6 research outputs found

    Sparse matrix methods for chemical process simulation

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    Phase-Change Ionic Liquids for Postcombustion CO<sub>2</sub> Capture

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    Phase-change ionic liquids, or PCILs, are salts that are solids at normal flue gas processing temperatures (e.g., 40–80 °C) and that react stoichiometrically and reversibly with CO<sub>2</sub> (one mole of CO<sub>2</sub> for every mole of salt at typical postcombustion flue gas conditions) to form a liquid. Thus, the melting point of the PCIL–CO<sub>2</sub> complex is below that of the pure PCIL. A new concept for CO<sub>2</sub> separation technology that uses this key property of PCILs offers the potential to significantly reduce parasitic energy losses incurred from postcombustion CO<sub>2</sub> capture by utilizing the heat of fusion (Δ<i>H</i><sub>fus</sub>) to provide part of the heat needed to release CO<sub>2</sub> from the absorbent. In addition, the phase transition yields almost a step-change absorption isotherm, so only a small pressure or temperature swing is required between the absorber and the stripper. Utilizing aprotic heterocyclic anions (AHAs), the enthalpy of reaction with CO<sub>2</sub> can be readily tuned, and the physical properties, such as melting point, can be adjusted by modifying the alkyl chain length of the tetra-alkylphosphonium cation. Here, we present data for four tetrabutylphosphonium salts that exhibit PCIL behavior, as well as detailed measurements of the CO<sub>2</sub> solubility, physical properties, phase transition behavior, and water uptake for tetraethylphosphonium benzimidazolide ([P<sub>2222</sub>]­[BnIm]). The process based on [P<sub>2222</sub>]­[BnIm] has the potential to reduce the amount of energy required for the CO<sub>2</sub> capture process substantially compared to the current technology that employs aqueous monoethanolamine (MEA) solvents
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