Piping Systems and Applications! - Resources, Tools and Basic Information for Engineering and Design.
Arithmetic Mean Temperature Difference - AMTD - and Logarithmic Mean Temperature Difference - LMTD - definition formulas with examples
Sponsored Links
According to Newton's Law of Cooling heat transfer rate is related to the instantaneous temperature difference between a hot and a cold media
The determination of the mean temperature difference in a heat transfer process depends upon the direction of fluid flow involved in the process. The primary and secondary fluid in an heat exchanger process may
With saturation of steam the primary fluid temperature can be taken as a constant because heat
is transferred as a result of a change of phase only. The temperature profile in the primary
fluid is not dependent on the direction of flow.
When the secondary fluid passes over the heat transfer surface, the highest rate of heat transfer
occurs at the inlet and progressively decays with higher secondary fluid temperature along its
way to the outlet.
The rise in secondary temperature is non-linear and is best represented by a logarithmic calculation. For this purpose the mean temperature difference chosen is termed the
LMTD can be expressed as:
LMTD = (TD2 - TD1) / ln(TD2 / TD1) (1)
where
LMTD = Logarithmic Mean Temperature Difference oF (oC)
TD1 = Tp1 - Ts2 - Entering primary fluid and leaving secondary fluid temperature difference oF (oC)
TD2 = Tp2 - Ts1 - Leaving primary fluid and entering secondary fluid temperature difference oF (oC)
An easier but less accurate way to calculate the mean temperature difference is to consider the
AMTD can be expressed as:
AMTD = (Tp1 + Tp2) / 2 - (Ts1 + Ts2) / 2 (2)
where
AMTD = Arithmetic Mean Temperature Difference oF (oC)
Tp1 = primary inlet temperature oF (oC)
Tp2 = primary outlet temperature oF (oC)
Ts1 = secondary inlet temperature oF (oC)
Ts2 = secondary outlet temperature oF (oC)
A linear increase in the secondary fluid temperature makes it more easy to do manual calculations. AMTD will in general give a satisfactory approximation for the mean temperature difference.
When heat is transferred as a result of a change of phase in condensation or evaporation heat exchangers, the temperature of the primary or secondary fluid remains constant. The equation can then be simplified by setting
Tp1 = Tp2 or Ts1 = Ts2 oF (oC)
Steam at 2 bar gauge heats water from 20oC to 50oC. The saturation temperature of steam at 2 bar gauge is 134oC.
Arithmetic Mean Temperature Difference can be calculated as:
AMTD = (134oC + 134oC) / 2 - (20oC + 50oC) / 2
= 99 oC
Log Mean Temperature Difference can be calculated as:
LMTD = (134oC - 20oC - (134oC - 50oC)) / ln((134oC - 20oC) / (134oC - 50oC))
= 98.24 oC
Sponsored Links
Difficult to find your favorite ToolBox page? Add a link to the page in your own personal Shortlist!
Translate this page to
Spanish
French
German
Italian
Dutch
Norwegian
© The Piping ToolBox
The content in The Piping ToolBox is copyrighted but can be used with NO WARRANTY or LIABILITY. Important information should always be double checked with alternative sources. All applicable national and local regulations and practices concerning this aspects must be strictly followed and adhered to.
We appreciate any comments and tips on how to make The Piping ToolBox a better information source. Please contact us by email if You find any faults, inaccurate, or otherwise unacceptable information.
5 12 1
View Engineering, Design and Construction news in the absolute FREE Automatic WebSite Viewer. Engineering Breaking News!