Membrane filter (pore size, 0.22-0.45 micro m; thickness, 150 micro m) passing-through activity of Pseudomonas aeruginosa and other bacterial species with indigenous infiltration ability

Bacteria growing on MF-Millipore filters (thickness, 150 micro m) passed through the underlying membrane by their infiltration activity. Bacillus subtilis, Staphylococcus aureus, Klebsiella pneumoniae, and Escherichia coli passed through a 0.45- micro m pore size filter within 48-96 h. Pseudomonas aeruginosa, Serratia marcescens, and Listeria monocytogenes passed through a 0.3- micro m pore size filter. P. aeruginosa passed through a 0.22- micro m pore size filter. The membranes which allowed passing-through of bacteria showed normal bubble point values in the integrity test. Studies with isogenic S. marcescens mutants indicated that flagellum-dependent motility or surface-active exolipid were important in the passing-through. P. aeruginosa PAO1 C strain defective in twitching motility was unable to pass through the 0.22- micro m filter. Scanning electron microscopy showed bacteria passing-through the 0.22- micro m filter. Millipore membrane filters having well-defined reticulate structures will be useful in the study of infiltration activity of microbes.     

Inhibitory effects of filter-sterilized media on microspore development and embryogenesis in <Emphasis Type="Italic">Brassica napus</Emphasis> and <Emphasis Type="Italic">Triticum aestivum</Emphasis>

Summary Plant tissue culture media, sterilized through commercial filter membrane units, inhibited plant cell growth and development. Embryogenesis was suppressed in microspore cultures of Brassica napus and anther cultures of Triticum aestivum, and in vitro pollen development was suppressed in B. napus. Inhibition of growth and development occurred on media that had been filter-sterilized in low volumes through non-washed filter membrane units of all brands tested, including Nalgene, Corning, Millipore, and Sartorius membrane products. Similar results were obtained with Costar Transwells and Millipore inserts (Millicell-CM.-HA, and-PCF). These deleterious effects were eliminated by washing the membranes with water followed by a small volume of the medium. Media sterilized by filtration through washed filters produced significant improvements of growth and development of embryos and pollen.     

Impact of manufacturing, irradiation and filtration steps to bacterial contamination of autologous fibrin sealant.

BACKGROUND: Preoperative production of autologous fibrin sealant has become a routine procedure during the last years. As a certain percentage of blood products is contaminated with bacteria, contamination of plasma used for the production of fibrin sealant cannot be excluded. Especially in the orthopaedic setting, application of contaminated fibrin sealant can cause severe infections. MATERIALS AND METHODS: We contaminated plasma with Staphylococcus epidermidis, Corynebacterium striatum, Bacillus subtilis or Escherichia coli and produced fibrin sealant by cryoprecipitation and alcohol precipitation. Additionally, the products were gamma-irradiated at a dose of 30 Gy, frozen at -55 degrees C and filtered through a 0.2 microm filter after thawing. After each preparation step, samples were drawn and numbers of colony forming units were counted after incubation on agar plates. RESULTS: Cryoprecipitation, irradiation, freezing at -55 degrees C, and alcohol precipitation have only little impact on numbers of colony forming units. Filtration through a bacterial filter results in a sterile product. CONCLUSION: Bacteria in plasma as a starting material for production of fibrin sealant survive all routine steps of production, including gamma irradiation and freezing. Filtration of the product through a qualified bacterial filter is the only safe means to provide a sterile product.     

Haemolysis,a tool to evaluate mechanical stress to cells in bioprocess equipment

Summary Suspensions of fragile sheep erythrocytes were used to compare the levels of mechanical stress in two different crossflow filter units of small pilot scale. The recycling pumps were identified as the critical components mainly responsible for haemolysis. The level of cell damage was largely determined by the pump type and the backpressure applied to increase the transmembrane pressure in the filter.     

A dense cell retention culture system using stirred ceramic membrane reactor

A novel reactor design incorporating porous ceramic tubes into a stirred jar fermentor was developed. The stirred ceramic membrane reactor has two ceramic tubular membrane units inside the vessel and maintains high filtration flux by alternating use for filtering and recovering from clogging. Each filter unit was linked for both extraction of culture broth and gas sparging. High permeability was maintained for long periods by applying the periodical control between filtering and air sparging during the stirred retention culture of Saccharomyces cerevisiae. The ceramic filter aeration system increased the k(L)a to about five times that of ordinary gas sparing. Using the automatic feeding and filtering system, cell mass concentration reached 207 g/L in a short time, while it was 64 g/L in a fed-batch culture. More than 99% of the growing cells were retained in the fermentor by the filtering culture. Both yield and productivity of cells were also increased by controlling the feeding of fresh medium and filtering the supernatant of the dense cells culture. (c) 1994 John Wiley & Sons, Inc.     

Selective isolation of bacteria for metagenomic analysis: Impact of membrane characteristics on bacterial filterability

For indirect DNA extraction for metagenomics studies, bacterial cells can be effectively separated from sample debris by using a simple size exclusion technique, such as filtration, and thereafter lysed. The requirement for the optimal recovery of cells in filtrates is critical to achieve sufficient DNA yield and a representative population. Particles smaller than the filter pore size are expected to be found in the filtrate, whereas particles larger than the filter pore sizes are excluded. However, this is not always the case. It is established that the membrane pore size influences filtration efficiency to some degree. In addition the physicochemical characteristics of the filter suspension and characteristics of the microbial cells being filtered influence the exclusion property of a membrane. This review provides an overview of membrane filtration techniques and the factors that affect filterability of bacteria cells through a filter membrane. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:853–866, 2015     

Enumeration of iron-oxidizing bacteria by the membrane filter technique

This work presents a simple methodology to enumerate ferrous-iron-oxidizing bacteria in solution, easily applicable in bioleaching industrial plants, because it does not require expertise or specific equipment. The enumeration is based on bacterial concentration by microfiltration through a membrane filter. The filter containing the bacteria is placed on an agarose plate containing ferrous sulphate for bacterial growth. No difference was observed for the enumeration of Acidithiobacillus ferrooxidans ATCC 19859 when either 0.1 or 0.22 m pore size membrane filters were used. However, when the technique was applied to bacteria present in pregnant leaching solution, the smaller bacteria present in these solutions passed through the 0.22 m pore size membrane. Therefore the number of bacteria could be underestimated if they are monitored and filtered using a filter with pore size greater than 0.1 m. The limit of detection of this technique was one ferrous-iron-oxidizing bacterium in the filtered solutions.     

The effects of membrane filters used in biopharmaceutical processes on the concentration and composition of polysorbate 20

Polysorbate 20 (PS‐20) is often included in the formulation for therapeutic proteins to reduce protein aggregation and surface adsorption. During the production process of therapeutic proteins, various membrane filters are used to filter product pools containing PS‐20. The purpose of this study is to quantify the effects of these membrane filtration processes on the concentration and composition of PS‐20. A quantitative understanding of this process provides the knowledge base for better controlling the consistency of formulation excipients in drug products. PS‐20 solutions (without protein) were filtered through either 0.2 µm sterilizing filters or membrane filters with 30 kDa MWCO. The concentration of PS‐20 was measured by a mixed‐mode chromatography method and a nuclear magnetic resonance spectroscopy (NMR) assay. The composition of PS‐20 was characterized by ¹H‐NMR and a reverse‐phase chromatography method. Non‐specific adsorption of PS‐20 on both the sterilizing filter and 30 kDa MWCO membrane filter was quantified. Composition of PS‐20 was altered after 30 kDa MWCO membrane filtration, possibly because the different interactions between heterogeneous PS‐20 components and the 30 kDa MWCO membrane were not uniform. As a result, the retentate after the 30 kDa MWCO membrane filtration step contains no POE sorbitan and increased amount of POE sorbitan di‐esters and tri‐esters. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1503–1511, 2013     

Effects of Membrane Filtering of Tomato Root Exudates on Conidial Germination of Fusarium oxysporum f. sp. lycopersici

The effect of different membrane filters on the bioactivity of tomato root exudates was tested in an in vitro assay addressing the germination of microconidia of the soil-borne fungus Fusarium oxysporum f. sp. lycopersici . Membrane filtration of unsterile root exudates with filters of different membrane materials and filter brands resulted in an increased microconidia germination. This effect varied depending on the used membrane filter but was lacking when sterile root exudates were used. The alteration of the bioactivity of unsterile root exudates therefore seems to be due to the presence of microbial contaminants. The varying effects of different filter brands may be due to their differential potential of retaining inhibitory compounds. When working with root exudates, such effects of membrane filtration have to be taken into account.     

