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Journal of the Association of Arab Universities for Basic

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ISSN: 1815-3852 (Print) (Online) Journal homepage: https://www.tandfonline.com/loi/tabs19

Semi-analytical investigation on micropolar fluid

flow and heat transfer in a permeable channel

using AGM

H. Mirgolbabaee, S.T. Ledari & D.D. Ganji

To cite this article:

H. Mirgolbabaee, S.T. Ledari & D.D. Ganji (2017) Semi-analytical investigation

on micropolar fluid flow and heat transfer in a permeable channel using AGM, Journal of the

Association of Arab Universities for Basic and Applied Sciences, 24:1, 213-222, DOI: 10.1016/

j.jaubas.2017.01.002

To link to this article: https://doi.org/10.1016/j.jaubas.2017.01.002

© 2017 University of Bahrain Published online: 27 Mar 2018.

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Semi-analytical investigation on micropolar fluid

flow and heat transfer in a permeable channel using

AGM

H. Mirgolbabaee

*

, S.T. Ledari, D.D. Ganji

Department of Mechanical Engineering, Babol Noshirvani University of Technology, P.O. Box 484, Babol, Iran

Received 16 July 2016; revised 29 November 2016; accepted 15 January 2017 Available online 21 February 2017

KEYWORDS Akbari–Ganji’s Method (AGM); Heat transfer; Mass transfer; Micropolar fluid; Permeable channel

Abstract In this paper, micropolar fluid flow and heat transfer in a permeable channel have been investigated. The main aim of this study is based on solving the nonlinear differential equation of heat and mass transfer of the mentioned problem by utilizing a new and innovative method in semi-analytical field which is called Akbari–Ganji’s Method (AGM). Results have been compared with numerical method (Runge–Kutte 4th) in order to achieve conclusions based on not only accuracy and efficiency of the solutions but also simplicity of the taken procedures which would have remark-able effects on the time devoted for solving processes.

Results are presented for different values of parameters such as: Reynolds number, micro rota-tion/angular velocity and Peclet number in which the effects of these parameters are discussed on the flow, heat transfer and concentration characteristics. Also relation between Reynolds and Peclet numbers with Nusselts and Sherwood numbers would found for both suction and injection

Furthermore, due to the accuracy and convergence of obtained solutions, it will be demonstrating that AGM could be applied through other nonlinear problems even with high nonlinearity.

Ó 2017 University of Bahrain. Publishing services by Elsevier B.V. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).

1. Introduction

Micropolar fluids are fluids with microstructure. They belong to a class of fluids with nonsymmetrical stress tensor that we shall call polar fluids, which could be mentioned as the well-established Navier–Stokes model of classical fluids. These flu-ids respond to micro-rotational motions and spin inertia and therefore, can support couple stress and distributed body

cou-ples. Physically, a micropolar fluid is one which contains sus-pensions of rigid particles. The theory of micropolar fluids was first formulated byEringen (1966). Examples of industri-ally relevant flows that can be studied with accordance to this theory include flow of low concentration suspensions, liquid crystals, blood, lubrication and so on. The micropolar theory has recently been applied and considered in different aspects of sciences and engineering applications. For instance,Gorla (1989), Gorla (1988), Gorla (1992) and Arafa and Gorla (1992)have considered the free and mixed convection flow of a micropolar fluid from flat surfaces and cylinders. Raptis (2000) studied boundary layer flow of a micropolar fluid through a porous medium by using the generalized Darcy * Corresponding author.

E-mail addresses:hadi.mirgolbabaee@gmail.com,h.mirgolbabaee@ stu.nit.ac.ir(H. Mirgolbabaee).

Peer review under responsibility of University of Bahrain.

Journal of the Association of Arab Universities for Basic and Applied Sciences (2017) 24, 213–222

University of Bahrain

Journal of the Association of Arab Universities for

Basic and Applied Sciences

www.elsevier.com/locate/jaaubas

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http://dx.doi.org/10.1016/j.jaubas.2017.01.002

1815-3852Ó 2017 University of Bahrain. Publishing services by Elsevier B.V.

