Introduction & Context

Flame sterilization is a critical thermal processing technique in the food and beverage industry, where sealed metal containers are subjected to high-intensity gas flames to achieve commercial sterility. The rotation of the can during this process is essential to ensure uniform heat distribution and to prevent localized overheating, known as scorching, at the container wall.

In process engineering, this calculation is used to determine the minimum rotational speed required to maintain the internal wall temperature below a critical threshold. By balancing the external heat flux delivered by the flame with the internal heat transfer coefficient provided by the rotational agitation of the product, engineers can optimize process throughput while maintaining product quality and safety.

Methodology & Formulas

The calculation relies on an energy balance at the can wall, where the heat flux from the flame must be effectively transferred into the bulk liquid to prevent the wall temperature from exceeding the scorch limit. The governing energy balance is defined as:

\[ h_{ext} \cdot (T_{flame} - T_{wall}) = h_{int} \cdot (T_{wall} - T_{bulk}) \]

To solve for the required rotational speed, we first determine the necessary internal heat transfer coefficient, \(h_{int}\), based on the scorch limit \(T_{wall} = T_{scorch}\):

\[ h_{int} = \frac{h_{ext} \cdot (T_{flame} - T_{scorch})}{T_{scorch} - T_{bulk}} \]

The internal heat transfer coefficient is derived from the Nusselt number (\(Nu\)), which is calculated using the following empirical correlation for agitated vessels:

\[ Nu = 0.36 \cdot Re^{2/3} \cdot Pr^{1/3} \cdot \left( \frac{\mu}{\mu_{wall}} \right)^{0.14} \]

Where the Reynolds number (\(Re\)) and the internal heat transfer coefficient are related to the rotational speed (\(N\)) as follows:

\[ Re = \frac{\rho \cdot N \cdot D^2}{\mu} \] \[ h_{int} = \frac{k \cdot Nu}{D} \]

By rearranging these equations, the rotational speed in revolutions per second is isolated as:

\[ N = \frac{Re \cdot \mu}{\rho \cdot D^2} \]
Regime / Condition Criteria
Turbulent Mixing (Standard Correlation) \(300 < Re < 3 \cdot 10^5\)
Laminar Film (Thermal Entry) \(Re \leq 300\)
External Correlation Validity \(100 < Re_{ext} < 10^5\)
Thermal Safety Constraint \(T_{scorch} > T_{bulk}\)