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PubMed2002

Assessment of bioaerosols in swine barns by filtration and impaction.

Bioaerosol concentrations inside one naturally ventilated and one mechanically ventilated swine finishing barn were assessed by sampling air using membrane filtration and impaction (six-stage Andersen sampler), and assayed by culture method. The barns, located on the same commercial farm in northeast Kansas, did not show any significant difference (p > 0.05) in concentrations of total and respirable airborne microorganisms. The overall mean total concentrations inside the two barns were 6.6 x 10(4) colony forming units (CFU)/m3 (SD = 3.8 x 10(4) CFU/m3 as measured by filtration and 8.6 x 10(4) CFU/m3 (SD = 5.1 x 10(4) CFU/m3) by impaction. The overall mean respirable concentrations were 9.0 x 10(3) CFU/m3 (SD = 4.1 x 10(3) CFU/m3) measured by filtration and 2.8 x 10(4) CFU/m3 (SD = 2.2 x 10(4) CFU/m3) by impaction. Total and respirable CFU concentrations measured by impaction were significantly (p < 0.05) higher than that by filtration. The persistent strains of microorganisms were various species of the following genera: Staphylococcus, Pseudomonas, Bacillus, Listeria, Enterococcus, Nocardia, Lactobacillus, and Penicillium. It appears that filtration sampling can be used for a qualitative survey of bioaerosols in swine barns while the Andersen sampler is suitable for both quantitative and qualitative assessments.

Aerosols↗
PubMed1999

Erbium filtration: a cost-effective, dose-reducing filter which maintains abdominal image quality.

The current study investigated the effect of erbium filtration on an anteroposterior abdominal image. The radiation dose reductions achievable and the cost effectiveness of this filter were also evaluated. An assessment of the radiation dose delivered employing either the standard total filtration (3 mm Al equivalent) or 0.1 mm of erbium filtration added to the standard filtration was undertaken on 21 patients. Image quality was assessed using the Commission of European Communities (CEC) criteria. Significant reductions of 64.6 % in entrance surface (p = 0.0001) and 23.4 % in effective dose (p = 0.0099) were recorded with erbium filtration. Image quality was maintained and the cost per man saved was pound 128. More widespread use of this dose reducing filter is advocated.

Adult↗
PubMed1979

Studies on the filtration properties of isolated renal basement membranes.

1. The filtration properties of films of renal basement membrane were studied in vitro using pressure filtration chambers. 2. Retention of cytochrome c by the films was found to be dependent upon the filtration pressure indicating that it was transferred across the films by convective as well as diffusive flow. In contrast, serum albumin was transferred by diffusive movement only. 3. When solutions containing both cytochrome c and IgG were filtered it was found that increasing the filtration pressure reduced the flux of cytochrome c across the films. A similar phenomenon occurred when serum was filtered, less protein passed through the films at high filtration pressures. These phenomena are explained by concentration-polarisation effects. 4. The flux of cytochrome c through the films was found to decrease in a non-linear manner as the films thickness was increased. With thin films, the flux of cytochrome c increased in a non-linear manner as the concentration of the protein in the overstanding solution was increased. With thicker films the flux was linearly dependent on concentration. These findings are interpreted as supporting the view that movement of cytochrome c occurs, at least in part, by convective flow.

Animals↗
PubMed1995

Leucodepletion of blood products by filtration.

The leucocytes present in red cell and platelet components have been implicated in several important immunological and infective complications of blood transfusion. Recent developments in blood filtration technology allow the production of leucodepleted blood products (residual leucocytes < 5 x 10(6) per transfused unit) in the laboratory or at the bedside with the potential to prevent these adverse effects. Quality assurance remains an important problem, particularly for bedside filtration. Prestorage filtration may have significant advantages for red cell and platelet production. There is strong clinical evidence that 3 log10 leucodepletion prevents or delays febrile reactions in patients receiving multiple red cell transfusions and can reduce cytomegalovirus transmission. Leucodepletion to prevent HLA alloimmunisation, platelet refractoriness and febrile reactions in patients receiving red cell and platelet support remains controversial. Transfused leucocytes induce 'immunosuppressive' changes in the recipient, but recent studies cast doubt on the association with cancer recurrence after surgery. However, leucodepleted blood may reduce the incidence of postoperative infection. Leucodepletion by filtration is expensive and there is a requirement for well-designed prospective clinical studies focusing on appropriate filtration technology (and alternatives), clinical outcome and cost-effectiveness.

