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
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Atm = (Δt1 + Δt2) / 2
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Btm = (Δt1 - Δt2) / ln(Δt1 / Δt2)
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Ctm = (Δt1 * Δt2) ^ 0.5
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Dtm = ln(Δt1 * Δt2)
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Etm = (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)