relation betweenfrictional forces and Ξ. The frictional forces have exactlyopposite behaviour when compared with that of pressuredifference. Figure 7(a) indicates the effects of four differentwave forms on pressure difference. It is noticed that thetrapezoidal wave has best peristaltic pumping characteristics,while the triangular wave has poor peristaltic pumping ascompared to the other waves. Figures 7(b)-7(c) show thatthe frictional forces at the walls have opposite behaviour ascompared to the pressure difference.
5.3. Heat and Mass Characteristics. Figure 8 depicts theeffects of heat transfer, concentration, and heat transfercoefficient on the peristaltic transport for various values ofπ½. We can observe that the temperature and concentrationprofiles are almost parabolic except whenπ½ = 0. It is observedfrom Figure 8(a) that the temperature increases with π½. Itis clear from Figure 8(b) that the concentration profile hasquite opposite behaviour of temperature profile. It is noticed
14 Journal of Fluids
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(a) π·π = 0.3, π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(b) π·π = 0.3, π = π/3
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(c) π·π = 0.35, π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(d) π·π = 0.35, π = π/3
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(e) π·π = 0.4, π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(f) π·π = 0.4, π = π/3
Figure 9: Streamlines for π = 0.5, π = 0.5, π = 1,π = 1, πΎ = 5, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2.
from Figure 8(c) that, due to the peristalsis, the heat transfercoefficient is in oscillatory behaviour. Moreover, the absolutevalue of heat transfer coefficient increases with increase of π½.
5.4. Trapping Phenomenon. In the wave frame, the stream-lines, in general, have a shape similar to the walls as thewalls are stationary. However under certain conditions somestreamlines can split to enclose a bolus of fluid particles inclosed streamlines. Hence some circulating regions occur. Inthe fixed frame of reference the fluid bolus is trapped with thewave and itmoves as awholewith thewave speed. To examinethe effects of π·
π, πΎ, and π in the symmetric and asymmetric
channels we have plotted Figures 9β11. In Figures 9 and 10,the left panels (a), (c), and (e) related to symmetric channeland the right panels (b), (d), and (f) are corresponding toasymmetric channel. It is observed from Figure 9 that whenπ·πincreases, the size of the trapped bolus decreases near
the left wall and increases near the right wall in both panels.However, the increase of Darcy number π·
πincreases the
trapped bolus near both walls when Gc = 0 and Gr = 0.The effects of πΎ on the trapping phenomena are displayedin Figure 10. It is shown that with the increasing πΎ decreasethe trapping phenomena for the symmetric and asymmetricchannels. Since πΎ = βπ/ππ
1, πΎ decreases as π increases
and hence increasing of couple stresses increases the sizeof trapped bolus. Figure 11 gives the trapping behaviour forvarious values of π. It is evident that as π increases, the trap-ping bolus decreases and when it reaches to π the trappingdisappears. Moreover, with the increase of π the bolus movesupward with decreasing effect. Figures 12 and 13 providethe variations of π½ on trapping for different wave shapes:(a) sinusoidal, (b) triangular, (c) square, and (d) trapezoidal.From these figures we observe that the size of the trappedbolus increases with increasing π½ in all the wave forms.
Journal of Fluids 15
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(a) πΎ = 5, π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(b) πΎ = 5, π = π/3
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1β0.2β0.3β0.4β0.5
β1.5 β1 β0.5
(c) πΎ = 5.05, π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(d) πΎ = 5.05, π = π/3
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(e) πΎ = 5.1, π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(f) πΎ = 5.1, π = π/3
Figure 10: Streamlines for π = 0.5, π = 0.5, π = 1,π = 1,π·π= 0.5, Gr = 0.5, Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.2.
6. Conclusions
The effects of heat and mass transfer on the peristalticflow of magnetohydrodynamic couple stress fluid throughporous medium in a vertical asymmetric channel havebeen analyzed. The governing equations are modeled underthe assumption of long wave length approximation. Theexact solutions for the stream function, pressure gradient,temperature, heat transfer coefficients, and concentrationare obtained. The effects of involved parameters on thevelocity characteristics, pumping characteristics, heat andmass characteristics, and the trapping due to the peristalsis ofthe walls are discussed in detail. From the analysis the mainfindings can be summarized as follows:
(i) Increasing of heat generation increases the peristalticpumping, size of the trapped bolus, and the magni-tude of heat transfer coefficient at the peristaltic walls.