Animals↗
PubMed2004

Leukoreduction filtration of blood with sickle cell trait.

Leukoreduction of cellular blood products by filtration has been shown to decrease the incidence of febrile nonhemolytic transfusion reactions, transmission of leukocyte-associated viruses, and HLA alloimmunization. However, the increasing popularity of leukofiltering blood products over the past few years has highlighted specific filtration failures associated with sickle trait (hemoglobin AS) blood. Sickle trait blood does not filter adequately, which leads to prolonged or incomplete filtration, often with a higher number of postfiltration leukocytes in the unit than the mandated minimal residual volume of <1 to 5 x 10(6). This review of the literature highlights various parameters that affect the adequacy of filtration of blood products, including effects of temperature, pH, osmolarity, type of anticoagulant, time of storage, and oxygen saturation of the blood unit. A combination of these factors likely contributes to the frequent filtration failure of sickle trait products. Although blood units are not routinely screened for sickle cell hemoglobin, administration of units with sickle trait red blood cells can be disadvantageous to certain patient populations. This review concludes with a discussion of different approaches to screening blood units for sickle cell trait.

Anticoagulants↗
PubMed2004

Development of a biological filtration model applied for advanced treatment of sewage.

A mathematical model of biological filtration process is developed in this paper. A biological filtration process has advantages that filtration action and biological activities are combined in a single reactor with aid of filter media. Both physical and biological functions are incorporated in this developed model to simulate both mechanisms. Backwashing is expressed by the assumption that a mean captured solids concentration is input as data, and a captured solids concentration is kept at that value during each filtration run. The developed model is applied to explain the experimental performance with biological filtration reactors, in which batch cultivation of autotrophic bacteria and continuous treatment of actual sewage are carried out. Its applicability is discussed by comparing the simulated results with the experimental data. This model can favourably estimate maximum accumulation of autotrophic bacteria on the medium in batch cultivation, long-term treatment performance in continuous treatment, details of water quality profiles through the filter bed, and biomass. Required hydraulic retention time for nitrification and an appropriate recirculation ratio in a winter season are discussed with this model. This model predicts that a HRT of 1.1 h or above is required to achieve nitrification with remaining NH4(+)-N of less than 1 mgN/L and that an appropriate recirculation ratio is 2-3.

Bioreactors↗
PubMed2006

Comparative performance of membrane filters vs. high-surface area filtration cartridges for the determination of element concentrations in freshwater systems.

Interdisciplinary studies on trace element cycles in aquatic environments may require the simultaneous use of small- and large-scale filtration devices to collect all the necessary sample aliquots for the different scientific objectives (e.g. trace element and organic carbon analysis, chronic toxicity testing, and characterization of colloidal matter). This study compares the performance of membrane filters (MF, Millipore-approx. surface area 0.002 m2) and two large-surface area filtration cartridges (Calyx, MSI and Polypro, CUNO approx. surface area 1 m2) in three freshwater systems with contrasting characteristics. Membrane filters and filtration cartridges fractionate water samples in a comparable way except for some elements (Al, Mn, Pb, and Ti) and when dealing with high-turbidity, organic-rich matrices. Estimation of the actual filters' pore size using the single particle counting technique gives cut-offs of 0.2-0.3, 0.7 and 2 microm for membrane filters, Polypro cartridge and Calyx cartridge respectively, explaining many of the differences observed between membrane and cartridge filters. Direct involvement of filter manufacturers to determine actual filter cut-offs during environmental applications would be highly beneficial to increase the comparability of the measurements of filterable element concentrations. Better harmonization of filtration procedures (filter type, actual filter cut-off, in situ vs. ex situ filtration) among laboratories in different countries is also necessary in order to improve consistency of environmental databases.

Carbon↗
PubMed1998

The effects of S-nitrosocaptopril on renal filtration and blood pressure in rats.

