Double Diffusive Nonlinear Convective MHD Unsteady Slip-Flow Regime
in a Rectangular Channel
ABDULHAKEEM YUSUF1,a*, TEMITOPE SAMSON ADEKUNLE2,
ABD’GAFAR TUNDE TIAMIYU3, ABUBAKAR MUSA ALIYU1
1Department of Mathematics,
Federal University of Technology Minna,
P.M.B. 65, Minna,
NIGERIA
2Department of Computer and Information Science,
Colorado State University,
Colorado,
USA
3Department of Mathematics,
The Chinese University of Hong Kong,
Hong Kong,
CHINA
aORCIDiD: 0000-0001-8675-5137
*Corresponding Author
Abstract: - In the paper, we numerically explored the combined impacts of non-linear thermal and mixed
convective unsteady flow in a channel with slip conditions. The flow is caused by a moving flat parallel surface
and is also electrically conductive. We analyse the mechanisms of heat, and mass transfer by incorporating
temperature and concentration jumps. To simplify the model problem, we apply appropriate similarity
transformations, reducing the prevailing problem to a nonlinear coupled ordinary boundary value problem. The
transformed problem is solved using the Chebyshev Collocation Approach (CCA). We performed a comparative
analysis by comparing the CCA with the literature to verify the accuracy of our approach, and a good agreement is
found. In addition, we conducted a comprehensive parametric study to analyze the trends in the solutions obtained.
The study reveals that the parameters
13
, , , Pr, and ScM

