Gebauer K H, Thömmes J, Kula M R
Institut für Enzymtechnologie, Heinrich-Heine-Universität Düsseldorf, Postfach 2050, D-52404 Jülich, Germany.
Biotechnol Bioeng. 1997 Apr 20;54(2):181-9. doi: 10.1002/(SICI)1097-0290(19970420)54:2<181::AID-BIT9>3.0.CO;2-H.
High capacity membrane adsorbents have been used as a stationary phase for the preparative chromatographic purification of human serum albumin. A two-step ion exchange fractionation scheme yields albumin with 98% purity from clarified, microfiltrated, and desalted human plasma. Experiments with laboratory and pilot scale membrane modules are compared to literature data obtained with conventional Fast Flow Sepharose in a similar purification protocol. Increased productivity in combination with excellent reproducibility and stability was found using the membrane adsorbents. Scale-up of the process based on standard microfiltration equipment was successful but resulted in reduced capacity and productivity due to deteriorated flow characteristics of the module. This was attributed to the effects of substantial axial dispersion in the pilot scale module. Methods to reduce this limitation were identified. The concept of membrane adsorption chromatography for the fast purification of proteins is illustrated and engineering aspects important for the process design are discussed.
高容量膜吸附剂已被用作固定相,用于人血清白蛋白的制备色谱纯化。两步离子交换分级分离方案可从澄清、微滤和脱盐的人血浆中获得纯度为98%的白蛋白。将实验室规模和中试规模膜组件的实验结果与在类似纯化方案中使用传统快速流动琼脂糖获得的文献数据进行了比较。使用膜吸附剂可提高生产率,并具有出色的重现性和稳定性。基于标准微滤设备的工艺放大成功,但由于组件流动特性变差,导致容量和生产率降低。这归因于中试规模组件中大量轴向扩散的影响。确定了减少此限制的方法。阐述了用于蛋白质快速纯化的膜吸附色谱概念,并讨论了对工艺设计很重要的工程方面。