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law. The influence of a chemical reaction and thermal radia-tion on the heat and mass transfer in MHD micropolar flow over a vertical moving plate in a porous medium with heat gen-eration was studied byMohamed and Abo-Dahab (2009).

It would be worthy to mention the fact that many scientists and researchers all around the world are working on the effects of using micropolar fluids and nanofluids on flow and heat transfer problems (Kelson and Desseaux, 2001; Sheikholeslami et al., 2016a,b; Rashidi et al., 2011; Sheikholeslami et al., 2015; Turkyilmazoglu, 2014c; Turkyilmazoglu, 2016b) which will lead to suitable perspective for future industrial and research applications such as: phar-maceutical processes, hybrid-powered engines, heat exchangers and so on.

In many engineering problems solving procedures will finally lead to whether mathematical formulation or model-ing processes. For obtainmodel-ing better understandmodel-ing in both of these factors, many researchers from different fields devote their time to expand relevant knowledge. As one of the most important type of these knowledge, we could men-tion analytical, semi-analytical methods and numerical tech-nics in solving nonlinear differential equations. By utilizing analytical and semi-analytical methods, solutions for each problem will approach to a unique function. Most of the heat transfer and fluid mechanics problems would engage with nonlinear equation which finding accurate and efficient solutions for these problem have been considered by many researchers recently. Therefore, for the purpose of achieving the mentioned facts, many researchers have tried to reach acceptable solution for these equations due to their nonlin-earity by utilizing analytical and semi-analytical methods such as: Perturbation Method byGanji et al. (2007), Homo-topy Perturbation Method by Turkyilmazoglu (2012), Sheikholeslami et al. (2013) and Mirgolbabaei et al. (2009), Variational Iteration Method by Turkyilmazoglu (2016a), Mirgolbabaei et al. (2009) and Samaee et al. (2015), Homo-topy Analysis Method by Sheikholeslami et al. (2014), Sheikholeslami et al. (2012) and Turkyilmazoglu (2011), Parameterized Perturbation Method (PPM) by Ashorynejad et al. (2014), Collocation Method (CM) by Hoshyar et al. (2015), Adomian Decomposition Method by Sheikholeslami et al. (2013), Least Square Method (LSM) by Fakour et al. (2014), Galerkin Method (GM) by Turkyilmazoglu (2014a,b)so on.

Its noteworthy to mentioned the fact that Semi-Analytical methods could be categorized into two perspectives due to their solving procedures as for simplicity we would call them as: Iterate-Base Method and Trial Function-Base Method. In Iterate-Base Method such as: HPM, VIM, ADM and etc., the important factor which affect the solving procedures is number of iterations. Although in this methods we may assume a trial functions, which are based on our in depended functions, however, in order to achieve solution in each step we have to solve previous steps at first. According to mentioned explanations, it’s obvious that whilst the iteration results in higher steps can’t be obtain by related software, we will face problem which will interrupt our solving procedures. Also these methods usually take more time for obtaining solutions. In Trial Function-Base Method such as: CM, LSM, Akbari– Ganji’s Method (AGM) and etc., the main factor which affect the solving procedures is trial function. In this methods we will assume an efficient trial function base on the problem’s

bound-ary and initial conditions which contains different constant coefficients. Afterward, due to the basic idea of each method, we are obligated for solving the constant coefficients. In most cases the constant coefficients will be obtain easily by solving set of polynomials. Although in these methods, number of terms in our trial function could be referred as needed itera-tions, however, it’s essential to mention the fact that utilized constants will obtain simultaneously in solving procedures. So in these methods the iteration problems have been eliminated.

In this article attempts have been made in order to obtain approximate solutions of the governing nonlinear differential equations of micropolar fluid flow. We have utilized a new and innovative semi-analytical method calling Akbari–Ganji’s Method which is developed by Akbari and Ganji by Akbari et al. (2014) and Rostami et al. (2014)in 2014 for the first time. Since then this method has been investigated by many authors to solve highly nonlinear equations in different aspects of engi-neering problems such as: Fluid Mechanics, Nonlinear Vibra-tion Problems, Heat Transfer ApplicaVibra-tions, Nanofluids and etc. Some of the excellence of proposed method could be referred as Ledari et al. (2015) and Mirgolbabaee et al. (2016a,b).

