Tube Bundle Flow-Induced Vibration Analysis

Category: Fluid–Structure Interaction | Revised 2026-10-01
CAE visualization for tube bundle vibration theory - technical simulation diagram
Tube Bundle Flow-Induced Vibration Analysis

Theory: flow and tube motion reinforcing each other

Overview

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We're considering a modification to raise flow through a shell-and-tube heat exchanger. Should tube vibration be a concern?

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Very much so. Crossflow over tubes creates forces that shake them. Most dangerous is fluidelastic instability: tube motion alters the surrounding flow, which drives the tube further — a self-reinforcing loop. Above a certain velocity (the critical velocity), amplitude jumps suddenly, and tubes can rub against neighbours or baffles and perforate within a short time. Before raising flow, compute tube natural frequency and critical velocity to confirm there's margin.

Tube natural frequency

$$ f_1 = \frac{\pi}{2L^2}\sqrt{\frac{EI}{m}}, \qquad m = m_{tube} + m_{inside} + C_m\,\rho\,\frac{\pi D^2}{4} $$

First natural frequency treating a baffle-supported tube as a pinned–pinned beam. $m$ includes the tube, fluid inside, and added mass from fluid moving outside (coefficient $C_m$).

The Connors equation

$$ U_c = K\,f\,D\,\sqrt{\frac{m\,\delta}{\rho D^2}}, \qquad \delta = 2\pi\zeta, \qquad f_s = \frac{St\,U}{D} $$

$D$ is tube OD, $\zeta$ the damping ratio and $K$ a constant set by tube pattern and flow direction (about 2.4–3 in design). $f_s$ is vortex-shedding frequency, with Strouhal number $St$ about 0.2–0.5 depending on pattern.

Coffee Break Trivia

What nuclear heat exchangers taught

In the 1960s–70s, nuclear steam generators and large heat exchangers repeatedly suffered tube perforations soon after start-up. Investigations found flow-induced vibration making tubes rub against their supports. In 1970 Connors, from wind-tunnel tests on tube rows, gave an equation for the critical velocity of the instability arising from tube–flow reinforcement. Data on its constant and on damping accumulated, and vibration assessment entered the US heat-exchanger standard (TEMA) and ASME guidance.

Worked example: varying baffle span

Steel tube 19.05 mm OD, 1.65 mm wall, water inside and out, added-mass coefficient 1.5, damping ratio 1.5%. Mass per length is 1.33 kg/m (tube 0.71, water inside 0.20, added mass 0.43):

Baffle spanNatural frequencyCritical velocity (K = 3.0)Critical velocity (K = 2.4)Shedding lock-in velocity
400 mm223 Hz7.5 m/s6.0 m/s12.9 m/s
600 mm99 Hz3.3 m/s2.7 m/s5.7 m/s
800 mm56 Hz1.9 m/s1.5 m/s3.2 m/s
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At a gap velocity of 2 m/s, 600 mm is safe but 800 mm is dangerous.

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Right. Natural frequency is inversely proportional to span squared, so a small increase in span cuts critical velocity sharply. At 800 mm even K = 3 gives 1.9 m/s, below 2 m/s. K scatters widely in experiments, and design often uses a conservative value around 2.4; then even 600 mm gives 2.7 m/s — only 1.35 times margin over 2 m/s. The basic practice is to allow for uncertainty in K and damping and keep ample margin over flow velocity (e.g. about 1.3–2 times). For a flow-increase modification, also check where velocity peaks locally, such as near inlets and outlets.

Assessment workflow

  1. Find the gap-velocity distribution (higher near inlets, outlets and baffle windows).
  2. Compute tube natural frequencies including support conditions and added mass.
  3. Compute fluidelastic critical velocity considering ranges of K and damping.
  4. Check vortex-shedding and acoustic frequencies don't coincide with tube or shell natural frequencies.
  5. Estimate wear life at supports from turbulent-buffeting amplitude.
Coffee Break Trivia

“Only a few tubes by the inlet failed”

After a flow-increase modification to a heat exchanger, only a few tubes directly beneath the shell inlet nozzle perforated within a year. Across the bundle the average velocity had margin against critical, but flow concentrated beneath the inlet, reaching nearly twice the average locally. CFD of the inlet region showed those tubes exceeded critical velocity. An impingement plate to spread the flow and tighter baffle spacing in that zone stopped the damage.

Common mistakes

Mistakes and fixes

MistakeEffectFix
Assessing by average velocityLocal instability missedMap velocity distribution
Ignoring added massFrequency overestimatedInclude fluid inside and out
Optimistic KCritical velocity overestimatedConservative K and margin
Assuming high dampingInstability missedData-based damping
Ignoring acoustic resonanceLoud noise and vibrationCheck shell acoustic modes
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