Logarithmic mean temperature difference (LMTD): Given inlet and outlet temperature differences Δt1 and Δt2 between hot and cold streams, the correct expression for the mean temperature difference is

Mechanical Engineering Heat Transfer, Refrigeration and Air Conditioning Difficulty: Medium
Choose an option
  • A
    tm = (Δt1 + Δt2) / 2
  • B
    tm = (Δt1 - Δt2) / ln(Δt1 / Δt2)
  • C
    tm = (Δt1 * Δt2) ^ 0.5
  • D
    tm = ln(Δt1 * Δt2)
  • E
    tm = (Δt1 - Δt2) * ln(Δt1 / Δt2)

Answer

Correct Answer: tm = (Δt1 - Δt2) / ln(Δt1 / Δt2)

Explanation

Introduction / Context:The LMTD method is widely used in heat exchanger analysis to compute heat transfer rate when terminal temperatures are known. The right formula is essential for accurate design.

Given Data / Assumptions:

  • Two fluids exchanging heat with constant overall heat transfer coefficient U and area A.
  • Terminal temperature differences Δt1 and Δt2 at the two ends of the exchanger.
  • No phase change and steady state for simplicity.

Concept / Approach:Since temperature difference varies exponentially along the length, the appropriate average is the logarithmic mean, not the arithmetic or geometric mean. Heat duty is Q = U * A * tm where tm = (Δt1 - Δt2) / ln(Δt1 / Δt2).

Step-by-Step Solution:Write local heat transfer: dQ = U * dA * Δt(x).Integrate along length using boundary conditions to derive tm.Obtain tm = (Δt1 - Δt2) / ln(Δt1 / Δt2).Use Q = U * A * tm to compute duty.

Verification / Alternative check:Limiting case Δt1 → Δt2 gives tm → Δt1 (using L’Hôpital’s rule), matching physical expectation of uniform Δt.

Why Other Options Are Wrong:

  • Arithmetic or geometric means do not satisfy the exponential temperature profile implied by energy balance.
  • ln(Δt1 * Δt2) and (Δt1 - Δt2) * ln(Δt1 / Δt2) are dimensionally or mathematically incorrect.

Common Pitfalls:Swapping Δt1 and Δt2 positions or using base-10 logarithm incorrectly (natural logarithm is standard in derivation).

Final Answer:tm = (Δt1 - Δt2) / ln(Δt1 / Δt2)

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