research article flow of an eyring-powell model fluid

8
Hindawi Publishing Corporation Chinese Journal of Engineering Volume 2013, Article ID 808342, 7 pages http://dx.doi.org/10.1155/2013/808342 Research Article Flow of an Eyring-Powell Model Fluid between Coaxial Cylinders with Variable Viscosity Azad Hussain, M. Y. Malik, and Farzana Khan Department of Mathematics, Quaid-i-Azam University, Islamabad 45320, Pakistan Correspondence should be addressed to Azad Hussain; [email protected] Received 21 July 2013; Accepted 18 August 2013 Academic Editors: G. Chen and S. Wei-dong Copyright © 2013 Azad Hussain et al. is is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. We consider the flow of Eyring-Powell model fluid in the annulus between two cylinders whose viscosity depends upon the temperature. We consider the steady flow in the annulus due to the motion of inner cylinder and constant pressure gradient. In the problem considered the flow is found to be remarkedly different from that for the incompressible Navier-Stokes fluid with constant viscosity. An analytical solution of the nonlinear problem is obtained using homotopy analysis method. e behavior of pertinent parameters is analyzed and depicted through graphs. 1. Introduction e analysis of the behaviour of the fluid motion of the non-Newtonian fluids becomes much complicated and subtle as compared to Newtonian fluids due to the fact that non- Newtonian fluids do not exhibit the linear relationship between stress and strain. Rivlin and Ericksen [1] and Trues- dell and Noll [2] classified viscoelastic fluids with the help of constitutive relations for the stress tensor as a function of the symmetric part of the velocity gradient and its higher (total) derivatives. In recent years, there have been several studies [312] on flows of non-Newtonian fluids. It is a well-known fact that it is not possible to obtain a single constitutive equation exhibiting all properties of all non- Newtonian fluids from the available literature. at is why several models of non-Newtonian fluids have been proposed in the literature. Eyring-Powell model fluid is one of these models. Eyring-Powell model was first introduced by Powell and Eyring in 1944. However, the literature survey indicates that very low energy has been devoted to the flows of Eyring- Powell model fluid with variable viscosity. Massoudi and Christie [13] have considered the effects of variable viscosity and viscous dissipation on the flow of a third grade fluid in a uniform pipe. Massoudi and Christie [13] found the numerical solutions with the help of straight forward finite difference method. ey also discussed that the flow of a fluid-solid mixture is very complicated and may depend on many variables such as physical properties of each phase and size and shape of solid particles. Later on, the influence of constant and space dependent viscosity on the flow of a third grade fluid in a pipe has been discussed analytically by Hayat et al. [14]. e approximate and analytical solution of non-Newtonian fluid with variable viscosity has been analyzed by Y¨ ur¨ usoy and Pakdermirli [15] and Pakdemirli and Yilbas [16]. e pipe flow of non-Newtonian fluid with variable viscosity keeping no slip and partial slip has been discussed analytically by Nadeem and Ali [17] and Nadeem et al. [18]. More recently, Nadeem and Akbar [19] studied the effects of temperature dependent viscosity on peristaltic flow of a Jeffrey-six constant fluid in a uniform vertical tube. e main aim of the present study is to venture further in the regime of Eyring-Powell model fluid with variable viscosity. To the best of the authors knowledge no attempt has been made to investigate Eyring-Powell model fluid in the annulus between two cylinders whose viscosity depends upon the temperature. e governing equations for Eyring- Powell model fluid are formulated considering cylindrical coordinates system. e equations are simplified using the assumptions of long wave length and low Reynolds number approximation. e obtained non-linear problem is solved

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Page 1: Research Article Flow of an Eyring-Powell Model Fluid

Hindawi Publishing CorporationChinese Journal of EngineeringVolume 2013 Article ID 808342 7 pageshttpdxdoiorg1011552013808342

Research ArticleFlow of an Eyring-Powell Model Fluid betweenCoaxial Cylinders with Variable Viscosity

Azad Hussain M Y Malik and Farzana Khan

Department of Mathematics Quaid-i-Azam University Islamabad 45320 Pakistan

Correspondence should be addressed to Azad Hussain azadhussainsamoteyahoocom

Received 21 July 2013 Accepted 18 August 2013

Academic Editors G Chen and S Wei-dong

Copyright copy 2013 Azad Hussain et al This is an open access article distributed under the Creative Commons Attribution Licensewhich permits unrestricted use distribution and reproduction in any medium provided the original work is properly cited

We consider the flow of Eyring-Powell model fluid in the annulus between two cylinders whose viscosity depends upon thetemperature We consider the steady flow in the annulus due to the motion of inner cylinder and constant pressure gradient In theproblem considered the flow is found to be remarkedly different from that for the incompressible Navier-Stokes fluid with constantviscosity An analytical solution of the nonlinear problem is obtained using homotopy analysis method The behavior of pertinentparameters is analyzed and depicted through graphs

1 Introduction

The analysis of the behaviour of the fluid motion of thenon-Newtonian fluids becomesmuch complicated and subtleas compared to Newtonian fluids due to the fact that non-Newtonian fluids do not exhibit the linear relationshipbetween stress and strain Rivlin and Ericksen [1] and Trues-dell and Noll [2] classified viscoelastic fluids with the helpof constitutive relations for the stress tensor as a function ofthe symmetric part of the velocity gradient and its higher(total) derivatives In recent years there have been severalstudies [3ndash12] on flows of non-Newtonian fluids It is awell-known fact that it is not possible to obtain a singleconstitutive equation exhibiting all properties of all non-Newtonian fluids from the available literature That is whyseveral models of non-Newtonian fluids have been proposedin the literature Eyring-Powell model fluid is one of thesemodels Eyring-Powell model was first introduced by Powelland Eyring in 1944 However the literature survey indicatesthat very low energy has been devoted to the flows of Eyring-Powell model fluid with variable viscosity Massoudi andChristie [13] have considered the effects of variable viscosityand viscous dissipation on the flow of a third grade fluidin a uniform pipe Massoudi and Christie [13] found thenumerical solutions with the help of straight forward finite

difference method They also discussed that the flow of afluid-solid mixture is very complicated and may depend onmany variables such as physical properties of each phaseand size and shape of solid particles Later on the influenceof constant and space dependent viscosity on the flow of athird grade fluid in a pipe has been discussed analyticallyby Hayat et al [14] The approximate and analytical solutionof non-Newtonian fluid with variable viscosity has beenanalyzed by Yurusoy and Pakdermirli [15] and Pakdemirliand Yilbas [16] The pipe flow of non-Newtonian fluid withvariable viscosity keeping no slip and partial slip has beendiscussed analytically by Nadeem and Ali [17] and Nadeemet al [18] More recently Nadeem and Akbar [19] studiedthe effects of temperature dependent viscosity on peristalticflow of a Jeffrey-six constant fluid in a uniform vertical tubeThe main aim of the present study is to venture furtherin the regime of Eyring-Powell model fluid with variableviscosity To the best of the authors knowledge no attempthas been made to investigate Eyring-Powell model fluid inthe annulus between two cylinders whose viscosity dependsupon the temperature The governing equations for Eyring-Powell model fluid are formulated considering cylindricalcoordinates system The equations are simplified using theassumptions of long wave length and low Reynolds numberapproximation The obtained non-linear problem is solved

2 Chinese Journal of Engineering

using homotopy analysis method [20ndash28] The effects ofthe emerging parameters are analyzed and depicted throughgraphs

2 Mathematical Model

The constitutive equation for a Cauchy stress in an Eyring-Powell model fluid is given by

S = 120583nabla119881 +

1

120573

sinhminus1 (1

119888

nabla119881)

sinhminus1 (1

119888

nabla119881) sim

1

119888

nabla119881 minus

1

6

(

1

119888

nabla119881)

3

1003816100381610038161003816100381610038161003816

1

119888

nabla119881

1003816100381610038161003816100381610038161003816

≪ 1

(1)

where 119881 is the velocity S is the Cauchy stress tensor 120583 isthe coefficient of shear viscosity and 120573 and 119888 are the materialconstants We take the velocity and stress as

