Protic ionic liquids as constituent of aqueous two-phase system based on acetonitrile: Synthesis, phase diagrams and genipin pre-purification

被引:17
作者
Alves Camelo, Lidia Cristina [1 ]
Dias Santos, Gabriela de Souza [1 ]
de Souza, Ranyere Lucena [1 ,2 ]
Faria Soares, Cleide Mara [1 ,2 ]
Brandao Pereira, Jorge Fernando [3 ]
Lima, Alvaro Silva [1 ,2 ]
机构
[1] Univ Tiradentes, Programa Posgrad Engn Proc, Av Murilo Dantas 300, BR-49032490 Aracaju, Sergipe, Brazil
[2] Inst Tecnol & Pesquisa, Av Murilo Dantas 300, BR-49032490 Aracaju, Sergipe, Brazil
[3] Sao Paulo State Univ UNESP, Sch Pharmaceut Sci, Dept Bioproc & Biotechnol, Rodovia Araraquara Jau Km 01, BR-14800903 Araraquara, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Protic ionic liquid; Phase equilibria; Genipin; Extraction; Integrated process; THERMOPHYSICAL PROPERTIES; BIOACTIVE COMPOUNDS; WATER MIXTURES; EXTRACTION; RECOVERY; GENIPOSIDE; SEPARATION; SOLVENTS; QUANTIFICATION; L;
D O I
10.1016/j.fluid.2019.112425
中图分类号
O414.1 [热力学];
学科分类号
摘要
The aim of this study was to evaluate the formation of aqueous two-phase systems (ATPS) based on different protic ionic liquids (PIL), synthesized using amines, and organic or inorganic acid, and acetonitrile (ACN). The ATPSs are used to pre-purify genipin from genipap (Genipa americana L.). All PILs (purity above 98%) were able to form ATPSs with ACN, the size of the biphasic region being directly dependent on salting-out aptitude of PIL anions and relative hydrophilicity of the corresponding cations. The highest solid liquid extraction of genipin from genipap was achieved by using aqueous ACN solution at 75% (16.79 +/- 0.06 mg g(-1) dry raw material) as extractant. After the extraction stage, the ATPS was used as an integrated platform to pre-purify the genipin present in the extract. Three different overall mixture point compositions were tested, and those formed by [MEA][H(2)Cit] (25 wt%) + ACN (45 wt%) + water (30 wt%) at 298.15 +/- 1.00 K and 0.10 +/- 0.01 MPa showed the highest selectivity (S = 4.202 +/- 0.009) and recovery of genipin in top phase (R-TG = 56.74 +/- 0.04%), and the purification factor in top phase was 5.9 fold. (C) 2019 Elsevier B.V. All rights reserved.
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页数:11
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