π Case Study
COβ Capture Solvent Screening for Natural Gas Sweetening
Solvent degradation and excessive reboiler duty with conventional MDEA
ποΈ Project Overview
Offshore LNG facility in Qatar handling 20 MMSCFD sour gas
π― Challenge
Solvent degradation and excessive reboiler duty with conventional MDEA
π§ Design Approach
Thermodynamic screening of blended amines (MDEA + piperazine) using eNRTL and rate-based modeling
π Design Diagram
AI-generated project design illustration
π Key Calculations
Reboiler Duty per kg COβ
Q_reb / αΉ_COβ
Result: 3.8 MJ/kg
Key economic driver for capture cost
COβ Loading Capacity
mol_COβ / mol_amine
Result: 0.82
Determines solvent circulation rate
π Results
37% lower reboiler duty, 2.1Γ faster absorption kinetics, extended solvent life >3 yearsπ‘ Lessons Learned
- β’Electrolyte thermodynamics essential for accurate loading predictions
- β’Vapor pressure data quality directly impacted column sizing
β Key Takeaways
- 1Electrolyte thermodynamics essential for accurate loading predictions
- 2Vapor pressure data quality directly impacted column sizing