V (119903) = (

0

0

V) S (119903) =

[

[

119878119903119903

119878119903120579

119878119903119911

119878120579119903

119878120579120579

119878120579119911

119878119911119903

119878119911120579

119878119911119911

]

]

(2)

3 Physical Model

Consider the steady flow of an Eyring-Powell model fluidwith variable temperature dependent viscosity between coax-ial cylindersThemotion is caused due to a constant pressuregradient and by themotion of the inner cylinder parallel to itslength whereas the outer cylinder is kept stationaryThe heattransfer analysis is also taken into accountThe dimensionlessproblem which can describe the flow is

120583

119903

119889V119889119903

+

119872

119903

119889V119889119903

+ 120583

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

120583Γ(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(3)

V (119903) = 1 120579 (119903) = 1 119903 = 1

V (119903) = 0 120579 (119903) = 0 119903 = 119887

(4)

whence

119903 =

119903

119877

Γ =

120583lowast

119881

2

0

119896 (120579119898

minus 120579119908

)

120579 =

(120579 minus 120579119908

)

(120579119898

minus 120579119908

)

119911 =

119881

2

0

119877

2

119888

2

1198621

=

120597119901

120597119911

119872 =

1

120573119888120583lowast

119870 =

119881

2

0

119877

2

119888

2

119861 =

1198621

119877

2

120583lowast

1198810

V =

VV0

120583 =

120583

120583lowast

(5)

where 120583lowast

120579119898

1198810

and Γ are respectively the reference viscos-ity a reference temperature (the bulk mean fluid tempera-ture) and reference velocity Γ is related to the Prandtl numberand Eckert number

4 Series Solutions for Reynoldsrsquo Model

Here the viscosity is expressed in the form

120583 = 119890

minus119875120579 (6)

which by Maclaurinrsquos series can be written as

120583 = 1 minus 119875120579 + 119874 (120579

2

) (7)

Note that119872 = 0 corresponds to the case of constant viscosityInvoking the above equation into (3) one has

119872

119903

119889V119889119903

+

1

119903

119889V119889119903

minus

119875120579

119903

119889V119889119903

+

119889

2V119889119903

2

minus 119875120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

Γ(

119889V119889119903

)

2

minus Γ119875120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(8)

For HAM solution we choose the following initial guesses

V0

(119903) =

(119903 minus 119887)

(1 minus 119887)

1205790

(119903) =

(119903 minus 119887)

(1 minus 119887)

(9)

The auxiliary linear operators are in the form

poundV119903 (V) = V10158401015840 (10)

pound120579119903

(120579) = 120579

10158401015840 (11)

which satisfy

LV119903 (1198601 + 1198611

119903) = 0 L120579119903

(1198602

+ 1198612

119903) = 0 (12)

where 1198601

1198602

1198611

and 1198612

are the constantsIf 119901 isin [0 1] is an embedding parameter and ℎV and ℎ

120579

areauxiliary parameters then the problems at the zero and 119898thorder are respectively given by

(1 minus 119901)LV [V (119903 119901) minus V0

(119903)] = 119901ℎV119873V [V (119903 119901) 120579 (119903 119901)]

(13)

(1 minus 119901)L120579

[120579 (119903 119901) minus 1205790

(119903)] = 119901ℎ120579

119873120579

[V (119903 119901) 120579 (119903 119901)]

(14)

LV [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℎV119877V (119903) (15)

L120579

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℎ120579

119877120579

(119903) (16)

V (119903 119901) = 120579 (119903 119901) = 1 119903 = 1 (17)

V (119903 119901) = 120579 (119903 119901) = 0 119903 = 119887 (18)

The boundary conditions at the 119898th order are

V119898

(119903 119901) = 120579119898

(119903 119901) = 0 119903 = 1

V119898

(119903 119901) = 120579119898

(119903 119901) = 0 119903 = 119887

(19)

Chinese Journal of Engineering 3

In (11)ndash(13)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119875120579

119903

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119889

2V119889119903

2

minus 119875120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ119875120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

(20)

119877V = minus

119875

119903

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+ V10158401015840119898minus1

minus 119875

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119877120579

= Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119875

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(21)

By Mathematica the solutions of (21) can be written as

V119898

(119903) =

3119898

sum

119899=0

119886119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889119898119899

119903

119899

119898 ge 0

(22)

where 119886119898119899

and 119889119898119899

are constants which can be determinedon substituting (22) into (15) and (16)

5 Series Solutions for Vogelrsquos Model

Here

120583 = 120583lowast

exp [

119860

(119905 + 120579)

minus 120579119908

] (23)

0

minus02

minus04

minus06

minus08

minus12 minus1 minus08 minus06 minus04 minus02 0

V998400998400

h

Γ = 01 K = 01M = 01 P = 001 and B = minus1

Figure 1 ℎ-curve for Reynoldsrsquo model for velocity profile

15

125

1

075

05

025

0 02 04 06 08 1 12 14

Q998400998400

h

Γ = 01 K = 01M = 01 P = 001 and B = minus1

Figure 2 ℎ-curve for Reynoldsrsquo model for temperature profile

V998400998400

h

3

2

1

minus1

minus2

minus2 minus15 minus1 minus05 0

0

Γ = 01 K = 01M = 01 s = minus01 A = 00001 t = 01 and B = minus01

Figure 3 ℎ-curve for Vogelrsquos model for velocity profile

which by Maclaurinrsquos series reduces to

120583 =

119861

119904

(1 minus

119860120579

119905

2

) (24)

4 Chinese Journal of EngineeringQ998400998400

h

175

125

15

1

075

05

025

0 02 04 06 08 1 12

B = minus01 q = minus01M = 01 A = 01 s = 01

Γ = 01 t = 01 z = 01 and u = 01

Figure 4 ℎ-curve for Vogelrsquos model for temperature profile

B = 100

B = 105

B = 110

40

30

20

10

0

Q(r)

1 12 14 16 18 2

r

Γ = 01 K = 01M = 01 and P = 001

Figure 5 Temperature profile for Reynoldsrsquo model for differentvalues of 119861

r

1

08

06

04

02

1 12 14 16 18 2

V(r)

B = minus1

B = minus2

B = minus3

Γ = 01 K = 01M = 01 and P = 001

Figure 6 Velocity profile for Reynoldsrsquo model for different values of119861

r

1

08

06

04

02

V(r)

1 12 14 16 18 2

P = 010

P = 020

P = 030

B = minus1 K = 01M = 01 and Γ = 01

Figure 7 Velocity profile for Reynoldsrsquo model for different values of119875

r

1

08

06

04

02

Q(r)

Γ = minus1Γ = minus2

Γ = minus3

1 12 14 16 18 2

B = minus1 K = 01M = 01 and P = 001

Figure 8 Temperature profile for Reynoldsrsquo model for differentvalues of Γ

Invoking the above expressions (1) become

minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(25)

Chinese Journal of Engineering 5

r

Q(r)

1

08

06

04

02

1 12 14 16 18 2

t = 00065t = 00070

t = 00085

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 9 Temperature profile for Vogelrsquos model for different valuesof 119905

t = 00083

t = 00084

t = 00085

12

1

08

06

04

02

1 12 14 16 18 2

V(r)

r

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 10 Velocity profile for Vogelrsquos model for different values of 119905

With the following initial guesses and auxiliary linear opera-tors

V0V (119903) =

(119903 minus 119887)

(1 minus 119887)

1205790V (119903) =

(119903 minus 119887)

(1 minus 119887)

poundVV (V) = V10158401015840 pound120579V (120579) = 120579

10158401015840

(26)

Γ = minus100

Γ = minus200Γ = minus300

1

08

06

04

02

1 12 14 16 18 2

Q(r)

r

B = minus01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 11 Temperature profile for Vogelrsquos model for different valuesof Γ

the 119898th-order deformation problems are

poundV119903 [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℏV119877V119903 (119903)

pound120579119903

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℏ120579

119877120579119903

(119903)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861

119903119904119905

2

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+

119861

119904

V10158401015840119898minus1

minus

119860119861

119904119905

2

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

6 Chinese Journal of EngineeringV(r)

r

3

25

2

15

1

05

1 12 14 16 18 2

s = 300

s = 500

s = 900

Γ = 01 K = 01M = 01 B = minus01 A = 00001 and t = 01

Figure 12 Velocity profile for Vogelrsquos model for different values of119904

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

V1015840119896

minus Γ

119860119861

119904119905

2

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(27)

