To find the temperature at the interface of the rods when equilibrium is established, we use the principle of thermal conduction. The heat flow rate through both rods A and B must be equal at equilibrium.
Given:
Formula:
The heat flow rate \((Q/t)\) for cylindrical rods is given by:
\( \frac{Q}{t} = \frac{KA(T_{\text{hot}} - T_{\text{cold}})}{L} \)
For both rods A and B at equilibrium, \( \frac{Q_A}{t} = \frac{Q_B}{t} \). Therefore:
\( \frac{K_A \pi r_A^2 (400 - T)}{L_A} = \frac{K_B \pi r_B^2 (T - 200)}{L_B} \)
Cancel \(\pi\) and substitute given ratios:
\( \frac{(1/2) \cdot (2r_B)^2 \cdot (400 - T)}{(1/2)L_B} = \frac{K_B \cdot r_B^2 \cdot (T - 200)}{L_B} \)
Simplify the equation:
\((1/2) \cdot 4 \cdot (400 - T) = T - 200\)
Thus:
\( 2 \cdot (400 - T) = T - 200 \)
Expand and solve for \( T \):
\( 800 - 2T = T - 200 \)
\( 800 + 200 = 3T \)
\( 1000 = 3T \)
\( T = \frac{1000}{3} \)
Thus, the temperature at the interface \( T = 333.33 \, \text{K} \).
Since this value is not in the expected range (360,360), please verify problem setup and data inputs for any discrepancies.
Step 1: Define the thermal resistance of each rod.
The thermal resistance \( R_{th} \) of a cylindrical rod is given by \( R_{th} = \frac{L}{KA} \),
where
\( L \) is the length,
\( K \) is the thermal conductivity, and
\( A \) is the cross-sectional area of the rod.
The cross-sectional area of a cylindrical rod with radius \( r \) is \( A = \pi r^2 \).
For rod A: Length \( L_A \) Radius \( r_A \) Thermal conductivity \( K_A \) Area \( A_A = \pi r_A^2 \)
Thermal resistance \( R_{th,A} = \frac{L_A}{K_A \pi r_A^2} \) For rod B:
Length \( L_B \) Radius \( r_B \) Thermal conductivity \( K_B \) Area \( A_B = \pi r_B^2 \)
Thermal resistance \( R_{th,B} = \frac{L_B}{K_B \pi r_B^2} \)
Step 2: Use the given ratios to relate the thermal resistances.
We are given \( \frac{L_A}{L_B} = \frac{1}{2} \), \( \frac{r_A}{r_B} = 2 \), and \( \frac{K_A}{K_B} = \frac{1}{2} \).
Consider the ratio of the thermal resistances: \[ \frac{R_{th,A}}{R_{th,B}} = \frac{\frac{L_A}{K_A \pi r_A^2}}{\frac{L_B}{K_B \pi r_B^2}} = \frac{L_A}{L_B} \cdot \frac{K_B}{K_A} \cdot \frac{\pi r_B^2}{\pi r_A^2} = \frac{L_A}{L_B} \cdot \frac{K_B}{K_A} \cdot \left(\frac{r_B}{r_A}\right)^2 \] Substitute the given ratios: \[ \frac{R_{th,A}}{R_{th,B}} = \left(\frac{1}{2}\right) \cdot \left(\frac{1}{1/2}\right) \cdot \left(\frac{1}{2}\right)^2 = \frac{1}{2} \cdot 2 \cdot \frac{1}{4} = \frac{1}{4} \] So, \( R_{th,A} = \frac{1}{4} R_{th,B} \), or \( R_{th,B} = 4 R_{th,A} \).
Step 3: Apply the concept of thermal current in series.
When the rods are joined in series, the rate of heat flow (thermal current \( I_{th} \)) through both rods is the same at equilibrium. Let the temperature of the interface be \( T \).
The thermal current through rod A is given by: \[ I_{th} = \frac{T_1 - T}{R_{th,A}} = \frac{400 - T}{R_{th,A}} \] The thermal current through rod B is given by: \[ I_{th} = \frac{T - T_2}{R_{th,B}} = \frac{T - 200}{R_{th,B}} \] Equating the thermal currents: \[ \frac{400 - T}{R_{th,A}} = \frac{T - 200}{R_{th,B}} \] Substitute \( R_{th,B} = 4 R_{th,A} \): \[ \frac{400 - T}{R_{th,A}} = \frac{T - 200}{4 R_{th,A}} \] Multiply both sides by \( 4 R_{th,A} \): \[ 4(400 - T) = T - 200 \] \[ 1600 - 4T = T - 200 \] \[ 1600 + 200 = T + 4T \] \[ 1800 = 5T \] \[ T = \frac{1800}{5} = 360 \, K \] The temperature of the rods interface is \( 360 \, K \).
Three conductors of same length having thermal conductivity \(k_1\), \(k_2\), and \(k_3\) are connected as shown in figure. Area of cross sections of 1st and 2nd conductor are same and for 3rd conductor it is double of the 1st conductor. The temperatures are given in the figure. In steady state condition, the value of θ is ________ °C. (Given: \(k_1\) = 60 Js⁻¹m⁻¹K⁻¹,\(k_2\) = 120 Js⁻¹m⁻¹K⁻¹, \(k_3\) = 135 Js⁻¹m⁻¹K⁻¹) 
Match the LIST-I with LIST-II
| LIST-I | LIST-II | ||
|---|---|---|---|
| (Type of Fouling) | (Fouling Mechanism) | ||
| A | Precipitation | IV | Precipitation of dissolved substances... |
| B | Freezing | III | Solidification of Liquid components... |
| C | Particulate | I | Accumulation of fine particles suspended... |
| D | Corrosion | II | Heat transfer surface reacts with ambient... |
An organic compound (X) with molecular formula $\mathrm{C}_{3} \mathrm{H}_{6} \mathrm{O}$ is not readily oxidised. On reduction it gives $\left(\mathrm{C}_{3} \mathrm{H}_{8} \mathrm{O}(\mathrm{Y})\right.$ which reacts with HBr to give a bromide (Z) which is converted to Grignard reagent. This Grignard reagent on reaction with (X) followed by hydrolysis give 2,3-dimethylbutan-2-ol. Compounds (X), (Y) and (Z) respectively are: