Design & Construction
Choose the alloy for what concentrates at the tube wall, not for what is in the pipe. The film is what corrodes, and it is frequently far more aggressive than the bulk stream that produced it.
Most U-tube duty is served by 304L, 316L or carbon steel, and choosing between them is straightforward. The interesting decisions happen at the edges: chlorides at temperature, acids, seawater, sour service and anywhere the cleaning chemistry is more aggressive than the process. Bend radius interacts with all of it, because cold bending work-hardens the material and leaves residual stress exactly where corrosion likes to start.
The alloy decision is made at the tube wall, where the fluid concentrates and the temperature is highest, not in the bulk stream. Carbon steel is the cost benchmark and tolerates corrosion with a stated allowance; 304L and 316L cover most of the rest and are limited by chlorides at temperature; duplex, Alloy 20, AL-6XN, Monel, titanium and copper-nickel are each the answer to a named problem and are worth their premium only where that problem exists.
The five pages in this section cover the alloys in that order, then the surface finish, polish and passivation that hygienic duty specifies on top. Send the two fluids, the temperatures, the chloride level if you know it and the cleaning chemistry, and the material conversation is usually short.
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Each page in this section takes one material or finish decision, the trade-off behind it and the specification wording that delivers the right result.
Call and talk it through with an engineer: 1-805-484-2992.
When 304L is enough, when 316L is needed, what dual certified material means, and the chloride stress-corrosion cracking limit both alloys share.
SA-516-70 shells with SA-179 or SA-214 tube, a stated corrosion allowance, coatings, and carbon steel shells paired with alloy bundles.
2205 and super duplex, Alloy 20, Hastelloy C-276, AL-6XN and Monel in U-tube service, and what tube bending does to each of them.
Seawater and brine bundles: grade 2 titanium and its chloride immunity, the velocity window copper-nickel needs, and where admiralty brass fits.
Why roughness decides cleanability, what an Ra number means in practice, and mechanical polish compared with electropolish and passivation.
Have both fluids named, with flow rates, inlet temperatures and required outlet temperatures, the operating and design pressures on each side, the allowable pressure drop, any code, alloy, hygienic or documentation requirement, and the space and orientation available.
Beyond the datasheet, four things change designs in practice: expected turndown, the fouling history you know of, how the unit will be cleaned and the clearance there is to pull the bundle. If any of it is unknown, tell us which part and we will size against a stated assumption rather than a guess.
Request a QuoteA shell usually outlives it's bundle. If yours is sound, a drop-in replacement bundle costs less: send the shell inside diameter, tube length, tube count and diameter, pass arrangement and tubesheet or flange dimensions with a photograph of the tubesheet face, and the new bundle keeps the original fit.
If the shell is corroded, the nozzles no longer suit the piping or the duty itself has changed, a complete exchanger rated to the new conditions is the better buy, and we will say so.
Every quote here comes from an engineer and lists the basis it was written on. Not sure which alloy or finish your duty needs? Send what you have, and we will point to the missing number and why it matters.
Call and talk it through with an engineer: 1-805-484-2992, 8am to 5pm, or email Sales@HeatX.com.
316L contains about two to three percent molybdenum, which raises it's resistance to chloride pitting and crevice attack; 304L has none and costs less. Both are limited by the same chloride stress-corrosion cracking mechanism at elevated temperature, so moving from 304L to 316L buys pitting resistance, not immunity from cracking. The typical mistake is specifying 316L for a chlorinated cooling-tower loop and expecting it to solve a cracking problem; it delays the failure, and the bundle still cracks at the U-bends where residual stress is highest. For clean steam and softened water, 304L tube is a sound and cheaper choice.
When chloride level, temperature and tensile stress together put a 300-series tube in the cracking zone, or when the chemistry is acidic, reducing or sour enough to attack the passive film. Each step up answers a named problem: duplex 2205 for chloride cracking at a cost not far above 316L, Alloy 20 for sulfuric acid, Hastelloy C-276 for mixed acids with chlorides, titanium for seawater. The decision point is the U-bend, because cold bending leaves residual stress exactly where chlorides concentrate. Send the chloride content and the hottest wall temperature, and the alloy choice is usually a short conversation.
Yes. Duplex and the nickel alloys work-harden faster than 304L or 316L, and titanium has less ductility and springs back more, so the bender needs a larger minimum centerline radius or the outside wall thins beyond what the code allows. For the same shell this costs tubes in the innermost rows, which is why an alloy upgrade on a replacement bundle can mean slightly less surface than the original. Order the alloy and the bend radius together so the rating absorbs the difference.
Often, yes: the shell sees only the shell-side fluid, so a carbon steel shell with a stated corrosion allowance and a 316L bundle puts the expensive alloy only where the process touches it. The pairing fails when the shell-side fluid is itself corrosive, or when the two metals are electrically coupled in a conductive liquid and the carbon steel becomes the anode, wasting away at the tubesheet gasket face. Check which fluid is on which side before accepting the saving. On steam shells it is the normal choice; on tower water the galvanic question needs answering first.
Ra is the average surface roughness in microinches, and a lower number leaves fewer grooves for soil and biofilm to anchor in, so it sets how well a clean-in-place cycle works. The mistake is specifying Ra alone: a mechanically polished tube can meet the number yet carry folded metal and embedded grit that an electropolished surface at the same Ra does not. State the Ra and the method together, and say whether the tube interior or the exterior is the product side, because polishing the inside of a U-tube is a different operation from polishing the outside of a bundle.