Evaluation of a sterile filtration process for viral vaccines using a model nanoparticle suspension

There is growing interest in the development of new vaccines based on live‐attenuated viruses (LAVs) and virus‐like particles. The large size of these vaccines, typically 100–400 nm, significantly complicates the use of sterile filtration. The objectives of this study are to examine the performance of several commercial sterile filters for filtration of a cytomegalovirus vaccine candidate (referred to as the LAV) and to develop and evaluate the use of a model nanoparticle suspension to perform a more quantitative assessment. Data obtained with a mixture of 200‐ and 300‐nm fluorescent particles provided yield and pressure profiles that captured the behavior of the viral vaccine. This included the excellent performance of the Sartorius Sartobran P filter, which provided greater than 80% yield of both the vaccine and model particles even though the average particle size was more than 250 nm. The particle yield for the Sartobran P was independent of filtrate flux above 200 L/m²/h, but increased with increasing particle concentration, varying from less than 10% at concentrations around 10⁷ particles/ml to more than 80% at concentrations above 10¹⁰ particles/ml due to saturation of particle capture/binding sites within the filter. These results provide important insights into the factors controlling transmission and fouling during sterile filtration of large vaccine products.     

Purification of plasmid DNA using tangential flow filtration and tandem anion-exchange membrane chromatography

A new bioprocess using mainly membrane operations to obtain purified plasmid DNA from Escherechia coli ferments was developed. The intermediate recovery and purification of the plasmid DNA in cell lysate was conducted using hollow-fiber tangential filtration and tandem anion-exchange membrane chromatography. The purity of the solutions of plasmid DNA obtained during each process stage was investigated. The results show that more than 97% of RNA in the lysate was removed during the process operations and that the plasmid DNA solution purity increased 28-fold. One of the main characteristics of the developed process is to avoid the use of large quantities of precipitating agents such as salts or alcohols. A better understanding of membrane-based technology for the purification of plasmid DNA from clarified E. coli lysate was developed in this research. The convenience of anion-exchange membranes, configured in ready-to-use devices can further simplify large-scale plasmid purification strategies.     

Investigation of fouling mechanisms of virus filters during the filtration of protein solutions using a high throughput filtration screening device

The downstream process development of novel antibodies (Abs) is often challenged by virus filter fouling making a better understanding of the underlying mechanisms highly desirable. The present study combines the protein characterization of different feedstreams with their virus filtration performance using a novel high throughput filtration screening system. Filtration experiments with Ab concentrations of up to 20 g/L using either low interacting or hydrophobically interacting pre-filters indicate the existence of two different fouling mechanisms, an irreversible and a reversible one. At the molecular level, size exclusion chromatography revealed that the presence of large amount of high molecular weight species—considered as irreversible aggregates—correlates with irreversible fouling that caused reduced Ab throughput. Results using dynamic light scattering show that a concentration dependent increase of the mean hydrodynamic diameter to the range of dimers (17 nm at 20 g/L) together with a negative DLS interaction parameter k_D (−18 mL/g) correlate with the propensity to form reversible aggregates and to cause reversible fouling, probably by a decelerated Ab transport velocity within the virus filter. The two fouling mechanisms are further supported by buffer flush experiments. Finally, concepts for reversible and irreversible fouling mechanisms are discussed together with strategies for respective fouling mitigation. © 2019 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2776, 2019.     

Antigenic activity of a gamma-ray inactivated, concentrated, purified cultured antirabies vaccine]

Concentrated purified cultural rabies vaccine inactivated with gamma-rays caused in intramuscular injection (2 ml twice at an interval of 23 and 21 days) production of virus-neutralizing antibodies both in experiments on animals and in the vaccinated volunteers in titres not below those obtained in persons given a complete course of cultural rabies vaccine inoculations. No untoward reactions occurred.     