The expressions of V119898

and 120579119898

are finally given by

V119898

(119903) =

3119898

sum

119899=0

119886

1015840

119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889

1015840

119898119899

119903

119899

119898 ge 0

(28)

6 Graphical Results and Discussion

In order to report the convergence of the obtained seriessolutions and the effects of sundry parameters in the present

1

08

06

04

02

1 12 14 16 18 2

r

V(r)

B = minus011

B = minus012B = minus013

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 13 Velocity profile for Vogelrsquos model for different values of119861

investigation we plotted Figures 1ndash13 Figures 1ndash4 are pre-pared to see the convergence region Figures 1 and 2 cor-respond to Reynoldsrsquo model whereas Figures 3 and 4 relateto Vogelrsquos model Figure 5 shows the temperature variationfor different values of 119861 for Reynoldsrsquo model It can be seenthat temperature decreases as 119861 increases Figure 6 depictsthe velocity variation for Reynoldsrsquo model for different valuesof 119861 Velocity also decreases as 119861 increases Figure 7 showsthe velocity variation for different values of 119875 for Reynoldsrsquomodel It can be seen that velocity increases as 119875 increasesFigure 8 is plotted in order to see the temperature variationfor Reynoldsrsquomodel for different values of Γ it is depicted thattemperature increases as Γ increases Figures 9ndash13 correspondto Vogelrsquos model Figure 9 depicts temperature variationfor Vogelrsquos model for different values of 119905 It is seen thattemperature increases as 119905 increases Figure 10 shows thevelocity variation for Vogelrsquos model for different values of 119905It is observed that velocity decreases as 119905 increases Figure 11is prepared to observe the temperature variation for Vogelrsquosmodel for different values of Γ It is observed that temperaturedecreases as Γ increases Figure 12 is plotted to see thethe velocity variation for Vogelrsquos model for different valuesof 119904 It is observed that velocity decreases as 119904 increasesFigure 13 depicts the velocity variation for Vogelrsquos model fordifferent values of 119861 It is observed that velocity decreases as119861 increases

7 Conclusions

In this paper we consider the flow of Eyring-Powell modelfluid in the annulus between two cylinders whose viscositydepends upon the temperature We discussed the steadyflow in the annulus due to the motion of inner cylinderand constant pressure gradient In the problem consideredthe flow is found to be remarkedly different from thatfor the incompressible Navier-Stokes fluid with constantviscosity The behavior of pertinent parameters is analyzed

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

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International Journal of

Page 2: Research Article Flow of an Eyring-Powell Model Fluid

2 Chinese Journal of Engineering

using homotopy analysis method [20ndash28] The effects ofthe emerging parameters are analyzed and depicted throughgraphs

2 Mathematical Model

The constitutive equation for a Cauchy stress in an Eyring-Powell model fluid is given by

S = 120583nabla119881 +

1

120573

sinhminus1 (1

119888

nabla119881)

sinhminus1 (1

119888

nabla119881) sim

1

119888

nabla119881 minus

1

6

(

1

119888

nabla119881)

3

1003816100381610038161003816100381610038161003816

1

119888

nabla119881

1003816100381610038161003816100381610038161003816

≪ 1

(1)

where 119881 is the velocity S is the Cauchy stress tensor 120583 isthe coefficient of shear viscosity and 120573 and 119888 are the materialconstants We take the velocity and stress as

V (119903) = (

0

0

V) S (119903) =

[

[

119878119903119903

119878119903120579

119878119903119911

119878120579119903

119878120579120579

119878120579119911

119878119911119903

119878119911120579

119878119911119911

]

]

(2)

3 Physical Model

Consider the steady flow of an Eyring-Powell model fluidwith variable temperature dependent viscosity between coax-ial cylindersThemotion is caused due to a constant pressuregradient and by themotion of the inner cylinder parallel to itslength whereas the outer cylinder is kept stationaryThe heattransfer analysis is also taken into accountThe dimensionlessproblem which can describe the flow is

120583

119903

119889V119889119903

+

119872

119903

119889V119889119903

+ 120583

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

120583Γ(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(3)

V (119903) = 1 120579 (119903) = 1 119903 = 1

V (119903) = 0 120579 (119903) = 0 119903 = 119887

(4)

whence

119903 =

119903

119877

Γ =

120583lowast

119881

2

0

119896 (120579119898

minus 120579119908

)

120579 =

(120579 minus 120579119908

)

(120579119898

minus 120579119908

)

119911 =

119881

2

0

119877

2

119888

2

1198621

=

120597119901

120597119911

119872 =

1

120573119888120583lowast

119870 =

119881

2

0

119877

2

119888

2

119861 =

1198621

119877

2

120583lowast

1198810

V =

VV0

120583 =

120583

120583lowast

(5)

where 120583lowast

120579119898

1198810

and Γ are respectively the reference viscos-ity a reference temperature (the bulk mean fluid tempera-ture) and reference velocity Γ is related to the Prandtl numberand Eckert number

4 Series Solutions for Reynoldsrsquo Model

Here the viscosity is expressed in the form

120583 = 119890

minus119875120579 (6)

which by Maclaurinrsquos series can be written as

120583 = 1 minus 119875120579 + 119874 (120579

2

) (7)

Note that119872 = 0 corresponds to the case of constant viscosityInvoking the above equation into (3) one has

119872

119903

119889V119889119903

+

1

119903

119889V119889119903

minus

119875120579

119903

119889V119889119903

+

119889

2V119889119903

2

minus 119875120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

Γ(

119889V119889119903

)

2

minus Γ119875120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(8)

For HAM solution we choose the following initial guesses

V0

(119903) =

(119903 minus 119887)

(1 minus 119887)

1205790

(119903) =

(119903 minus 119887)

(1 minus 119887)

(9)

The auxiliary linear operators are in the form

poundV119903 (V) = V10158401015840 (10)

pound120579119903

(120579) = 120579

10158401015840 (11)

which satisfy

LV119903 (1198601 + 1198611

119903) = 0 L120579119903

(1198602

+ 1198612

119903) = 0 (12)

where 1198601

1198602

1198611

and 1198612

are the constantsIf 119901 isin [0 1] is an embedding parameter and ℎV and ℎ

120579

areauxiliary parameters then the problems at the zero and 119898thorder are respectively given by

(1 minus 119901)LV [V (119903 119901) minus V0

(119903)] = 119901ℎV119873V [V (119903 119901) 120579 (119903 119901)]

(13)

(1 minus 119901)L120579

[120579 (119903 119901) minus 1205790

(119903)] = 119901ℎ120579

119873120579

[V (119903 119901) 120579 (119903 119901)]

(14)

LV [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℎV119877V (119903) (15)

L120579

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℎ120579

119877120579

(119903) (16)

V (119903 119901) = 120579 (119903 119901) = 1 119903 = 1 (17)

V (119903 119901) = 120579 (119903 119901) = 0 119903 = 119887 (18)

The boundary conditions at the 119898th order are

V119898

(119903 119901) = 120579119898

(119903 119901) = 0 119903 = 1

V119898

(119903 119901) = 120579119898

(119903 119901) = 0 119903 = 119887

(19)

Chinese Journal of Engineering 3

In (11)ndash(13)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119875120579

119903

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119889

2V119889119903

2

minus 119875120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ119875120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

(20)

119877V = minus

119875

119903

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+ V10158401015840119898minus1

minus 119875

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119877120579

= Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119875

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(21)

By Mathematica the solutions of (21) can be written as

V119898

(119903) =

3119898

sum

119899=0

119886119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889119898119899

119903

119899

119898 ge 0

(22)

where 119886119898119899

and 119889119898119899

are constants which can be determinedon substituting (22) into (15) and (16)

