Efficient and predictable recovery of viruses from water by small scale ultrafiltration systems.

Current methods to concentrate viruses from large volumes of water are prone to inconsistent results and are costly and complex procedurally. Ultrafiltration can utilize size exclusion rather than adsorption and (or) elution to concentrate viruses and, therefore, may offer greater flexibility in developing methods that can provide more consistent recoveries among different viruses and widely varying water conditions. Two small scale ultrafiltration systems (hollow fiber and tangential flow) were tested with a virus suspended in 2 L of reagent grade, tap, ground, or surface water. Three model viruses were used (bacteriophages PP7 and T1 and poliovirus) to compare and characterize the recovery of viruses with the two ultrafiltration systems. Pretreatment of the ultrafilters with blocking agents and the use of elution agents can serve to prevent viral adsorption to the filter surface or to elute bound virus and keep viral agents suspended in the retentate. The use of a blocking and elution step concentrated viruses (>60% recovery) from widely varying water qualities, including surface water, such that a single method can be used to efficiently concentrate viruses from all of the water types tested. Both ultrafiltration systems appear to be able to efficiently recover viruses; however, the hollow fiber systems provided slightly better results in the 2-L volumes tested.     

Hollow-fiber ultrafiltration of Cryptosporidium parvum oocysts from a wide variety of 10-L surface water samples

An optimized hollow-fiber ultrafiltration system (50 000 MWCO) was developed to concentrate Cryptosporidium oocysts from 10-L samples of environmental water. Seeded experiments were conducted using a number of surface-water samples from the southwestern U.S.A. and source water from four water districts with histories of poor oocyst recovery. Ultrafiltration produced a mean recovery of 47.9% from 19 water samples (55.3% from 39 individual tests). We also compared oocyst recoveries using the hollow-fiber ultrafiltration system with those using the Envirochek filter. In limited comparison tests, the hollow-fiber ultrafiltration system produced recoveries similar to those of the Envirochek filter (hollow fiber, 74.1% (SD = 2.8); Envirochek, 71.9% (SD = 5.2)) in low-turbidity (3.9 NTU) samples and performed better than the Envirochek filter in high-turbidity (159.0 NTU) samples (hollow fiber, 27.5%; Envirochek, 0.4%). These results indicate that hollow-fiber ultrafiltration can efficiently recover oocysts from a wide variety of surface waters and may be a cost-effective alternative for concentrating Cryptosporidium from water, given the reusable nature of the filter.     

Recovery of insect cells using hollow fiber microfiltration

An efficient method was developed for media separation and cell collection for eukaryotic cells growing in suspension. The method is based on tangential flow microfiltration using an open channel arrangement in a hollow fiber configuration. Best results (highest processing flux rate) for polysulfone hollow fibers were obtained using fibers with internal diameter of 0.75 mm, 0.45 mum pore size, and a cell suspension flow at a shear rate of 14000 s(-1) (0.032 L/min per fiber). A flux rate of 500 L/m(2) h can be obtained by maintaining the surface area/cell ratio at 0.05 m(2)/10 L of cells at a concentration of 2.5 x 10(6) cells/mL. Forty liters of infected insect cells can be concentrated 10 times in 20 min without affecting cell viability. (c) 1995 John Wiley & Sons, Inc.     

Pilot-scale adenovirus seed production through concurrent virus release and concentration by hollow fiber filtration

Recovery of recombinant adenoviruses from infected mammalian cell cultures often requires multiple unit operations such as cell lysis for virus release, microfiltration for clarification, and ultrafiltration for concentration. While development of these multiple unit operations is relatively straightforward, implementation under aseptic conditions in a closed system can be challenging for the production of virus seed at industrial scales. In this study, we have developed a simple, single-step, scaleable process to effectively recover adenoviruses from infected PER.C6 cell cultures for the production of concentrated adenovirus seeds under aseptic conditions. Specifically, hollow fiber tangential flow filtration technology was applied to maximize cell lysis of infected cultures for virus release while simultaneously concentrating the virus to an appropriate level of volume reduction. Hollow fiber filters with small lumen diameter of 0.5 mm were chosen to maximize the wall shear for a highly effective cell lysis and virus release. Cell lysis and virus release were shown to correlate with the exposure time in the hollow fiber cartridge: the shear zone. In most cases, a virus recovery yield of more than 80% and a 15- to 20-fold concentration (or up to 95% volume reduction) was achieved in less than 2 h of processing time. The virus seeds prepared using this process at lab scale and at 300-L scale without clarification have been successfully tested for sterility and potency and used for subsequent infection with consistent virus productivity. This process should enable rapid production of adenovirus seeds with minimal unit operations and high efficiency recovery for adenovirus production at 1000-L scale.     