The present investigation was performed to evaluate the effects of S-nitrosocaptopril, a novel vasodilator possessing the capacities of both an angiotensin converting enzyme inhibitor and an NO donor, on blood pressure and renal function in rats. S-nitrosocaptopril produced acute reductions in mean arterial pressure after both oral dosing (5, 10, 50 mg/kg) to chronically-catheterized awake rats and intravenous administrations (0.125, 1.25, 12.5 mg/kg) to anesthetized rats. The hypotensive magnitude and duration of S-nitrosocaptopril were dose-dependent. Acute pressure-associated reductions in the glomerular filtration rate and urine flow were observed only at high concentration of S-nitrosocaptopril (12.5 mg/kg, i.v.) in both awake and anesthetized rats. These decreases were transient, followed by an overshoot of glomerular filtration rate and urine flow above basal values. In contrast, captopril (i.v.) did not produce any significant acute effects on mean blood pressure and glomerular filtration rate in either awake or anesthetized rats. In rats with acute hypertension induced by NG-monomethyl-L-arginine (L-NMMA, 30 mg/kg, i.v.), S-nitrosocaptopril (0.125 mg/kg, i.v.) significantly abolished the hypertensive effects. In contrast, the hypertension was not affected by captopril. In two-kidney one-clipped Goldblatt hypertensive rats, oral administration of S-nitrosocaptopril (25 mg/kg, b.i.d.) for 10 days significantly reduced systolic blood pressure and preserved glomerular filtration rate. The oral antihypertensive effect of S-nitrosocaptopril was more potent than captopril (P < 0.05). In conclusion, these findings indicate that: (1) S-nitrosocaptopril provides both acute and chronic anti-hypertensive effects orally and intravenously, whereas captopril has only moderate chronic oral effects; and (2) S-nitrosocaptopril preferentially decreases blood pressure without markedly affecting glomerular filtration rate.

Administration, Oral↗
PubMed2003

Removal of viable and inactivated Cryptosporidium by dual- and tri-media filtration.

The limited efficacy of disinfectants, other than ultraviolet irradiation and ozonation, as a barrier against Cryptosporidium parvum in drinking water treatment has underscored the increased importance of oocyst removal by filtration. Currently, no reliable surrogates have been identified for C. parvum removal by filtration. As a result, evaluations of the Cryptosporidium removal by treatment operations have been performed using oocysts. It has typically been assumed that chemically inactivated oocysts are suitable surrogates for viable oocysts. Measurements of electrophoretic mobility, however, have shown that chemical inactivation changes the surface charge of Cryptosporidium oocysts. The present bench-scale research indicated that formalin-inactivated oocysts are reliable surrogates for viable oocysts during both stable filter operation and periods where filtration processes are challenged, such as coagulation failure. This finding is important because of the practical difficulties associated with using viable oocysts in filtration investigations. Poor coagulation conditions severely compromised removal of viable and inactivated oocysts by dual- and tri-media filters compared to stable operating conditions and filter ripening, emphasizing the importance of optimized chemical pre-treatment (coagulation) for the successful removal of oocysts during filtration. The treatment optimization experiments also indicated that tri-media filters offered only marginally higher oocyst removals than dual-media filters.

Animals↗
PubMed1984

A rapid filtration method for receptor binding: characterization with mu and delta opiate receptors.

A commercially available (Skatron) cell harvester was adapted for use in mu (3H-naloxone-labeled) and delta (3H-DADLE-labeled) opiate receptor assays and compared with a widely used conventional manifold for a number of binding characteristics. Whatman GF/B glass fiber filters and the less expensive filters available with the harvester were also compared and produced similar binding characteristics on the harvester and manifold if the harvester filters were used double-ply, and if the rinse time was less than 12.5 sec. Longer rinse times produced lower binding with 2-ply Skatron filters. Kd values, Hill coefficients, and Scatchard plot regression coefficients were very similar for the two filtration devices and filter types. A significantly reduced maximum number of sites (Bmax) was observed after filtration on the harvester, reflecting the smaller filter surface area relative to that of the manifold. The filter surface area on the harvester, nevertheless, is considerably larger than that of other manifolds with microplate spacing. This provides the advantages of rapid filtration with less restriction on tissue concentrations. Specific binding was linear with protein concentration up to at least 800 micrograms protein, which is well within the range of most neurotransmitter and peptide receptor binding studies. At about 1 mg protein the rinse buffer flow was slower due to the high tissue concentration. Although the results of filtration with the harvester and the conventional manifold were similar, the time requirements differed considerably. With the harvester, one experimenter could conduct the filtration process 2-3 times faster than 2 experimenters using the manifold.(ABSTRACT TRUNCATED AT 250 WORDS)

Animals↗
PubMed2002

Influence of the charge of low molecular weight proteins on their efficacy of filtration and/or adsorption on dialysis membranes with different intrinsic properties.