5 Series Solutions for Vogelrsquos Model

Here

120583 = 120583lowast

exp [

119860

(119905 + 120579)

minus 120579119908

] (23)

0

minus02

minus04

minus06

minus08

minus12 minus1 minus08 minus06 minus04 minus02 0

V998400998400

h

Γ = 01 K = 01M = 01 P = 001 and B = minus1

Figure 1 ℎ-curve for Reynoldsrsquo model for velocity profile

15

125

1

075

05

025

0 02 04 06 08 1 12 14

Q998400998400

h

Γ = 01 K = 01M = 01 P = 001 and B = minus1

Figure 2 ℎ-curve for Reynoldsrsquo model for temperature profile

V998400998400

h

3

2

1

minus1

minus2

minus2 minus15 minus1 minus05 0

0

Γ = 01 K = 01M = 01 s = minus01 A = 00001 t = 01 and B = minus01

Figure 3 ℎ-curve for Vogelrsquos model for velocity profile

which by Maclaurinrsquos series reduces to

120583 =

119861

119904

(1 minus

119860120579

119905

2

) (24)

4 Chinese Journal of EngineeringQ998400998400

h

175

125

15

1

075

05

025

0 02 04 06 08 1 12

B = minus01 q = minus01M = 01 A = 01 s = 01

Γ = 01 t = 01 z = 01 and u = 01

Figure 4 ℎ-curve for Vogelrsquos model for temperature profile

B = 100

B = 105

B = 110

40

30

20

10

0

Q(r)

1 12 14 16 18 2

r

Γ = 01 K = 01M = 01 and P = 001

Figure 5 Temperature profile for Reynoldsrsquo model for differentvalues of 119861

r

1

08

06

04

02

1 12 14 16 18 2

V(r)

B = minus1

B = minus2

B = minus3

Γ = 01 K = 01M = 01 and P = 001

Figure 6 Velocity profile for Reynoldsrsquo model for different values of119861

r

1

08

06

04

02

V(r)

1 12 14 16 18 2

P = 010

P = 020

P = 030

B = minus1 K = 01M = 01 and Γ = 01

Figure 7 Velocity profile for Reynoldsrsquo model for different values of119875

r

1

08

06

04

02

Q(r)

Γ = minus1Γ = minus2

Γ = minus3

1 12 14 16 18 2

B = minus1 K = 01M = 01 and P = 001

Figure 8 Temperature profile for Reynoldsrsquo model for differentvalues of Γ

Invoking the above expressions (1) become

minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(25)

Chinese Journal of Engineering 5

r

Q(r)

1

08

06

04

02

1 12 14 16 18 2

t = 00065t = 00070

t = 00085

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 9 Temperature profile for Vogelrsquos model for different valuesof 119905

t = 00083

t = 00084

t = 00085

12

1

08

06

04

02

1 12 14 16 18 2

V(r)

r

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 10 Velocity profile for Vogelrsquos model for different values of 119905

With the following initial guesses and auxiliary linear opera-tors

V0V (119903) =

(119903 minus 119887)

(1 minus 119887)

1205790V (119903) =

(119903 minus 119887)

(1 minus 119887)

poundVV (V) = V10158401015840 pound120579V (120579) = 120579

10158401015840

(26)

Γ = minus100

Γ = minus200Γ = minus300

1

08

06

04

02

1 12 14 16 18 2

Q(r)

r

B = minus01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 11 Temperature profile for Vogelrsquos model for different valuesof Γ

the 119898th-order deformation problems are

poundV119903 [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℏV119877V119903 (119903)

pound120579119903

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℏ120579

119877120579119903

(119903)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861

119903119904119905

2

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+

119861

119904

V10158401015840119898minus1

minus

119860119861

119904119905

2

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

6 Chinese Journal of EngineeringV(r)

r

3

25

2

15

1

05

1 12 14 16 18 2

s = 300

s = 500

s = 900

Γ = 01 K = 01M = 01 B = minus01 A = 00001 and t = 01

Figure 12 Velocity profile for Vogelrsquos model for different values of119904

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

V1015840119896

minus Γ

119860119861

119904119905

2

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(27)

The expressions of V119898

and 120579119898

are finally given by

V119898

(119903) =

3119898

sum

119899=0

119886

1015840

119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889

1015840

119898119899

119903

119899

119898 ge 0

(28)

6 Graphical Results and Discussion

In order to report the convergence of the obtained seriessolutions and the effects of sundry parameters in the present

1

08

06

04

02

1 12 14 16 18 2

r

V(r)

B = minus011

B = minus012B = minus013

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 13 Velocity profile for Vogelrsquos model for different values of119861

investigation we plotted Figures 1ndash13 Figures 1ndash4 are pre-pared to see the convergence region Figures 1 and 2 cor-respond to Reynoldsrsquo model whereas Figures 3 and 4 relateto Vogelrsquos model Figure 5 shows the temperature variationfor different values of 119861 for Reynoldsrsquo model It can be seenthat temperature decreases as 119861 increases Figure 6 depictsthe velocity variation for Reynoldsrsquo model for different valuesof 119861 Velocity also decreases as 119861 increases Figure 7 showsthe velocity variation for different values of 119875 for Reynoldsrsquomodel It can be seen that velocity increases as 119875 increasesFigure 8 is plotted in order to see the temperature variationfor Reynoldsrsquomodel for different values of Γ it is depicted thattemperature increases as Γ increases Figures 9ndash13 correspondto Vogelrsquos model Figure 9 depicts temperature variationfor Vogelrsquos model for different values of 119905 It is seen thattemperature increases as 119905 increases Figure 10 shows thevelocity variation for Vogelrsquos model for different values of 119905It is observed that velocity decreases as 119905 increases Figure 11is prepared to observe the temperature variation for Vogelrsquosmodel for different values of Γ It is observed that temperaturedecreases as Γ increases Figure 12 is plotted to see thethe velocity variation for Vogelrsquos model for different valuesof 119904 It is observed that velocity decreases as 119904 increasesFigure 13 depicts the velocity variation for Vogelrsquos model fordifferent values of 119861 It is observed that velocity decreases as119861 increases

7 Conclusions

In this paper we consider the flow of Eyring-Powell modelfluid in the annulus between two cylinders whose viscositydepends upon the temperature We discussed the steadyflow in the annulus due to the motion of inner cylinderand constant pressure gradient In the problem consideredthe flow is found to be remarkedly different from thatfor the incompressible Navier-Stokes fluid with constantviscosity The behavior of pertinent parameters is analyzed

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

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DistributedSensor Networks

International Journal of

Page 3: Research Article Flow of an Eyring-Powell Model Fluid

Chinese Journal of Engineering 3

In (11)ndash(13)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119875120579

119903

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119889

2V119889119903

2

minus 119875120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ119875120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

(20)

119877V = minus

119875

119903

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+ V10158401015840119898minus1

minus 119875

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119877120579

= Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119875

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(21)

By Mathematica the solutions of (21) can be written as

V119898

(119903) =

3119898

sum

119899=0

119886119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889119898119899

119903

119899

119898 ge 0

(22)

where 119886119898119899

and 119889119898119899

are constants which can be determinedon substituting (22) into (15) and (16)

5 Series Solutions for Vogelrsquos Model

Here

120583 = 120583lowast

exp [

119860

(119905 + 120579)

minus 120579119908

] (23)

0

minus02

minus04

minus06

minus08

minus12 minus1 minus08 minus06 minus04 minus02 0

V998400998400

h

Γ = 01 K = 01M = 01 P = 001 and B = minus1

Figure 1 ℎ-curve for Reynoldsrsquo model for velocity profile

15

125

1

075

05

025

0 02 04 06 08 1 12 14

Q998400998400

h

Γ = 01 K = 01M = 01 P = 001 and B = minus1

Figure 2 ℎ-curve for Reynoldsrsquo model for temperature profile

V998400998400

h

3

2

1

minus1

minus2

minus2 minus15 minus1 minus05 0

0

Γ = 01 K = 01M = 01 s = minus01 A = 00001 t = 01 and B = minus01

Figure 3 ℎ-curve for Vogelrsquos model for velocity profile

which by Maclaurinrsquos series reduces to

120583 =

119861

119904

(1 minus

119860120579

119905

2

) (24)