Purification of hemoglobin by tangential flow filtration with diafiltration

A recent study by Palmer, Sun, and Harris (Biotechnol. Prog., 25:189–199, 2009) demonstrated that tangential flow filtration (TFF) can be used to produce HPLC‐grade bovine and human hemoglobin (Hb). In this current study, we assessed the quality of bovine Hb (bHb) purified by introducing a 10 L batch‐mode diafiltration step to the previously mentioned TFF Hb purification process. The bHb was purified from bovine red blood cells (RBCs) by filtering clarified RBC lysate through 50 nm (stage I) and 500 kDa (stage II) hollow fiber (HF) membranes. The filtrate was then passed through a 100 kDa (stage III) HF membrane with or without an additional 10 L diafiltration step to potentially remove additional small molecular weight impurities. Protein assays, SDS‐PAGE, and LC‐MS of the purified bHb (stage III retentate) reveal that addition of a diafiltration step has no effect on bHb purity or yield; however, it does increase the methemoglobin level and oxygen affinity of purified bHb. Therefore, we conclude that no additional benefit is gained from diafiltration at stage III and a three stage TFF process is sufficient to produce HPLC‐grade bHb. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Purification of a conjugated polysaccharide vaccine using tangential flow diafiltration

Conjugated vaccines prepared from the capsular polysaccharide of Streptococcus pneumoniae can provide immunization against invasive pneumococcal disease, meningitis, and otitis media. One of the critical steps in the production of these vaccines is the removal of free (unreacted) polysaccharides from the protein-polysaccharide conjugate. Experimental studies were performed to evaluate the effects of membrane pore size, filtrate flux, and solution conditions on the transmission of both the conjugate and free polysaccharide through different ultrafiltration membranes. Conjugate purification was done using diafiltration performed in a linearly-scalable tangential flow filtration cassette. More than 98% of the free polysaccharide was removed within a 5-diavolume diafiltration process, which is a significant improvement over previously reported results for purification of similar conjugated vaccines. These results clearly demonstrate the opportunities for using ultrafiltration/diafiltration for the final purification of conjugated vaccine products.     

A closed system for the filtration of Mycobacterium bovis liquid cultures using disposable capsule filters

A filtration system was designed to sterilize large volumes of Mycobacterium bovis BCG Tokyo culture safely, needed to purify protein antigens for immunodiagnosis of bovine tuberculosis. A closed system consists of culture bottles connected to three disposable filter capsules of decreasing pore size in series : a depth prefilter over a 1·2 μm filter ; a 0·8 μm prefilter over a 0·45 μm filter ; and a 0·2 μm sterile filter. Low air pressure (3 psi) forces liquid from below the bacillary pellicle. The system features a stainless steel clamp to hold rubber stoppers on the culture bottles, pleated filters to exclude bacillary clumps, a quick disconnector to minimize aerosols, and a closed system with plastic disposable filters that can be autoclaved as a unit without dismantling.     

Purification of human platelet membrane glycoproteins IIb and IIIa using high-performance liquid chromatography gel filtration

A method for purifying platelet membrane glycoproteins IIb and IIIa to homogeneity has been developed. The procedure involves high-pressure gel filtration chromatography using a TSK-4000SW column in the presence of sodium dodecyl sulfate. This technique is capable of rapidly preparing milligram quantities of each glycoprotein with greater than 90% recovery. The use of this technique should aid in defining the structural and functional properties of GPIIb and GPIIIa.     

Results of treatment of dysentery patients with streptomycin-dependent vaccine in comparison with other methods of treatment]

Comparative study of various methods of treatment was carried out on 777 patients suffering from acute dysentery with a bacteriologically confirmed diagnosis. To assess the therapeutic efficacy, along with consideration of clinical signs of the disease, immunoglobulin level was examined in the blood and coprofiltrates; also the state of reparative processes in the mucosa was appreciated by the histological examination of the biopsy material. Results of the work carried out indicated the inexpediency of the treatment of this disease with a combination of levomycetin and phthalazol. The use of live streptomycin-dependent dysentery vaccine was indicated in protracted torpid dysentery and was of no avail in acute form of the disease. A good therapeutic effect was observed with the application of pathogenetic therapy alone.     

Anaerobic treatment of highly concentrated aniline wastewater using packed-bed biofilm reactor

The performance of packed-bed biofilm reactor (PBBR) with self-floating bio-carriers was investigated to treat highly concentrated organic nitrogenous aniline wastewater with a COD value as high as 24,000 mg/L. With 45 vol% of carrier charge inside the reactor, the aniline wastewater can be effectively treated with 94% of COD removal efficiency at a low organic loading rate (OLR) of 0.9 kg COD/(m³ d). The removal efficiency decreased gradually down to 75% when OLR increased to 12.27 kg COD/(m³ d) that corresponded to 1 day of HRT. Separate tests with biofilm alone showed that the conversion contribution of the biofilm was about half of the overall COD conversion by the biofilm plus sludge system at the same OLRs of 3–4 kg COD/(m³ d), and that the biofilm had higher activity than suspended sludge. Ammonium released from decomposed aniline was increased gradually from 500 to 1700 mg/L with the OLR increase from 0.9 to 12.27 kg COD/(m³ d), which resulted in inhibitory effect to the microorganism due to the toxicity of free ammonia. Batch anaerobic toxicity tests showed that the biofilm was less sensitive to toxic compounds than suspended sludge and could tolerate higher concentration of free ammonia.     