基于小波变换的心肌梗塞体表电位特征分析

小波变换已被很多心电学者用于ＥＣＧ信号的特征分析检测,在虚拟心脏基础上,选取合适的小波,对心肌梗塞的仿真体表电位进行小波变换细节分量处理,提出了一种新的体表电位形态特征的分析方法。结果表明,基于小波变换处理后体表电位图可以更地提示不同部位心肌在体表电位分布的特征,其表征出的拓扑形态对体表电位和虚拟心脏方法用于心肌梗塞临床诊断提供了一种新的途径。     

Microcount Method for Petrolatum-Based Topical Ointments Containing Waxes

A practical solvent system for the detection of microorganisms in topical ointments has been developed. The method involves dissolving 0.5 g of topical ointment in 50 ml of a solvent mixture (92 parts isopropyl myristate, 6 parts carbon disulfide, and 2 parts xylene) and filtering it through a 0.45-mum membrane filter. Residual solvent is then washed from the filter pad with 200 ml of sterile 0.5% Brain Heart Infusion broth containing 0.1% Tween 80. The filter pad is then removed and placed on a petri plate containing Trypticase Soy Agar medium. The petri plates thus prepared are then incubated at 37 C for 7 days, and the colonies produced are then counted. The toxicity of the solvent mixture was determined against Staphylococcus aureus, Escherichia coli, Pseudomonas aeruginosa, Salmonella newington, and spores of Bacillus subtilis and was found to be less toxic than the heat-sterilized isopropyl myristate and comparable to the filter-sterilized isopropyl myristate.     

Multipronged approach to managing beta‐glucan contaminants in the downstream process: Control of raw materials and filtration with charge‐modified nylon 6,6 membrane filters

(1→3)‐β‐d ‐Glucans (beta‐glucans) have been found in raw materials used in the manufacture of recombinant therapeutics. Because of their biological activity, beta‐glucans are considered process contaminants and consequently their level in the product needs to be controlled. Although beta‐glucans introduced into the cell culture process can readily be removed by bind‐and‐elute chromatography process steps, beta‐glucans can also be introduced into the purification process through raw materials containing beta‐glucans as well as leachables from filters made from cellulose. This article reports a multipronged approach to managing the beta‐glucan contamination in the downstream process. Raw material screening and selection can be used to effectively limit the level of beta‐glucan introduced into the downstream process. Placement of a cellulosic filter upstream of the last bind‐and‐elute column step or effective preuse flushing can also limit the level of contaminant introduced. More importantly, this article reports the active removal of beta‐glucan from the downstream process when necessary. It was discovered that the Posidyne^® filter, a charge‐modified nylon 6,6 membrane filter, was able to effectively remove beta‐glucans from buffers at relatively low pH and salt concentrations. An approach of using low beta‐glucan buffer components combined with filtration of the buffer with a Posidyne membrane has been successfully demonstrated at preparative scale. Additionally, the feasibility of active removal of beta‐glucan from in‐process product pools by Posidyne membrane filtration has also been demonstrated. Based on the data presented, a mechanism for binding is proposed, as well as a systematic approach for sizing of the Posidyne filter. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:672–680, 2013     

Role of membrane structure on the filtrate flux during monoclonal antibody filtration through virus retentive membranes