Due to recently achievements from this method and also the Trial Function-Base characteristics of this method, it could precisely conclude that AGM has high efficiency and accuracy for solving nonlinear problems with high nonlinear-ity. It is necessary to mention that a summary of the excel-lence of this method in comparison with the other approaches can be considered as follows: Boundary condi-tions are needed in accordance with the order of differential equations in the solution procedure but when the number of boundary conditions is less than the order of the differential equation, this approach can create additional new boundary conditions in regard to the own differential equation and its derivatives.

2. Mathematical formulation

We consider the steady laminar flow of a micropolar fluid along a two-dimensional channel with parallel porous walls through which fluid is uniformly injected or removed with speed v0which is represented inFig. 1. The geometry of

prob-lem has defined clearly inFig. 1. By utilizing Cartesian coordi-nates, the governing equations for flow areSibanda and Awad (2010): @u @xþ @v @y¼ 0 ð1Þ q u @u @xþ v @u @y   ¼ @P @xþ l þ jð Þ @2 u @x2þ @2 u @2 y   þ j@N @y ð2Þ q u @v @xþ v @v @y   ¼ @P@xþ ðl þ jÞ @ 2 v @x2þ @2 v @2 y    j@N@x ð3Þ q u @N @xþ v @N @y   ¼ j j 2Nþ @u @y @v @x   þ ts j   @2 N @x2 þ @2 N @2y   ð4Þ

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q u @T @xþ v @T @y   ¼k1 cp @2 T @y2 ð5Þ q u @C @xþ v @C @y   ¼ D@2C @y2 ð6Þ

wherets¼ ðl þk2Þ. Also due to the fact that we have defined

the constants in Eqs.(1)–(7) in the nomenclature section, so we have refused to announce these again for the purpose of celerity and brevity. The appropriate boundary conditions are:

y¼ h ) v ¼ u ¼ 0; n ¼ s@u@y y¼ þh ) v ¼ 0; u ¼v0x h ; n ¼ v0x h2 ð7Þ

where s is a boundary parameter and declare the degree to which the microelements are free to rotate near channel walls. The case s= 0 represents non rotatable concentrated microelements close to the wall. Also s = 0.5 represents weak concentrations and the vanishing of the antisymmetric part of the stress tensor and s = 1 represents turbulent flow. We intro-duce the following dimensionless variables:

g ¼y h; w ¼ v0xfðgÞ; N ¼ v0x h2 gðgÞ; hðgÞ ¼TT2 T1T2; /ðgÞ ¼ CC2 C1C2 ð8Þ

where T2= T1– Ax;, C2= C1 Bx with A and B as

con-stants. The stream function is defined as its original form as follows:

u¼@w

@y; v ¼  @w

@x ð9Þ

Eqs.(1)–(7)will reduce to the following coupled system of nonlinear differential equations:

ð1 þ N1ÞfIV N1g Reðff000 f0f00Þ ¼ 0 ð10Þ N2g00 N1ðf00 2gÞ  N3Reðfg0 f0gÞ ¼ 0 ð11Þ h00þ Pe hðf0h  fh0Þ ¼ 0 ð12Þ /00þ Pe mðf0/  f/0Þ ¼ 0 ð13Þ

Which the boundary conditions are listed as follows: g ¼ 1 ) f ¼ f0¼ g ¼ 0; h ¼ / ¼ 1

g ¼ þ1 ) f ¼ h ¼ / ¼ 0; f0¼ 1; g ¼ 1 ð14Þ

The parameters of primary interests are the buoyancy ratio N, the Peclet numbers for the diffusion of heat Pehand mass