耦合中空纤维膜超滤分离游离细胞催化合成ATP

对耦合中空纤维膜超滤分离进行游离细胞催化合成ATP过程进行了实验研究,考察了细胞的催化效率和膜组件的操作稳定性。结果显示,中空纤维超滤膜的耦合分离能有效地截留反应液中的游离酶,其中乙醇脱氢酶(ADH)和已糖激酶(HK)的稳态截留效率在95%以上。耦合膜分离的酵母细胞催化ATP合成反应可重复使用2.5～3.0次,酶的利用率比普通分离的细胞提高2.0～2.5倍。中空纤维超滤膜于0.1Mpa工作压力下连续11批耦合分离操作,膜的渗透性无明显下降,过滤速率保持在初速率的95%以上。在稀释速率0.25h-1下,反应体系保持了连续5h的ATP高转化率合成与分离耦合的拟稳态操作。     

pH-induced flocculation,indirect electrocoagulation,and hollow fiber filtration techniques for harvesting the saltwater microalga Dunaliella

This research assessed the efficacy of three harvesting methods on a strain of Dunaliella viridis. While there is strong potential to use lipids from microalgae as a feedstock for biofuels to replace petroleum-based fuel, at present microalgal harvesting for biofuel production is not yet economically feasible or energy efficient. pH-induced flocculation (by adjusting the pH of exponentially growing cells), indirect electrocoagulation (applying aluminum hydroxide coagulant to culture), and hollow fiber filtration (separating biomass from medium using tangential flow) were compared as potential harvesting mechanisms for small-scale (3–10 L) and large-scale (30–150 L) volumes of D. viridis. Both pH-induced flocculation and electrocoagulation yielded significant biomass recovery (>95 %), but both methods required removal of added chemicals and/or coagulant before the medium could be reused. In contrast, hollow fiber filtration did not require added chemicals or coagulant, and as another advantage, the filtrate was successfully reused as culture medium without apparent detrimental effects on cell size, cell shape, or cell production. When high salinity stress was imposed on the concentrate produced from the filtration method, total fatty acids (FAs) did not increase. However, total FAs did significantly increase after hollow fiber filtration (49 %) in comparison to FA content before filtration (36 %). This research indicates that hollow fiber filtration as a commercial harvesting mechanism offers attractive advantages as a harvesting mechanism for microalgae such as Dunaliella, relative to pH-induced flocculation and indirect electrocoagulation.     

Combined haploid and insertional mutation screen in the zebrafish

To identify genes required for development of the brain and somites, we performed a pilot screen of gynogenetic haploid zebrafish embryos produced from mothers mutagenized by viral insertion. We describe an efficient method to identify new mutations and the affected gene. In addition, we report the results of a small-scale screen that identified five genes required for brain development, including novel alleles of nagie oko, pou5f1, ribosomal protein L36, and n-cadherin, as well as a novel allele of the laminin g1 gene that is required for normal skeletal muscle fiber organization and somite patterning.     

Recovery of Small Quantities of Viruses from Clean Waters on Cellulose Nitrate Membrane Filters

A method is described for quantitatively recovering small amounts of viruses from large volumes of buffered, distilled water. Development of the method was motivated by the anticipated need for testing large volumes of renovated sewage for viruses. The method consists of adsorbing viruses onto cellulose nitrate membrane filters (0.45 mum pore size) from water containing sufficient Na(2)HPO(4) to produce a molarity of 0.05 and sufficient citric acid to produce a pH of 7, and eluting the adsorbed viruses in 3% beef extract under extended sonic treatment. Complete recovery of poliovirus 1, echovirus 7, and coxsackievirus B3 resulted when less than 100 plaque-forming units were added to 1-liter quantities of water. Recoveries of reovirus 1 were almost as good. Preliminary studies indicate that good recoveries can be made from 25-gal quantities of water. The method described is efficient in waters of high quality and may be useful for recovering viruses in renovated, and perhaps in tap waters, but not in waters containing certain organic matter unless that matter is first removed.     

Use of bituminous coal as an alternative technique for field concentration of waterborne viruses

A filter system that sandwiches a bituminous coal preparation between two prefilters was comparable to those presently used to recover human viruses from large volumes of water. This filter was effective over a pH range of 3.0 to 7.0. Poliovirus type 1 recoveries from 100-liter seeded samples of Cincinnati tap water did not vary significantly when compared with those of identical samples processed through Filterite and Millipore filters. In studies with raw domestic sewage, virus recoveries were nearly identical from comparable samples filtered through coal and Millipore disk filters. Thus, the availability of coal makes this filter system an inexpensive analytical tool, especially in developing nations, for virus concentration.     

