Mass Transfer and Phase Diagram Study for Crystallization-Extraction Coupling Enantioseparation of ( <i>RS</i> )-1-(1-Naphthyl)ethylamine and Mother Liquor Reuse

Diastereomeric crystallization is a prevalent method for enantioseparation; however, it is hindered by the significant generation of waste mother liquor. Therefore, our previous research introduced a pairwise crystallization-circulating extraction coupling (PC-CE) method for mother liquor regeneration and reuse. Despite its potential, the circulating extraction requires several hours (4–20 h), highlighting the need for enhanced mass transfer rates to expedite the process. This study examines the mass transfer intensification in three sets of PC-CE equipment (designated as Equipment Nos. 1–3) by enhancing phase separation capabilities. Specifically, the crystallization-extraction coupling devices of Equipment Nos. 1–3 were developed through structural modifications of a “gas-washing bottle”, a “Soxhlet extractor”, and a “volatile oil extractor”, respectively. The diastereomeric crystallization of (RS)-1-(1-naphthyl)ethylamine was investigated, with enantiomeric excess (ee) values and the mixing degree (h) of the mother liquors measured at various flow rates. As a result, Equipment Nos. 2 and 3 exhibit a lower mixing degree (<4.03%) and significantly reduced circulating extraction time (20 to 60 min) compared to Equipment No. 1. Furthermore, the crystallization process was studied from the perspective of phase equilibrium. Initially, the impact of various factors was investigated, which was followed by the deduction of phase diagrams to provide a theoretical explanation for PC-CE and to predict the total solute dosage range (lines f2_q0 and f′2_q′0). Ultimately, Equipment No. 3 with a flow rate of 14.7 × 10–4 m/s and a circulating extraction time of 45 min was selected for mother liquor reuse. The ee values of the two (R)-/(S)-1-(1-naphthyl)ethylamine salt crystals obtained through 15 cycles of crystallization reuse ranged from 94.34% to 99.02% and from 93.66% to 97.02%, respectively. This research represents a significant reduction in regeneration time from the previous 4–6 h to just 45 min, thereby enhancing the practicality of the PC-CE method.

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Journal
Industrial & Engineering Chemistry Research
Published
2026-04-13
DOI
https://doi.org/10.1021/acs.iecr.6c00566
Primary Topic
Crystallization and Solubility Studies
Type
article
Field-Weighted Citation Impact
0.00

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Mass Transfer and Phase Diagram Study for Crystallization-Extraction Coupling Enantioseparation of ( RS )-1-(1-Naphthyl)ethylamine and Mother Liquor Reuse

Bei Zhu, Jianxian Zeng, Shibo Liang, Qian Liu et al.
Industrial & Engineering Chemistry Research
Crystallization and Solubility Studies
article

Mass Transfer and Phase Diagram Study for Crystallization-Extraction Coupling Enantioseparation of ( RS )-1-(1-Naphthyl)ethylamine and Mother Liquor Reuse

Bei Zhu, Jianxian Zeng, Shibo Liang, Qian Liu, Lelin Zeng, Lvqing Liao, Xiaoqin Tang, Li Peng, Bart Van der Bruggen, Jian Jian
article en

Abstract

Diastereomeric crystallization is a prevalent method for enantioseparation; however, it is hindered by the significant generation of waste mother liquor. Therefore, our previous research introduced a pairwise crystallization-circulating extraction coupling (PC-CE) method for mother liquor regeneration and reuse. Despite its potential, the circulating extraction requires several hours (4–20 h), highlighting the need for enhanced mass transfer rates to expedite the process. This study examines the mass transfer intensification in three sets of PC-CE equipment (designated as Equipment Nos. 1–3) by enhancing phase separation capabilities. Specifically, the crystallization-extraction coupling devices of Equipment Nos. 1–3 were developed through structural modifications of a “gas-washing bottle”, a “Soxhlet extractor”, and a “volatile oil extractor”, respectively. The diastereomeric crystallization of (RS)-1-(1-naphthyl)ethylamine was investigated, with enantiomeric excess (ee) values and the mixing degree (h) of the mother liquors measured at various flow rates. As a result, Equipment Nos. 2 and 3 exhibit a lower mixing degree (<4.03%) and significantly reduced circulating extraction time (20 to 60 min) compared to Equipment No. 1. Furthermore, the crystallization process was studied from the perspective of phase equilibrium. Initially, the impact of various factors was investigated, which was followed by the deduction of phase diagrams to provide a theoretical explanation for PC-CE and to predict the total solute dosage range (lines f2_q0 and f′2_q′0). Ultimately, Equipment No. 3 with a flow rate of 14.7 × 10–4 m/s and a circulating extraction time of 45 min was selected for mother liquor reuse. The ee values of the two (R)-/(S)-1-(1-naphthyl)ethylamine salt crystals obtained through 15 cycles of crystallization reuse ranged from 94.34% to 99.02% and from 93.66% to 97.02%, respectively. This research represents a significant reduction in regeneration time from the previous 4–6 h to just 45 min, thereby enhancing the practicality of the PC-CE method.

Industrial & Engineering Chemistry ResearchVol. 65(15)
Hunan Institute of Science and Technology (CN), Hunan University of Science and Technology (CN), Ministry of Education of the People's Republic of China (CN), Korea University (KR), KU Leuven (BE)
National Natural Science Foundation of China, Natural Science Foundation of Hunan Province, Science and Technology Program of Hunan Province, Scientific Research Foundation of Hunan Provincial Education Department
Openalex Percentile: Top 25%
Crystallization and Solubility Studies
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