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DNVGL RP F101 Local Incident Pressure

Calculate DNVGL RP F101 local incident pressure and local external pressure from design pressure and elevation.

The local incident pressure is calculated from the design pressure and the elevation. Fluid density is assumed constant. Use the Result Plot option to plot local pressure and reference pressure versus elevation.

Reference : DNVGL-RP-F101 : Corroded Pipelines (Download from the DNVGL website)

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CALCULATOR : DNVGL-RP-F101 Section 3.7 Pipeline Local Incident Pressure And External Pressure From Elevation [FREE]   ±

Calculate pipeline incident pressure, local incident pressure and local external pressure from design pressure and elevation (DNVGL-RP-F101 Section 3.7). Fluid density is assumed constant.

Tool Input

  • pletype : Local External Pressure Type
    • Pleu : User Defined External Pressure At Local Elevation
  • ginctype : Incidental To Design Pressure Ratio Type
    • γincu : User Defined Incidental Pressure Factor
  • plitype : Local Incidental Pressure Type
    • Prdu : User Defined Design Pressure At Reference Elevation
    • Priu : User Defined Incidental Pressure At Reference Elevation
    • Pliu : User Defined Incidental Pressure At Local Elevation
  • ρf : Internal Fluid Density
  • ρe : External Fluid Density
  • Zr : Reference Elevation
  • Zl : Local Elevation
  • Zs : Surface Elevation

Tool Output

  • ΔPl : Delta Pressure Across Pipe Wall At Local Elevation
  • Δz : Local Elevation Relative To Reference Elevation
  • γinc : Incidental Pressure Factor
  • Ple : External Pressure At Local Elevation
  • Pli : Incidental Pressure At Local Elevation
  • Prd : Design Pressure At Reference Elevation
  • Pri : Incidental Pressure At Reference Elevation
  • wd : Water Depth

CALCULATOR : DNVGL-RP-F101 Section 3.7 Three Phase Black Oil Density [FREE]   ±

Calculate pipeline fluid density for single phase gas, oil or water, two phase liquid (oil and water), or three phase black oil (oil, water and gas).

Water cut is measured relative to the total liquid volume (gas volume is ignored). Gas oil ratio (GOR) is measured relative to the oil volume at standard conditions (water volume is ignored).

Reference : DNVGL-RP-O501 : Managing Sand Production And Erosion : Section 4.4

Tool Input

  • mvtype : Fluid Density Type
    • GORu : User Defined Gas Oil Ratio
    • WCu : User Defined Water Cut
    • ρu : User Defined Fluid Density
  • ρo : Oil Density
  • ρw : Water Density
  • P : Fluid Pressure
  • T : Fluid Temperature
  • Z : Gas Compressibility Factor
  • SG : Gas Specific Gravity

Tool Output

  • ρf : Average Fluid Density
  • ρg : Gas Density
  • ρl : Liquid Density
  • GOR : Gas Oil Ratio
  • WC : Water Cut
  • Xmg : Gas Mass Fraction
  • Xml : Liquid Mass Fraction
  • Xmo : Oil Mass Fraction
  • Xmw : Water Mass Fraction
  • Xvg : Gas Volume Fraction
  • Xvl : Liquid Volume Fraction
  • Xvo : Oil Volume Fraction
  • Xvw : Water Volume Fraction
  • vg : Gas Mole Volume (At T P)

CALCULATOR : DNVGL-RP-F101 Section 3.7 Two Phase gas Liquid Density [FREE]   ±

Calculate pipeline fluid density for single phase gas or liquid, or two gas liquid.

Gas oil ratio (GOR) is measured relative to the oil volume at standard conditions.

Reference : DNVGL-RP-O501 : Managing Sand Production And Erosion : Section 4.4

Tool Input

  • mvtype : Fluid Density Type
    • GORu : User Defined Gas Oil Ratio
    • Xmu : User Defined Gas Mass Fraction
    • Xvu : User Defined Gas Volume Fraction
    • ρu : User Defined Fluid Density
  • ρl : Liquid Density
  • P : Fluid Pressure
  • T : Fluid Temperature
  • Z : Gas Compressibility Factor
  • SG : Gas Specific Gravity

Tool Output

  • ρf : Average Fluid Density
  • ρg : Gas Density (At T P)
  • GOR : Gas Oil Ratio
  • Xm : Gas Mass Fraction
  • Xv : Gas Volume Fraction (At T P)
  • vg : Gas Mole Volume (At T P)