Balasundaram B, Harrison S T L, Li J, Chase H A
Bioprocess Engineering Research Unit, Department of Chemical Engineering, University of Cape Town, Cape Town, South Africa.
Biotechnol Bioeng. 2008 Feb 15;99(3):614-24. doi: 10.1002/bit.21586.
Expanded bed adsorption chromatography is used to capture products directly from unclarified feedstocks, thus combining solid-liquid separation, product concentration and preliminary purification into a single step. However, when non-specific ion-exchangers are used as the adsorbent in the expanded bed, there is the possibility that electrostatic interactions of cells or cell debris with the adsorbent may interfere with the adsorption of soluble products. These interactions depend on the particle size of the cell debris and its surface charge, which in turn depend on the extent of disruption used to release the intracellular products. The interactions occurring during expanded bed adsorption between the anionic ion-exchanger STREAMLINE DEAE and particulate yeast homogenates obtained by high pressure homogenisation at different intensities of disruption achieved by operating at different pressures were studied, while maintaining all other parameters constant. In-bed sampling from the expanded bed using ports fitted up the height of expanded bed was used to study the retention of yeast cells and cell debris within the bed and its influence on the adsorption of total soluble protein and alpha-glucosidase within various zones of the expanded bed. The retention of the biomass present in the homogenate obtained at a lower intensity of disruption was found to be high at the lower end of the column (17% from 13.8 MPa sample compared to 1% from 41.4 MPa sample). This interaction of the particulate material with the adsorbent was found to reduce the dynamic binding capacity of the adsorbent for total soluble protein from 3.6 mg/mL adsorbent for 41.4 MPa sample to 3.0 mg/mL adsorbent for 13.8 MPa sample. The adsorption of alpha-glucosidase was found to increase with an increase in the concentration of the enzyme in the feed, which increased with the intensity of disruption. Selective adsorption of 6,732 U alpha-glucosidase per mg of total protein bound, was noticed for the feedstock prepared at a higher disruption intensity at 41.4 MPa compared to adsorption of 1,262 U/mg of total protein bound for that prepared at 13.8 MPa. The selective adsorption of alpha-glucosidase due to its high concentration together with simultaneous high specific activity of the enzyme in the feed indicated the significance of selective release of enzymes during microbial cell disruption for efficient expanded bed adsorption processes.
扩张床吸附色谱法用于直接从未澄清的原料中捕获产物,从而将固液分离、产物浓缩和初步纯化合并为一个步骤。然而,当使用非特异性离子交换剂作为扩张床中的吸附剂时,细胞或细胞碎片与吸附剂之间的静电相互作用可能会干扰可溶性产物的吸附。这些相互作用取决于细胞碎片的粒径及其表面电荷,而这又取决于用于释放细胞内产物的破碎程度。研究了在不同压力下通过高压匀浆在不同破碎强度下获得的阴离子离子交换剂STREAMLINE DEAE与颗粒状酵母匀浆在扩张床吸附过程中发生的相互作用,同时保持所有其他参数不变。使用沿扩张床高度安装的端口从扩张床进行床内采样,以研究酵母细胞和细胞碎片在床内的保留情况及其对扩张床不同区域内总可溶性蛋白和α-葡萄糖苷酶吸附的影响。发现在较低破碎强度下获得的匀浆中存在的生物质在柱的下端保留率较高(13.8 MPa样品为17%,而41.4 MPa样品为1%)。发现这种颗粒物质与吸附剂的相互作用使吸附剂对总可溶性蛋白的动态结合容量从41.4 MPa样品的3.6 mg/mL吸附剂降低到13.8 MPa样品的3.0 mg/mL吸附剂。发现α-葡萄糖苷酶的吸附随着进料中酶浓度的增加而增加,而酶浓度随着破碎强度的增加而增加。与在13.8 MPa下制备的原料相比,在41.4 MPa的较高破碎强度下制备的原料每毫克结合总蛋白可选择性吸附6732 Uα-葡萄糖苷酶,而在13.8 MPa下制备的原料每毫克结合总蛋白吸附1262 U。由于进料中α-葡萄糖苷酶的高浓度及其同时具有的高比活性,其选择性吸附表明在微生物细胞破碎过程中酶的选择性释放对于高效扩张床吸附过程的重要性。