Showing posts with label LMTD. Show all posts
Showing posts with label LMTD. Show all posts

Corrected Log Mean Temperature Difference for Shell-and-Tube Heat Exchangers

This Excel spreadsheet calculates the corrected LMTD for shell-and-tube heat exchangers with multiple shell-side passes.


True log mean temperature differences are only valid in double-pipe (or tubular) heat exchangers; hence for more complex shell-and-tube arrangements, we have to muliply the LMTD by a factor.

The equations used in the spreadsheet are taken from the work of Bowman et al (1940) and are given below.
Note that R is the temperature change ratio of the hot and cold streams, while P is the temperature change of the cold fluid divided by the maximum temperature difference.  F is the LMTD correction factor.

Perrys Chemical Engineers' Handbook states LMTD correction factors lower than 0.8 indicate inefficient heat exchanger design, while the Heat Exchanger Design Handbook advises that the minimum value should be 0.75.

Download Excel spreadsheet to calculate Corrected Log Mean Temperature Difference

Preliminary Heat Exchanger Design

Introduction
This article will help you understand how you can estimate the initial design characteristics of a heat exchanger.  An Excel spreadsheet using the equations developed in this article is also provided. The equations are derived from a simple heat balance, and a few other elementary relationships.

These equations act as initial estimates, and the results will need to be refined by more sophisticated calculations.  If you just want the spreadsheet then click here, but read the rest of the article if you want to understand the theory.

Theory
Consider a heat exchanger operating in countercurrent flow.

Assume that we know the
  • desired input and output temperatures of all streams, 
  • specific heat capacities, 
  • the overall heat transfer coefficient, 
  • and the mass flowrate of the cold stream.  
We will now calculate
  • the flowrate of the hot stream, 
  • the heat transfer rate 
  • and the heat transfer area.
A heat balance on the cold and hot streams gives


Qc gives the overall heat transfer rate.

But Qh = Qc.  Equating both equations and rearranging for the mass flowrate of the hot liquid stream gives


The log mean temperature difference is


The overall heat transfer rate Qc can be defined in terms of the log mean temperature difference


The final two equations can be easily rearranged to give the overall heat transfer area A in terms of the heat transfer rate Qc, the heat transfer area A and the log mean temperature difference.

Excel Implementation
Implementing these basic heat transfer equations in Excel is easy, and no special explanation is required.


Download Excel Spreadsheet for Preliminary Heat Exchanger Design

Related article: Modeling the Temperature Dynamics of a Cross-Flow Heat Exchanger