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<strong>International</strong> <strong>Journal</strong> <strong>of</strong> <strong>Applied</strong> <strong>Information</strong> <strong>Systems</strong> (IJAIS) – ISSN : 2249-0868<br />

Foundation <strong>of</strong> Computer Science FCS, New York, USA<br />

Volume 4– No.7, December 2012 – www.ijais.org<br />

*<br />

The x -axis is taken along the plate in the vertically upward<br />

*<br />

direction and the y -axis is taken normal to the plate.<br />

Initially the plate and the fluid are at the same temperature<br />

*<br />

*<br />

T in the stationary condition with concentration level<br />

at all points. At time,<br />

accelerated with a velocity<br />

C <br />

*<br />

t 0 , the plate is exponentially<br />

**<br />

* at<br />

o<br />

u U e<br />

in its own plane<br />

and the temperature <strong>of</strong> the plate is raised at a uniform rate and<br />

the level <strong>of</strong> concentration near the plate is raised linearly with<br />

time. All the physical properties <strong>of</strong> the fluid are considered to<br />

be constant. The unsteady flow is governed by the following<br />

equations:<br />

* 2 *<br />

u u<br />

g T T g C C<br />

* *2<br />

t y<br />

* 2 *<br />

C C<br />

D K C C<br />

* *2<br />

t y<br />

Tk T Q<br />

t y <br />

* * * * *<br />

<br />

* * *<br />

*<br />

* T T<br />

* 2 *<br />

* <br />

C *2<br />

0<br />

C<br />

<br />

The initial and boundary conditions relevant to the fluid flow<br />

are:<br />

* * * * * *<br />

t* 0 : u 0, T T , C C For all y <br />

<br />

*<br />

<br />

**<br />

* at T<br />

q * * * <br />

t* 0 : u U e , , C C at y 0<br />

o *<br />

w <br />

y<br />

k<br />

<br />

* * * * * *<br />

u 0, T T , C C as y <br />

<br />

(4)<br />

*<br />

*<br />

*<br />

Where u is the axial velocity, t is time, T the fluid<br />

*<br />

temperature, is coefficient <strong>of</strong> volume, C is the fluid<br />

concentration,<br />

(1)<br />

(2)<br />

(3)<br />

*<br />

C w is wall concentration, D the mass<br />

*<br />

is the<br />

diffusivity, K is chemical reaction parameter,<br />

coefficient <strong>of</strong> concentration expansion.<br />

3. ANALYTICAL SOLUTION<br />

To solve the governing equations in dimensionless form, the<br />

following non-dimensional quantities were introduced:<br />

* * * 2<br />

y U0 u t U0 Q<br />

0<br />

y , U , t ,, F 2 <br />

U0 cU<br />

0 <br />

* * * * *<br />

T T C C a <br />

, c , a,<br />

<br />

* * 2<br />

q k Cw CU0 <br />

*<br />

(5)<br />

K c<br />

K , Sc ,Pr , <br />

2<br />

U0 D k<br />

<br />

<br />

2<br />

* * *<br />

gq g CwC Gr , Gc 4 3 <br />

kU 0 U0<br />

<br />

The governing equations on using (5) into (1) to (4) reduce to<br />

the following<br />

2<br />

u u<br />

Nc<br />

2<br />

t y<br />

<br />

tScy 2<br />

c 1 c<br />

Kc<br />

2<br />

2<br />

1 <br />

F<br />

2<br />

t Pr y<br />

Subject to the boundary conditions<br />

For t 0: u c 0,<br />

<br />

<br />

t <br />

for 0 y 1<br />

at ue , 1,<br />

y<br />

u 0, 0, c 0<br />

For 0:<br />

c 1 at y 0<br />

, as y <br />

To obtain the solutions, we apply the Laplace transform to (6)<br />

– (8) and the boundary conditions to get<br />

2<br />

d <br />

Pr 2 PF 0<br />

(9)<br />

dy<br />

2<br />

dC<br />

Sc 2 P K C<br />

dy<br />

(6)<br />

(7)<br />

(8)<br />

0<br />

(10)<br />

2<br />

dU<br />

PU NC<br />

2<br />

dy<br />

(11)<br />

The boundary conditions are<br />

t 0 : U C 0, y 1<br />

<br />

<br />

1 d<br />

1 1 <br />

t 0 : U , , C , at y 0<br />

P a dy P P <br />

U 0, 0, C 0, as y <br />

<br />

The solutions to (9) to (11) subject to (12) give<br />

(<br />

y, p)<br />

<br />

e<br />

C( y, p)<br />

<br />

Pr<br />

e<br />

k1<br />

y Z<br />

Z F<br />

k2Z<br />

Z K<br />

Z<br />

(12)<br />

(13)<br />

(14)<br />

22

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