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Question: Two slabs $A$ and $B$ of equal surface area are placed one over the other such that their surface ar...

Two slabs AA and BB of equal surface area are placed one over the other such that their surface are completely in contact. The thickness of slab AA is twice that of BB. The coefficient of thermal conductivity of slab AA is twice that of BB. The first surface of slab AA is maintained at 100100 ^\circC, while the second surface of slab BB is maintained at 2525 ^\circC. The temperature at the contact of their surface is.

A

62.5 ^\circC

B

45 ^\circC

C

55 ^\circC

D

85 ^\circC

Answer

62.5 ^\circC

Explanation

Solution

Let LAL_A and LBL_B be the thicknesses of slabs A and B, respectively, and KAK_A and KBK_B be their thermal conductivities. Let AA be the surface area of each slab. We are given that LA=2LBL_A = 2 L_B and KA=2KBK_A = 2 K_B. The first surface of slab A is maintained at T1=100T_1 = 100 ^\circC, and the second surface of slab B is maintained at T2=25T_2 = 25 ^\circC. Let TiT_i be the temperature at the contact surface between slabs A and B.

In the steady state, the rate of heat transfer through slab A is equal to the rate of heat transfer through slab B. The rate of heat transfer through a slab is given by Fourier's law of conduction: Q=KAΔTLQ = \frac{K A \Delta T}{L}.

For slab A, the temperature difference is T1TiT_1 - T_i. The heat flow rate through slab A is QA=KAA(T1Ti)LAQ_A = \frac{K_A A (T_1 - T_i)}{L_A}.

For slab B, the temperature difference is TiT2T_i - T_2. The heat flow rate through slab B is QB=KBA(TiT2)LBQ_B = \frac{K_B A (T_i - T_2)}{L_B}.

Since the slabs are in series and in steady state, QA=QBQ_A = Q_B.

KAA(T1Ti)LA=KBA(TiT2)LB\frac{K_A A (T_1 - T_i)}{L_A} = \frac{K_B A (T_i - T_2)}{L_B}

Substitute the given relationships LA=2LBL_A = 2 L_B and KA=2KBK_A = 2 K_B:

(2KB)A(100Ti)2LB=KBA(Ti25)LB\frac{(2 K_B) A (100 - T_i)}{2 L_B} = \frac{K_B A (T_i - 25)}{L_B}

The term 2KBA2LB\frac{2 K_B A}{2 L_B} simplifies to KBALB\frac{K_B A}{L_B}. So the equation becomes:

KBA(100Ti)LB=KBA(Ti25)LB\frac{K_B A (100 - T_i)}{L_B} = \frac{K_B A (T_i - 25)}{L_B}

Assuming KB0K_B \neq 0, A0A \neq 0, and LB0L_B \neq 0, we can cancel the term KBALB\frac{K_B A}{L_B} from both sides:

100Ti=Ti25100 - T_i = T_i - 25

Now, we solve for TiT_i:

100+25=Ti+Ti100 + 25 = T_i + T_i

125=2Ti125 = 2 T_i

Ti=1252T_i = \frac{125}{2}

Ti=62.5T_i = 62.5 ^\circC

Alternatively, we can use the concept of thermal resistance. The thermal resistance of a slab is R=LKAR = \frac{L}{KA}.

For slab A, RA=LAKAA=2LB(2KB)A=LBKBAR_A = \frac{L_A}{K_A A} = \frac{2 L_B}{(2 K_B) A} = \frac{L_B}{K_B A}.

For slab B, RB=LBKBAR_B = \frac{L_B}{K_B A}.

We observe that RA=RBR_A = R_B.

When two thermal resistances are in series, the temperature drop across each resistance is proportional to its value. The heat flow rate is Q=ΔTRQ = \frac{\Delta T}{R}.

Q=T1TiRA=TiT2RBQ = \frac{T_1 - T_i}{R_A} = \frac{T_i - T_2}{R_B}.

Since RA=RBR_A = R_B, we have T1TiRA=TiT2RA\frac{T_1 - T_i}{R_A} = \frac{T_i - T_2}{R_A}, which implies T1Ti=TiT2T_1 - T_i = T_i - T_2.

T1+T2=2TiT_1 + T_2 = 2 T_i

Ti=T1+T22T_i = \frac{T_1 + T_2}{2}

Substitute the values T1=100T_1 = 100 ^\circC and T2=25T_2 = 25 ^\circC:

Ti=100+252=1252=62.5T_i = \frac{100 + 25}{2} = \frac{125}{2} = 62.5 ^\circC.

The temperature at the contact of their surface is 62.5 ^\circC.