Shell-and-tube heat exchangers – Purpose of shell-side baffles What is the principal effect of installing baffles on the shell side of a shell-and-tube heat exchanger?
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Aincrease the cross-section of the shell side liquid.
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Bforce the liquid to flow parallel to the bank.
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Cincrease the shell side heat transfer co-efficient.
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Ddecrease the shell side heat transfer co-efficient.
Answer
Correct Answer: increase the shell side heat transfer co-efficient.
Explanation
Introduction / Context:Baffles are common internals in shell-and-tube exchangers. Their geometry and spacing critically impact shell-side hydrodynamics, pressure drop, and heat transfer. Understanding their role guides trade-offs between performance and pumping cost.
Given Data / Assumptions:
- Single-phase shell-side flow; no phase change considered.
- Reasonable baffle cut and spacing practices.
- Goal: enhance heat transfer without excessive vibration or bypassing.
Concept / Approach:Baffles direct shell-side flow across the tube bundle, creating crossflow and local turbulence, interrupting boundary layers, and reducing bypass streams. This increases the shell-side heat transfer coefficient h_s. It does not increase cross-sectional flow area; rather, it constrains flow path and raises velocity, typically increasing pressure drop as a trade-off.
Step-by-Step Solution:
Add baffles ⇒ induce crossflow and turbulence.Crossflow interrupts thermal boundary layers ⇒ higher h_s.Parallel flow is minimized; leakage/bypass controlled with proper sealing strips.Therefore, the main effect is increased shell-side heat transfer coefficient.Select option (c).Verification / Alternative check:Bell–Delaware methods quantify h_s and pressure drop improvements due to baffles and associated correction factors for leakage and bypass streams.
Why Other Options Are Wrong:
- Increase cross-section: Opposite; effective flow area is restricted.
- Force parallel flow: Incorrect; baffles create crossflow.
- Decrease h_s: Contradicts the purpose of baffles.
Common Pitfalls:Over-tight spacing causing high pressure drop and tube vibration; optimal design balances heat transfer gains and mechanical limits.
Final Answer:increase the shell side heat transfer co-efficient.