have about 20% stronger impact on the nonlinear
system compared to the linear system on both surfaces of the horizontal channel.
Key-Words: - Double diffusive, Nonlinear Convection, Slip-flow, Channel flow, MHD, Variable distance,
Chebyshev Collocation Approach
Received: December 14, 2022. Revised: October 21, 2023. Accepted: November 16, 2023. Published: December 19, 2023.
1 Introduction
Any fluid, whether liquid or gas used in heating or
cooling is an example of heat transfer fluid. Heat
transfer fluid has a lot of industrial applications and
are distinct ranging from the less complex static
design of advanced multi-loop systems. The process
by which heat is transferred to a moving fluid via a
heated surface is known as convective heat transfer
which can be viewed in two ways. The first is the
natural convection, also known as free convection
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Abdulhakeem Yusuf, Temitope Samson Adekunle,
Abd’gafar Tunde Tiamiyu, Abubakar Musa Aliyu
E-ISSN: 2224-347X
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which occurs due to density differences caused by
temperature gradient and thus resulting in internal
buoyancy. This phenomenon is commonly observed
in bioreactors and some jacket designs prone to
internal free convection at low flow rates. However,
when external devices such as stirrers or pump
ensure the flow rate, forced convection is
predominant. As described by, [1], combined
convection exists if the impact of buoyancy in non-
free convection and the impact of forced flow in
free convection are prevalent. They play a
significant role in the atmospheric boundary layer
flow, solar collectors, electronic equipment, and
nuclear reactors.
Numerous scientists examined the significance
of convection flow via stretching sheets with
variable boundary conditions as seen in, [2], [3].
[4], explored the nonlinear flow of thermal
boundary over a linear surface. The examination of
time-dependent natural convection flow of a
Jefferey fluid with a moving surface along with the
impact of temperature and velocity was considered,
[5]. In their work, [6], carried out a study on
generalized Mittag-Leffler via the analytical
solution of natural convection flow of Prabhakal
fractional Maxwell fluid with Newton heating. The
impact of various fluid behaviors of combined
convective heat transport with a nonlinear moving
sheet was explored by, [7]. The influence of Dufour
and Soret on convective viscoelastic fluid flow over
a moving surface enclosed in a porous medium was
examined in, [8]. In addition, [9], Explored
viscoelastic Walter-B combined convective
nanofluid through a non-linear vertical plate with
various sizes of parameters. [10], scrutinize a 3D
study of non-linear convection in a Maxwell
nanofluid along a non-linear radiation numerically.
A review of thermal boundary conditions of
Magnetohydrodynamics (MHD) free convective
nanofluid in a square enclosure is reported by, [11].
Various other works on convective heat transfer can
be found in, [12], [13], [14], [15], [16], [17], and
related literature.
The numerous advantages of convective
problems of electrically conducting fluid on a
magnetic field have attracted significant attention
due to their wide applicability in Geophysics,
Plasma physics, Astrophysics, Missile Technology,
and more. The application of the MHD principle has
also been found in Biology and Medicine. [18],
explored the impacts of Magnetohydrodynamics
natural convective rotating nanofluid flow with
radiation-absorption, Soret, Hall, and ion slip over a
semi-infinite permeable surface and constant heat
source. In the presence of Hall current, [19],
considered water-based nanofluid MHD squeezing
flow between parallel disks through a saturated
medium. Ion slip influence on unsteady
magnetohydrodynamics rotating convective flow
has been explored by, [20]. [21], examined
magnetohydrodynamics micropolar fluid flow over
a curved surface. The work of MHD flow with
convection over a vertically oscillating porous wall
with constant heat flux is explored by, [22]. With
exponential permeable stretching porous surface,
[23], reported the study of magnetohydrodynamics
convective flow of a nanofluid. For more studies
conducted on MHD flow, interested individuals can
refer to references, [24], [25], [26], [27], [28], [29],
[30], [31], [32].
Due to a recent industrial application regime of
slip-flow, researchers in their numbers have
developed an interest in it. In this period of modern
industrialization, technology, and science, the
significance of the slip-flow regime can never be
over-emphasized. In practical terms, the velocity of
the particle to the boundary no longer has the same
values as the surface. The surface particle takes a
definite velocity and slips on the plate. This kind of
flow is known as slip-flow regime and its impact
cannot be neglected. The phenomenon of this flow
regime is prevalent in microchannels, nanochannels,
and geothermal regions. Moreover, efforts of the
slip-flow regime in a channel have been discussed
by various authors including, [33], [34], [35], [36],
[37], [38].
From the literature available, the current study
introduces a novel aspect of incorporating nonlinear
mixed convection into the model proposed by [39].
The model assumes a first-order slip, with
temperature and concentration jumps. To solve the
resulting model, the Chebyshev Collocation
Approach (CCA) will be employed to obtain the
numerical approximations. The combination of a
nonlinear mixed convection, the varying conditions,
and concentration represents a new contribution to
the existing literature.
2 Mathematical Analysis
Considering 2D unsteady, laminar boundary layer
fluid flow in a horizontal rectangular wall with the
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horizontal wall at
0y
and at a variable distance
y h t
. The first wall is assumed slippery and
stretches with velocity
, temperature
T
of
0
T
,
concentration
C
of
0
C
while the upper wall has
/ / / 0u y T y C y
and
/v h t
, at
y h t
.
Following the work of, [39], and, [40], based on
the assumption above, the model equation of the
problem with nonlinear convection and slip-flow
conditions as depicted in Figure 1 written as:
0
uv
xy



, (1)
22
0
2
22
1 2 3
(
)
h
h h h
u u u u B
u v u g T T
t x y y
T T C C C C

,
(2)
2
*
2
T T T T
uv
t x y y



, (3)
2
2
M
C C C C
u v D
t x y y



, (4)
1
0 2 0 3
0 : , 0,
1
,
: 0, , 0, 0
bx u
y u a v
ty
TC
T T a C C a
yy
u h T C
y h t v
y t y y



(5)
Fig. 1: Model configuration
To simplify the above set of nonlinear partial
differential (continuity, momentum, temperature,
and concentration profiles) equations (1) (4)
together with the given boundary conditions (5), the
following similarity solutions will be used to
compact the boundary value problem into a set of
non-linear ODEs:
, ( ),
(1 ) 1
( )
(1 )
b y bx
uf
tt
b
vf
t





,
12
,
hh
T T D x C C D x

(6)
The transformed set of nonlinear ordinary equations
is:
2
1 2 3 4
2
1 1 0
fs f ff f Mf

(7)
0
Pr 2
s f f


(8)
0
2
s f f
Sc


(9)
with the boundary conditions
1
23
0 : (0) 0, (0) 1 (0),
(0) 1 (0), (0) 1 (0)
1: (1) , (1) 0, (1) 0, (1) 0
2
f f f
s
ff