4 Chinese Journal of EngineeringQ998400998400

h

175

125

15

1

075

05

025

0 02 04 06 08 1 12

B = minus01 q = minus01M = 01 A = 01 s = 01

Γ = 01 t = 01 z = 01 and u = 01

Figure 4 ℎ-curve for Vogelrsquos model for temperature profile

B = 100

B = 105

B = 110

40

30

20

10

0

Q(r)

1 12 14 16 18 2

r

Γ = 01 K = 01M = 01 and P = 001

Figure 5 Temperature profile for Reynoldsrsquo model for differentvalues of 119861

r

1

08

06

04

02

1 12 14 16 18 2

V(r)

B = minus1

B = minus2

B = minus3

Γ = 01 K = 01M = 01 and P = 001

Figure 6 Velocity profile for Reynoldsrsquo model for different values of119861

r

1

08

06

04

02

V(r)

1 12 14 16 18 2

P = 010

P = 020

P = 030

B = minus1 K = 01M = 01 and Γ = 01

Figure 7 Velocity profile for Reynoldsrsquo model for different values of119875

r

1

08

06

04

02

Q(r)

Γ = minus1Γ = minus2

Γ = minus3

1 12 14 16 18 2

B = minus1 K = 01M = 01 and P = 001

Figure 8 Temperature profile for Reynoldsrsquo model for differentvalues of Γ

Invoking the above expressions (1) become

minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(25)

Chinese Journal of Engineering 5

r

Q(r)

1

08

06

04

02

1 12 14 16 18 2

t = 00065t = 00070

t = 00085

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 9 Temperature profile for Vogelrsquos model for different valuesof 119905

t = 00083

t = 00084

t = 00085

12

1

08

06

04

02

1 12 14 16 18 2

V(r)

r

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 10 Velocity profile for Vogelrsquos model for different values of 119905

With the following initial guesses and auxiliary linear opera-tors

V0V (119903) =

(119903 minus 119887)

(1 minus 119887)

1205790V (119903) =

(119903 minus 119887)

(1 minus 119887)

poundVV (V) = V10158401015840 pound120579V (120579) = 120579

10158401015840

(26)

Γ = minus100

Γ = minus200Γ = minus300

1

08

06

04

02

1 12 14 16 18 2

Q(r)

r

B = minus01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 11 Temperature profile for Vogelrsquos model for different valuesof Γ

the 119898th-order deformation problems are

poundV119903 [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℏV119877V119903 (119903)

pound120579119903

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℏ120579

119877120579119903

(119903)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861

119903119904119905

2

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+

119861

119904

V10158401015840119898minus1

minus

119860119861

119904119905

2

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

6 Chinese Journal of EngineeringV(r)

r

3

25

2

15

1

05

1 12 14 16 18 2

s = 300

s = 500

s = 900

Γ = 01 K = 01M = 01 B = minus01 A = 00001 and t = 01

Figure 12 Velocity profile for Vogelrsquos model for different values of119904

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

V1015840119896

minus Γ

119860119861

119904119905

2

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(27)

The expressions of V119898

and 120579119898

are finally given by

V119898

(119903) =

3119898

sum

119899=0

119886

1015840

119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889

1015840

119898119899

119903

119899

119898 ge 0

(28)

6 Graphical Results and Discussion

In order to report the convergence of the obtained seriessolutions and the effects of sundry parameters in the present

1

08

06

04

02

1 12 14 16 18 2

r

V(r)

B = minus011

B = minus012B = minus013

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 13 Velocity profile for Vogelrsquos model for different values of119861

investigation we plotted Figures 1ndash13 Figures 1ndash4 are pre-pared to see the convergence region Figures 1 and 2 cor-respond to Reynoldsrsquo model whereas Figures 3 and 4 relateto Vogelrsquos model Figure 5 shows the temperature variationfor different values of 119861 for Reynoldsrsquo model It can be seenthat temperature decreases as 119861 increases Figure 6 depictsthe velocity variation for Reynoldsrsquo model for different valuesof 119861 Velocity also decreases as 119861 increases Figure 7 showsthe velocity variation for different values of 119875 for Reynoldsrsquomodel It can be seen that velocity increases as 119875 increasesFigure 8 is plotted in order to see the temperature variationfor Reynoldsrsquomodel for different values of Γ it is depicted thattemperature increases as Γ increases Figures 9ndash13 correspondto Vogelrsquos model Figure 9 depicts temperature variationfor Vogelrsquos model for different values of 119905 It is seen thattemperature increases as 119905 increases Figure 10 shows thevelocity variation for Vogelrsquos model for different values of 119905It is observed that velocity decreases as 119905 increases Figure 11is prepared to observe the temperature variation for Vogelrsquosmodel for different values of Γ It is observed that temperaturedecreases as Γ increases Figure 12 is plotted to see thethe velocity variation for Vogelrsquos model for different valuesof 119904 It is observed that velocity decreases as 119904 increasesFigure 13 depicts the velocity variation for Vogelrsquos model fordifferent values of 119861 It is observed that velocity decreases as119861 increases

7 Conclusions

In this paper we consider the flow of Eyring-Powell modelfluid in the annulus between two cylinders whose viscositydepends upon the temperature We discussed the steadyflow in the annulus due to the motion of inner cylinderand constant pressure gradient In the problem consideredthe flow is found to be remarkedly different from thatfor the incompressible Navier-Stokes fluid with constantviscosity The behavior of pertinent parameters is analyzed

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

International Journal of

AerospaceEngineeringHindawi Publishing Corporationhttpwwwhindawicom Volume 2014

RoboticsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Active and Passive Electronic Components

Control Scienceand Engineering

Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

International Journal of

RotatingMachinery

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporation httpwwwhindawicom

Journal ofEngineeringVolume 2014

Submit your manuscripts athttpwwwhindawicom

VLSI Design

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Shock and Vibration

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Civil EngineeringAdvances in

Acoustics and VibrationAdvances in

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Electrical and Computer Engineering

Journal of

Advances inOptoElectronics

Hindawi Publishing Corporation httpwwwhindawicom

Volume 2014

The Scientific World JournalHindawi Publishing Corporation httpwwwhindawicom Volume 2014

SensorsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Modelling amp Simulation in EngineeringHindawi Publishing Corporation httpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Chemical EngineeringInternational Journal of Antennas and

Propagation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Navigation and Observation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

DistributedSensor Networks

International Journal of

Page 4: Research Article Flow of an Eyring-Powell Model Fluid

4 Chinese Journal of EngineeringQ998400998400

h

175

125

15

1

075

05

025

0 02 04 06 08 1 12

B = minus01 q = minus01M = 01 A = 01 s = 01

Γ = 01 t = 01 z = 01 and u = 01

Figure 4 ℎ-curve for Vogelrsquos model for temperature profile

B = 100

B = 105

B = 110

40

30

20

10

0

Q(r)

1 12 14 16 18 2

r

Γ = 01 K = 01M = 01 and P = 001

Figure 5 Temperature profile for Reynoldsrsquo model for differentvalues of 119861

r

1

08

06

04

02

1 12 14 16 18 2

V(r)

B = minus1

B = minus2

B = minus3

Γ = 01 K = 01M = 01 and P = 001

Figure 6 Velocity profile for Reynoldsrsquo model for different values of119861

r

1

08

06

04

02

V(r)

1 12 14 16 18 2

P = 010

P = 020

P = 030

B = minus1 K = 01M = 01 and Γ = 01

Figure 7 Velocity profile for Reynoldsrsquo model for different values of119875

r

1

08

06

04

02

Q(r)

Γ = minus1Γ = minus2

Γ = minus3

1 12 14 16 18 2

B = minus1 K = 01M = 01 and P = 001

Figure 8 Temperature profile for Reynoldsrsquo model for differentvalues of Γ

Invoking the above expressions (1) become

minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861 = 0

Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

= 0

(25)

Chinese Journal of Engineering 5

r

Q(r)

1

08

06

04

02

1 12 14 16 18 2

t = 00065t = 00070

t = 00085

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 9 Temperature profile for Vogelrsquos model for different valuesof 119905

t = 00083

t = 00084

t = 00085

12

1

08

06

04

02

1 12 14 16 18 2

V(r)

r

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 10 Velocity profile for Vogelrsquos model for different values of 119905

With the following initial guesses and auxiliary linear opera-tors

V0V (119903) =

(119903 minus 119887)

(1 minus 119887)

1205790V (119903) =

(119903 minus 119887)

(1 minus 119887)

poundVV (V) = V10158401015840 pound120579V (120579) = 120579

10158401015840

(26)

Γ = minus100

Γ = minus200Γ = minus300

1

08

06

04

02

1 12 14 16 18 2

Q(r)

r

B = minus01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 11 Temperature profile for Vogelrsquos model for different valuesof Γ

the 119898th-order deformation problems are

poundV119903 [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℏV119877V119903 (119903)

pound120579119903

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℏ120579

119877120579119903

(119903)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861

119903119904119905

2

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+

119861

119904

V10158401015840119898minus1

minus

119860119861

119904119905

2

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

6 Chinese Journal of EngineeringV(r)

r

3

25

2

15

1

05

1 12 14 16 18 2

s = 300

s = 500

s = 900

Γ = 01 K = 01M = 01 B = minus01 A = 00001 and t = 01

Figure 12 Velocity profile for Vogelrsquos model for different values of119904

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

V1015840119896

minus Γ

119860119861

119904119905

2

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(27)

The expressions of V119898

and 120579119898

are finally given by

V119898

(119903) =

3119898

sum

119899=0

119886

1015840

119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889

1015840

119898119899

119903

119899

119898 ge 0

(28)

6 Graphical Results and Discussion

In order to report the convergence of the obtained seriessolutions and the effects of sundry parameters in the present

1

08

06

04

02

1 12 14 16 18 2

r

V(r)

B = minus011

B = minus012B = minus013

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 13 Velocity profile for Vogelrsquos model for different values of119861

investigation we plotted Figures 1ndash13 Figures 1ndash4 are pre-pared to see the convergence region Figures 1 and 2 cor-respond to Reynoldsrsquo model whereas Figures 3 and 4 relateto Vogelrsquos model Figure 5 shows the temperature variationfor different values of 119861 for Reynoldsrsquo model It can be seenthat temperature decreases as 119861 increases Figure 6 depictsthe velocity variation for Reynoldsrsquo model for different valuesof 119861 Velocity also decreases as 119861 increases Figure 7 showsthe velocity variation for different values of 119875 for Reynoldsrsquomodel It can be seen that velocity increases as 119875 increasesFigure 8 is plotted in order to see the temperature variationfor Reynoldsrsquomodel for different values of Γ it is depicted thattemperature increases as Γ increases Figures 9ndash13 correspondto Vogelrsquos model Figure 9 depicts temperature variationfor Vogelrsquos model for different values of 119905 It is seen thattemperature increases as 119905 increases Figure 10 shows thevelocity variation for Vogelrsquos model for different values of 119905It is observed that velocity decreases as 119905 increases Figure 11is prepared to observe the temperature variation for Vogelrsquosmodel for different values of Γ It is observed that temperaturedecreases as Γ increases Figure 12 is plotted to see thethe velocity variation for Vogelrsquos model for different valuesof 119904 It is observed that velocity decreases as 119904 increasesFigure 13 depicts the velocity variation for Vogelrsquos model fordifferent values of 119861 It is observed that velocity decreases as119861 increases

7 Conclusions

In this paper we consider the flow of Eyring-Powell modelfluid in the annulus between two cylinders whose viscositydepends upon the temperature We discussed the steadyflow in the annulus due to the motion of inner cylinderand constant pressure gradient In the problem consideredthe flow is found to be remarkedly different from thatfor the incompressible Navier-Stokes fluid with constantviscosity The behavior of pertinent parameters is analyzed

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

International Journal of

AerospaceEngineeringHindawi Publishing Corporationhttpwwwhindawicom Volume 2014

RoboticsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Active and Passive Electronic Components

Control Scienceand Engineering

Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

International Journal of

RotatingMachinery

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporation httpwwwhindawicom

Journal ofEngineeringVolume 2014

Submit your manuscripts athttpwwwhindawicom

VLSI Design

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Shock and Vibration

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Civil EngineeringAdvances in

Acoustics and VibrationAdvances in

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Electrical and Computer Engineering

Journal of

Advances inOptoElectronics

Hindawi Publishing Corporation httpwwwhindawicom

Volume 2014

The Scientific World JournalHindawi Publishing Corporation httpwwwhindawicom Volume 2014

SensorsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Modelling amp Simulation in EngineeringHindawi Publishing Corporation httpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Chemical EngineeringInternational Journal of Antennas and

Propagation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Navigation and Observation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

DistributedSensor Networks

International Journal of

Page 5: Research Article Flow of an Eyring-Powell Model Fluid

Chinese Journal of Engineering 5

r

Q(r)

1

08

06

04

02

1 12 14 16 18 2

t = 00065t = 00070

t = 00085

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 9 Temperature profile for Vogelrsquos model for different valuesof 119905

t = 00083

t = 00084

t = 00085

12

1

08

06

04

02

1 12 14 16 18 2

V(r)

r

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and B = minus01

Figure 10 Velocity profile for Vogelrsquos model for different values of 119905

With the following initial guesses and auxiliary linear opera-tors

V0V (119903) =

(119903 minus 119887)

(1 minus 119887)

1205790V (119903) =

(119903 minus 119887)

(1 minus 119887)

poundVV (V) = V10158401015840 pound120579V (120579) = 120579

10158401015840

(26)

Γ = minus100

Γ = minus200Γ = minus300

1

08

06

04

02

1 12 14 16 18 2

Q(r)

r

B = minus01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 11 Temperature profile for Vogelrsquos model for different valuesof Γ

the 119898th-order deformation problems are

poundV119903 [V119898 (119903) minus 120594119898

V119898minus1

(119903)] = ℏV119877V119903 (119903)

pound120579119903

[120579119898

(119903) minus 120594119898

120579119898minus1

(119903)] = ℏ120579

119877120579119903

(119903)

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861120579

119903119904119905

2

119889V119889119903

+

1

119903

119889V119889119903

+

119872

119903

119889V119889119903

+

119861

119904

119889

2V119889119903

2

+ 119872

119889

2V119889119903

2

minus

119860119861

119904119905

2

120579

119889

2V119889119903

2

minus 3119870(

119889V119889119903

)

2

119889

2V119889119903

2

minus

119870

119903

(

119889V119889119903

)

3

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ(

119889V119889119903

)

2

minus Γ

119860119861

119904119905

2

120579(

119889V119889119903

)

2

+ 119872Γ(

119889V119889119903

)

2

minus Γ119870(

119889V119889119903

)

4

minus

1

119903

119889120579

119889119903

minus

119889

2

120579

119889119903

2

119873V [V (119903 119901) 120579 (119903 119901)]

= minus

119860119861

119903119904119905

2

119898minus1

sum

119896=0

V1015840119898minus1minus119896

120579119896

+

1

119903

V1015840119898minus1

+

119872

119903

V1015840119898minus1

+

119861

119904

V10158401015840119898minus1

minus

119860119861

119904119905

2

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

120579119896

+ 119872V10158401015840119898minus1

minus 3119870

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V10158401015840119897

6 Chinese Journal of EngineeringV(r)

r

3

25

2

15

1

05

1 12 14 16 18 2

s = 300

s = 500

s = 900

Γ = 01 K = 01M = 01 B = minus01 A = 00001 and t = 01

Figure 12 Velocity profile for Vogelrsquos model for different values of119904

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

V1015840119896

minus Γ

119860119861

119904119905

2

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(27)

The expressions of V119898

and 120579119898

are finally given by

V119898

(119903) =

3119898

sum

119899=0

119886

1015840

119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889

1015840

119898119899

119903

119899

119898 ge 0

(28)

6 Graphical Results and Discussion

In order to report the convergence of the obtained seriessolutions and the effects of sundry parameters in the present

