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Aspen HYSYSPeng-Robinson EOS

Cross-Country Natural Gas Pipeline Simulation | Terrain & Pipe Sizing

Modeling a 120 km high-pressure natural gas transmission pipeline in Aspen HYSYS, assessing hydraulic pressure drop, elevation/terrain impacts, sizing requirements, and compressor station power.

Cross-Country Natural Gas Pipeline Simulation | Terrain & Pipe Sizing

1. Project Overview & Context

Modeling a 120 km high-pressure natural gas transmission pipeline in Aspen HYSYS, assessing hydraulic pressure drop, elevation/terrain impacts, sizing requirements, and compressor station power.

2. Problem Statement

Gas transmission across undulating terrain causes liquid condensate dropout, localized pressure drops, and risk of hydrate formation when gas temperature falls below dew point.

3. Objectives

1. Model gas hydraulics across elevation profile in Aspen HYSYS Pipeline Segment. 2. Determine optimal pipe diameter (24-inch vs 30-inch) to maintain delivery pressure above 55 bar. 3. Evaluate compressor station power requirements and hydrate inhibitor dosing.

4. Simulation Setup & Thermodynamic Selection

Software Environment
Aspen HYSYS
Property Method / EOS
Peng-Robinson EOS

Sub-nodal pipe hydraulic modeling using Peng-Robinson EOS with Beggs & Brill two-phase flow correlation. Terrain elevation points mapped every 5 km across a 120 km route.

5. Process Flow & Reduction Chemistry

Sub-nodal pipe hydraulic modeling using Peng-Robinson EOS with Beggs & Brill two-phase flow correlation. Terrain elevation points mapped every 5 km across a 120 km route.

6. Model Input Variables & Boundary Conditions

ParameterValueUnitsEngineering Source
Operating PressureVariablebarProcess Specification
Feed Flow RateNominalkg/hSimulation Balance

8. Results & Findings

SIMULATION RESULTS: - 30-inch line maintained end-of-pipe pressure at 58.4 bar (vs 41.2 bar in 24-inch line under peak flow) - Compressor Duty Saved: 2.8 MW by optimizing pipe diameter - Hydrate formation temperature calculated at 11.5 °C at 65 bar.

9. Engineering Discussion & Trade-Off Analysis

Sizing the line at 30 inches eliminates the need for an intermediate booster station, lowering capital expenditure by $4.2M despite higher initial piping costs. Heat loss model verified minimum gas delivery temperature at 14.8 °C.

10. Financial Impact & Decision-Support Platform

Economic feasibility evaluations assess capital expenditures, operational utility consumption, and payback thresholds to validate commercial viability.

11. Environmental Impact & Decarbonization Value

Significant reductions in carbon emissions and fuel waste achieved through rigorous process simulation and heat integration.

12. Model Limitations & Scope Boundaries

Assumes constant ambient soil temperature (15 °C) without seasonal freeze-thaw variations.

13. Engineering Conclusions

Rigorous terrain profile integration in Aspen HYSYS prevents liquid holdup slugging and optimizes compressor power consumption in cross-country natural gas delivery.

14. Future Development & Digital Twin Integration

Transient flow simulation in Aspen HYSYS Dynamics to model pigging operations and sudden valve closure shock waves.

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