Nucleate boiling regime is formed approximately between
5°C ≤ ΔTexcess ≤ 50°C
Boiling is a phase transition process where a liquid turns into a vapor. When heat is added to a liquid, its temperature rises until it reaches the saturation temperature. Further heat addition at constant pressure results in boiling. Boiling can occur in different regimes depending on the temperature difference between the heating surface and the saturation temperature of the liquid. This temperature difference is often called the excess temperature, denoted by $\Delta T_{\text{excess}}$.
$\Delta T_{\text{excess}} = T_{surface} - T_{saturation}$
Where:
As the excess temperature increases, the boiling process changes significantly, leading to different boiling regimes:
The nucleate boiling regime is particularly important because it provides very effective heat transfer. This regime starts when discrete bubbles begin to form and ends when the surface becomes mostly covered by a vapor film (the critical heat flux point). The range of excess temperature for nucleate boiling depends on the fluid and the surface properties, but for water boiling at atmospheric pressure on a clean surface, typical values are:
Thus, the nucleate boiling regime is formed approximately between 5°C and 50°C excess temperature.
Let's look at the given options for the range of $\Delta T_{\text{excess}}$ for the nucleate boiling regime:
Based on the typical characteristics of boiling curves and the ranges for different boiling regimes, the range 5°C $\le \Delta T_{\text{excess}} \le$ 50°C corresponds to the nucleate boiling regime.
An ic engine has a bore and a stroke length of 4 cm each. The total surface area through which heat transfer takes place in cm2 is.
Which of the following is not the regimes of pool boiling?
Analogy between momentum and heat transfer is known as
For flow through a pipe of radius R, the velocity and temperature distribution are as follows:
\(u\left( {r,x} \right) = {C_1},and\ T\left( {r,x} \right) = {C_2}{\left[{1 - (\frac{r}{R})^3} \right]}\), where C1 and C2 are constants. The bulk mean temperature is given by \({T_m} = \frac{2}{{{u_m}{R^2}}}\mathop \smallint \limits_0^R u\left( {r,x} \right)T\left( {r,x} \right)rdr,\)
with Um being the mean velocity of flow. The value of Tm is
The unit of overall heat transfer coefficient is