Pemrespectively, the Reynolds number Re where for suction

Re > 0 and for injection Re < 0 also Grashof number Gr given by: N1¼ j l ;N2¼ ts lh2; N3¼ j h2; Re ¼ v0 th Pr¼tqcp k1 ; Sc ¼ t D; Gr ¼ gbTAh 4 t2 Peh¼ Pr Re; Pem¼ Sc Re ð15Þ

where Pr is the Prandtl number, Sc is the generalized Schmidt number, N1 is the coupling parameter and N2 is the

spin-gradient viscosity parameter. In technological processes, Nus-selt and Sherwood numbers are being considered widely which are defined as follows:

Nux¼ q00y¼hx ðT1 T2Þk1 ¼ h0ð1Þ ð16Þ Shx¼ m00y¼hx ðC1 C2ÞD ¼ /0ð1Þ ð17Þ

where q00and m00are local heat flux and mass flux respectively. 3. Basic idea of Akbari–Ganji’s method (AGM)

Physics of the problems in every fields of engineering sciences lead to set of linear or nonlinear differential equations as its gov-erning equations. According to physics of these problems and their obtained mathematical formulation, sufficient boundary or initial conditions should be applied in order to achieve solu-tion for considered problems. Since procedures of applying ana-lytical methods for obtaining solution of linear and nonlinear differential equations are not an exception from mentioned fact, so we could recognize the importance of these boundary and ini-tial conditions in determining the accuracy and efficiency of analytical methods in achieving acceptable solution due to phy-sic of problems. In order to comprehend the given method in this paper, the entire process has been declared clearly.

In accordance with the boundary conditions, the general manner of a differential equation is as follows:

pk: f u; u0; u00; . . . ; uðmÞ

 

¼ 0; u ¼ uðxÞ ð18Þ

The nonlinear differential equation of p which is a function of u, the parameter u which is a function of x and their deriva-tives are considered as follows:

Boundary conditions: uðxÞ ¼ u0; u0ðxÞ ¼ u1; . . . ; uðm1ÞðxÞ ¼ um1 at x¼ 0 uðxÞ ¼ uL0; u 0ðxÞ ¼ u L1; . . . ; u ðm1ÞðxÞ ¼ u Lm1 at x¼ L ( ð19Þ Fig. 1 (a) Geometry of the problem (b) x y view.

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To solve the first differential equation with respect to the boundary conditions in x = L in Eq.(19), the series of letters in the nth order with constant coefficients which we assume as the solution of the first differential equation is considered as follows:

uðxÞ ¼X

n

i¼0

aixi¼ a0þ a1x1þ a2x2þ    þ anxn ð20Þ

The more choice of series sentences from Eq. (20) cause more precise solution for Eq.(18). For obtaining solution of differential Eq.(18)regarding the series from degree (n), there are (n + 1) unknown coefficients that need (n + 1) equations to be specified. The boundary conditions of Eq.(19)are used to solve a set of equations which is consisted of (n + 1) ones. 3.1. Applying the boundary conditions

(a) The application of the boundary conditions for the answer of differential Eq.(20)is in the form of:

When x = 0: uð0Þ ¼ a0¼ u0 u0ð0Þ ¼ a1¼ u1 u00ð0Þ ¼ a2¼ u2 ... ... ... 8 > > > > < > > > > : ð21Þ And when x = L: uðLÞ ¼ a0þ a1Lþ a2L2þ    þ anLn¼ uL0 u0ðLÞ ¼ a1þ 2a2Lþ 3a3L2þ    þ nanLn1¼ uL1 u00ðLÞ ¼ 2a2þ 6a3Lþ 12a4L2þ    þ nðn  1ÞanLn2¼ uLm1 ... ... ... ... ... ... 8 > > > > < > > > > : ð22Þ (b) After substituting Eq.(22)into Eq.(18), the application of the boundary conditions on differential Eq. (18) is done according to the following procedure:

p0: fðuð0Þ; u0ð0Þ; u00ð0Þ; . . . ; uðmÞð0ÞÞ p1: fðuðLÞ; u0ðLÞ; u00ðLÞ; . . . ; uðmÞðLÞÞ

... ... ... ... ...

ð23Þ

With regard to the choice of n; (n < m) sentences from Eq.