Hemodialysis membranes eliminate by filtration low-molecular-weight toxic metabolites (urea and creatinine) with minimum interactions between blood components and the membrane itself. However, the ability of a membrane to adsorb specific proteins could be beneficial if the accumulation of these same proteins is implicated in the genesis of a pathological condition. Beta-amyloidosis which accompanies the elevation of beta2-microglobulin (11.8 kDa) in the plasma of dialysed patients is one such condition (Biochem. Biophys. Res. Commun. 129 (3) (1985) 701-706: Lancet 1 (1986) 1240-1311). To determine whether increases in plasma beta2-microglobulin levels were due to differences in filtration efficacy of the membrane used and/or to certain characteristics of this protein, e.g. its charge (pI 5.7) the adsorption and filtration of [3H] beta2-microglobulin and [3H] lysozyme of similar MW 14.5 kDa, but pI: 10.8 were compared on different membranes. It was found that, neither [3H] beta2-microglobulin nor [3H] lysozyme are removed by cuprophan, whereas over 75% of beta2-microglobulin is removed by filtration on polyacrylonitrile, polyacrylonitrile-polyethyleneimine, polysulfone and >95% by adsorption to polymethylmethacrylate-BK. For lysozyme, removal by adsorption is >95% on polyacrylonitrile and polyacrylonitrile-polyethyleneimine, 72% on polymethylmethacrylate-BK and by filtration is 95% on polysulfone. Hemodialysis membranes must therefore not simply be considered as filters of low-molecular-weight metabolites but should be equally assessed for their capacity to eliminate potentially deleterious low-molecular-weight plasma proteins.

Adsorption↗
PubMed1993

[Filtration technology].

The leukocyte removal technology of platelet and red blood cell concentrates is now based on the only method: the filtration. In order to perfectly control this technology, it is necessary to know the different parameters that interfere in the quality of the leukocyte removal. These different parameters are studied here. They are classified in two types: the parameters that are related to the concentrate to filtrate: method used for the preparation, age, state (temperature, aggregates), concentration of red blood cells, platelets and leukocytes; the parameters that are related to the leukocyte removal technology and to the different steps of its carrying out: filter type (composition, size, geometry), prefilter, priming of the filter, flow rate during the filtration, rinsing and centrifugation after the filtration, elimination of the air inside the filter and the filtered concentrate, sterile connections, and finally good behavior in front of the difficulties and hitchs that could occur during the filtration procedure.

Cell Separation↗
PubMed1993

[Assessment of filtration performance].

The technique of filtration which has constantly been improved over past years makes it possible to obtain highly pure blood products (the rate of leukocyte depletion can reach 3 to 5 log). Several study groups (BEST, PSL) and international committees of experts have defined a number of standards with which leukocyte depleted blood products must comply. Assessment of filtration procedures is thus made necessary, it applies to the different steps of the filtration procedure: preparation techniques of red cell or platelet suspension, priming and rinsing of the filter. Likewise a number of parameters have to be checked: filtration time, temperature, age of suspensions. Moreover quality control procedures must be implemented, using adapted and validated measuring methods (Nageotte hemacytometer, for instance). The parameters to be monitored include the number of residual leukocytes, (mean value: 1 x 10(6), i.e. about 4 WBCs/microliters), and the rate of hemoglobin or platelet recovery. Any new filtering equipment or material must satisfy strict requirements and standards including clinically acceptable limits as part of the same quality approach. Validation, in this case, consists in determining the maximal leukocyte content which the filter can absorb (capacity) and the average rate of leukocyte removal (efficacy). The constant monitoring of filtration performance contributes to improving the quality of red blood cell or platelet suspensions and thus meet clinicians' requirements for their patients.

Erythrocyte Count↗
PubMed1992

Removal of micro-organisms by filtration through unwoven cloth coated with a pyridinium-type polymer.

Unwoven cloth coated with 32 mg/g of a copolymer of N-benzyl-4-vinyl-pyridinium chloride and styrene was found to be effective in removing micro-organisms from water. In experiments demonstrating removal of Escherichia coli by filtration through ten sheets of the unwoven cloth, the rate of removal was 99.99% at a filtration rate of 2.6 cm/h, and remained at 99% even at a high filtration rate of 300 cm/h and a low influent concentration of the bacterial cells such as 10(3) cells/ml. The rate of removal tended to increase with a decrease in the influent bacterial concentration. Seven other bacteria and two yeasts were effectively removed by filtration through the unwoven cloth. Filtration through the unwoven cloth was also effective in removing spores of fungi from water but was not very effective in removing bacteriophage T4 from aqueous solution.

