The logarithmic mean temperature difference for parallel flow heat exchangers is
Heat exchangers are devices that transfer heat between two or more fluids at different temperatures. Understanding the temperature variation along the length of the heat exchanger is crucial for its design and analysis. The temperature difference between the hot and cold fluids often varies along the heat exchanger's length. To account for this variation in heat transfer calculations, the concept of Logarithmic Mean Temperature Difference (LMTD) is used.
Heat exchangers can operate in different flow arrangements. Two common types are:
The Logarithmic Mean Temperature Difference (LMTD), denoted as \(\Delta T_{lm}\) or \(\text{LMTD}\), is a method to determine the average temperature difference between the two fluids in a heat exchanger. It is used when the temperature difference varies significantly along the heat transfer surface. The general formula for LMTD is given by:
\[ \text{LMTD} = \frac{\Delta T_1 - \Delta T_2}{\ln\left(\frac{\Delta T_1}{\Delta T_2}\right)} \]
Where:
For a parallel flow heat exchanger, the two temperature differences, \(\Delta T_1\) and \(\Delta T_2\), correspond to the temperature differences at the inlet and outlet ends, respectively.
Consider:
\(\theta_1\) = Temperature difference at the inlet of the parallel flow heat exchanger
\(\theta_2\) = Temperature difference at the outlet of the parallel flow heat exchanger
Using these notations, the formula for the Logarithmic Mean Temperature Difference (LMTD) for a parallel flow heat exchanger is:
\[ \text{LMTD}_{\text{parallel flow}} = \frac{\theta_1 - \theta_2}{\ln\left(\frac{\theta_1}{\theta_2}\right)} \]
This formula helps in calculating the total heat transfer rate (Q) in the heat exchanger using the equation:
\[ Q = U A \, \text{LMTD} \]
Where U is the overall heat transfer coefficient and A is the heat transfer area.
Let's examine the given options and compare them with the standard LMTD formula for parallel flow heat exchangers.
| Option | Formula | Comparison with LMTD Standard Formula \(\left(\frac{\theta_1 - \theta_2}{\ln(\theta_1 / \theta_2)}\right)\) |
|---|---|---|
| 1 | \(\rm \frac{\theta_1 - \theta_2}{ \ln (\theta_1 - \theta_2)}\) | Incorrect. The denominator should be \(\ln(\theta_1 / \theta_2)\), not \(\ln(\theta_1 - \theta_2)\). |
| 2 | \(\rm \frac{\theta_2 - \theta_1}{ \ln (\theta_1 / \theta_2)}\) | Incorrect. The numerator should be \(\theta_1 - \theta_2\), not \(\theta_2 - \theta_1\), to maintain consistency with the order in the logarithm. The LMTD must be a positive value. |
| 3 | \(\rm \frac{\theta_1 - \theta_2}{ \ln (\theta_1 + \theta_2)}\) | Incorrect. The denominator should be \(\ln(\theta_1 / \theta_2)\), not \(\ln(\theta_1 + \theta_2)\). |
| 4 | \(\rm \frac{\theta_1 - \theta_2}{ \ln (\theta_1 / \theta_2)}\) | Correct. This formula perfectly matches the definition of LMTD for parallel flow heat exchangers where \(\theta_1\) and \(\theta_2\) are the temperature differences at the two ends. |
Based on the standard formula for Logarithmic Mean Temperature Difference for parallel flow heat exchangers, option 4 is the correct representation.
The fin effectiveness can be enhanced by selecting _____ value of heat transfer co-efficient.
NTU, which is a measure of effectiveness of heat exchanger, stands for _________.
LMTD stands for _______.
Water (Cp = 4.18 kJ/kg.K) at 80°C enters a counter flow heat exchanger with a mass flow rate of 0.5 kg/s. Air (Cp = 1 kJ/kg.K) enters at 30°C with a mass flow rate of 2.09 kg/s. If the effectiveness of the heat exchanger is 0.8, the LMTD (in °C) is
For a heat exchanger, ΔTmax is the maximum temperature difference and ΔTmin is the minimum temperature difference between the two fluids. LMTD is the log mean temperature difference. Cmin and Cmax are the minimum and the maximum heat capacity rates. The maximum possible heat transfer (Qmax) between the two fluids is