(20)and in order to make a set of equations which is consisted of (n + 1) equations and (n + 1); unknowns, we confront with a number of additional unknowns which are indeed the same coefficients of Eq. (20). Therefore, to remove this problem, we should derive m times from Eq.(18)according to the addi-tional unknowns in the afore-mentioned sets of differential equations and then apply the boundary conditions on them.

p0k: fðu0; u00; u000; . . . ; uðmþ1ÞÞ p00k: fðu00; u000; uðIVÞ; . . . ; uðmþ2ÞÞ ... ... ... ... ...

ð24Þ

(c) Application of the boundary conditions on the derivatives of the differential equation Pk in Eq. (24) is done in the

form of: p0k: fðu 0ð0Þ; u00ð0Þ; u000ð0Þ; . . . ; uðmþ1Þð0ÞÞ fðu0ðLÞ; u00ðLÞ; u000ðLÞ; . . . ; uðmþ1ÞðLÞÞ ( ð25Þ p00k: fðu 00ð0Þ; u000ð0Þ; . . . ; uðmþ2Þð0ÞÞ fðu00ðLÞ; u000ðLÞ; . . . ; uðmþ2ÞðLÞÞ ( ð26Þ

(n + 1) equations can be made from Eq.(21)to Eq.(26)so that (n + 1) unknown coefficients of Eq.(20)such as a0, a1,

a2. . ..an. ll be compute. The solution of the nonlinear

differen-tial Eq.(18)will be gained by determining coefficients of Eq.

(20). To comprehend the procedures of applying the following explanation we have presented the relevant process step by step in following part.

4. Application of Akbari–Ganji’s Method (AGM)

According to mentioned coupled system of nonlinear differen-tial equations and also by considering the basic idea of the method, we rewrite Eqs.(10)–(13)in the following order: FðgÞ ¼ ð1 þ N1ÞfIV N1g Reðff000 f0f00Þ ¼ 0 ð27Þ GðgÞ ¼ N2g00 N1ðf00 2gÞ  N3Reðfg0 f0gÞ ¼ 0 ð28Þ HðgÞ ¼ h00þ Pe hðf0h  fh0Þ ¼ 0 ð29Þ UðgÞ ¼ /00þ Pe mðf0/  f/0Þ ¼ 0 ð30Þ

Due to the basic idea of AGM, we have utilized a proper trial function as solution of the considered differential equa-tion which is a finite series of polynomials with constant coef-ficients, as follows: fðgÞ ¼X 9 i¼0 aigi ¼ a0þ a1g1þ a2g2þ a3g3þ a4g4þ a5g5þ a6g6 þ a7g7þ a8g8þ a9g9 ð31Þ gðgÞ ¼X 9 i¼0 bigi ¼ b0þ b1g1þ b2g2þ b3g3þ b4g4þ b5g5þ b6g6 þ b7g7þ b8g8þ b9g9 ð32Þ hðgÞ ¼X 7 i¼0 cigi ¼ c0þ c1g1þ c2g2þ c3g3þ c4g4þ c5g5þ c6g6 þ c7g7 ð33Þ /ðgÞ ¼X 7 i¼0 digi ¼ d0þ d1g1þ d2g2þ d3g3þ d4g4þ d5g5þ d6g6 þ d7g7 ð34Þ

4.1. Applying boundary conditions

In AGM, the boundary conditions are applied in order to compute constant coefficients of Eqs. (31)–(34)according to the following approaches:

(a) Applying the boundary conditions on Eqs.(31)–(34)are expressed as follows:

