TY - JOUR
T1 - Experimental performance and techno-economic assessment of an ionic liquid-based scrubber for maritime SO2 capture
AU - Huang, Kuniadi Wandy
AU - Doliente, Stephen Salve
AU - Liu, Yu
AU - Lam, Jasmine Siu Lee
AU - Barnea, Zach
AU - Sasson, Yoel
N1 - Publisher Copyright:
© 2025 Institution of Chemical Engineers
PY - 2025/8
Y1 - 2025/8
N2 - Sulfur dioxide (SO2) emissions from maritime exhaust pose environmental and regulatory challenges. This study evaluates a scrubber system using 1-butyl-3-methylimidazolium chloride ([BMIM][Cl]) for SO2 capture in shipping. Experimental results show high absorption capacity (512 mmol SO2/mol IL at 50°C) and over 95 % SO2 capture efficiency across multiple cycles. The system utilizes water as a solvent for ionic liquid regeneration, demonstrating effective and practical desorption performance at a low water-to-IL mole ratio (3:1), ensures efficient desorption with minimal water and energy use. Techno-economic comparisons against seawater, NaOH, and Wellman–Lord scrubbers reveal the [BMIM][Cl] system as the most cost-effective, with annual savings up to USD 5.26 million over VLSFO use and up to USD 558,000 over NaOH systems. Energy use is low (31.5 kW), with thermal demand fully offset by waste heat. Space requirements (27 m3) are far lower than those of NaOH (200 m3) and Wellman–Lord systems (118 m3). Environmental assessment confirms lower greenhouse gas emissions than NaOH but higher than Wellman-Lord process. Potential long-term stability concerns, detailed study on viscosity, and oxygen exposure effects are noted for future investigation. Overall, the [BMIM][Cl] scrubber emerges as a compact, energy-efficient, and cost-effective alternative for SO2 compliance in shipping.
AB - Sulfur dioxide (SO2) emissions from maritime exhaust pose environmental and regulatory challenges. This study evaluates a scrubber system using 1-butyl-3-methylimidazolium chloride ([BMIM][Cl]) for SO2 capture in shipping. Experimental results show high absorption capacity (512 mmol SO2/mol IL at 50°C) and over 95 % SO2 capture efficiency across multiple cycles. The system utilizes water as a solvent for ionic liquid regeneration, demonstrating effective and practical desorption performance at a low water-to-IL mole ratio (3:1), ensures efficient desorption with minimal water and energy use. Techno-economic comparisons against seawater, NaOH, and Wellman–Lord scrubbers reveal the [BMIM][Cl] system as the most cost-effective, with annual savings up to USD 5.26 million over VLSFO use and up to USD 558,000 over NaOH systems. Energy use is low (31.5 kW), with thermal demand fully offset by waste heat. Space requirements (27 m3) are far lower than those of NaOH (200 m3) and Wellman–Lord systems (118 m3). Environmental assessment confirms lower greenhouse gas emissions than NaOH but higher than Wellman-Lord process. Potential long-term stability concerns, detailed study on viscosity, and oxygen exposure effects are noted for future investigation. Overall, the [BMIM][Cl] scrubber emerges as a compact, energy-efficient, and cost-effective alternative for SO2 compliance in shipping.
KW - Ionic liquid-based scrubber
KW - Maritime SO capture
KW - Techno-economic analysis
KW - Waste heat recovery
KW - [BMIM][Cl]
UR - https://www.scopus.com/pages/publications/105009814485
U2 - 10.1016/j.cherd.2025.07.002
DO - 10.1016/j.cherd.2025.07.002
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AN - SCOPUS:105009814485
SN - 0263-8762
VL - 220
SP - 117
EP - 133
JO - Chemical Engineering Research and Design
JF - Chemical Engineering Research and Design
ER -