用超滤法从猪血中分离纯化猪血红蛋白

为了给人工红细胞的研究提供较高纯度和浓度的血红蛋白,采用超滤膜分离的方法,通过研究分析,在一定超滤条件,从新鲜猪血中分离纯化得到猪血红蛋白。并应用SDS-PAGE凝胶电泳、紫外-可见分光光度计对纯化后的血红蛋白进行了鉴定分析。经分析,优化的超滤条件为:操作压力0.05Mpa、料液温度12℃;在此条件下分离纯化的猪血红蛋白,纯度达到了99%以上,浓度较纯化前提高了近20倍。     

超滤法浓缩谷氨酰胺转胺酶的影响因素研究

对微生物谷氨酰胺转胺酶(MTG)超滤浓缩的工艺条件进行了探讨及优化。实验采用截留分子量为30 kDa的聚醚砜(PES)膜,当发酵液初始pH为7,超滤浓缩倍数为4倍时,可以得到理想的MTG回收率。同时对超滤液中蛋白酶的变化进行了分析,发现随着超滤倍数的提高蛋白酶也逐渐提高,但在浓缩4倍以后达到较稳定的水平。聚醚砜(PES)超滤膜使用后用稀释的NaOH溶液浸泡清洗处理50 min后,膜通量可以恢复98.12%。     

Effect of solution pH on protein transport through ultrafiltration membranes

Although a number of previous studies have demonstrated that solution pH can have a dramatic effect on protein transport through ultrafiltration membranes, the exact origin of this behavior has been unclear. Experimental data were obtained for the transport of a broad range of proteins with different surface charge and molecular weight. The effective hydrodynamic size of the proteins was evaluated using size‐exclusion chromatography. The membrane charge, both before and after exposure to a given protein, was evaluated using streaming potential measurements. In most cases, the electrostatic interactions were dominated by the distortion of the electrical double layer surrounding the protein, leading to a distinct maximum in protein transmission at the protein isoelectric point. Attractive electrostatic interactions did occur when the protein and membrane had a large opposite charge, causing a second maximum in transmission at a pH between the isoelectric points of the protein and membrane. The sieving data were in good agreement with theoretical calculations based on available models for the partitioning of charged solutes in cylindrical pores. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 64: 27–37, 1999.     

以豆粕为氮源生产虫草菌丝体的研究

采用豆粕粉取代蚕蛹粉作氮源进行了虫草菌丝体的发酵试验,生产出无异臭味的虫草菌丝体,扩大了它的应用范围;对虫草菌丝体的抽提液进行超滤处理,测定了虫草多糖的含量和分子量。     

Albumin denaturation during ultrafiltration: effects of operating conditions and consequences on membrane fouling

Ultrafiltration of high-purity grade bovine serum albumin has been carried out under various temperature between 5 and 30 degrees C and at various cross-flow velocities, pressures, and concentrations with the aim of studying protein denaturation and its consequences on the process. Three different pump heads have been tested. Denaturation of proteins in solution has been monitored by laser light scattering and size exclusion chromatography. The rate of protein denaturation increases with temperature, cross-flow, and time. It is observed that membrane fouling is different whether denaturation has occurred or not. Under high-concentration polarization, denaturation can occur in the boundary layer if the wall concentration exceeds 400 g/L. It is shown how the residence time, operating temperature, and pressure play an important part in membrane fouling. This can provide guidelines for process design and control.     

Bismuth dimercaptopropanol (BisBAL) inhibits the expression of extracellular polysaccharides and proteins by Brevundimonas diminuta: implications for membrane microfiltration

A 2:1 molar ratio preparation of bismuth with a lipophilic dithiol (3-dimercapto-1-propanol, BAL) significantly reduced extracellular polymeric substances (EPS) expression by Brevundimonas diminuta in suspended cultures at levels just below the minimum inhibitory concentration (MIC). Total polysaccharides and proteins secreted by B. diminuta decreased by approximately 95% over a 5-day period when exposed to the bismuth-BAL chelate (BisBAL) at near MIC (12 microM). Fourier-transform infrared spectroscopy (FTIR) suggested that a possible mechanism of biofilm disruption by BisBAL is the inhibition of carbohydrate O-acetylation. FTIR also revealed extensive homology between EPS samples with and without BisBAL treatment, with proteins, polysaccharides, and peptides varying predominantly only in the amount expressed. EPS secretion decreased following BisBAL treatment as verified by atomic force microscopy and scanning electron microscopy. Without BisBAL treatment, a slime-like EPS matrix secreted by B. diminuta resulted in biofouling and inefficient hydrodynamic backwashing of microfiltration membranes.     