(10)
The critical quantities are the coefficient of skin
friction, Nusselt number and Sherwood number
obtained as:
(0)
Re
f
x
Cf


,
(0)
Re
x
x
Nu

, and
(0)
Re
x
x
Sh

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3 Numerical Solution
The reduced nonlinear coupled ODEs corresponding
to equations (7)-(10) are solved using the
Chebyshev Collocation. This method involves the
use of Chebyshev polynomial as basis function by
assigning it to an unknown coefficient. The trial
function is then implemented on the conditions
(Boundary) and the problem of obtaining the
residue. Thereby, utilizing a collocation method to
generate the error to almost zero. The accuracy of
the Colocation technique is found to be high and no
ambiguity to implement, [41], [42], [43], [44].
3.1 Chebyshev Collocation Approach
Implementation
The functions to be determined
( ), ( ) and ( )f
are expressed in the form
of a sum of Chebyshev base functions below:
0
( ) (2 1)
N
nn
n
f a T


,
0
( ) (2 1)
N
nn
n
bT

and
0
( ) (2 1)
N
nn
n
cT

Where
, b , and c
n n n
a
are the constants to be
determined and
(2 1) :[ 1,1] [0,1]
n
T
. In
order to obtain the values of the unknown constants,
the Chebyshev base functions are substituted into
the boundary conditions in (10) corresponding to:
00
2
2
00
0
00
0
00
0
2
2
0
(2 1) 0,
(2 1) (2 1) 1 0,
(2 1) (2 1) 1 0,
(2 1) (2 1) 1 0,
(2 1) 0
N
nn
n
NN
n n n n
nn
NN
n n n n
nn
NN
n n n n
nn
N
nn
n
aT
dd
a T a T
dd
d
b T b T
d
d
c T c T
d
daT
d























01
1
01
0, (2 1) 0,
(2 1) 0
N
nn
n
N
nn
n
dbT
d
dcT
d








(11)
The base functions are then substituted into
equations (7)-(9) to generate the residues
( , , , ), ( , , ), and ( , , )
f n n n n n n n
R a b c R a b R a c

. The residues are then minimized using the
Collocation techniques as follows:
1, =
()
0, otherwise
i
i


(12)
0
( , , , ) ( , , , ) 0,
for 1, 2,3,... 2
Lf n n n f n n n
R a b c d R a b c
iN


(13)
0
( , , ) ( , , ) 0,
for 1, 2,3,... 1
Ln n f n n
R a b d R a b
iN


(14)
0
( , , ) ( , , ) 0,
for 1, 2,3,... 1
Ln n n n
R a c d R a c
iN



(15)
Where are the Collocation points expressed as:
11 cos
2
ii
N







,for i=1, 0,…N (16)
Equations (12) to (15) is a 3N+3 x 3N+3 system of
equations with unknown coefficients
, b , and c
n n n
a
to be obtained.
The corresponding residue equation for equations
(7)-(9) is given as:
2
1
1 2 3 4
2
11
f
R s f ff f Mf

(17)
2Pr 2
R s f f


(18)
32
R s f f
Sc


(19)
The collocation points are presented in Table. 1
below:
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Table 1. Collocation points
i
i
i
i
0.0
0.000000
10.0
0.578217
1.0
0.006155
11.0
0.654508
2.0
0.054496
12.0
0.726995
3.0
0.095491
13.0
0.793893
4.0
0.146447
14.0
0.853553
5.0
0.206107
15.0
0.904508
6.0
0.273004
16.0
0.945503
7.0
0.345491
17.0
0.975528
8.0
0.421782
18.0
0.993844
9.0
0.500000
19.0
1.000000
Newton’s method is employed to obtain the
solution of the system and Mathematical symbolic
package (MATHEMATICA 11.3) is used to carry
out all the computations.
Table 2. Comparison of Nusselt number (
(0)
)
for
1, 0.0, 0.0, 0.1,M s Sc
1 2 3 4 1 2 3 0
4 Results and Discussions
The solution to the highly nonlinear coupled
expressions in (7-9) with their conditions in (10) are
numerically approximated with the Chebyshev
Collocation Method. The implementation of this
method has various advantages ranging from the
fact that its construction is integration-based as
against the traditional differentiation, which allows
the incorporation of more than one boundary
condition efficiently and faster convergence rate
than conventional approaches. To check the
accuracy of this method, a comparative analysis is
carried out with the literature. An excellent
agreement is observed as presented in Table 2.
Figure 2a-2c describe the features of
magnetization on
, f and