Virus removal filtration is a critical step in the manufacture of monoclonal antibody products, providing a robust size-based removal of both enveloped and non-enveloped viruses. Many monoclonal antibodies show very large reductions in filtrate flux during virus filtration, with the mechanisms governing this behavior and its dependence on the properties of the virus filter and antibody remaining largely unknown. Experiments were performed using the highly asymmetric Viresolve® Pro and the relatively homogeneous Pegasus™ SV4 virus filters using a highly purified monoclonal antibody. The filtrate flux for a 4 g/L antibody solution through the Viresolve® Pro decreased by about 10-fold when the filter was oriented with the skin side down but by more than 1000-fold when the asymmetric filter orientation was reversed and used with the skin side up. The very large flux decline observed with the skin side up could be eliminated by placing a large pore size prefilter directly on top of the virus filter; this improvement in filtrate flux was not seen when the prefilter was used inline or as a batch prefiltration step. The increase in flux due to the prefilter was not related to the removal of large protein aggregates or to an alteration in the extent of concentration polarization. Instead, the prefilter appears to transiently disrupt reversible associations of the antibodies caused by strong intermolecular attractions. These results provide important insights into the role of membrane morphology and antibody properties on the filtrate flux during virus filtration.     

Cellulolytic Bacteria in the Foregut of the Dromedary Camel (Camelus dromedarius)

Foregut digesta from five feral dromedary camels were inoculated into three different enrichment media: cotton thread, filter paper, and neutral detergent fiber. A total of 283 16S rRNA gene sequences were assigned to 33 operational taxonomic units by using 99% species-level identity. LIBSHUFF revealed significant differences in the community composition across all three libraries.     

Direct on air sampling filter quantification of cat allergen

A direct on sampling filter in solution (DOSIS) method for quantification of airborne cat allergens has been developed. In this method, the allergens firmly adsorbed to a porous polytetrafluoroethylene filter are reacted with specific antibodies conjugated to alkaline phosphatase, generating a matrix-bound allergen-antibody-phosphatase complex. The treated filter is subsequently floated on a commercially available chemiluminescent phosphatase substrate solution. Aliquots of this solution are removed and analyzed luminometrically. The light intensity of the product is linearly related to the amount of allergen over a large mass range, 0-100 SQ units (1 SQ unit is about 146 pg of the allergenic protein Fel d 1). DOSIS demonstrated intra- and interassay precisions of 9% and 8% and 14% and 21% for the levels 4 and 20 SQ units per filter, respectively. The limit of quantification was estimated to 0.4 SQ units (58 pg Fel d 1) of cat allergen per filter. Application of DOSIS to analysis of cat allergen concentrations of indoor air in homes with and without cats revealed, on average, a six times higher concentration in the former (142 SQ units/m(3)) as compared to the latter (24 SQ units/m(3)). The recorded concentrations for airborne cat allergen in homes with cats are in accordance with previously reported figures. Allergen-specifically stained sampling filters revealed the particulate nature of airborne cat allergen which seemed predominantly to be carried by numerous large dust particles.     

Virus filtration of high‐concentration monoclonal antibody solutions

The ability to process high‐concentration monoclonal antibody solutions (> 10 g/L) through small‐pore membranes typically used for virus removal can improve current antibody purification processes by eliminating the need for feed stream dilution, and by reducing filter area, cycle‐time, and costs. In this work, we present the screening of virus filters of varying configurations and materials of construction using MAb solutions with a concentration range of 4–20 g/L. For our MAbs of interest—two different humanized IgG1s—flux decay was not observed up to a filter loading of 200 L/m² with a regenerated cellulose hollow fiber virus removal filter. In contrast, PVDF and PES flat sheet disc membranes were plugged by solutions of these same MAbs with concentrations >4 g/L well before 50 L/m². These results were obtained with purified feed streams containing <2% aggregates, as measured by size exclusion chromatography, where the majority of the aggregate likely was composed of dimers. Differences in filtration flux performance between the two MAbs under similar operating conditions indicate the sensitivity of the system to small differences in protein structure, presumably due to the impact of these differences on nonspecific interactions between the protein and the membrane; these differences cannot be anticipated based on protein pI alone. Virus clearance data with two model viruses (XMuLV and MMV) confirm the ability of hollow fiber membranes with 19 ± 2 nm pore size to achieve at least 3–4 LRV, independent of MAb concentration, over the range examined. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Zonal rate model for axial and radial flow membrane chromatography,part II: Model‐based scale‐up

