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Solve Problem 1 if the sides x=0and x=1are insulated (see Problems 2.14 and 2.15), and T=0for y=2, T=1−x fory=0.

Short Answer

Expert verified

The steady-state temperature distribution is obtained by,

T=14(2−y)+4π2∑oddn1n2sinh(2nπ)sinhnπ(2−y)cos(nπx).

Step by step solution

01

Given Information:

It has been given that the rectangular plate is covering the area 0<x<1, 0<y<2, if T=0 for x=0, x=1, y=2and T=1-xfor y=0.

02

Definition of Laplace’s equation.

Laplace’s equation in cylindrical coordinates is,

∇2u=1r∂∂r(r∂u∂r)+1r2∂2u∂θ2+∂2u∂z2=0

And to separate the variable the solution assumed is of the formu=R(r)Θ(θ)Z(z).

03

Solve the differential equation:

Assume that the plate is so long compared to its width that the mathematical approximation can be made that it extends to infinity in the y direction, the temperature T satisfies Laplace's equation inside the plate that is∇2T=0.

To solve this equation, try a solution of the form mentioned below. T(x,y)=X(x)Y(y) ….. (1 Yd2Xdx2+Xd2Ydy2=0 ….. (2)

Divide the above equation by XY

1Xd2Xdx2+1Yd2Ydy2=0 ….. (3)

Now, following the process of separation of variables, it can be written

1Xd2Xdx2=−1Yd2Ydy2=constant=−k2, â¶Ä‰â¶Ä‰k≥0 ….. (4)

X''=−k2XandY''=k2Y.

Here, the constant k2is called the separation constant. The solutions for these equations fork≠0.

role="math" localid="1664343493282" X(x)=sin(kx)cos(kx)Y(y)=sinh(ky)cosh(ky) ….. (5)

The solution for k=0.

X(x)=1xY(y)=1y ….. (6)

04

Apply Boundary condition:

Write the relevant boundary conditions.

T(x,0)=1−x â¶Ä‰â¶Ä‰T(x,2)=0

∂T∂x(0,y)=∂T∂x(1,y)=0

The boundary condition T(x,2)=0implies that Y(2)=0. Thus, the possible solutions for Y(x)are mentioned below.

Y(y)=sinhk(2−y),fork≠02−y,fork=0

The boundary condition ∂T∂x(0,y)=0implies the condition given below.

∂X∂x|x=0=0

Write the possible solutions for X(x).

X(x)=cos(kx),fork≠01,fork=0

The boundary condition is,

∂T∂x(1,y)=0

This implies that∂X∂x|x=1=0

Impose this on eq. (4), see that constant solution is still allowed for the case of k=0. If k≠0, then eq. (5) yields that k=nπ.Using the above results, the form of T(x,y)prior to applying the fourth boundary condition.

T(x,y)=c0(2−y)+∑n=1∞cnsinh(nπ(2−y))cos(nπx)

05

Step 5:Apply fourth boundary condition:

Apply the fourth boundary condition T=1−xfor Y=2, b0=4c0, bn=cnsinh(2nπ), forn=1,2,3,….

We have the equation mentioned below.

1−x=b02+∑n=1∞bnsinh(2nπ)cos(nπx)

Invert the Fourier series to determine the coefficients.

b0=2∫01(1−x)dx=1

bn=12∫01(1−x)cos(nπx)dx=2(1−cos(nπ)(nπ)2)=1(nπ)2(1−(−1)n)={0ifniseven2(nπ)2ifnisodd

Write final T(x,y)expression.

Inserting b0and bninto the above expression of T(x,y)it ends up with

T=14(2−y)+4π2∑oddn1n2sinh(2nπ)sinhnπ(2−y)cos(nπx)

Hence, this is the steady-state temperature distribution.

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