**overall heat transfer coefficient,**known as a

**U-factor**. The U-factor is defined by an expression analogous to

**Newton’s law of cooling.**Moreover, engineers also use the logarithmic mean temperature difference (

**LMTD**) to determine the temperature driving force for heat transfer in heat exchangers.

A **heat exchanger** typically involves two flowing fluids separated by a solid wall. Many of the heat transfer processes encountered in the industry involve composite systems and even involve a combination of both conduction and convection. Heat is first transferred from the hot fluid to the wall by convection, through the wall by conduction, and then to the cold fluid again by convection.

It is often convenient to work with an** overall heat transfer coefficient, **known as a **U-factor **with these composite systems. The U-factor is defined by an expression analogous to **Newton’s law of cooling**:

The **overall heat transfer coefficient, U,** is related to the total thermal resistance and depends on the geometry of the problem. For example, heat transfer in a steam generator involves convection from the bulk of the reactor coolant to the steam generator inner tube surface, conduction through the tube wall, and convection (boiling) from the outer tube surface to the secondary side fluid.

In cases of combined heat transfer for a heat exchanger, there are two values for h. The convective heat transfer coefficient (h) for the fluid film inside the tubes and a convective heat transfer coefficient for the fluid film outside the tubes. The tube wall’s thermal conductivity (k) and thickness (Δx) must also be accounted for.

**Online monitoring of commercial heat exchangers is done by tracking the overall heat transfer coefficient because the overall heat transfer coefficient tends to decline over time due to fouling. By periodically calculating the overall heat transfer coefficient from exchanger flow rates and temperatures, the operator of the heat exchanger can estimate the lifetime of heat exchangers.**

## Example: Calculation of Heat Exchanger

Consider a **parallel-flow heat exchanger** used to cool oil from 70°C to 40°C using water available at 30°C. The outlet temperature of the water is 36°C, and the rate of flow of oil is 1 kg/s. The specific heat of the oil is 2.2 kJ/kg K. The overall heat transfer coefficient **U = 200 W/m ^{2} K**.

Calculate the** logarithmic mean temperature difference**. Determine the **area** of this heat exchanger required for this performance.

**LMTD**

The logarithmic mean temperature difference can be calculated simply using its definition:

- Area of Heat Exchanger

To calculate the area of this heat exchanger, we have to calculate the heat flow rate using the mass flow rate of oil and LMTD.

The required area of this heat exchanger can be then directly calculated using the general heat transfer equation: