πŸ“‹ Case Study

COβ‚‚ Capture Solvent Screening for Natural Gas Sweetening

Solvent degradation and excessive reboiler duty with conventional MDEA

πŸ—οΈ Project Overview

Offshore LNG facility in Qatar handling 20 MMSCFD sour gas

🎯 Challenge

Solvent degradation and excessive reboiler duty with conventional MDEA

πŸ”§ Design Approach

Thermodynamic screening of blended amines (MDEA + piperazine) using eNRTL and rate-based modeling

πŸ“ Design Diagram

MDEA Feed(30 wt%)BlendMDEA + PZSweet GasCOβ‚‚ < 2%Challengeβ€’ Degradation\nβ€’ High Q_rebDesign OutcomeQ_reb = 3.8 MJ/kg\nΞ± = 0.82 mol/mol

AI-generated project design illustration

πŸ“ Key Calculations

Reboiler Duty per kg COβ‚‚

Q_reb / ṁ_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

πŸ“Š Results

37% lower reboiler duty, 2.1Γ— faster absorption kinetics, extended solvent life >3 years

πŸ’‘ Lessons Learned

  • β€’Electrolyte thermodynamics essential for accurate loading predictions
  • β€’Vapor pressure data quality directly impacted column sizing

βœ… Key Takeaways

  • 1Electrolyte thermodynamics essential for accurate loading predictions
  • 2Vapor pressure data quality directly impacted column sizing