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Purification of the recombinant enhanced green fluorescent protein from Escherichia coli using alcohol plus salt aqueous two-phase systems
被引:32
|作者:
Lo, Sewn Cen
[1
]
Ramanan, Ramakrishnan Nagasundara
[1
]
Tey, Beng Ti
[1
]
Tan, Wen Siang
[2
]
Show, Pau Loke
[3
]
Ling, Tau Chuan
[4
]
Ooi, Chien Wei
[1
]
机构:
[1] Monash Univ Malaysia, Sch Engn, Chem Engn Discipline, Jalan Lagoon Selatan, Bandar Sunway 47500, Selangor, Malaysia
[2] Univ Putra Malaysia, Fac Biotechnol & Biomol Sci, Dept Microbiol, Upm Serdang 43400, Selangor, Malaysia
[3] Univ Nottingham, Dept Chem & Environm Engn, Bioseparat Res Grp, Fac Engn, Malaysia Campus,Jalan Broga, Semenyih 43500, Selangor, Malaysia
[4] Univ Malaya, Inst Biol Sci, Fac Sci, Kuala Lumpur 50603, Malaysia
关键词:
Enhanced green fluorescent protein;
Aqueous two-phase systems;
Alcohol;
Salt;
Back extraction;
LIQUID-LIQUID EQUILIBRIUM;
GFP FUSION PROTEINS;
RAPID PURIFICATION;
EXTRACTION;
EXPRESSION;
SEPARATION;
OPTIMIZATION;
RECOVERY;
BEHAVIOR;
YIELD;
D O I:
10.1016/j.seppur.2017.09.072
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
The enhanced green fluorescent protein (EGFP) is widely used as a marker in life science. Currently, purifications of the EGFP mostly involve chromatographic methods, which are multistep, time-consuming and costly. In the present study, the recombinant EGFP expressed in Escherichia colt was purified using an economic aqueous two-phase system (ATPS). Short-chain aliphatic alcohol and organic salt were chosen as the phase-forming components owing to their recyclability and biodegradability, respectively. The partition behaviour of EGFP was evaluated under the varying conditions of ATPS, including types and concentrations of phase-forming components, feedstock concentration, and pH. In an optimal primary 2-g ATPS comprising 1-propanol and tripotassium citrate, a high recovery of EGFP (i.e., 92.1%) was attained in the salt-rich bottom phase. To facilitate the easy recovery of purified EGFP, a secondary ATPS was used to back extract the EGFP to a new top ethanol-rich top phase, and the ethanol was removed from the purified EGFP via evaporation. The 1-propanol and ethanol used in the primary and secondary ATPSs (i.e. 20-g system) were successfully recycled in three successive rounds of EGFP purification, yielding the average EGFP purification factor of 11.34 and 75.7% of EGFP yield. The purification of EGFP using the two stages of alcohol + salt ATPSs is efficient in terms of operation time, cost and process scalability.
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页码:130 / 139
页数:10
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