Latest Downloads
-
Water Bath Indirect Heaters
Art Montemayor - Oct 12 2018 02:35 PM
-
Petroleum: A Primer for Kansas
Art Montemayor - Oct 12 2018 02:27 PM
-
Spray Tower for Flue Gas Scrubbing Design
ankur2061 - May 02 2018 02:31 PM
-
Selection of Vertical Tanks
ankur2061 - Apr 19 2018 07:42 AM
-
Pressure Drop Calculator for Strainers 1
ankur2061 - Mar 24 2017 02:04 PM
-
Horizontal Pig Trap System Design Guidelines
ankur2061 - Jan 14 2017 02:54 PM
-
Performance Prediction of 3-Stage Propane Refrigeration System
ankur2061 - Aug 08 2016 02:43 PM
-
Centrifugal Pump Troubleshooting Checklist
ankur2061 - Dec 17 2015 08:18 AM
-
Compressor Troubleshooting Checklist
ankur2061 - Sep 08 2015 11:43 AM
-
Amine Sweetening Unit Preliminary Design
ankur2061 - May 19 2015 09:35 AM
Popular Store Titles
Tank Jacket Calculator
Specification Sheet Collection
PIPESIZE
Relief Valve Sizing
Rupture Disc Sizing
Chemical and Process Engineering Resources
Submitted Chris Haslego, Nov 21 2011 11:21 AM | Last updated Nov 21 2011 01:29 PM
Category: | Heat Transfer Technology |
Question: | For a heat exchanger, will the overall heat transfer coefficient increase along with an increase in LMTD (log mean temperature difference) around the unit? |
Keywords: | lmtd,u-value,heat,transfer,coefficient |
Answer: | The overall heat transfer coefficient is generally weakly dependent on temperature. As the temperatures of the fluids change, the degree to which the overall heat transfer coefficient will be affected depends on the sensitivity of the fluid's viscosity to temperature. If both fluids are water, for example, the overall heat transfer coefficient won't vary much with temperature because water's viscosity doesn't change dramatically with temperature. If, however, one of the fluids is oil which may have a viscosity of 1000 cP at 50 ??F and 5 cP at 400 ??F, then indeed the overall heat transfer coefficient would be much better at higher temperatures since the oil side would be limiting.Realize that the overall heat transfer coefficient is dictated by the local heat transfer coefficients and the wall resistances of the heat exchanger. The local heat transfer coefficients are dictated by the fluid's physical properties and the velocity of the fluid through the exchanger. So, for a given heat exchanger, fluid flow rates, and characteristics of each fluid....the area of the exchanger and the overall heat transfer coefficients are fixed (theoretically anyway....as the overall heat transfer coefficient does vary slightly along the length of the exchanger with temperature as I've noted and the U-value will decrease over time with fouling). But, if the inlet temperatures of the fluids change, the heat duty (Q) is where variable that will change with it for the most part. For example, for an installed heat exchanger, if the LMTD or log mean temperature difference increases or decreases based on temperature variations of the fluids, then a given, fixed exchanger will simply transfer more heat (for a larger LMTD) or less heat (for a small LMTD). In short, temperature difference is the "driving force" which determines how much heat is transferred. If the LMTD decreases, but you want to keep Q the same, then you have two choice: increase the heat transfer area or find a way to increase the overall heat transfer coefficient (U-value) via heat transfer enhancement or a different heat exchanger technology.Again, with an increased temperature, the viscosity of the fluids will decrease (to what degree depends on the fluids), so there would technically be an increase in the U-value, but often times, it won't be substantial. |
Links: | Basics of Industrial Heat Transfer Correlations for Convective Heat Transfer |
Forum Quick Links
Tech Q & A Category List
-
Bulk Solids
-
ChE Outside the Plant
-
Chemical Process Business
-
Chemistry Basics
-
Corrosion
-
Equipment Design
-
Experimentation and Testing
-
Fluid Dynamics
-
Heat Transfer Technology
-
Industrial Utilities
-
Mass Transfer
-
Physical Property Information
-
Plant Basics
-
Plant Economics
-
Preparing to Become an Engineer
-
Process Control
-
Reactions and Processes
-
Refining
-
Safety
-
Separation Technology
-
The Environment
-
Thermodynamics
0 Comments