🛢️ Pipeline Linepack Inventory

Calculate high-pressure gas transmission pipeline linepack inventory (Sm³ and tons), AGA average line pressure, usable draft buffer, and autonomy time.

⚡ Fortran 90 Engine Double Precision (IEEE 754) ✓ ISO / ASME Validated
📊 Solver Telemetry ● ACTIVE
👁️ Consultations 44
⚡ Calculs faits 35
💾 Téléchargements 419 📦 Code Fortran 4.4 KB
📅 Mise en service Jun 2026
⏱️ Latence < 1 ms
⚡ Outils & Rapports :
💾 Télécharger Fortran 90

🛢️ High-Pressure Transmission Pipeline Linepack & Dynamic Storage

Real-time visual simulation of pressure gradient decay P(x) & in-situ gas mass inventory

📝 Configuration & Presets

🔥 36" Trunkline (150 km) 🏙️ 16" Feeder (40 km) 🌊 42" Offshore (220 km) 🏭 10" Plant Loop (12 km)
📐 Pipeline Dimensions & Pressures
💨 Gas Properties & Storage Limits
Methane: 16.04, Natural Gas blend: 16.5–18.0
Used to calculate pipeline autonomy duration
AGA Linepack Formulations:
• Average Pressure: P̄ = ⅔ [ P₁ + P₂² / (P₁ + P₂) ]
• Standard Inventory: Vstd = Vgeom · (P̄ / Pstd) · (Tstd / T̄) · (1/Z)
• Usable Buffer: Vusable = Vstd(P̄) − Vstd(Pmin)
• Autonomy Time: τ = Vusable / Qdemand [hours]

📊 Linepack Inventory Results

Configure inputs and click Compute to view results.

📘 Calculation Methodology & AGA Formulations

Non-Linear Pressure Profile P(x)

Due to gas compressibility and expansion, the pressure decay along a transmission pipeline is parabolic rather than linear:

P(x) = √[ P₁² − (x/L)(P₁² − P₂²) ]

Dynamic Linepack Storage Capacity

Transmission pipelines act as large storage reservoirs ("virtual gas holders"), allowing operators to absorb daily peak demand swings by packing or drafting the line.

Key Engineering Assumptions

  • Isothermal steady-state gas transmission.
  • Standard conditions evaluated at $15^\circ\text{C}$ and $1.01325\,\text{bar a}$ (ISO 13443).
  • Compressibility factor $Z$ computed across average pipeline conditions.