Membrane chromatography (MC) systems are finding increasing use in downstream processing trains for therapeutic proteins due to the unique mass‐transfer characteristics they provide. As a result, there is increased need for model‐based methods to scale‐up MC units using data collected on a scaled‐down unit. Here, a strategy is presented for MC unit scale‐up using the zonal rate model (ZRM). The ZRM partitions an MC unit into virtual flow zones to account for deviations from ideal plug‐flow behavior. To permit scale‐up, it is first configured for the specific device geometry and flow profiles within the scaled‐down unit so as to achieve decoupling of flow and binding related non‐idealities. The ZRM is then configured for the preparative‐scale unit, which typically utilizes markedly different flow manifolds and membrane architecture. Breakthrough is first analyzed in both units under non‐binding conditions using an inexpensive tracer to independently determine unit geometry related parameters of the ZRM. Binding related parameters are then determined from breakthrough data on the scaled‐down MC capsule to minimize sample requirements. Model‐based scale‐up may then be performed to predict band broadening and breakthrough curves on the preparative‐scale unit. Here, the approach is shown to be valid when the Pall XT140 and XT5 capsules serve as the preparative and scaled‐down units, respectively. In this case, scale‐up is facilitated by our finding that the distribution of linear velocities through the membrane in the XT140 capsule is independent of the feed flow rate and the type of protein transmitted. Introduction of this finding into the ZRM permits quantitative predictions of breakthrough over a range of industrially relevant operating conditions. Biotechnol. Bioeng. 2014;111: 1587–1594. © 2014 Wiley Periodicals, Inc.     

A simple cell disrupter designed for small cells with relatively large nuclei

A simple cell disrupter that is particularly suitable for breaking small cells with relatively large nuclei is described. Cells are disrupted by the shearing forces set up as they are pushed by a positive N2 pressure through a 0.8- to 1.5-micrometer stainless-steel filter. The total procedure takes only a few minutes, it is highly reproducible, and the yield is good. The cell homogenate obtained is a good starting source for the isolation of plasma membranes, intracellular organelles, and nuclei.     

A new method for purification of mature elastin.

Stable low-noise dual-beam spectrophotometric detection systems have been built to measure protein in the effluent from chromatographic columns. Measurements are carried out at the magnesium 285.2 nm atomic resonance line isolated either by the technique of selective modulation or by the use of a narrow bandpass interference filter. The noise level is about 0.0005-0.001 absorbance units and the drift rate is ±0.001 absorbance units in 24 hr. While slightly better noise performance could be obtained using the interference filter, selective modulation gives better linearity at higher absorbance values (up to 2.0).     

Leukocyte telomeres are longer in African Americans than in whites: the National Heart, Lung, and Blood Institute Family Heart Study and the Bogalusa Heart Study

Leukocyte telomere length (LTL) is ostensibly a bio-indicator of human aging. Here we report that African Americans have longer LTL than whites. We studied cross-sectionally 2453 individuals from the National Heart, Lung, and Blood Institute (NHLBI) Family Heart Study (age = 30–93 years) and the Bogalusa Heart Study (age = 19–37 years), comprising 1742 whites and 711 African Americans. We measured LTL by Southern blots of the terminal restriction fragments length. In 234 participants, telomere repeats were also measured by quantitative polymerase chain reaction (qPCR). Adjusted for age and body mass index (BMI), the respective leukocyte telomere lengths (mean ± SEM) were considerably longer in African Americans than in whites both in the Family Heart Study (7.004 ± 0.033 kb vs. 6.735 ± 0.024 kb, p  < 0.0001) and the Bogalusa Heart Study (7.923 ± 0.063 kb vs. 7.296 ± 0.039 kb, p  < 0.0001). We confirmed the racial effect on LTL by qPCR (3.038 ± 0.565 T/S units for African Americans vs. 2.714 ± 0.487 T/S units for whites, p  < 0.001). Cross-sectionally, sex- and BMI-adjusted LTL became shorter with age (range 19–93 years) at a steeper slope in African Americans than in whites (0.029 kb year⁻¹ vs. 0.020 kb year⁻¹, respectively, p  = 0.0001). We suggest that racial difference in LTL arises from a host of interacting biological factors, including replication rates of hematopoietic stem cells.