从未澄清的原料中高效生产和直接纯化EGFP的综合策略

IF 3.7 3区 生物学 Q2 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Jyun-Liang Liu , Shih-Pang Lin , The Duc Hanh Nguyen , Chanin Panjapornpon , Paweena Prapainainar , Kulpavee Jitapunkul , Chen‑Yaw Chiu , Bing-Lan Liu , Kuei-Hsiang Chen , Yu-Kaung Chang
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引用次数: 0

摘要

从未澄清的原料中高效回收重组蛋白仍然是生物加工的主要挑战。增强型绿色荧光蛋白(EGFP)被广泛用作模型蛋白,但其纯化通常涉及多个澄清步骤,增加了处理时间和成本。本研究提出了一种优化EGFP生产和回收的上游培养和下游纯化的综合策略。采用两水平、三因素分数析因设计(FFD)优化环境变量,确定pH 7.0、26°C和1.75 h诱导时间为最佳条件。优化后的培养物在5 L的生物反应器中放大,从50% % (w/v)被破坏的大肠杆菌细胞中产生3.66 mg/mL的EGFP和36.86 mg/mL的总蛋白。使用流线型DEAE吸附剂的搅拌流化床吸附(SFBA)能够从未澄清的原料中直接提纯。在线速度为100 cm/h,搅拌速度为100 rpm的条件下,SFBA工艺回收率为96.3% %,纯化系数为2.9倍,产率为2.82 × 10−2 mg/mL/min,超过了先前报道的方法。这些结果证明了一种有效的、可扩展的纯化方法,可以直接从粗裂解物中回收EGFP,无需离心或过滤。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Integrated strategy for efficient production and direct purification of EGFP from unclarified feedstocks
Efficient recovery of recombinant proteins from unclarified feedstocks remains a major challenge in bioprocessing. Enhanced green fluorescent protein (EGFP) is widely used as a model protein, but its purification typically involves multiple clarification steps, increasing processing time and cost. This study presents an integrated strategy to optimize both upstream cultivation and downstream purification for EGFP production and recovery. A two-level, three-factor fractional factorial design (FFD) was employed to optimize environmental variables, identifying optimal conditions at pH 7.0, 26 °C, and 1.75 h of induction time. The optimized culture was scaled up in a 5 L bioreactor, yielding 3.66 mg/mL of EGFP and 36.86 mg/mL of total protein from 50 % (w/v) disrupted E. coli cells. Stirred fluidized bed adsorption (SFBA) using STREAMLINE DEAE adsorbent enabled direct purification from unclarified feedstock. At a linear velocity of 100 cm/h and a stirring speed of 100 rpm, the SFBA process achieved 96.3 % recovery, a 2.9-fold purification factor, and a productivity of 2.82 × 10−2 mg/mL/min—surpassing previously reported methods. These results demonstrate an efficient, scalable purification approach for EGFP recovery directly from crude lysates, eliminating the need for centrifugation or filtration.
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来源期刊
Biochemical Engineering Journal
Biochemical Engineering Journal 工程技术-工程:化工
CiteScore
7.10
自引率
5.10%
发文量
380
审稿时长
34 days
期刊介绍: The Biochemical Engineering Journal aims to promote progress in the crucial chemical engineering aspects of the development of biological processes associated with everything from raw materials preparation to product recovery relevant to industries as diverse as medical/healthcare, industrial biotechnology, and environmental biotechnology. The Journal welcomes full length original research papers, short communications, and review papers* in the following research fields: Biocatalysis (enzyme or microbial) and biotransformations, including immobilized biocatalyst preparation and kinetics Biosensors and Biodevices including biofabrication and novel fuel cell development Bioseparations including scale-up and protein refolding/renaturation Environmental Bioengineering including bioconversion, bioremediation, and microbial fuel cells Bioreactor Systems including characterization, optimization and scale-up Bioresources and Biorefinery Engineering including biomass conversion, biofuels, bioenergy, and optimization Industrial Biotechnology including specialty chemicals, platform chemicals and neutraceuticals Biomaterials and Tissue Engineering including bioartificial organs, cell encapsulation, and controlled release Cell Culture Engineering (plant, animal or insect cells) including viral vectors, monoclonal antibodies, recombinant proteins, vaccines, and secondary metabolites Cell Therapies and Stem Cells including pluripotent, mesenchymal and hematopoietic stem cells; immunotherapies; tissue-specific differentiation; and cryopreservation Metabolic Engineering, Systems and Synthetic Biology including OMICS, bioinformatics, in silico biology, and metabolic flux analysis Protein Engineering including enzyme engineering and directed evolution.
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