期刊
SEPARATION AND PURIFICATION TECHNOLOGY
卷 310, 期 -, 页码 -出版社
ELSEVIER
DOI: 10.1016/j.seppur.2023.123213
关键词
Liquid -liquid extraction; Aromatics-alkanes separation; Deep eutectic solvent; Molecular dynamics simulation; Light cycle oil
This study systematically investigates the effect of aromatic and alkane structures on extraction performance from experimental and theoretical perspectives. Liquid-liquid extraction experiments show that the distribution coefficient and extraction efficiency depend on the aromatic structure, while the selectivity and theoretical purity of aromatics rely on the alkane structure. Molecular dynamics simulation is used to elucidate the extraction mechanism. Process simulation using the NRTL thermodynamic model confirms that a high extraction performance can be achieved for model LCO containing more diaromatics. It is therefore preferable to incorporate aromatics-alkanes extractive separation into the pre-hydrotreating step of LCO upgrading process.
Unravelling solute effect on extractive separation of aromatics and alkanes is highly required toward its rational incorporation into economical upgrading of light cycle oil (LCO). This work systematically examines the effect of aromatic and alkane structures on extraction performance from experimental and theoretical perspectives. Liquid-liquid extraction experiments demonstrate that the distribution coefficient and extraction efficiency strongly depend on the aromatic structure, whereas the selectivity and theoretical purity of aromatics signifi-cantly rely on the alkane structure. The extraction mechanism is elucidated from interaction strength and interfacial thickness analysis using molecular dynamics simulation. The diaromatics of 1-methylnaphthalene has stronger affinity to deep eutectic solvent (DES) than the monoaromatics of tetralin, while longer alkyl-chain in hexadecane enhances its repulsive interaction with DES than dodecane. Extraction process simulation was then carried out with well-regressed parameters of NRTL thermodynamic model. Process simulation confirms that a high extraction performance can be achieved for model LCO containing more diaromatics. Therefore, it is preferable to incorporate aromatics-alkanes extractive separation into the pre-hydrotreating step of LCO upgrading process.
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