Heat Transfer Flashcards
7 cards from real NCEES practice questions. Tap to flip, then mark Knew It or Still Learning — missed cards come back until you master them.
Read the first 7 Heat Transfer flashcards as text
Thermal diffusivity α is defined as which of the following combinations of material properties?
Answer: k/(ρcp)
Thermal diffusivity α = k/(ρcp) represents how quickly a material conducts heat relative to its ability to store it.
For a hollow cylinder with inner radius r₁, outer radius r₂, length L, and thermal conductivity k, the conductive thermal resistance is:
Answer: ln(r₂/r₁) / (2πkL)
Integrating Fourier's Law in cylindrical coordinates gives R_cyl = ln(r₂/r₁)/(2πkL).
The Log Mean Temperature Difference (LMTD) method is primarily used to analyze:
Answer: Heat exchanger performance
LMTD provides the effective mean driving temperature difference for heat exchangers where temperatures vary along the length.
In a counterflow heat exchanger compared to a parallel-flow arrangement with the same inlet conditions and UA product, which statement is correct?
Answer: Counterflow achieves higher LMTD and greater heat transfer
Counterflow maintains a more uniform temperature difference along its length, yielding a higher LMTD and therefore greater heat transfer capacity.
Fin efficiency (η_f) is defined as:
Answer: Actual fin heat transfer divided by maximum heat transfer if entire fin were at base temperature
Fin efficiency η_f = q_actual / q_max, where q_max = hA_f(T_b − T∞) assumes the entire fin surface is at the base temperature.
For radiation exchange between two large parallel plates with emissivities ε₁ and ε₂, the net heat flux is given by:
Answer: q" = σ(T₁⁴ − T₂⁴) / (1/ε₁ + 1/ε₂ − 1)
The radiation network for two large parallel plates gives q" = σ(T₁⁴−T₂⁴)/(1/ε₁ + 1/ε₂ − 1), accounting for surface resistances.
The Prandtl number (Pr) for a fluid is defined as the ratio of:
Answer: Momentum diffusivity to thermal diffusivity (ν/α)
Pr = ν/α = μcp/k; it characterizes the relative thickness of the velocity and thermal boundary layers.
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