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u¼ uðB:CÞ ð35Þ where BC is the abbreviation of boundary condition. Accord-ing to the above explanations, the boundary conditions are applied on Eqs.(31)–(34); in the following form:

fð1Þ ¼ 0 ! a9þ a8 a7þ a6 a5þ a4 a3 þ a2 a1þ a0¼ 0 ð36Þ fðþ1Þ ¼ 0 ! a9þ a8þ a7þ a6þ a5þ a4 þ a3þ a2þ a1þ a0¼ 0 ð37Þ f0ð1Þ ¼ 0 ! 9a9 8a8þ 7a7 6a6þ 5a5 4a4 þ 3a3 2a2þ a1¼ 0 ð38Þ f0ðþ1Þ ¼ 1 ! 9a9þ 8a8þ 7a7þ 6a6þ 5a5 þ 4a4þ 3a3þ 2a2þ a1¼ 1 ð39Þ gð1Þ ¼ 0 ! b9þ b8 b7þ b6 b5þ b4 b3 þ b2 b1þ b0¼ 0 ð40Þ gðþ1Þ ¼ 1 ! b9þ b8þ b7þ b6þ b5þ b4 þ b3þ b2þ b1þ b0¼ 1 ð41Þ hð1Þ ¼ 1 ! c7þ c6 c5þ c4 c3þ c2 c1þ c0¼ 1 ð42Þ hðþ1Þ ¼ 0 ! c7þ c6þ c5þ c4þ c3þ c2þ c1þ c0¼ 0 ð43Þ hð1Þ ¼ 1 ! d7þ d6 d5þ d4 d3þ d2 d1þ d0¼ 1 ð44Þ /ðþ1Þ ¼ 0 ! d7þ d6þ d5þ d4þ d3þ d2þ d1þ d0¼ 0 ð45Þ (b) Applying the boundary conditions on the main differential equations, which in this case study are Eqs.(27)–(30), and also on theirs derivatives is done after substituting Eqs.(31)–(34)

into the main differential equations as follows:

FðfðgÞÞ ! FðfðB:CÞÞ ¼ 0; F0ðfðB:CÞÞ ¼ 0; . . . ð46Þ GðgðgÞÞ ! GðgðB:CÞÞ ¼ 0; G0ðgðB:CÞÞ ¼ 0; . . . ð47Þ HðhðgÞÞ ! HðhðB:CÞÞ ¼ 0; H0ðhðB:CÞÞ ¼ 0; . . . ð48Þ

Uð/ðgÞÞ ! Uð/ðB:CÞÞ ¼ 0; U0ð/ðB:CÞÞ ¼ 0; . . . ð49Þ

The boundary conditions on the achieved differential equa-tion are applied based on the above equaequa-tions. In fact, due to the excellence of AGM from other methods, we have to reach to set of polynomials in the processes of solution according to the overall number of used constant coefficients in trial func-tions which finally we would be able to obtain these only by simple calculations. Since in the proposed problem we have engaged with four trial functions which contain 36 constant coefficients and we have 10 equations according to Eqs.

(36)–(45), we have to create 26 additional equations from Eqs.(46)–(49)in order to achieve a set of polynomials which contains of 36 equations and 36 constants.

According to the above explanations we have created addi-tional equations Eqs.(46)–(49)in the following order:

I. 6 equations have been created by calculating obtained equations from F(1) = 0, F ðþ1Þ ¼ 0; F0ð1Þ ¼ 0; F0ðþ1Þ ¼ 0; F00ð1Þ ¼ 0; F00ðþ1Þ ¼ 0

II. 8 equations have been created by calculating obtained equations from G( - 1) = 0, Gðþ1Þ ¼ 0; G0ð1Þ ¼ 0; G0ðþ1Þ ¼ 0; G00ð1Þ ¼ 0; G00ðþ1Þ ¼ 0; G000ð1Þ ¼ 0;

G000ðþ1Þ ¼ 0

III. 6 equations have been created by calculating obtained equations from H( - 1) = 0, Hðþ1Þ ¼ 0; H0ð1Þ ¼ 0; H0ðþ1Þ ¼ 0; H00ð1Þ ¼ 0; H00ðþ1Þ ¼ 0

IV. 6 equations have been created by calculating obtained equations from U( - 1) = 0, Uðþ1Þ ¼ 0; U0ð1Þ ¼ 0; U0ðþ1Þ ¼ 0; U00ð1Þ ¼ 0; U00ðþ1Þ ¼ 0

