<p>Rising atmospheric CO<InlineEquation ID="IEq1"><EquationSource Format="TEX">\(_2\)</EquationSource></InlineEquation> levels and increasing emissions from internal combustion (IC) engines highlight the need for compact carbon-capture technologies suitable for distributed emission sources. This study presents a simulation-based analysis of an electrochemical CO<InlineEquation ID="IEq2"><EquationSource Format="TEX">\(_2\)</EquationSource></InlineEquation> absorption system for engine exhaust using an aqueous NaCl electrolyte. A dynamic MATLAB/Simulink model is developed by coupling gas–liquid mass transfer, Henry’s-law solubility, simplified electrochemical kinetics, Faraday-based hydroxide generation, and pH-dependent carbonate/bicarbonate speciation. Under the corrected baseline conditions of <InlineEquation ID="IEq3"><EquationSource Format="TEX">\(60~\mathrm {L \times min^{-1}}\)</EquationSource></InlineEquation> exhaust flow containing <InlineEquation ID="IEq4"><EquationSource Format="TEX">\(12~{vol\%}\)</EquationSource></InlineEquation> CO<InlineEquation ID="IEq5"><EquationSource Format="TEX">\(_2\)</EquationSource></InlineEquation>, the system captures <InlineEquation ID="IEq6"><EquationSource Format="TEX">\(69.38~\textrm{g}\)</EquationSource></InlineEquation> CO<InlineEquation ID="IEq7"><EquationSource Format="TEX">\(_2\)</EquationSource></InlineEquation> over a <InlineEquation ID="IEq8"><EquationSource Format="TEX">\(1~\textrm{h}\)</EquationSource></InlineEquation> operating period, corresponding to a cycle-integrated capture efficiency of <InlineEquation ID="IEq9"><EquationSource Format="TEX">\(8.93\%\)</EquationSource></InlineEquation>. At the simulated bulk pH of approximately <InlineEquation ID="IEq10"><EquationSource Format="TEX">\(8.8{-}9.0\)</EquationSource></InlineEquation>, bicarbonate formation is dominant; therefore, the effective electron requirement is treated as <InlineEquation ID="IEq11"><EquationSource Format="TEX">\(n_{\textrm{eff}}\approx 1\)</EquationSource></InlineEquation> rather than assuming complete carbonate formation. Using a representative Faradaic efficiency of <InlineEquation ID="IEq12"><EquationSource Format="TEX">\(85\%\)</EquationSource></InlineEquation>, the current required to support the corrected capture rate is <InlineEquation ID="IEq13"><EquationSource Format="TEX">\(49.7~\textrm{A}\)</EquationSource></InlineEquation>, giving a corrected cell-level specific energy consumption of <InlineEquation ID="IEq14"><EquationSource Format="TEX">\(2.72~\mathrm {kWh \times kg^{-1}_{CO_2}}\)</EquationSource></InlineEquation>. When first-order auxiliary loads for gas handling, cooling, electrolyte circulation, and control electronics are included, the estimated system-level energy requirement increases to approximately <InlineEquation ID="IEq15"><EquationSource Format="TEX">\(4.24~\mathrm {kWh \times kg^{-1}_{CO_2}}\)</EquationSource></InlineEquation>. Sensitivity and optimization analyses indicate that mass-transfer performance, electrode area, electrolyte concentration, Faradaic efficiency, and auxiliary power demand strongly influence overall system performance. Because the model is not experimentally validated, the results should be interpreted as a preliminary feasibility and sensitivity assessment rather than a definitive prediction of reactor performance. The Bangladesh case study is used only to illustrate potential deployment relevance for distributed exhaust sources, while experimental validation, improved electrode kinetics, chloride-management strategies, and detailed techno-economic assessment are identified as essential future work.</p>

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Electrochemical CO2 capture from engine exhaust using NaCl electrolyte: System modeling, optimization, and economic assessment

  • Md Sadman A. Rahman,
  • Allama Rejuan,
  • Shah Mohazzem Hossain,
  • Marran Al Qwaid,
  • Hezerul Bin Abdul Karim,
  • Md Tanjil Sarker

摘要

Rising atmospheric CO\(_2\) levels and increasing emissions from internal combustion (IC) engines highlight the need for compact carbon-capture technologies suitable for distributed emission sources. This study presents a simulation-based analysis of an electrochemical CO\(_2\) absorption system for engine exhaust using an aqueous NaCl electrolyte. A dynamic MATLAB/Simulink model is developed by coupling gas–liquid mass transfer, Henry’s-law solubility, simplified electrochemical kinetics, Faraday-based hydroxide generation, and pH-dependent carbonate/bicarbonate speciation. Under the corrected baseline conditions of \(60~\mathrm {L \times min^{-1}}\) exhaust flow containing \(12~{vol\%}\) CO\(_2\), the system captures \(69.38~\textrm{g}\) CO\(_2\) over a \(1~\textrm{h}\) operating period, corresponding to a cycle-integrated capture efficiency of \(8.93\%\). At the simulated bulk pH of approximately \(8.8{-}9.0\), bicarbonate formation is dominant; therefore, the effective electron requirement is treated as \(n_{\textrm{eff}}\approx 1\) rather than assuming complete carbonate formation. Using a representative Faradaic efficiency of \(85\%\), the current required to support the corrected capture rate is \(49.7~\textrm{A}\), giving a corrected cell-level specific energy consumption of \(2.72~\mathrm {kWh \times kg^{-1}_{CO_2}}\). When first-order auxiliary loads for gas handling, cooling, electrolyte circulation, and control electronics are included, the estimated system-level energy requirement increases to approximately \(4.24~\mathrm {kWh \times kg^{-1}_{CO_2}}\). Sensitivity and optimization analyses indicate that mass-transfer performance, electrode area, electrolyte concentration, Faradaic efficiency, and auxiliary power demand strongly influence overall system performance. Because the model is not experimentally validated, the results should be interpreted as a preliminary feasibility and sensitivity assessment rather than a definitive prediction of reactor performance. The Bangladesh case study is used only to illustrate potential deployment relevance for distributed exhaust sources, while experimental validation, improved electrode kinetics, chloride-management strategies, and detailed techno-economic assessment are identified as essential future work.