Purification of hemoglobin from red blood cells using tangential flow filtration and immobilized metal ion affinity chromatography

Two methods for purifying hemoglobin (Hb) from red blood cells (RBCs) are compared. In the first method, red blood cell lysate is clarified with a 50 nm tangential flow filter and hemoglobin is purified using immobilized metal ion affinity chromatography (IMAC). In the second method, RBC lysate is processed with 50 nm, 500 kDa, and 50-100 kDa tangential flow filters, then hemoglobin is purified with IMAC. Our results show that the hemoglobins from both processes produce identical Hb products that are ultrapure and retain their biophysical properties (except for chicken hemoglobin, which shows erratic oxygen binding behavior after purification). Therefore, the most efficient method for Hb purification appears to be clarification with a 50 nm tangential flow filter, followed by purification with IMAC, and sample concentration/polishing on a 10-50 kDa tangential flow filter.     

Inactivation of Cryptosporidium parvum oocysts in water using ultrasonic treatment

Ultrasound in a liquid phase cause mass and heat transfer across the liquid through cavitational processes which act as nanoreactors to generate unstable mechanical equilibrium. The effect of 1 MHz ultrasound on the inactivation of Cryptosporidium parvum was investigated. Continuous irradiation of ultrasound (20 min) increased temperature due to cavitational phenomena. Ultrasound irradiation of liquid containing C. parvum showed significant quantitative changes in pH, temperature and inactivation of C. parvum (102.7 oocysts killed/s) with a minimum energy consumption (0.05 oocysts/s).     

超滤过结合密度梯度离心纯化鲍曼不动杆菌噬菌体方法的建立

目的 探讨获得低浓度内毒素和高滴度鲍曼不动杆菌噬菌体的方法,为制备安全的噬菌体生物制剂提供参考.方法 用可截留100 kD以上分子量的超滤离心管浓缩噬菌体裂解液并滤出分子量约为10 kD的内毒素,然后用蔗糖密度梯度离心纯化噬菌体浓缩液;分别测定超滤前、超滤后和纯化后的噬菌体滴度,采用鲎试验测定超滤前后内毒素的浓度,通过SDS-PAGE分析超滤前后和纯化后噬菌体蛋白的纯度.结果 经超滤离心法噬菌体滴度从3.9×1010 PFU/mL提高至1.68×1012PFU/mL,并可去除99.2％的内毒素;超滤过结合密度梯度离心后的SDS-PAGE可清晰呈现7种蛋白,分子量为29～100 kD.结论 超滤过结合密度梯度离心是一种简便、快速浓缩和纯化噬菌体的方法,并可有效地去除裂解液中的内毒素.     

Anaerobic treatment of winery wastewater using laboratory-scale multi- and single-fed filters at ambient temperatures

A lab-scale investigation was conducted to examine the effectiveness of a multi-fed upflow anaerobic filter process for the methane production from a rice winery effluent at ambient temperatures. The experiment was carried in two identical 3.0-l upflow filters, a single-fed reactor and a multi-fed reactor. The results showed that the multi-fed reactor, operated at the ambient temperatures of 19–27 °C and influent chemical oxygen demand (COD) of 8.34–25.76 g/l, could remove over 82% of COD even at an organic loading rate (OLR) of 37.68 g-COD/l d and a short hydraulic retention time (HRT) of 8 h. This reactor produced biogas with a methane yield of 0.30–0.35 l-CH₄/g-COD_removed. The multi-fed upflow anaerobic filter was proved to be more efficient than the single-fed reactor in terms of COD removal efficiency and stability against hydraulic loading shocks. A linear-regression model with influent COD concentration and HRT terms adequately described the multi-fed upflow anaerobic filter system for the treatment of rice winery wastewater at ambient temperatures.