Answer
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Hint : In this solution, we will assume that the system has been in a steady-state for a long time. Then both the slabs will have the same rate of heat transfer and we will use this to determine the solution of the interface.
Formula used: In this solution, we will use the following formula:
Rate of heat transfer in a slab with different temperatures: $ Q = \dfrac{{kA\Delta T}}{L} $ where $ A $ is the area of the surface, $ \Delta T $ is the temperature difference, and $ L $ is the length of the slab.
Complete step by step answer
In the system given to us, we will assume that the system has been left in this situation for a long time. This implies that the heat transfer will have occurred over a long time and the system can be said to have achieved a steady-state.
In this steady-state situation, we can say that the heat transfer in both the slabs will be the same. Let us assume that the temperature of the surface is $ \theta $ . Then since the heat flow rate is constant for both the surfaces will be the same and we can write
$ \dfrac{{3kA({\theta _2} - \theta )}}{d} = \dfrac{{kA(\theta - {\theta _1})}}{{3d}} $
Dividing both sides by $ kA/d $ and cross multiplying the denominators, we get
$ 9{\theta _2} - 9\theta = \theta - {\theta _1} $
Solving for $ \theta $ , we get
$\Rightarrow \theta = \dfrac{{9{\theta _2}}}{{10}} + \dfrac{{{\theta _1}}}{{10}} $ which corresponds to option (B).
Note
Unless mentioned otherwise, we must take such systems to be in a steady-state i.e. the system has been in this state for a long time. Only with this assumption can we assume that both the slabs will have the same rate of heat transfer.
Formula used: In this solution, we will use the following formula:
Rate of heat transfer in a slab with different temperatures: $ Q = \dfrac{{kA\Delta T}}{L} $ where $ A $ is the area of the surface, $ \Delta T $ is the temperature difference, and $ L $ is the length of the slab.
Complete step by step answer
In the system given to us, we will assume that the system has been left in this situation for a long time. This implies that the heat transfer will have occurred over a long time and the system can be said to have achieved a steady-state.
In this steady-state situation, we can say that the heat transfer in both the slabs will be the same. Let us assume that the temperature of the surface is $ \theta $ . Then since the heat flow rate is constant for both the surfaces will be the same and we can write
$ \dfrac{{3kA({\theta _2} - \theta )}}{d} = \dfrac{{kA(\theta - {\theta _1})}}{{3d}} $
Dividing both sides by $ kA/d $ and cross multiplying the denominators, we get
$ 9{\theta _2} - 9\theta = \theta - {\theta _1} $
Solving for $ \theta $ , we get
$\Rightarrow \theta = \dfrac{{9{\theta _2}}}{{10}} + \dfrac{{{\theta _1}}}{{10}} $ which corresponds to option (B).
Note
Unless mentioned otherwise, we must take such systems to be in a steady-state i.e. the system has been in this state for a long time. Only with this assumption can we assume that both the slabs will have the same rate of heat transfer.
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