Vonmises Engineering
← Service indexSheet 03 of 06

Services · 03

Piping and fittings, calculated — and analysed where the code requires it.

We have developed our own Excel sheets for mechanical calculations on commonly used piping codes, and carry out flexibility and stress analysis in industry-trusted software where it governs.

Stainless steel process piping skid with valves and flanged joints
Process piping skid

The B31 series

Four codes, four different sets of rules

 ASME B31.1ASME B31.3ASME B31.5ASME B31.12
ApplicationBoiler external pipingRefineries, chemical, pharmaceutical, pulp and paper, semiconductor, cryogenicRefrigeration and secondary coolant systemsHydrogen piping and pipelines
Basic allowablelesser of UTS/3.5 and 2/3 × Yieldlesser of UTS/3.0 and 2/3 × Yieldas B31.3 basisB31.3 basis, reduced by a material performance factor
Service gradingNone — single serviceCategory D, Normal, Category M, High Pressure, High PurityRefrigerant servicePart IP industrial piping · Part PL pipelines
ExaminationLargely fixed by pressure and temperatureScales with fluid category — from spot checks to 100%Prescriptive for refrigerant jointsMore stringent than B31.3 throughout
Design responsibilityOperating companyExplicitly assigned to the OwnerOwner and installerOwner

Non-standard fittings

Designed to ASME code

Standard-compliant fittings are the straightforward case. Fittings such as valves, measurement devices — thermowells, Coriolis meters and various flow meters — Y strainers, sight glasses and expansion joints can be designed to the B31.3 or B31.1 code. We have developed Excel sheets and also use numerical methods to evaluate non-standard fittings, and can provide pressure–temperature ratings for your non-standard fitting catalogue — the basis of a Fitting CRN.

Why it is required

Pipe stress analysis

ASME B31.3 does not demand formal analysis of every system. Para. 319.4.1 exempts a system that duplicates or replaces without significant change a system with a successful service record, that can readily be judged adequate by comparison with previously analysed systems, or that is of uniform size, has no more than two points of fixation, no intermediate restraints, and falls within the limits of the empirical equation given in para. 319.4.

Anything outside those three cases requires formal analysis. In practice that captures most real systems — anything with intermediate supports, changing diameter, more than two anchors, or connections to sensitive equipment. The Code itself cautions that no general proof exists that the empirical equation always produces accurate or conservative results.

Where the analysis earns its keep

Equipment nozzle loads
Rotating equipment and air-cooled exchangers have tight allowables, and exceeding them causes misalignment and seal failure rather than pipe failure — the most common reason a system fails analysis.
Flange leakage
Joints that pass a stress check can still separate under combined moment and thermal load.
Support and structure loads
The analysis produces the reactions the structural design needs — without them, supports are sized by assumption.
Spring hanger selection
Sizing and travel for systems with significant vertical thermal movement.
Skids and spools
Compact routing produces stiff systems with little natural flexibility, so thermal growth has nowhere to go.
High-temperature service
Thermal expansion, creep range behaviour and cold spring where specified.
Occasional loads
Wind, seismic, relief valve reaction, water hammer and slug flow.
Buried and jacketed piping
Soil restraint or the jacket changes the restraint condition entirely.
Troubleshooting
Investigating vibration, support failures or cracking in systems already in service.
Next sheet · 04Plant 3D & Piping Design

Get in touch

Send us the scope. We’ll tell you what it takes.