离心、超滤技术在甲型肝炎减毒活疫苗生产工艺中的应用

采用离心和超滤技术进行甲型肝炎减毒活疫苗生产 ,达到提高病毒的收获率。将含有甲型肝炎病毒的细胞收获液离心 ,上清进行超滤浓缩 ,回收病毒 ,病毒回收效果好。实验证明 ,该方法适合规模化生产。     

The role of phytoplankton in pollutant transfer processes in rivers. Example of River Marne (France)

The impact of the spring phytoplanktonic blooms on the partition of nutrients and metals between the dissolved and particulate phases was studied over two years in the river Marne, upstream of its confluence with the river Seine. Particular attention was devoted to copper and manganese, determined in the dissolved phase (< 0.22 m), subdivided into the colloidal phase and the 'truly dissolved' phase (< 10 KDaltons) obtained by tangential ultrafiltration. During the algal growth peaks, a sharp reduction of nutrients was observed in the dissolved phase: in 1994, consumption of 70% of silica, 50% of ammonium and 40% of soluble phosphorus present before the phytoplanktonic bloom.The water concentration peaks of suspended matter (SM) and of particulate metals, phosphorus and carbon coincide with those of chlorophyll. The highly significant correlations between pH and chlorophyll (r = 0.92, P < 0.001), pH and SM (r = 0.97, P < 0.001) and chlorophyll and SM (r = 0.93, P < 0.001) confirmed the phytoplanktonic nature of SM and the determining role of pH in the partition of metals, its increase being responsible for the coprecipitation of metal. As a corollary to the increase in the particulate phase, a decrease of 55% was observed for copper and manganese in the 'truly dissolved' phase compared to the concentrations outside bloom periods.The importance of the colloidal fraction was also shown. During the strong algal growth periods, the proportion of 'colloidal metal' in the dissolved phase (< 0.22 m) reached 60% and the increase in the colloidal fraction was 4 times stronger for copper than for manganese. While manganese seemed to be more associated with macroparticles, copper was more associated with fine colloidal biological particles intrinsic to the phytoplankton.     

Efficiency of ultrafiltration/diafiltration in removing organic and elemental process equipment related leachables from biological therapeutics

In the production of biological therapeutics such as monoclonal antibodies (mAbs), ultrafiltration and diafiltration (UF/DF) are widely regarded as effective downstream processing steps capable of removing process equipment related leachables (PERLs) introduced upstream of the UF/DF step. However, clearance data available in the literature are limited to species with low partition coefficients (log P) such as buffer ions, hydrophilic organic compounds, and some metal ions. Additional data for a wide range of PERLs including hydrophobic compounds and elemental impurities are needed to establish meaningful, comprehensive safety risk assessments. Herein, we report the results from studies investigating the clearance of seven different organic PERLs representing a wide range of characteristics (i.e., log P (−0.3 to 18)), and four model elements with different chemical properties spiked into a mAb formulation at 10 ppm and analyzed during clearance using gas chromatography–mass spectrometry (GC–MS), liquid chromatography-photodiode-array-mass spectrometry (LC-PDA-MS), and inductively coupled plasma mass spectrometry (ICP-MS). The clearance data showed ideal clearance and sieving of spiked organic PERLs with log P < 4, partial clearance of PERLs with 4 < log P < 9, and poor clearance of highly hydrophobic PERLs (log P > 9) after nine diafiltration volumes (DVs). Supplemental clearance studies on seven additional PERLs present at much lower concentration levels (0.1–1.5 ppm) in the mAb formulation upstream of UF/DF and three PERLs associated with the tangential flow filtration (TFF) equipment also demonstrated the similar correlations between log P and % clearance. For model elements, the findings suggest that UF/DF in general provides ideal clearance for elements. Evidence showed that the UF/DF process does not only help mitigate leachables risk from PERLs introduced upstream of UF/DF, but also from the TFF operation itself as all three TFF-related PERLs were effectively cleared. Overall, the UF/DF clearance presented in this work demonstrated whereas highly hydrophobic PERLs and elements that exist as charged species, particularly transition metal ions, may not be as effectively cleared and thus warrant further risk assessment; hydrophilic and some hydrophobic PERLs (log P < 4) are indeed well-cleared and thus present a lower overall safety risk.     

Concentrating rotavirus and recombinant enhanced green fluorescent protein fromE. coli using a temperature-sensitive hydrogel

Recombinant enhanced green fluorescent protein (EGFP) fromE. coli was concentrated 1.9 times by ultrafiltration using a temperature-sensitive hydrogel. Protein recovery and separation efficiency were 64% and 45%, respectively. Increased concentration of recombinant EGFP was confirmed by SDS-PAGE. Rotavirus was concentrated 3.2 times by ultrafiltration using a temperature-sensitive hydrogel, at 95% of virus recovery and 93% of separation efficiency. Hydrogel ultrafiltration appears to be an attractive alternative for the concentration of rotavirus and recombinant proteins fromE. coli.