Use of bituminous coal as an alternative technique for field concentration of waterborne viruses.

A filter system that sandwiches a bituminous coal preparation between two prefilters was comparable to those presently used to recover human viruses from large volumes of water. This filter was effective over a pH range of 3.0 to 7.0. Poliovirus type 1 recoveries from 100-liter seeded samples of Cincinnati tap water did not vary significantly when compared with those of identical samples processed through Filterite and Millipore filters. In studies with raw domestic sewage, virus recoveries were nearly identical from comparable samples filtered through coal and Millipore disk filters. Thus, the availability of coal makes this filter system an inexpensive analytical tool, especially in developing nations, for virus concentration.     

A new integrated membrane filtration and chromatographic device

To improve protein separation, a novel integrated device combining membrane filtration and chromatography has been developed. The device basically consists of a hollow fiber filtration module whose shell side is filled with chromatographic resin beads. However, there is an essentially impermeable coated zone near the hollow fiber module outlet. The integrated device enjoys the advantages of both membrane filtration and chromatography; it also allows one to load the chromatographic media directly from the fermentation broth or lysate and separate the adsorbed proteins through the subsequent elution step in a cyclic process. Interfacial polymerization was carried out to coat the bottom section of the hollow fiber membrane; the rest of the hollow fiber membrane remained unaffected. Myoglobin (Mb) and alpha-lactalbumin (alpha-LA) were primarily used as model proteins in a binary mixture; binary mixtures of Mb and bovine serum albumin (BSA) were also investigated. Separation behaviors of binary protein mixtures were studied in devices having either an ultrafiltration (UF) or a microfiltration (MF) membrane. Experimental results show that the breakthrough time and the protein loading capacities were dramatically improved after introducing the impermeable coating in both UF and MF modules. For a synthetic yeast fermentation broth feed, four loading-washing-elution-reequilibration-based cyclic runs for separation of Mb and alpha-LA were performed in the device using a MF membrane with a coated zone without cleaning in between. The Mb and alpha-LA elution profiles for the four consecutive runs were almost superimposable. Due to lower transmembrane flux in this device plus the periodical washing-elution during the chromatographic separation, fouling was not a problem, unlike in conventional microfiltration.     

重组人血清白蛋白在Pichia pastoris中的表达与纯化

为实现重组人血清白蛋白（ｒＨＳＡ）的开发,对构建的酵母工程菌Ｐｉｃｈｉａ ｐａｓｔｏｒｉｓ ＧＳ１１５／ＨＳＡ进行了表达条件的优化,摇瓶中将表达ｒＨＳＡ的量提高到１５０ｍｇ／Ｌ。经中空纤维柱浓缩、Ｐｈｅｎｙｌ－Ｓｅｐｈａｒｏｓｅ分离和抗ＨＳＡ－Ｓｅｐｈａｒｏｓｅ亲和层析纯化获得电泳纯的重组人血清白蛋白。     

Tangential-flow ultrafiltration with integrated inhibition detection for recovery of surrogates and human pathogens from large-volume source water and finished drinking water

Tangential-flow ultrafiltration was optimized for the recovery of Escherichia coli, Enterococcus faecalis, Clostridium perfringens spores, bacteriophages MS2 and PRD1, murine norovirus, and poliovirus seeded into 100-liter surface water (SW) and drinking water (DW) samples. SW and DW collected from two drinking water treatment plants were then evaluated for human enteric viruses.     

Enzymatic synthesis of glucuronides using lipophilic hollow fiber membranes

A lipophilic hollow fiber membrane preparation was used for the enzymatic glucuronidation of lipophilic aromatic compounds. A crude solubilized microsomal enzyme preparation was circulated on the external side of the lipophilic membrane while the phenol containing buffer solution was circulated through the internal side of the hollow fiber membrane. Phenols, which accumulate in and penetrate the lipophilic membrane, were converted by UDP-glucuronyltransferase to the corresponding glucuronides. During this process the lipophilic compounds are converted to hydrophilic substances, which are not able to rediffuse through the lipophilic membrane into the donor side of the hollow fiber module. The produced glucuronide is separated by means of a coupled dialysis with a module of hydrophilic surface (cellulose acetate), while the enzyme protein is retained.On the stripping side of the dialysing module the glucuronide can be separated by solid phase extraction (Lichroprep RP-18) while a continuous substitution of cofactor into this compartment is possible. UDPGA follows its own concentration gradient and migrates into the enzymatic mixture, where it is utilized. This new technique using hollow fiber modules offers completely new possibilities for long-term high-capacity, highly specific glucuronidation of phenolic compounds. Fields of application are not only the economical production of special glucuronides, but also the specific elimination of phenols from waste fluids or from serum and blood of patients.For the production of glucuronides by this technique the use of highly purified enzymes is not essential. Cheap crude enzyme preparations are quite adequate for an optimal reaction. Using a crude enzyme preparation with a specific batch activity of 13 nMol/min per mg of protein, the activity in the reactor system was observed to be 4.6 nMol/min of 2-naphtol glucuronide formed per mg of protein. This corresponds to 3.6 nMol/h of product formed per mg of protein per cm² of hollow fiber surface.Using a membrane surface of 0.5 m² the production of 18 mMol of glucuronide per h and mg protein can be achieved.     

