Pipe Stress Analysis
Pipe Stress Analysis & Flexibility VerificationCAESAR II Stress Analysis Input Checklist & Boundary Condition Guide
Lead Stress Specialist
Principal Flexibility Analyst, Deep Ocean
Published: 2026-05-02•9 min read

Governing Standards:ASME B31.3ASME B31.1API 610
Key Engineering Takeaways
Inaccurate valve center-of-gravity or missing insulation weight skews stress results by up to 35%.
Thermal growth of connected equipment nozzles must be calculated and applied as imposed displacements at terminal anchors.
Corrosion allowance must be included in pressure design checks but excluded from stiffness/flexibility calculations.
Friction coefficients (typically $\mu = 0.3$ for steel-on-steel, $0.1$ for PTFE/Teflon) alter restraint reaction loads.
1. Primary Input Document Checklist
Prior to opening CAESAR II, the stress analyst must assemble certified engineering inputs:
1. **Latest Piping Isometrics / 3D Model:** Verifying accurate 3D coordinates, elevations, and line orientation.
2. **Process Line List:** Extracting design pressure, design temperature, operating temperature, fluid specific gravity, and test media density.
3. **Piping Material Specification (PMS):** Material grade (e.g., ASTM A106 Gr. B, A312 TP304L), pipe schedule, corrosion allowance, and mill tolerance.
4. **Valve & In-line Instrument Cut Sheets:** Vendor-certified valve weights, actuator heights, and center-of-gravity offsets.
5. **Equipment Nozzle Load Data Sheets:** Allowable nozzle forces and moments from rotating equipment vendors (API 610, API 617, NEMA SM 23) or pressure vessel fabricators.
2. Equipment Nozzle Thermal Growth & Imposed Displacements
Treating an equipment nozzle connection as a 100% rigid zero-movement anchor ($DX=0, DY=0, DZ=0$) is a major engineering flaw when the connected vessel operates at high temperatures.
Thermal vertical growth ($Delta Y$) of a top vessel nozzle is determined by:
$$Delta Y = alpha imes L imes (T_{operating} - T_{ambient})$$
Where:
- $alpha$ = Mean coefficient of thermal expansion for the vessel shell material.
- $L$ = Distance from the vessel support base (skirt or lug) to the nozzle centerline.
- $T_{operating} - T_{ambient}$ = Temperature differential.
This calculated displacement must be entered into CAESAR II as an imposed anchor displacement ($DX, DY, DZ$) for each operating temperature case, accurately capturing nozzle uplift on connected piping.
3. Modeling Restraints & Friction Coefficients
Real-world pipe supports do not exhibit infinite stiffness or frictionless sliding. Stress engineers must configure:
- **Restraint Gaps:** Specifying actual guide clearances (e.g., $1.5$ mm gap on lateral guides).
- **Friction Coefficients ($mu$):**
* Steel-on-Steel support sliding: $mu = 0.30$
* Steel-on-Concrete: $mu = 0.40$
* PTFE / Teflon slide plates: $mu = 0.10$
* Polished Stainless on Bronze: $mu = 0.15$
- **Rotational Stiffness:** Specifying rotational restraints ($RX, RY, RZ$) only when the physical structure possesses sufficient rigidity to prevent rotation under maximum pipe bending moments.
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