Vemula Sandeep, Thunuguntla Rahul, Dedaniya Akshay, Kokkiligadda Sujana, Palle Chaitanya, Ronda Srinivasa Reddy
K L E F University, Centre for Bioprocess Technology, Department of Biotechnology, Guntur 522 502, Andhra Pradesh, India.
K L E F University, Centre for Bioprocess Technology, Department of Biotechnology, Guntur 522 502, Andhra Pradesh, India.
Protein Expr Purif. 2015 Apr;108:62-72. doi: 10.1016/j.pep.2015.01.010. Epub 2015 Feb 4.
This work reports the upstream and downstream process of recombinant human granulocyte colony stimulating factor (rhG-CSF) expressed in Escherichia coli BL21 (DE3)pLysS. The fed batch mode was selected for the maximum output of biomass (6.4g/L) and purified rhG-CSF (136mg/L) under suitable physicochemical environment. The downstream processing steps viz., recovery, solubilization, refolding and concentration were optimized in this study. The maximum rhG-CSF inclusion bodies recovery yield (97%) was accomplished with frequent homogenization and sonication procedure. An efficient solubilization (96%) of rhG-CSF inclusion bodies were observed with 8M urea at pH 9.5. Refolding efficiency studies showed maximum refolding ⩾86% and ⩾84% at 20°C and pH 9 respectively. The renatured protein solution was concentrated, clarified and partially purified (⩾95%) by the cross flow filtration technique. The concentrated protein was further purified by a single step size exclusion chromatography with ⩾98% purity. The characterization of purified rhG-CSF molecular mass as evidenced by SDS-PAGE, western blot and LC/MS analysis was shown to be 18.8kDa. The secondary structure of rhG-CSF was evaluated by the CD spectroscopic technique based on the helical structural components. The biological activity of the purified rhG-CSF showed a similar activity of cell proliferation with the standard rhG-CSF. Overall, the results demonstrate an optimized downstream process for obtaining high yields of biologically active rhG-CSF.
本研究报道了在大肠杆菌BL21(DE3)pLysS中表达的重组人粒细胞集落刺激因子(rhG-CSF)的上下游工艺。为了在适宜的理化环境下实现生物质(6.4g/L)和纯化的rhG-CSF(136mg/L)的最大产量,选择了补料分批培养模式。本研究对下游加工步骤,即回收、溶解、复性和浓缩进行了优化。通过频繁的匀浆和超声处理程序,rhG-CSF包涵体的最大回收率(97%)得以实现。在pH 9.5条件下,用8M尿素可有效溶解(96%)rhG-CSF包涵体。复性效率研究表明,在20°C和pH 9条件下,最大复性率分别≥86%和≥84%。通过错流过滤技术对复性后的蛋白溶液进行浓缩、澄清和部分纯化(≥95%)。浓缩后的蛋白通过一步尺寸排阻色谱进一步纯化,纯度≥98%。通过SDS-PAGE、western blot和LC/MS分析证实,纯化的rhG-CSF分子量为18.8kDa。基于螺旋结构成分,通过圆二色光谱技术评估了rhG-CSF的二级结构。纯化的rhG-CSF的生物学活性与标准rhG-CSF显示出相似的细胞增殖活性。总体而言,结果表明优化的下游工艺可获得高产量的具有生物活性的rhG-CSF。