1

08

06

04

02

1 12 14 16 18 2

r

V(r)

B = minus011

B = minus012B = minus013

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 13 Velocity profile for Vogelrsquos model for different values of119861

investigation we plotted Figures 1ndash13 Figures 1ndash4 are pre-pared to see the convergence region Figures 1 and 2 cor-respond to Reynoldsrsquo model whereas Figures 3 and 4 relateto Vogelrsquos model Figure 5 shows the temperature variationfor different values of 119861 for Reynoldsrsquo model It can be seenthat temperature decreases as 119861 increases Figure 6 depictsthe velocity variation for Reynoldsrsquo model for different valuesof 119861 Velocity also decreases as 119861 increases Figure 7 showsthe velocity variation for different values of 119875 for Reynoldsrsquomodel It can be seen that velocity increases as 119875 increasesFigure 8 is plotted in order to see the temperature variationfor Reynoldsrsquomodel for different values of Γ it is depicted thattemperature increases as Γ increases Figures 9ndash13 correspondto Vogelrsquos model Figure 9 depicts temperature variationfor Vogelrsquos model for different values of 119905 It is seen thattemperature increases as 119905 increases Figure 10 shows thevelocity variation for Vogelrsquos model for different values of 119905It is observed that velocity decreases as 119905 increases Figure 11is prepared to observe the temperature variation for Vogelrsquosmodel for different values of Γ It is observed that temperaturedecreases as Γ increases Figure 12 is plotted to see thethe velocity variation for Vogelrsquos model for different valuesof 119904 It is observed that velocity decreases as 119904 increasesFigure 13 depicts the velocity variation for Vogelrsquos model fordifferent values of 119861 It is observed that velocity decreases as119861 increases

7 Conclusions

In this paper we consider the flow of Eyring-Powell modelfluid in the annulus between two cylinders whose viscositydepends upon the temperature We discussed the steadyflow in the annulus due to the motion of inner cylinderand constant pressure gradient In the problem consideredthe flow is found to be remarkedly different from thatfor the incompressible Navier-Stokes fluid with constantviscosity The behavior of pertinent parameters is analyzed

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

International Journal of

AerospaceEngineeringHindawi Publishing Corporationhttpwwwhindawicom Volume 2014

RoboticsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Active and Passive Electronic Components

Control Scienceand Engineering

Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

International Journal of

RotatingMachinery

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporation httpwwwhindawicom

Journal ofEngineeringVolume 2014

Submit your manuscripts athttpwwwhindawicom

VLSI Design

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Shock and Vibration

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Civil EngineeringAdvances in

Acoustics and VibrationAdvances in

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Electrical and Computer Engineering

Journal of

Advances inOptoElectronics

Hindawi Publishing Corporation httpwwwhindawicom

Volume 2014

The Scientific World JournalHindawi Publishing Corporation httpwwwhindawicom Volume 2014

SensorsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Modelling amp Simulation in EngineeringHindawi Publishing Corporation httpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Chemical EngineeringInternational Journal of Antennas and

Propagation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Navigation and Observation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

DistributedSensor Networks

International Journal of

Page 6: Research Article Flow of an Eyring-Powell Model Fluid

6 Chinese Journal of EngineeringV(r)

r

3

25

2

15

1

05

1 12 14 16 18 2

s = 300

s = 500

s = 900

Γ = 01 K = 01M = 01 B = minus01 A = 00001 and t = 01

Figure 12 Velocity profile for Vogelrsquos model for different values of119904

minus

119870

119903

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897

minus 119861

119873120579

[V (119903 119901) 120579 (119903 119901)]

= Γ

119898minus1

sum

119896=0

V10158401015840119898minus1minus119896

V1015840119896

minus Γ

119860119861

119904119905

2

119898minus1

sum

119896=0

119896

sum

119897=0

V1015840119898minus1minus119896

V1015840119896minus119897

120579

1015840

119897

+ 119872Γ

119898minus1

sum

119896=0

V1015840119898minus1minus119896

V1015840119896

minus Γ119870

119898minus1

sum

119896=0

119896

sum

119897=0

119897

sum

119904=0

V1015840119898minus1minus119896

V1015840119896minus119897

V1015840119897minus119904

V1015840119904

minus

1

119903

120579

1015840

119898minus1

minus 120579

10158401015840

119898minus1

(27)

The expressions of V119898

and 120579119898

are finally given by

V119898

(119903) =

3119898

sum

119899=0

119886

1015840

119898119899

119903

119899

119898 ge 0

120579119898

(119903) =

3119898+1

sum

119899=0

119889

1015840

119898119899

119903

119899

119898 ge 0

(28)

6 Graphical Results and Discussion

In order to report the convergence of the obtained seriessolutions and the effects of sundry parameters in the present

1

08

06

04

02

1 12 14 16 18 2

r

V(r)

B = minus011

B = minus012B = minus013

Γ = 01 K = 01M = 01 s = minus01 A = 00001 and t = 01

Figure 13 Velocity profile for Vogelrsquos model for different values of119861

investigation we plotted Figures 1ndash13 Figures 1ndash4 are pre-pared to see the convergence region Figures 1 and 2 cor-respond to Reynoldsrsquo model whereas Figures 3 and 4 relateto Vogelrsquos model Figure 5 shows the temperature variationfor different values of 119861 for Reynoldsrsquo model It can be seenthat temperature decreases as 119861 increases Figure 6 depictsthe velocity variation for Reynoldsrsquo model for different valuesof 119861 Velocity also decreases as 119861 increases Figure 7 showsthe velocity variation for different values of 119875 for Reynoldsrsquomodel It can be seen that velocity increases as 119875 increasesFigure 8 is plotted in order to see the temperature variationfor Reynoldsrsquomodel for different values of Γ it is depicted thattemperature increases as Γ increases Figures 9ndash13 correspondto Vogelrsquos model Figure 9 depicts temperature variationfor Vogelrsquos model for different values of 119905 It is seen thattemperature increases as 119905 increases Figure 10 shows thevelocity variation for Vogelrsquos model for different values of 119905It is observed that velocity decreases as 119905 increases Figure 11is prepared to observe the temperature variation for Vogelrsquosmodel for different values of Γ It is observed that temperaturedecreases as Γ increases Figure 12 is plotted to see thethe velocity variation for Vogelrsquos model for different valuesof 119904 It is observed that velocity decreases as 119904 increasesFigure 13 depicts the velocity variation for Vogelrsquos model fordifferent values of 119861 It is observed that velocity decreases as119861 increases

7 Conclusions

In this paper we consider the flow of Eyring-Powell modelfluid in the annulus between two cylinders whose viscositydepends upon the temperature We discussed the steadyflow in the annulus due to the motion of inner cylinderand constant pressure gradient In the problem consideredthe flow is found to be remarkedly different from thatfor the incompressible Navier-Stokes fluid with constantviscosity The behavior of pertinent parameters is analyzed

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

International Journal of

AerospaceEngineeringHindawi Publishing Corporationhttpwwwhindawicom Volume 2014

RoboticsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Active and Passive Electronic Components

Control Scienceand Engineering

Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

International Journal of

RotatingMachinery

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporation httpwwwhindawicom

Journal ofEngineeringVolume 2014

Submit your manuscripts athttpwwwhindawicom

VLSI Design

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Shock and Vibration

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Civil EngineeringAdvances in

Acoustics and VibrationAdvances in

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Electrical and Computer Engineering

Journal of

Advances inOptoElectronics

Hindawi Publishing Corporation httpwwwhindawicom

Volume 2014

The Scientific World JournalHindawi Publishing Corporation httpwwwhindawicom Volume 2014

SensorsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Modelling amp Simulation in EngineeringHindawi Publishing Corporation httpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Chemical EngineeringInternational Journal of Antennas and

Propagation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Navigation and Observation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

DistributedSensor Networks

International Journal of

Page 7: Research Article Flow of an Eyring-Powell Model Fluid

Chinese Journal of Engineering 7

and depicted through graphs Using usual similarity transfor-mations the governing equations have been transformed intonon-linear ordinary differential equations The highly non-linear problem is then solved by homotopy analysis methodEffects of the various parameters on velocity and temperatureprofiles are examined

