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Techno-economic feasibility and sensitivity analysis of aqueous ionic liquid-amine hybrid solvents-based CO2 chemical capture processes
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DOI：10.1016/j.ceja.2026.101407.png)
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Abstract
En 中文
• MDEA-PZ-[BMIM][AC] shows CO₂ loading capacity of 2.182 mol mol−1 at 50 bar. • DOE reveals combined effects of IL conc., temperature, pressure on CO₂ uptake. • Thermodynamic-kinetic model accurately simulates high-pressure absorption-desorption. • Capture costs of 78.03-125 USD t⁻¹ CO₂; OPEX and throughput are key cost drivers. • Experimental-modeling framework confirms ILAH solvents for industrial CO₂ capture.
Keywords:
CO₂ capture
Techno-economic analysis
Ionic liquid-amine hybrids
High-pressure absorption
Sensitivity analysis
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