Venkiteshwaran Adith, Heider Patrick, Teysseyre Laure, Belfort Georges
Howard P. Isermann Department of Chemical and Biological Engineering, Center for Biotechnology and Interdisciplinary Studies, Rensselaer Polytechnic Institute, Troy, New York, USA.
Biotechnol Bioeng. 2008 Dec 1;101(5):957-66. doi: 10.1002/bit.21964.
Efficient and economic recovery of immunoglobulins (Igs) from complex biological fluids such as serum, cell culture supernatant or fermentation cell lysate or supernatant, represents a substantial challenge in biotechnology. Methods such as protein A affinity chromatography and anion exchange chromatography are limited by cost and selectivity, respectively, while membrane chromatography is limited by low adsorptive area, flow distribution problems and scale-up difficulties. By combining the traditional salt-assisted precipitation process for selective removal of Igs from serum followed by constant-permeate flux membrane microfiltration for low fouling, we demonstrate an exciting new, efficient and economic hybrid method. The high selectivity of an ammonium sulfate-induced precipitation step was used to precipitate the Igs leaving the major undesirable impurity, the bovine serum albumin (BSA), in solution. Crossflow membrane microfiltration in diafiltration mode was then employed to retain the precipitate, while using axial flow rates to optimize removal of residual soluble BSA to the permeate. The selectivity between immunoglobulin G (IgG) and BSA obtained from the precipitation step was approximately 36, with 97% removal of the BSA with diafiltration in 5 diavolumes with resulting purity of the IgG of approximately 93% after the membrane microfiltration step. Complete resolubilization of the IgG was obtained without any aggregation at the concentrations of ammonium sulfate employed in this work. Further, membrane pore size and axial Reynolds number (recirculation rate) were shown to be important for minimizing fouling and loss of protein precipitate.
从血清、细胞培养上清液或发酵细胞裂解物或上清液等复杂生物流体中高效且经济地回收免疫球蛋白(Ig),是生物技术领域面临的一项重大挑战。诸如蛋白A亲和色谱法和阴离子交换色谱法等方法,分别受到成本和选择性的限制,而膜色谱法则受到吸附面积低、流动分布问题以及放大困难的限制。通过将传统的盐辅助沉淀工艺(用于从血清中选择性去除Ig)与恒通量膜微滤工艺(用于减少污染)相结合,我们展示了一种令人兴奋的新型高效经济的混合方法。硫酸铵诱导沉淀步骤的高选择性用于沉淀Ig,而将主要的不良杂质牛血清白蛋白(BSA)留在溶液中。然后采用错流膜微滤的渗滤模式来保留沉淀,同时利用轴向流速优化将残留可溶性BSA去除到渗透液中。沉淀步骤中获得的免疫球蛋白G(IgG)和BSA之间的选择性约为36,在5倍料液体积的渗滤过程中,BSA的去除率为97%,膜微滤步骤后IgG的纯度约为93%。在本工作中使用的硫酸铵浓度下,IgG完全重新溶解且没有任何聚集。此外,膜孔径和轴向雷诺数(再循环率)对于最小化污染和蛋白质沉淀损失很重要。