The mentioned equations in (I)-(IV) subsections are too large to be displayed graphically. So by utilizing the above pro-cedures we have obtained a set of polynomials containing 36 equations and 36 constants which by solving them we would be able to obtain Eqs. (31)–(34). For instance, when Re¼ 0:1; N1¼ 0:1; N2¼ 0:1; N3¼ 0:1; Peh ¼ 0:1; Pem¼ 0:1,

by substituting obtained constant coefficients from mentioned procedures Eqs.(31)–(34)could easily be yielded as follows: fðgÞ ¼ 0:0000011226g9þ 0:00007769g8 0:0016237g7  0:004568g6 0:0321635g5 0:060965g4 0:306566g3  0:341988g2þ 0:1596354g þ 0:0924003 ð50Þ gðgÞ ¼ 0:00001106g9þ 0:0000777g8þ 0:0016237g7 þ 0:004568g6þ 0:0321635g50:060966g4þ 0:306566g3 þ 0:341988g2þ 0:159635g þ 0:0924004 ð51Þ hðgÞ ¼ 0:000001704g7 0:00001289g6 0:0012362g5 þ 0:0021367g4þ 0:00413266g3 0:0126272g2  0:50289g þ 0:510503 ð52Þ /ðgÞ ¼ 0:000001704g7 0:00001289g6 0:0012362g5 þ 0:0021367g4þ 0:00413266g3 0:0126272g2  0:50289g þ 0:510503 ð53Þ

5. Result and discussion

In this paper, Akbari–Ganji’s Method (AGM) has been utilized in order to solve the nonlinear differential equation of heat and mass transfer equation of steady laminar flow of a micropolar fluid along a two-dimensional channel with porous walls. The geometry of the problem has been shown inFig. 1. Although the processes of obtaining analytical solution for the proposed problem have been explained clearly in the previous sections, it is noteworthy to mention the fact that the mentioned trial functions have been chosen in logical order in which applica-tions of boundary condiapplica-tions due to basic idea of AGM can be satisfied and also symmetric condition would be able to applied in both boundary points which are startpoint =1 and endpoint = +1 in this case. We have shown AGM effi-ciency and accuracy through proper figures and table.

Fig. 2shows the difference between obtained solution by AGM and numerical method (Runge–Kutte 4th) in which we have introduced error percentage as follow:

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%Error ¼ uðgÞNM uðgÞAGM

uðgÞNM



   100 ð54Þ

where u(g)NM is value obtained by numerical method

(Runge–Kutte 4th) and u(g)AGM is value obtained by

AGM. Eq. (54) has been applied through functions of Eqs. (31)–(34) so the parameter u has only been defined as a symbol of data in this case.

InFig. 3(a)–(d), the convergence issue has been considered which shows that by increasing steps in our assumed trial func-tions we will obtain more accurate solufunc-tions. In these figures we have obtained our results due to critical points inFig. 2. Which are shown as follows:

Comparison between AGM and numerical results for dif-ferent values of active parameters is shown inFigs. 4–6and

Table. 1. The obtained results in comparison with numerical results represented that AGM has enough accuracy and effi-ciency so it would be applicable for solving nonlinear equa-tions of coupled system.

Afterward, effect of different parameters such as: Reynolds number, micro rotation/angular velocity and Peclet number on the flow, heat transfer and concentration characteristics are discussed.Fig. 7 shows set of figures which in each of these effects of on parameter has been represented. Generally values of micro rotation profile (g) decrease with increase of Re, N1,

N3, however, it increases when N2increases. It is noteworthy to

mention that when N1> 1 and N2< 1 the behavior of the

angular velocity is oscillatory and irregular.

Since Nusselt and Sherwood numbers have great usage in technological processes, we have shown changes of these dimensionless numbers inFigs. 8and9. The effects of Peclet number on the fluid temperature and concentration profile are shown inFigs. 8(a) and9(a). As shown inFig. 8(a) the fluid temperature increases with increase of Peclet number and also due to Fig. 9(a) concentration profile increases while Peclet number increases. On the other hand, according toFig. 8(b), increase in Peclet number and Reynolds number leads to increase in Nusselt number. Also according to Fig. 9(b) the same could be concluded for Sherwood number which increase in Peclet number and Reynolds number leads to increase in Sherwood number.