respectively for both
linear
24
( 0)


and nonlinear
24
( 0, 0)


combined convection. It is
explored that the horizontal velocity
f
in Figure 2a
retarded for improving M due to the magnetization
of the lower wall to help weaken the fluid
momentum. Fluid energy
and concentration
are escalated in Figure 2b and Figure 2c
respectively. The fluid velocities drop faster for
linear convection than nonlinear convection and the
temperature and concentration enhance faster with
linear convection. This phenomenon implies that the
Lorentz force has a greater impact on the linear
mixed convection compared to the nonlinear.
(a)
(b)
(c)
Fig. 2: The profiles of
, f and

for various
values of
M
The variation of the mixed convection parameter
1
is seen on
, f and

in Figure 3 (a-c). Here,
Pr
[45]
[46]
[47]
Present
results
1
1.0000
-
1.0000
1.0008
3
1.9237
-
1.9237
1.9233
6.7
-
3.0002
3.0003
3.0000
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it is examined that
f
is increasing due to the
presence of the buoyancy effect while
and

decay for larger values of
1
. The nonlinear
1
has
a greater influence on
, f and

than linear
which signifies that the magnitude of buoyancy
forces is more prevalent in the nonlinear case. The
fluid horizontal velocity has the tendencies of
approaching the free stream at the upper wall.
(a)
(b)
(c)
Fig. 3: The Profiles of
, f and

for various
value of
1
The influence of modified mixed convection
, f and

is elaborated in Figure 4 (a-c)
respectively. The fluid velocity appreciates due to
buoyancy force in Figure 4a while the temperature
and concentration decelerate in Figure 4a and Figure
b as
3
improved. The nonlinear modified mixed
convection
3
has a significant effect on
, f and

on compared to linear case.
Additionally,
3
has a greater impact on the fluid
variables to
1
.
(a)
(b)
(c)
Fig. 4: The Profiles of
, f and

for various
value of
3
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The significance of Pr on
and

is
characterized in Figure 5 (a and b). The usefulness
of Prandtl number in industrial activities to attain
higher quality products can never be over-
emphasized. Appropriate values of Pr are necessary
in industrial heating/cooling. It is explored here that
larger values of Prandtl number cause
and

to
drop. Reduction in thermal diffusivity is the major
characteristic in Pr. This factor resulted in the
decrease of the thermal boundary layer and solutal
concentration. Thus, Pr causes the fluid and solutal
concentration to drop quicker in the nonlinear sense.
Figure 6 (a and b) portrays the rheological
illustration of the profiles of
and

for
improving values of
Sc
. It is explored that
and

lessens as
Sc
is enhanced due to the
prevalent nature of the Brownian diffusion presence.
The weak coefficient of Brownian diffusion
signifies large values of Schmidt number which in
turns lower the temperature profiles and solutal
concentration. The Brownian diffusion’s less
prevalence in the presence of non-linear convection
resulted in the fluid energy and concentration to
drop faster compared to linear case.
(a)
(b)
Fig. 5: The Profiles of
and

for various value of
Pr
(a)
(b)
Fig. 6: The Profile of
and

for various values of
Sc
Figure 7 (a-c) displays the impact of mixed
convection and modified mixed convection
13
and

in the nonlinear sense on
, , and
f x x
C Nu Sh
. Since the buoyancy
parameters enhance the fluid velocity, the fluid
particles gather momentum because of this
enhancement causing more heat loss to the
surrounding and thereby dropping the skin friction
and increasing the Nusselt number and Sherwood
number. This result agrees with, [48].
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(a)
(b)
(c)
Fig. 7: The profiles of
(0), - (0), f
and
- (0)
for various values of
13
and

