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Question

A spherical thermocouple junction of diameter 0.706 mm is to be used for measurement of temperature of a gas stream. The convective heat transfer coefficient on bead surface is \(400~\frac{W}{{{m^2} - K}}\). The thermo physical properties of thermocouple material are \(k = 20~\frac{W}{{m - K}},\ c = 400\frac{J}{{kg - K}},\ \rho = 8500~\frac{{kg}}{{{m^3}}}\). If the thermocouple initially at 30°C is placed in a hot stream of 300°C, the time taken by the bead to reach 298°, is

The correct answer is

4.9 sec

Thermocouple Response Time Calculation for Gas Stream Temperature Measurement

This problem involves determining the time it takes for a thermocouple junction to reach a specific temperature when exposed to a different environment. This is a classic transient heat transfer problem that can often be solved using the lumped system analysis, provided the internal resistance to heat conduction is small compared to the resistance to convection.

Lumped System Analysis Principle

The lumped system analysis assumes that the temperature within the object (the thermocouple bead in this case) is uniform at any given time. This is valid when the Biot number ($Bi$) is less than 0.1. The transient heat transfer is governed by Newton's law of cooling:

$$ \rho V c \frac{dT}{dt} = -h A (T - T_\infty) $$

Where:

  • $\rho$ = Density of the thermocouple material ($\frac{kg}{m^3}$)
  • $V$ = Volume of the thermocouple bead ($m^3$)
  • $c$ = Specific heat of the thermocouple material ($\frac{J}{kg \cdot K}$)
  • $T$ = Temperature of the thermocouple bead at time $t$ ($^\circ C$)
  • $t$ = Time ($s$)
  • $h$ = Convective heat transfer coefficient ($\frac{W}{m^2 \cdot K}$)
  • $A$ = Surface area of the thermocouple bead ($m^2$)
  • $T_\infty$ = Temperature of the surrounding fluid (gas stream) ($^\circ C$)

The solution to this first-order ordinary differential equation is:

$$ \frac{T(t) - T_\infty}{T_i - T_\infty} = e^{-\left(\frac{hA}{\rho V c}\right)t} $$

The term $\tau = \frac{\rho V c}{hA}$ is known as the thermal time constant.

$$ \frac{T(t) - T_\infty}{T_i - T_\infty} = e^{-t/\tau} $$

Rearranging to solve for time $t$:

$$ t = -\tau \ln\left(\frac{T(t) - T_\infty}{T_i - T_\infty}\right) $$

Calculating Necessary Parameters

First, let's list the given values and calculate the required geometric parameters for the spherical thermocouple junction.

  • Diameter, $D = 0.706~\text{mm} = 0.706 \times 10^{-3}~\text{m}$
  • Radius, $r = D/2 = 0.353 \times 10^{-3}~\text{m}$
  • Convective heat transfer coefficient, $h = 400~\frac{W}{m^2 \cdot K}$
  • Thermal conductivity, $k = 20~\frac{W}{m \cdot K}$
  • Specific heat, $c = 400~\frac{J}{kg \cdot K}$
  • Density, $\rho = 8500~\frac{kg}{m^3}$
  • Initial temperature, $T_i = 30^\circ C$
  • Gas stream temperature, $T_\infty = 300^\circ C$
  • Target temperature, $T(t) = 298^\circ C$

Geometric Properties of the Sphere

For a sphere:

  • Surface Area, $A = \pi D^2$
  • Volume, $V = \frac{4}{3}\pi r^3 = \frac{4}{3}\pi \left(\frac{D}{2}\right)^3 = \frac{\pi D^3}{6}$

The ratio $\frac{A}{V}$ is crucial for calculating the time constant:

$$ \frac{A}{V} = \frac{\pi D^2}{\frac{\pi D^3}{6}} = \frac{6}{D} $$ $$ \frac{A}{V} = \frac{6}{0.706 \times 10^{-3}~\text{m}} \approx 8498.58~\text{m}^{-1} $$

Calculating the Thermal Time Constant ($\tau$)

Now, we can calculate the thermal time constant $\tau$:

$$ \tau = \frac{\rho V c}{hA} = \frac{\rho c}{h \left(\frac{A}{V}\right)} $$ $$ \tau = \frac{(8500~\frac{kg}{m^3}) (400~\frac{J}{kg \cdot K})}{(400~\frac{W}{m^2 \cdot K}) \left(\frac{6}{0.706 \times 10^{-3}~\text{m}}\right)} $$ $$ \tau = \frac{8500 \times 400}{400 \times \frac{6}{0.706 \times 10^{-3}}} = \frac{8500 \times 0.706 \times 10^{-3}}{6} $$ $$ \tau = \frac{5990 \times 10^{-3}}{6} = \frac{5.99}{6} \approx 0.9983~\text{seconds} $$

Calculating the Time Taken

We need to find the time $t$ when the thermocouple temperature reaches $298^\circ C$. Plugging the values into the rearranged formula:

$$ t = -\tau \ln\left(\frac{T(t) - T_\infty}{T_i - T_\infty}\right) $$

Substitute the temperatures:

$$ \frac{T(t) - T_\infty}{T_i - T_\infty} = \frac{298^\circ C - 300^\circ C}{30^\circ C - 300^\circ C} = \frac{-2}{-270} = \frac{2}{270} = \frac{1}{135} $$

Now calculate the time $t$:

$$ t = -(0.9983~\text{s}) \ln\left(\frac{1}{135}\right) $$

Using the property $\ln(1/x) = -\ln(x)$:

$$ t = (0.9983~\text{s}) \ln(135) $$

Calculate the natural logarithm of 135:

$$ \ln(135) \approx 4.9053 $$

Finally, calculate the time:

$$ t \approx (0.9983~\text{s}) \times 4.9053 \approx 4.900~\text{seconds} $$

Conclusion

The time taken for the thermocouple bead to reach $298^\circ C$ is approximately 4.9 seconds. This result aligns with option 4.

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Important Questions from Transient Heat Transfer

  1. Consider the following statements about the thermal diffusivity of a substance:

    1. It is directly proportional to density.

    2. It is inversely proportional to specific heat.

    3. It is inversely proportional to thermal conductivity.

    4. It is directly proportional to thermal conductivity.

    Which of the given statements are INCORRECT?

  2. Lumped heat transfer analysis of a solid object suddenly exposed to a fluid medium at a different temperature is valid when

  3. The dimensionless numbers used for analyzing the transient heat conduction problems in a plane wall, cylinder, and sphere is ________.
  4. Choose the correct statement.

    The curve for unsteady state heating and cooling of bodies with Bi < 0.1 is

  5. A body cools from 90°C to 80°C in 5 minutes. Under the same external conditions to cool from 80°C to 70°C the body will take

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