Piping Engineering & Stress
Piping Design & Stress AnalysisASME B31.3 Process Piping vs. ASME B31.1 Power Piping: Practical Engineering & Code Comparison
Principal Piping Engineer
Head of Plant Engineering, Deep Ocean
Published: 2026-03-15•9 min read

Governing Standards:ASME B31.3 (2022/2024)ASME B31.1 (2022/2024)ASME Section II Part D
Key Engineering Takeaways
ASME B31.1 applies strictly to boiler external piping (BEP) and non-boiler external piping in power stations, adopting higher safety factors.
ASME B31.3 applies across petroleum refineries, chemical plants, and terminal facilities, featuring tighter allowable stress margins based on tensile and yield.
Thermal expansion allowable stress range (SA) differs: B31.3 incorporates longitudinal stress in flexibility calculation, whereas B31.1 uses a simplified formulation.
Post-weld heat treatment (PWHT) and non-destructive examination (NDE) thresholds are significantly more stringent under B31.1 for high-energy steam lines.
1. Jurisdictional Scopes & Facility Boundaries
Understanding the jurisdictional boundary between ASME B31.1 (Power Piping) and ASME B31.3 (Process Piping) is the primary step in any industrial piping engineering development.
ASME B31.1 covers piping typically found in electric power generating stations, industrial power plants, and central heating facilities. Crucially, B31.1 governs Boiler External Piping (BEP)—piping directly connected to the power boiler up to the first block valve, where the ASME Boiler and Pressure Vessel Code (BPVC Section I) mandates B31.1 compliance and ASME code stamping.
Conversely, ASME B31.3 governs all piping within petroleum refineries, chemical synthesis facilities, pharmaceutical plants, LNG terminals, and related processing plants. Even within a chemical plant, an auxiliary utility steam generation package may fall under B31.1 up to the battery limit, transitioning into B31.3 once past the main header isolation valve. Misclassifying these boundaries can cause major regulatory delays during boiler inspector audits.
Engineering Rule of Thumb
Whenever steam piping operates above 100 psig or water above 160 psig and 250°F generated by a power boiler, ASME B31.1 BEP rules govern until the first authorized isolation boundary.
2. Allowable Stress Criteria & Safety Margin Comparison
The fundamental mathematical divergence between ASME B31.1 and B31.3 lies in their allowable stress determination at design temperature:
Under ASME B31.1, the allowable stress ($S$) at temperature is determined using a more conservative design margin. Historically, B31.1 utilized a design margin of 4.0 against minimum tensile strength ($S_T$), subsequently updated to 3.5 in alignment with ASME Section II Part D Table 1A.
In contrast, ASME B31.3 employs a design factor of 3.0 against tensile strength at temperature ($S_T / 3.0$), while capping allowable stress at two-thirds of yield strength ($2/3 S_Y$) for materials other than austenitic stainless steels. For austenitic alloys, B31.3 permits up to 90% of yield strength where minor plastic deformation does not compromise joint tightness.
// ASME B31.3 Allowable Expansion Stress Range (Clause 302.3.5)
SA = f * [ 1.25 * (Sc + Sh) - SL ]
Where:
Sc = Basic allowable stress at minimum metal temperature
Sh = Basic allowable stress at maximum metal temperature
SL = Calculated longitudinal stress from sustained loads (P + W)
f = Stress range reduction factor based on total equivalent cycles (N)3. Thermal Flexibility & Pipe Stress Analysis Nuances
When configuring flexibility analysis models in CAESAR II, selecting the appropriate governing code changes how sustained and thermal expansion load cases are evaluated:
1. **Sustained Load Formulation:**
In ASME B31.3, the longitudinal stress $S_L$ comprises axial pressure stresses, bending stresses from weight and sustained forces, and torsional moments. Under recent editions of B31.3, the code explicitly incorporates sustained stress indices ($I_i, I_o$) derived from ASME B31J, eliminating ambiguity around intensification factors for tees and reducers.
2. **Allowable Expansion Stress Range ($S_A$):**
Notice that in the B31.3 formula, the calculated sustained stress $S_L$ directly reduces the available thermal expansion budget. If sustained loads are low, the leftover margin transfers to thermal expansion (the "liberal allowable" approach). Under ASME B31.1, the basic allowable expansion range without liberal credit is simply $S_A = f(1.25 S_c + 0.25 S_h)$.
At Deep Ocean, our stress engineering team models every high-energy system in CAESAR II with rigorous consideration of these code-specific displacement formulas to guarantee that piping runs do not overload sensitive rotating equipment nozzles.
- B31.3 accounts for sustainment deduction directly through SL subtraction.
- B31.1 requires formal cold spring verification if designers attempt expansion stress mitigation through pre-stretched cold gaps.
- Both codes mandate integration of ASME B31J flexibility factors for non-standard branch connections.
4. Non-Destructive Examination (NDE) & Post-Weld Heat Treatment
Inspection severity reflects the differing risk profiles of power utilities versus chemical process environments:
- **ASME B31.1 Power Piping:** Demands 100% volumetric inspection (Radiographic Testing or Ultrasonic Testing) for all high-pressure and high-temperature circumferential butt welds operating above 750°F or 1025 psig, irrespective of pipe diameter.
- **ASME B31.3 Process Piping:** Uses Fluid Service categories (Normal, Category D, Category M, High Pressure, High Purity). For Normal Fluid Service, random 5% visual and radiographic examination is baseline, scaling to 100% RT for Category M (toxic fluids) and Severe Cyclic Conditions.
Post-weld heat treatment (PWHT) soak times and temperature ramps are rigorously enforced in both codes for P-No. 1 carbon steels exceeding 0.75" (19 mm) nominal wall thickness, and across all wall thicknesses for P-No. 4 (1.25Cr-0.5Mo) and P-No. 5A (2.25Cr-1Mo) creep-resistant alloy systems.
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