What is the form of the overall heat transfer equation?

Study for the EPRI Heat Transfer and Fluid Flow Test. Prepare with flashcards and multiple choice questions, each with hints and explanations. Get ready for your exam!

Multiple Choice

What is the form of the overall heat transfer equation?

Explanation:
The main idea is that the rate of heat transfer through a surface or exchanger is described by the overall heat transfer form Q = U A ΔT_lm. Here, U is the overall heat transfer coefficient that bundles together conduction through walls and convection on both sides, A is the heat transfer area, and ΔT_lm is the log-mean temperature difference between the two fluids or sides. The temperature difference typically isn’t constant along the length of an exchanger, especially in counterflow or parallel-flow configurations, so using a single ΔT would misrepresent the driving force. The log-mean temperature difference correctly averages that varying driving force to give the true heat transfer rate. The other expressions represent different situations. Q = U A ΔT would be valid only if the temperature difference were effectively constant along the length, which is not generally the case. Q = h A ΔT is the local form for convection at a single surface with a heat transfer coefficient h. Q = k A ΔT / L comes from Fourier’s law for conduction through a solid slab of thickness L with thermal conductivity k.

The main idea is that the rate of heat transfer through a surface or exchanger is described by the overall heat transfer form Q = U A ΔT_lm. Here, U is the overall heat transfer coefficient that bundles together conduction through walls and convection on both sides, A is the heat transfer area, and ΔT_lm is the log-mean temperature difference between the two fluids or sides. The temperature difference typically isn’t constant along the length of an exchanger, especially in counterflow or parallel-flow configurations, so using a single ΔT would misrepresent the driving force. The log-mean temperature difference correctly averages that varying driving force to give the true heat transfer rate.

The other expressions represent different situations. Q = U A ΔT would be valid only if the temperature difference were effectively constant along the length, which is not generally the case. Q = h A ΔT is the local form for convection at a single surface with a heat transfer coefficient h. Q = k A ΔT / L comes from Fourier’s law for conduction through a solid slab of thickness L with thermal conductivity k.

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