5 Conclusion
This study launched an investigation into the
thermophysical properties of nonlinear/linear
combined convective boundary layer slip-flow in a
channel with a magnetic effect. Similarity solutions
are introduced to transform the governing equation
assisting the flow. Therefore, the solution to the
nonlinear coupled set of ODE is numerically
approximated using CCA. The approach gave an
excellent result as illustrated in Table 1. In
conclusion:
1. Magnetic parameters shrink the fluid
momentum. Thus, the temperature and
solutal concentration are enhanced.
2. The combined convective parameter and the
modified mixed parameter have the same
impact on the fluid variables. However, the
modified mixed convection illustrates a
greater impact.
3. Prandtl number Pr and Schmidt number Sc
are reduction agents on the fluid energy and
concentration.
4. Due to the influence slippery on the lower
wall, the friction between the fluid and the
wall surface drops with improve mixed and
modified mixed convection. However, the
Nusselt number and Sherwood number
improved.
Interestingly, this analysis is significant in
optimizing and modeling of Nonlinear
combined convection in a horizontal channel
with slip-flow regime rate of fluid material in
each system. To improve the optimality of heat
transfer conditions, nanofluids will be
introduced in future work with slip-flow in a
more complex geometry and the data will be
trained using an ANN model to forecast the
characteristics of heat and mass transfer.
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Volume 18, 2023
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DOI: 10.37394/232013.2023.18.19
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Nomenclature
t
Time (s)
3
Modified mixed convective parameter
2
( / Re )
xx
Gc
1 2 3
,,a a a
Slip constants
4
Nonlinear solutal buoyancy parameter
3 0 2
( ( ) / )
h
TT


k
Thermal conductivity (
/W mK
)
Pr
Prandtl number
( / *)

()ht
Wall distance
( (1 ) / )tb

(m)
Sc
Schmidt number
/M
D
g
Acceleration due to gravity (
2
/ms
)
1
Velocity slip parameter
1
( ( / ) / (1 ))a b t

T
Fluid temperature (
K
)
2
Temperature slip parameter
2
( ( / ) / (1 ))a b t

,xy
Fluid directions (m)
3
Concentration slip parameter
3
( ( / ) / (1 ))a b t

,uv
Fluid velocities along (
/ms
)
,xy
f
C
Coefficient of skin friction
b
Stretching constant (-)
x
Nu
Coefficient of Nusselt number
0
T
Fluid temperature at lower wall (K)
x
Sh
Coefficient of Sherwood number
h
T
Fluid temperature at upper wall (K)
1
D
Temperature difference
0
( ( ) / )
h
T T x
(K)
C
Fluid concentration (
3
/kg m
)
2
D
Solutal difference
0
( ( ) / )
h
C C x
(
3
/kg m
)
o
C
Fluid concentration at the lower wall
(
3
/kg m
)
Greek Symbols
h
C
Fluid concentration at upper wall(
3
/kg m
)
Fluid dimensionless distance (m)
f
Fluid dimensionless Velocity
/ms
,

Squeezing characteristic parameters (-)
s
Dimensionless measure of
unsteadiness
( / )b
Kinematic viscousity (
21
ms
)
M
Magnetic parameter (
2
0/B

)
Dimensionless temperature
x
Gt
Thermal Grashof number
32
00
( ( ) / )
h
g T T x


Dimensionless concentration
x
Gc
Solutal Grashof number
32
20
( ( ) / )
h
g C C x


Fluid density (
3
kgm
)
Squeezing parameter
2
()
Electrical conductivity
Rex
Reanold number
2
( / (1 ) )bx t


01
,

Coefficient of thermal expansion
1
Mixed convective parameter
2
( / Re )
xx
Gt
23
,

Coefficient of solutal expansion
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DOI: 10.37394/232013.2023.18.19
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2
Nonlinear thermal buoyancy
parameter
1 0 0
( ( ) / )
h
TT


Superscript
B
Magnetic effect
0/1Bt
'
Derivative with respect to
Stretching value
( / (1 ))bx t

*
Thermal diffusivity
M
D
Molecular Diffusion
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Volume 18, 2023