Meana Petro

Instalaciones e integridad

Espesor de pared y MAOP

Required wall thickness and maximum allowable operating pressure under B31.3, B31.4 or B31.8, with the class location, joint and temperature factors applied.

Datos de entrada

The MAOP is computed from this.

Resultados

Cargando el cálculo…

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Cómo se calcula

  • B31.3 process piping: t = PD / (2(SEW + PY)), with Y the temperature coefficient.
  • B31.4 liquid pipeline: t = PD / (2 × 0.72 × SMYS × E) — the design factor is fixed by the code.
  • B31.8 gas pipeline: t = PD / (2 × SMYS × F × E × T), with F from the class location and T from the temperature derating table.
  • Ordered thickness = (required + corrosion allowance) grossed up for mill tolerance, so the thinnest delivered wall still satisfies the design.

Estándares que habla

Dónde deja de ser cierto

This is the internal-pressure hoop stress calculation and nothing else. Real design also has to cover external pressure and collapse, bending and axial stress from soil movement, thermal expansion, vibration and fatigue, seismic loading, and — for anything sour — the materials requirements of NACE MR0175/ISO 15156, which frequently governs the grade selection outright. The temperature derating table here is abbreviated. A wall thickness from this tool is an input to a design, not a design.

Herramientas relacionadas

  • Resistencia remanente B31G

    A metal-loss defect assessed by both original and modified B31G, giving the failure pressure, the safe operating pressure and the longest defect your MAOP can carry.

  • Caída de presión en tubería

    Single-phase liquid by Darcy–Weisbach with a real Colebrook friction factor, and gas by Weymouth with both Panhandle equations alongside it.