Ultrafiltration of highly concentrated antibody solutions: Experiments and modeling for the effects of module and buffer conditions

Although ultrafiltration is currently used for the concentration and formulation of nearly all biotherapeutics, obtaining the very high target concentrations for monoclonal antibody products is challenging. The objective of this work was to examine the effects of the membrane module design and buffer conditions on both the filtrate flux and maximum achievable protein concentration during the ultrafiltration of highly concentrated monoclonal antibody solutions. Experimental data were obtained using both hollow fiber and screened cassettes and in the presence of specific excipients that are known to alter the solution viscosity. Data were compared with predictions of a recently developed model that accounts for the complex thermodynamic and hydrodynamic behavior in these systems, including the effects of back‐filtration arising from the large pressure drop through the module due to the high viscosity of the concentrated antibody solutions. Model calculations were in good agreement with experimental data in hollow fiber modules with very different fiber length and in screened cassettes having different screen geometries. These results provide important insights into the key factors controlling the filtrate flux and maximum achievable protein concentration during ultrafiltration of highly concentrated antibody solutions as well as a framework for the development of enhanced ultrafiltration processes for this application. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:692–701, 2016     

Hollow fiber countercurrent dialysis for continuous buffer exchange of high-value biotherapeutics

Buffer exchange, desalting, and formulation of high-value biotherapeutics are currently performed using batch diafiltration (DF); however, this type of tangential flow filtration process may be difficult to implement as part of a fully continuous biomanufacturing process. The objective of this study was to explore the potential of using countercurrent dialysis for continuous protein formulation and buffer exchange. Experiments were performed using concentrated solutions of immunoglobuin G (IgG) with commercially available hollow fiber dialyzers having 1.5 and 1.8 m² membrane surface area. More than 99.9% buffer exchange was obtained over a range of conditions, as determined from the removal of a model impurity (vitamin B₁₂). The dialyzers were able to process more than 0.5 kg of IgG per day in an easily scalable low-cost process. In addition, buffer requirements were less than 0.02 L of buffer per gram IgG, which is several times less than that used in current batch DF processes. These results clearly demonstrate the potential of using low-cost hollow fiber dialyzers for buffer exchange and product formulation in continuous bioprocessing. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2763, 2019.     

水体病毒钙离子絮凝浓缩新方法研究

研究建立了一种从水体中浓缩病毒的新方法,即钙离子絮凝-柠檬酸缓冲液洗溶法,该方法的要点是先用一定量的钙离子溶液和钙离子絮凝剂絮凝水体中的病毒,再用pH5.0的0.3mol/L的柠檬酸缓冲液洗溶,然后再进一步超滤浓缩。此法可方便地将水体中的病毒浓缩10000倍以上。应用该法分别对人工播种于饮用水中的f2噬菌体和脊髓灰质炎疫苗病毒(PV1)进行了浓缩,结果发现f2噬菌体的平均回收率达96%,而PV1的回收率为100%,均显著高于阳电膜过滤法(P<0.05)。该方法快速、简便、有效。     

Influence of a swirl motion on the interaction between microalgal cells and environmental medium during ultrafiltration of a culture of Tetraselmis suecica

The role of the environmental medium of a marine microalga culture (Tetraselmis suecica) in membrane fouling phenomenon is quantified for two ultrafiltration units: one generating a classical tangential plane flow and another involving a swirling decaying flow induced by a tangential inlet. Compared to the plane unit, the swirling configuration increases the performances of the ultrafiltration process (augmentation of 20% in terms of limiting flux). Interactions between the culture medium and cells depend on the module design. Furthermore, experiments emphasize the significant role of the particles whatever the module design: more than 70% of the total hydraulic resistance could be due to the microalgal cells, while about 30% of membrane fouling is relevant to soluble materials.