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Codes and Standards

Most exchangers need more than one code

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Design & Construction

Codes and Standards

Codes answer different questions. ASME says the vessel will hold pressure. TEMA says how robustly it is built. 3-A and BPE say whether it can be cleaned and documented. Most exchangers need more than one.

Getting the code package right is largely about not over-specifying. ASME Section VIII is essentially universal in North America. TEMA class should match service severity. 3-A and ASME BPE apply to hygienic work and are not interchangeable. API 660, PED and Canadian CRN are jurisdiction or industry driven, and each adds cost and schedule that should be a deliberate choice.

Each code answers a different question, which is why most exchangers need more than one. The pressure code makes the unit legal to install; the construction class sets how heavily it is built; the hygienic standards decide whether it can be cleaned, drained and qualified; and the jurisdictional requirements - an industry standard, a European directive, a Canadian registration - arrive from outside the design and need to be known at inquiry, because each adds cost and schedule.

The five pages in this section take one requirement each: what it governs, where it belongs in a specification, where it is habitually over-applied, and what paperwork it produces. Read the one your project names, then tell us which apply and we will quote to them - with the code-driven items priced as separate lines so the cost of each is visible.

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Photo of a stainless steel shell-and-tube exchanger on a blue test stand with hoses and a pressure gauge during hydrostatic testing

Codes & Standards Decisions

Each page here covers one code or standard, the trade-off it brings and the specification wording that gets it right.
Call and talk it through with an engineer: 1-805-484-2992.

ASME Section VIII

What the U-stamp covers on a U-tube unit: Division 1 design, the U-1 data report, hydrostatic testing, third-party inspection and National Board registration.

TEMA Classes R, C & B

How Class R, C and B differ in tolerances, thicknesses and corrosion allowance, and what moving between them does to price.

3-A Sanitary Standards

Scope of the 3-A standards, how symbol authorization and third-party verification work, and where 3-A sits beside FDA and USDA expectations.

ASME BPE

The BPE points a validation engineer checks on a U-tube unit: surface designations, weld examination and records, dead legs, drainability and traceable material.

API 660, PED & CRN

Refinery service to API 660, PED compliance for Europe and CRN registration for Canada, with the schedule each one adds to a U-tube order.

Have This Ready When You Call

For a sizing we need both fluids with their flow rates, inlet temperatures and the outlet temperatures you require, the operating and design pressure on each side and the pressure drop you can allow. Add every code, alloy, hygienic or documentation requirement, the space available and the orientation the site can take.

The details that most often change a design come next: the turndown you expect, any fouling history, the cleaning method and the clearance available to withdraw the bundle. Where a number is unknown, say so instead of guessing and the sizing will state the assumption it used.

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Complete Exchanger or Bundle Only?

When a bundle fails, the shell is usually still sound, and a drop-in bundle is the less expensive route. Send the shell inside diameter, tube length, tube count and diameter, pass arrangement and the tubesheet or flange dimensions, plus a photograph of the tubesheet face, and the original fit is held.

A corroded shell, nozzles that no longer match the piping or a changed duty make a complete unit rated to the new conditions the right answer, and we will tell you which case you are in.

Talk It Through

An engineer writes every quote on this site and states what it was based on. Unsure which code or construction detail applies? Send what you have and we will name the missing number and explain why it matters.

Call and talk it through with an engineer: 1-805-484-2992, 8am to 5pm, or email Sales@HeatX.com.

Code Paperwork Explained

No. Jurisdictions set exemptions by volume, diameter and pressure, and a small low-pressure heater can fall below them, but nearly every insurer and plant standard asks for the U-stamp anyway. The practical test is who signs off the installation. A plant inspector who finds an unstamped vessel in a stamped plant will normally reject it, and a stamp cannot be added afterward because the Authorized Inspector was not present during fabrication. The mistake we see is a buyer saving a little on a utility heater, then paying for a complete second unit when the commissioning paperwork is reviewed. Specify the stamp unless the jurisdiction has confirmed in writing that the unit is exempt.

The U-1 is the Manufacturer's Data Report that ships with an ASME Section VIII Division 1 vessel, signed by the fabricator and the Authorized Inspector. For a U-tube exchanger it records design pressure and temperature on each side, shell and tubesheet materials, tube count and size, the hydrostatic test pressure and the National Board number if the vessel was registered. Keep it in the plant vessel files rather than the maintenance shop, because fifteen years later it is the document that lets a drop-in bundle be built without a tape measure. A nameplate photograph is a poor substitute: it carries the ratings, not the tube geometry.

Yes, because they do not overlap: ASME sets pressure integrity, TEMA sets mechanical construction tolerances and 3-A sets hygienic design, so one unit can satisfy all three. What changes is the cost of agreement between them. A TEMA R corrosion allowance adds wall thickness, and 3-A then wants that thicker surface finished and drainable. The usual conflict is a crevice: a rolled tube joint is acceptable to the pressure code, but a 3-A inspector wants it seal welded. Resolve those points on the drawing before fabrication, and name all three on the inquiry so each is priced as its own line.

ASME Section VIII Division 1 does, at 1.3 times the design pressure corrected for the ratio of allowable stress at test temperature to that at design temperature. TEMA adds that each side be tested seperately so a tube-to-tubesheet leak shows up. On a U-tube unit that means a shell-side test with the bonnet off and the tubesheet face visible, the only time a weeping tube end can be seen directly. Ask for the test report with the U-1 and file them together.

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Quotes - Engineering - Sales