Water enters a tube of diameter, \( D = 60 \, {mm} \) with mass flow rate of 0.01 kg/s\(^{-1}\) as shown in the figure below. The inlet mean temperature is \( T_{{in},i} = 293 \, {K} \) and the uniform heat flux at the surface of the tube is 2000 W/m\(^{-2}\). For the exit mean temperature of \( T_{{m},o} = 353 \, {K} \), the length of the tube, \( L \) is _________m (rounded off to 1 decimal place).
Use the specific heat of water as 4181 J kg\(^{-1}\) K\(^{-1}\).
We are given:
Mass flow rate, \( \dot{m} = 0.01 \, {kg/s} \),
Inlet temperature, \( T_{{in},i} = 293 \, {K} \),
Exit temperature, \( T_{{m},o} = 353 \, {K} \),
Heat flux at the surface, \( q = 2000 \, {W/m}^2 \),
Specific heat of water, \( C_p = 4181 \, {J/kg·K} \),
Diameter of the tube, \( D = 60 \, {mm} = 0.06 \, {m} \).
Step 1: Heat Transfer Equation
The heat transferred to the water is given by the heat flux at the surface: \[ Q = \dot{m} C_p \Delta T \] where \( \Delta T = T_{{m},o} - T_{{in},i} = 353 - 293 = 60 \, {K} \).
Step 2: Heat Flux
The heat flux is also given by: \[ Q = q \cdot A \] where \( A \) is the surface area of the tube. For a cylindrical tube: \[ A = \pi D L \] Substituting this into the equation for heat transfer: \[ q \cdot \pi D L = \dot{m} C_p (T_{{m},o} - T_{{in},i}) \] Substituting the given values: \[ 2000 \cdot \pi \cdot 0.06 \cdot L = 0.01 \cdot 4181 \cdot 60 \] Solving for \( L \), we get: \[ L = \frac{0.01 \cdot 4181 \cdot 60}{2000 \cdot \pi \cdot 0.06} \] \[ L \approx 6.8 \, {m} \] Thus, the length of the tube is \( L \approx 6.8 \, {m} \).
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