Difficulty: Medium
Correct Answer: De = 4 * (P^2 - (π * d^2)/4) / (π * d)
Explanation:
Introduction / Context:
On the shell side of a shell-and-tube heat exchanger, fluid weaves through the tube bundle and baffle windows. For pressure drop and heat-transfer estimation, engineers use an equivalent or hydraulic diameter that reflects the characteristic length scale of flow passages formed by tube pitch and tube diameter.
Given Data / Assumptions:
Concept / Approach:
The equivalent (hydraulic) diameter is defined as De = 4 * (flow area) / (wetted perimeter). For a square pitch array, the net flow area per tube cell is P^2 - (π d^2)/4. The wetted perimeter per cell against which fluid shears is approximately π d. Substituting these into the definition gives a compact expression for De.
Step-by-Step Solution:
Compute net flow area per tube cell: A = P^2 - (π d^2)/4.Compute wetted perimeter per cell: Pw = π d.Hydraulic diameter: De = 4 * A / Pw.Therefore, De = 4 * (P^2 - (π d^2)/4) / (π d).
Verification / Alternative check:
Numerically, 4/π ≈ 1.273 and (π/4) ≈ 0.785, so an equivalent form is De ≈ 1.27 * (P^2 - 0.785 d^2) / d. Both are algebraically identical, confirming correctness.
Why Other Options Are Wrong:
Common Pitfalls:
Mixing triangular and square pitch constants; forgetting that flow area excludes the tube's circular cross-section area; confusing shell-side De with tube-side diameter.
Final Answer:
De = 4 * (P^2 - (π * d^2)/4) / (π * d)
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