Bio-production of eicosapentaenoic acid from the diatom Nanofrustulum shiloi via two-step high performance countercurrent chromatography

被引:4
作者
Barcenas-Perez, Daniela [1 ,2 ]
Lukes, Martin [1 ]
Hrouzek, Pavel [1 ]
Zapal, Jakub [3 ]
Kuzma, Marek [3 ]
Kopecky, Jiri [1 ]
Kubac, David [1 ]
Arredondo-Vega, Bertha O. [4 ]
Cheel, Jose [1 ]
机构
[1] Czech Acad Sci, Lab Algal Biotechnol Ctr ALGATECH, Inst Microbiol, Opatovicky Mlyn 37981, Trebon, Czech Republic
[2] Univ South Bohemia, Fac Sci, Branisovska 1760, Ceske Budejovice 37005, Czech Republic
[3] Czech Acad Sci, Lab Mol Struct Characterizat, Inst Microbiol, Videnske 1083, Prague 14220, Czech Republic
[4] Ctr Invest Biol Noroeste CIBNOR, Lab Biotecnol Microalgas, Av Inst Politecn Nacl 195, La Paz 23096, Baja Calif Sur, Mexico
关键词
Eicosapentaenoic acid; Nanofrustulum shiloi; Diatom; High performance countercurrent chromatography (HPCCC); CENTRIFUGAL PARTITION CHROMATOGRAPHY; POLYUNSATURATED FATTY-ACIDS; PHAEODACTYLUM-TRICORNUTUM; EXTRACTION METHODS; (DHA)-RICH LIPIDS; SEPARATION; MICROALGAE; PURIFICATION; ESTERS; FUCOXANTHIN;
D O I
10.1007/s10811-022-02816-w
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Eicosapentaenoic acid (EPA) is an essential polyunsaturated fatty acid of nutritional and physiological relevance for humans. It is commercially produced mainly from fish oil, but new sustainable sources are required. In this study, pure EPA ethyl ester was produced from Nanofrustulum shiloi biomass by integrating two separation steps via high performance countercurrent chromatography (HPCCC). The HPCCC first step consisted of a 10 separation cycles (1200 mg sample per cycle) process, each cycle consisting of three stages comprising EPA fraction separation in reversed phase elution mode (lower polar phase used as mobile phase); with stationary phase extrusion (by switching the pumping of the mobile phase to the stationary phase, while maintaining the column rotation); and hydrodynamic equilibrium achievement inside the column. The process led to 982.1 mg of a fraction rich in EPA with a purity of 71%. To improve the purity of the EPA fraction, an HPCCC second step was performed leading to 698.97 mg of EPA ethyl ester with a purity of 99%, and a recovery of 98%. To avoid unnecessary waste of solvents, liquid phases were formulated based on a priori NMR measurement. The HPCCC process throughput was 0.936 g h(-1), while the efficiency per gram of EPA was 0.054 g h(-1). Environmental risk and process evaluation factors were used for the evaluation of the separation process. Overall, this isolation approach may represent a useful model for the efficient production of pure EPA from microalgae.
引用
收藏
页码:2995 / 3010
页数:16
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