Madadkar Pedram, Nino Sergio Luna, Ghosh Raja
Department of Chemical Engineering, McMaster University, 1280 Main St W, Hamilton, Ontario, L8S 4L8, Canada.
Department of Chemical Engineering, McMaster University, 1280 Main St W, Hamilton, Ontario, L8S 4L8, Canada.
J Chromatogr B Analyt Technol Biomed Life Sci. 2016 Nov 1;1035:1-7. doi: 10.1016/j.jchromb.2016.09.014. Epub 2016 Sep 14.
We discuss the use of a laterally-fed membrane chromatography (or LFMC) device for single-step purification of mono-PEGylated lysozyme. Recent studies have shown such LFMC devices to be suitable for high-resolution, multi-component separation of proteins in the bind-and-elute mode. The device used in this study contained a stack of rectangular cation-exchange membranes having 9.25mL bed volume. PEGylation of lysozyme was carried out in batch mode using 5kDa methoxy-polyethyleneglycol propionaldehyde (or m-PEG propionaldehyde) in the presence of sodium cyanoborohydride as reducing agent. Membrane chromatographic separation was carried out at 1.62 membrane bed volumes per minute flow rate, in the bind-and-elute mode. When a salt gradient was applied, the higher PEGylated forms of lysozyme (i.e. the byproducts) eluted earlier than mono-PEGylated lysozyme (the target product), while lysozyme eluted last. Under elution conditions optimized for resolution and speed, the separation could be carried out in less than 15 membrane bed volumes. High purity and recovery of mono-PEGylated lysozyme was obtained. The resolution of separation of mono-PEGylated lysozyme obtained under the above condition was comparable to that reported in the literature for equivalent cation-exchange resin columns while the flow rate expressed in bed volumes/min was 21.7 times higher. Also, the number of theoretical plates per meter was significantly higher with the LFMC device. Therefore the LFMC based purification process discussed in this paper combined high-productivity with high-resolution.
我们讨论了使用横向进料膜色谱(LFMC)装置对单聚乙二醇化溶菌酶进行一步纯化。最近的研究表明,这种LFMC装置适用于在结合-洗脱模式下对蛋白质进行高分辨率、多组分分离。本研究中使用的装置包含一堆矩形阳离子交换膜,床体积为9.25mL。溶菌酶的聚乙二醇化采用分批模式,使用5kDa甲氧基聚乙二醇丙醛(m-PEG丙醛),并以氰基硼氢化钠作为还原剂。膜色谱分离在每分钟1.62个膜床体积的流速下,以结合-洗脱模式进行。当施加盐梯度时,溶菌酶的较高聚乙二醇化形式(即副产物)比单聚乙二醇化溶菌酶(目标产物)洗脱得早,而溶菌酶最后洗脱。在针对分辨率和速度进行优化的洗脱条件下,分离可在不到15个膜床体积内完成。获得了高纯度和高回收率的单聚乙二醇化溶菌酶。在上述条件下获得的单聚乙二醇化溶菌酶的分离分辨率与文献中报道的等效阳离子交换树脂柱相当,而以床体积/分钟表示的流速则高21.7倍。此外,LFMC装置每米的理论塔板数明显更高。因此,本文讨论的基于LFMC的纯化过程结合了高生产率和高分辨率。