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When a tube is bent into a U-shape for a heat exchanger, the outer wall of the bend is forced to stretch while the inner wall is compressed. That redistribution of metal is the reason U bend tubes almost always show some wall thinning right at the extrados, and it is exactly the area an inspector has to look at first. Wall thinning at the bend section is not a defect by itself; it only becomes a problem when it goes beyond what the design code allows. The job of inspection is to measure that thinning accurately, judge it against the right standard, and decide whether the tube can stay in service.
During bending, the outside fiber of the tube is in tension and the inside fiber is in compression. The neutral axis shifts toward the intrados, so the strain on the outer wall is greater than a simple geometric estimate would suggest. In tight-radius bends, with high D/t ratios, that strain shows up as a measurable reduction in wall thickness on the extrados. The opposite side of the bend can also show thickening, which is usually less critical but still worth recording because it changes the local flow area inside the heat efficiency tube.
Because thinning is concentrated on the outside of the curve, the inspection plan has to focus on the crown of the bend, the tangent points where the curve meets the straight leg, and the root on the intrados. Skipping any of these points is a common reason inspectors miss the worst case.
Before any gauge touches the tube, the inspector needs to know what the design called for: nominal outside diameter, nominal wall thickness, material grade, and the acceptance limits from the governing code. For most industrial pressure tubes, those limits come from ASME B31.3 or from the relevant ASTM product standard such as A213, A249, A269, or A312. For U bend tube bundles in heat exchangers, the reference is usually the heat exchanger specification, TEMA, and the client’s ITP.
Tools should be calibrated for the job. A digital ultrasonic thickness gauge with a dual-element probe in the 5 MHz range is suitable for typical stainless steel and carbon steel tubes. A surface profile comparator is useful for judging whether roughness is a cosmetic issue or a sign of strain. The tube surface must be clean, dry, and at a stable temperature, since a wet or hot surface can produce false readings on both UT and eddy current instruments.
The core of the inspection is a wall thickness survey at and around the bend. The standard practice is to take readings on the extrados at the center of the bend, at 45° on either side of the center, and at the two tangent points where the bend meets the straight leg. Each reading is compared with the nominal wall thickness to calculate the thinning percentage. As a practical rule, thinning on a high-pressure carbon or alloy steel pressure tube is normally capped at 12.5%, while a heat exchanger tube in less severe service is usually allowed about 10%. For high-pressure boiler and superheater service, the limit tightens further to roughly 5%.
A reliable geometric estimate for thinning is:
t_min = t_nom × R / (R + 0.5 × D)
where t_min is the predicted minimum wall thickness on the extrados, t_nom is the nominal wall thickness of the straight tube, R is the centerline bend radius, and D is the outside diameter. This estimate gives a quick sanity check before the gauge readings come in. If the measured thickness at the extrados falls below t_min, the bending process needs to be reviewed even if the percentage thinning is still inside the code limit.
Couplant selection matters on small-radius bends. A high-viscosity gel stays in place on the crown of a tight U-bend where a thin liquid would run off, and it gives a more stable reading. Probe positioning should be perpendicular to the surface, with the probe axis aligned along the tube length so the sound path goes straight through the wall rather than along it.
Wall thinning does not happen alone. The same bending strain that thins the extrados also tends to flatten the cross-section, especially when the bend is tight and the wall is relatively thin. Ovality is measured at the center of the bend with a vernier or a pi tape, and is calculated as:
Ovality (%) = (D_max − D_min) / D_nom × 100
For most process piping, 8% ovality is the upper limit, and for heat exchanger tubes feeding into pipe fittings or headers, 5% is a more realistic target. Beyond that, the tube will not seat properly in the tube sheet.
The intrados should be checked for wrinkling, rippling, or orange peel. Light orange peel is cosmetic; deep ripples or actual folds indicate that the bend was made without adequate internal support, and the affected tube should be rejected regardless of the wall thickness numbers. The same is true for visible cracks, gouges, or die marks along the extrados. These are stress concentrators and will shorten the fatigue life of the heat efficiency tube even when the wall thickness is acceptable.
Ultrasonic thickness gauging is the main method for wall thinning, but it is usually combined with at least one other non-destructive test. Eddy current testing is widely used on stainless steel and copper-nickel U bend tubes to detect surface-breaking defects such as fatigue cracks, pitting, and erosion-corrosion on the extrados. A bobbin probe or a rotating probe can scan the inside of the bend from the tube end, which is often the only practical way to inspect the intrados in service.
For carbon and low-alloy steel tubes in pressure service, magnetic particle testing is a reliable check for surface and near-surface cracks at the bend, especially after a hot bending or a stress-relief operation. Liquid penetrant testing serves the same purpose on austenitic stainless steel and nickel alloy tubes, where magnetic methods do not work. For critical components such as rcc-m section ii nuclear tube applications, the inspection plan typically requires 100% ultrasonic testing in addition to surface NDT, with the recorded traces kept as part of the quality file.
The acceptance decision is a comparison of three numbers: the measured minimum wall at the extrados, the measured ovality at the bend, and the surface condition after NDT. The tube passes only if all three are inside their limits. A typical acceptance window for an austenitic stainless steel heat exchanger tube is:
| Parameter | Limit | How it is checked |
|---|---|---|
| Wall thinning at extrados | ≤ 10% of nominal, tighter for high-pressure service | UT thickness survey at crown, 45° points, tangents |
| Ovality at bend | ≤ 5% of nominal OD | Pi-tape or vernier at center of bend |
| Surface defects | No cracks, no folds, no die marks > 0.2 mm deep | Visual + LPT or ECT on extrados |
| Subsurface defects | No indications above the rejection level of ASTM E213 | UT scan along bend and straight legs |
If any one of these limits is exceeded, the tube is either reworked, repaired, or scrapped. Light surface marks can sometimes be blended out, but any reduction in wall thickness from grinding has to be added to the measured thinning before the final acceptance decision is made.
Every reading should be written down with the tube identification, the position along the bend, the instrument used, the calibration block, and the date. For pressure tubes that go into a registered boiler or pressure vessel, this record is part of the manufacturing traceability book and may be reviewed by the third-party inspector. Digital thickness gauges that log directly to a file reduce transcription errors and make it easier to plot thinning profiles along the bend.
Photographs of the bend before and after cleaning, NDT images, and the signed inspection sheet together form the evidence package. If a tube is later found to have a service issue, this package is what allows the original inspection to be checked against the operating record.
A few mistakes show up again and again in practice. Measuring wall thickness on the intrados and treating it as the worst case is one: the inside of the bend is the compression side and is usually thicker, not thinner. Another is using a single reading at the very center of the bend and ignoring the 45° points, where thinning can sometimes be even higher. A third is forgetting to subtract the paint, cladding, or internal fouling layer from the UT reading, which leads to a falsely optimistic wall thickness. Finally, inspecting only one tube in a batch and assuming the rest are the same is risky; sampling plans should follow the inspection and test plan, not convenience.
Wall thinning at the bend section of a U-shaped tube is a predictable result of the bending process, not an automatic defect. What matters is how much it has thinned, whether that value is inside the design limit, and whether the inspection has been thorough enough to find the worst spot. A combination of ultrasonic thickness mapping at the extrados, ovality measurement, surface NDT, and proper documentation gives a clear answer. For buyers and EPC teams sourcing U bend tubes for heat exchangers, boilers, or petrochemical facilities, asking the supplier for the actual inspection records—rather than a generic certificate—is the most reliable way to confirm that the bend section is fit for service.
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