Conflict of Interests

The authors declare that there is no conflict of interestsregarding the publication of this paper

References

[1] R S Rivlin and J L Ericksen ldquoStress deformation relations forisotropic materialsrdquo Rational Mechanics and Analysis Journalvol 4 pp 323ndash425 1955

[2] C Truesdell and W Noll The Non-Linear Field Theories ofMechanics Springer New York NY USA 2nd edition 1992

[3] K R Rajagopal ldquoA note on unsteady unidirectional flows ofa non-Newtonian fluidrdquo International Journal of Non-LinearMechanics vol 17 no 5-6 pp 369ndash373 1982

[4] K R Rajagopal and A S Gupta ldquoAn exact solution for theflow of a non-newtonian fluid past an infinite porous platerdquoMeccanica vol 19 no 2 pp 158ndash160 1984

[5] K R Rajagopal and R K Bhatnagar ldquoExact solutions for somesimple flows of an Oldroyd-B fluidrdquo Acta Mechanica vol 113no 1ndash4 pp 233ndash239 1995

[6] K R Rajagopal ldquoOn the creeping flow of the second-orderfluidrdquo Journal of Non-Newtonian Fluid Mechanics vol 15 no2 pp 239ndash246 1984

[7] K R Rajagopal ldquoLongitudinal and torsional oscillations of arod in a non-Newtonian fluidrdquoActaMechanica vol 49 no 3-4pp 281ndash285 1983

[8] A M Benharbit and A M Siddiqui ldquoCertain solutions of theequations of the planarmotion of a second grade fluid for steadyand unsteady casesrdquo Acta Mechanica vol 94 no 1-2 pp 85ndash961992

[9] T Hayat S Asghar and A M Siddiqui ldquoPeriodic unsteadyflows of a non-Newtonian fluidrdquo Acta Mechanica vol 131 no3-4 pp 169ndash175 1998

[10] A M Siddiqui T Hayat and S Asghar ldquoPeriodic flows of anon-Newtonian fluid between two parallel platesrdquo InternationalJournal of Non-Linear Mechanics vol 34 no 5 pp 895ndash8991999

[11] T Hayat S Asghar and A M Siddiqui ldquoOn the moment of aplane disk in a non-Newtonian fluidrdquo Acta Mechanica vol 136no 3 pp 125ndash131 1999

[12] T Hayat S Asghar and A M Siddiqui ldquoSome unsteadyunidirectional flows of a non-Newtonian fluidrdquo InternationalJournal of Engineering Science vol 38 no 3 pp 337ndash346 2000

[13] M Massoudi and I Christie ldquoEffects of variable viscosity andviscous dissipation on the flow of a third grade fluid in a piperdquoInternational Journal of Non-LinearMechanics vol 30 no 5 pp687ndash699 1995

[14] T Hayat R Ellahi and S Asghar ldquoThe influence of variableviscosity and viscous dissipation on the non-Newtonian flowan analytical solutionrdquo Communications in Nonlinear Scienceand Numerical Simulation vol 12 no 3 pp 300ndash313 2007

[15] M Yurusoy and M Pakdermirli ldquoApproximate analytical solu-tions for flow of a third grade fluid in a piperdquo InternationalJournal ofNon-LinearMechanics vol 37 no 2 pp 187ndash195 2002

[16] M Pakdemirli and B S Yilbas ldquoEntropy generation for pipeflow of a third grade fluid with Vogel model viscosityrdquo Interna-tional Journal of Non-Linear Mechanics vol 41 no 3 pp 432ndash437 2006

[17] S Nadeem and M Ali ldquoAnalytical solutions for pipe flow ofa fourth grade fluid with Reynold and Vogelrsquos models of vis-cositiesrdquo Communications in Nonlinear Science and NumericalSimulation vol 14 no 5 pp 2073ndash2090 2009

[18] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[19] S Nadeem and N S Akbar ldquoEffects of temperature dependentviscosity on peristaltic flow of a Jeffrey-six constant fluid ina non-uniform vertical tuberdquo Communications in NonlinearScience andNumerical Simulation vol 15 no 12 pp 3950ndash39642010

[20] M Y Malik A Hussain and S Nadeem ldquoAnalytical treatmentof an oldroyd 8-constant fluid between coaxial cylinders withvariable viscosityrdquo Communications in Theoretical Physics vol56 no 5 pp 933ndash938 2011

[21] S Nadeem T Hayat S Abbasbandy and M Ali ldquoEffects ofpartial slip on a fourth-grade fluid with variable viscosity ananalytic solutionrdquo Nonlinear Analysis Real World Applicationsvol 11 no 2 pp 856ndash868 2010

[22] M Y Malik A Hussain S Nadeem and T Hayat ldquoFlow ofa third grade fluid between coaxial cylinders with variableviscosityrdquo Zeitschrift fur Naturforschung A vol 64 no 9-10 pp588ndash596 2009

[23] S J Liao Beyond Perturbation Introduction to HomotopyAnalysis Method CRC Press Boca Raton Fla USA 2003

[24] S J Liao ldquoOn the homotopy analysis method for nonlinearproblemsrdquo Applied Mathematics and Computation vol 147 no2 pp 499ndash513 2004

[25] S J Liao ldquoAn analytic solution of unsteady boundary-layerflows caused by an impulsively stretching platerdquo Communica-tions in Nonlinear Science and Numerical Simulation vol 11 no3 pp 326ndash339 2006

[26] S Abbasbandy ldquoThe application of homotopy analysis methodto nonlinear equations arising in heat transferrdquo Physics LettersA vol 360 no 1 pp 109ndash113 2006

[27] S Abbasbandy ldquoHomotopy analysis method for heat radiationequationsrdquo International Communications in Heat and MassTransfer vol 34 no 3 pp 380ndash387 2007

[28] S Abbasbandy Y Tan and S J Liao ldquoNewton-homotopyanalysis method for nonlinear equationsrdquo Applied Mathematicsand Computation vol 188 no 2 pp 1794ndash1800 2007

International Journal of

AerospaceEngineeringHindawi Publishing Corporationhttpwwwhindawicom Volume 2014

RoboticsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Active and Passive Electronic Components

Control Scienceand Engineering

Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

International Journal of

RotatingMachinery

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporation httpwwwhindawicom

Journal ofEngineeringVolume 2014

Submit your manuscripts athttpwwwhindawicom

VLSI Design

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Shock and Vibration

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Civil EngineeringAdvances in

Acoustics and VibrationAdvances in

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Electrical and Computer Engineering

Journal of

Advances inOptoElectronics

Hindawi Publishing Corporation httpwwwhindawicom

Volume 2014

The Scientific World JournalHindawi Publishing Corporation httpwwwhindawicom Volume 2014

SensorsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Modelling amp Simulation in EngineeringHindawi Publishing Corporation httpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Chemical EngineeringInternational Journal of Antennas and

Propagation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Navigation and Observation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

DistributedSensor Networks

International Journal of

Page 8: Research Article Flow of an Eyring-Powell Model Fluid

International Journal of

AerospaceEngineeringHindawi Publishing Corporationhttpwwwhindawicom Volume 2014

RoboticsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Active and Passive Electronic Components

Control Scienceand Engineering

Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

International Journal of

RotatingMachinery

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporation httpwwwhindawicom

Journal ofEngineeringVolume 2014

Submit your manuscripts athttpwwwhindawicom

VLSI Design

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Shock and Vibration

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Civil EngineeringAdvances in

Acoustics and VibrationAdvances in

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Electrical and Computer Engineering

Journal of

Advances inOptoElectronics

Hindawi Publishing Corporation httpwwwhindawicom

Volume 2014

The Scientific World JournalHindawi Publishing Corporation httpwwwhindawicom Volume 2014

SensorsJournal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Modelling amp Simulation in EngineeringHindawi Publishing Corporation httpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Chemical EngineeringInternational Journal of Antennas and

Propagation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

Navigation and Observation

International Journal of

Hindawi Publishing Corporationhttpwwwhindawicom Volume 2014

DistributedSensor Networks

International Journal of