(ii) Increasing of couple stresses increases the size oftrapped bolus.
(iii) Increasing of heat generation increases the tempera-ture and decreases the concentration.
(iv) The trapezoidal wave has best peristaltic pumping ascompared to the other wave shapes.
(v) The frictional forces have an opposite behaviour ascompared to the pressure difference.
Symbols
π1, π2: Wave amplitudes
π: Wave lengthπ: Propagation velocityπ‘: Time
16 Journal of Fluids
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(a) π = 0
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(b) π = π/4
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(c) π = π/2
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(d) π = 2π/3
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(e) π = 5π/6
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(f) π = π
Figure 11: Streamlines for π = 0.5, π = 0.5, π = 1,π = 1,π·π= 0.5, Gr = 0.5, Gc = 0.5, πΎ = 5, Sc = 0.4, Sr = 0.4, Ξ = 2, and π½ = 0.2.
π,π: Coordinates of fixed frameπ: Pressure in the fixed frameπ: Velocity vectorπ : Darcyβs resistance in the porous mediumπ: Densityπ: Viscosityπ: Material constant associated with couple stressπ½: Electric current densityπ΅: Total magnetic fieldπ: Acceleration due to the gravityπ½π: Coefficient of thermal expansion
π½πΆ: Coefficient of expansion with concentration
ππ: Specific heat at constant pressure
π: TemperatureπΆ: Mass concentration
πβ: Thermal conductivityπ0: Heat generation parameter
π·: Coefficient of mass diffusivityπΎπ: Thermal diffusion ratio
ππ: Mean temperature
π0: Permeability parameter
π,π: Velocity components in the fixed frameπ: Pressure in the fixed frameπ: Electrical conductivity of the fluidπ΅0: Uniform applied magnetic field
πΏ: Dimensionless wave lengthπ₯, π¦: Coordinates of wave frameπ: Pressure in the wave frameπ’, V: Velocity components in the wave frameRe: Reynolds number
Journal of Fluids 17
0 0.5 1 1.5
00.10.20.30.40.50.60.7
x
y
β0.1
β0.2β1.5 β1 β0.5
(a) Sinusoidal wave
0 0.5 1 1.5
00.10.20.30.40.50.60.7
x
y
β0.1
β0.2β1.5 β1 β0.5
(b) Triangular wave
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(c) Square wave
0 0.5 1 1.5
00.10.20.30.40.50.60.7
x
y
β0.1
β0.2β1.5 β1 β0.5
(d) Trapezoidal wave
Figure 12: Streamlines for various wave forms for fixed values of π = 0.7, π = 0.5, π = 1,π·π= 0.5,π = 1, πΎ = 5, π = π/3, Gr = 0.5, Gc = 0.5,
Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 0.
0 0.5 1 1.5
00.10.20.30.40.50.60.7
x
y
β0.1
β0.2β1.5 β1 β0.5
(a) Sinusoidal wave
0 0.5 1 1.5
00.10.20.30.40.50.60.7
x
y
β0.1
β0.2β1.5 β1 β0.5
(b) Triangular wave
0 0.5 1 1.5
00.10.20.30.40.5
x
y
β0.1
β0.2
β0.3
β0.4
β0.5β1.5 β1 β0.5
(c) Square wave
0 0.5 1 1.5
00.10.20.30.40.50.60.7
x
y
β0.1
β0.2β1.5 β1 β0.5
(d) Trapezoidal wave
Figure 13: Streamlines for various wave forms for fixed values of (a) π = 0.7, π = 0.5, π = 1, π·π= 0.5,π = 1, πΎ = 5, π = π/3, Gr = 0.5,
Gc = 0.5, Sr = 0.4, Sc = 0.4, Ξ = 2, and π½ = 5.
18 Journal of Fluids
π: Hartman numberπ·π: Darcy number
πΎ: Couple stress parameterGr: Local temperature Grashof numberGc: Local concentration Grashof numberPr: Prandtl numberπ: Dimensionless temperatureΞ¦: Dimensionless concentrationπ½: Dimensionless heat generation parameterSc: Schmidt numberSr: Soret numberπ: Stream functionΞ: Time mean flow rate in the fixed frameπΉ: Time mean flow rate in the wave frameπ: Volume flow rate in the fixed frameπ: Volume flow rate in the wave frame.
Conflict of Interests
The authors declare that there is no conflict of interestsregarding the publication of this paper.
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