Fig. 3 Obtained error at different time steps for (a) f(g), (b) g(g), (c)h(g), (d) U(g).

Fig. 2 Obtained error for f(g), g(g), h(g), /(g) when Re = 1, N1= N2= N3= 0.1, Peh= 0.2, Pem= 0.5.

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Fig. 7 Effects of Re, N1, N2, N3 on micro rotation profile (g)

when (a) N1= N2= N3= 1 (b) Re = N2= N3= 1; (c) N1=

Re = N3= 1 (d) N1= N2= Re = 1.

Fig. 4 Comparison between numerical and AGM solution results for f(g).

Fig. 5 Comparison between numerical and AGM solution results for g(g).

Fig. 6 Comparison between numerical and AGM solution results forh(g).

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6. Conclusion

In this study, AGM has been utilized in order to solve nonlin-ear differential equation of heat and mass transfer equation of steady laminar flow of a micropolar fluid along a

two-dimensional channel with porous walls. Comparisons have been done among AGM and numerical method (Runge–Kutte 4th) by different parameters values. Data from error figure represent that obtained solutions with AGM has minor differences with exact solutions and also convergence figure represent that by applying more terms of AGM we would be able to obtain more accurate solutions. Furthermore, Fig. 9 (a) Effects of Pemon concentration profile at Re = N1=

N2= N3= Peh= 1, (b) effects of Re and Peh= Pem on

Sherwood number when N1= N2= N3= 1.

Table 1 Comparison between the numerical results and AGM solution for /(g) at various Re, Pem when Peh= 0.2,

N1= N2= N3= 0.1.

g Re = 1, Pem= 0.5 Re = 0.5, Pem= 0.2

Num AGM Error Num AGM Error

1 1 1 0 1 1 0 0.8 0.9192939269 0.9193811169 0.0000948446 0.9077116680 0.907720689 0.000009938 0.6 0.8356460368 0.8358088531 0.0001948388 0.8142102267 0.814227024 0.000020630 0.4 0.7471790040 0.7473962040 0.0002906933 0.7187421955 0.718764563 0.000031120 0.2 0.6530205940 0.6532642196 0.0003730750 0.6209800569 0.621005159 0.000040423 0 0.5531286373 0.5533690723 0.0004346819 0.5209385166 0.520963368 0.000047706 0.2 0.4481088763 0.4483206457 0.0004725848 0.4188891701 0.418911173 0.000052526 0.4 0.3390200357 0.3391859739 0.0004894642 0.3152725867 0.315289927 0.000055001 0.6 0.2271589176 0.2272708614 0.0004927993 0.2106066932 0.210618442 0.000055789 0.8 0.1138170680 0.1138730124 0.0004915290 0.1053902317 0.105396114 0.000055816 1 0 0 0 0 0 0

Fig. 8 (a) Effects of Pehon temperature profile at Re = N1=

N2= N3= Pem= 1, (b) effects of Re and Peh= Pemon Nusselt

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according to achieved results, Reynolds number has direct relationship with Nusselt number and Sherwood number, however, peclet number has reverse relationship with them.

Finally, it will be obvious that AGM is a convenient analyt-ical method and due to its accuracy, efficiency and convergence it could be applied for solving nonlinear problems.

Nomenclature

AGM Akbari–Ganji’s Method C species concentration

D* thermal conductivity and molecular diffusivity

f dimensionless stream function g dimensionless micro rotation

h width of channel

j micro-inertia density

N micro rotation/angular velocity

N1,2,3 dimensionless parameter Nu Nusselt number Sh Sherwood number Sc Schmidt number p pressure Pr Prandtl number Pe Peclet number

q mass transfer parameter

Re Reynolds number

T fluid temperature

s micro rotation boundary condition (u, v) Cartesian velocity components (x, y) Cartesian coordinate components g similarity variable

h dimensionless temperature l dynamic viscosity j coupling coefficient

q fluid density

qs micro rotation/spin-gradient viscosity

w stream function

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