Bacteria↗
PubMedDate not supplied

Effects of filtration seeding on cell density, spatial distribution, and proliferation in nonwoven fibrous matrices.

The cell seeding density and spatial distribution in a 3-D scaffold are critical to the morphogenetic development of an engineered tissue. A dynamic depth-filtration seeding method was developed to improve the initial cell seeding density and spatial distribution in 3-D nonwoven fibrous matrices commonly used as tissue scaffolds. In this work, trophoblast-like ED27 cells were seeded in poly(ethylene terephthalate) (PET) matrices with various porosities (0.85-0.93). The effects of the initial concentration of cells in the suspension used to seed the PET matrix and the pore size of the matrix on the resulting seeding density and subsequent cell proliferation and tissue development were studied. Compared to the conventional static seeding method, the dynamic depth-filtration seeding method gave a significantly higher initial seeding density (2-4 x 10(7) vs 4 x 10(6) cells/cm3), more uniform cell distribution, and a higher final cell density in the tissue scaffold. The more uniform initial cell spatial distribution from the filtration seeding method also led to more cells in S phase and a prolonged proliferation period. However, both uniform spatial cell distribution and the pore size of the matrices are important to cell proliferation and morphological development in the seeded tissue scaffold. Large-pore matrices led to the formation of cell aggregates and thus might reduce cell proliferation. The dynamic depth-filtration seeding method is better in providing a higher initial seeding density and more uniform cell distribution and is easier to apply to large tissue scaffolds. A depth-filtration model was also developed and can be used to simulate the seeding process and to predict the maximum initial seeding densities in matrices with different porosities.

Biocompatible Materials↗
PubMed1998

Investigation on fouling mechanisms for recombinant human growth hormone sterile filtration.

During sterile filtration of recombinant human growth hormone solutions, severe membrane fouling was experienced compared to other protein preparations of significantly higher molecular weights and concentrations. This phenomenon was attributed to rhGH aggregation/adsorption occurring in the filter pore. To better understand this phenomenon, we examined several possible fouling mechanisms: (1) pore constriction, (2) adsorption due to nonspecific binding between protein and the membrane, (3) shear-induced adsorption, (4) hydrophobic interface-induced aggregation/adsorption. The protein solutions were sterily filtered using 0.22 mm filters, and their filtration fluxes were monitored. Filtration on the capillary and the noncapillary filters suggested that constraints by pore constriction and tortuosity played only a limited role. Filtration using filters with different degrees of protein binding tendency suggested that nonspecific adsorption was insignificant. The shear stress acting on the protein during filtration was small. RhGH which was intentionally sheared in a high-speed concentrically rotating device did not aggravate fouling tendency, suggesting that the shear-induced adsorption might not be the major fouling mechanism. The dynamic light scattering data showed a trace amount of rhGH aggregates always present in equilibrium with the hydrophobic (air-water and membrane-water) interface. These aggregates tended to be adsorbed to the membrane, and more aggregates were generated presumably due to the equilibrium between aggregates and protein monomers. This adsorption/aggregation process eventually fouled the membrane. When the hydrophobic interface was occupied by surfactant molecules, the equilibration kinetics ceased to generate aggregates, thereby minimizing membrane fouling. This study clarified the cause of such an unusual fouling phenomenon upon microfiltration.

Adsorption↗
PubMed2000

Penetration of nitrogen oxides and particles from outdoor into indoor air and removal of the pollutants through filtration of incoming air.

We studied the effect of ventilation and air filtration systems on indoor air quality in a children's day-care center in Finland. Ambient air nitrogen oxides (NO, NO2) and particles (TSP, PM10) were simultaneously measured outdoors and indoors with automatic nitrogen oxide analyzers and dust monitoring. Without filtration nitrogen oxides and particulate matter generated by nearby motor traffic penetrated readily indoors. With chemical filtration 50-70% of nitrogen oxides could be removed. Mechanical ventilation and filtration also reduced indoor particle levels. During holidays and weekends when there was no opening of doors and windows and no particle-generating activity indoors, the indoor particle level was reduced to less than 10% of the outdoor level. At times when outdoor particle concentrations were high during weekdays, the indoor level was about 25% of the outdoor level. Thus, the possible adverse health effects of nitrogen oxides and particles indoors could be countered by efficient filtration. We also showed that inclusion of heat recovery equipment can make new ventilation installations economical.

Air Pollutants↗
PubMed1986

The renal action of atrial natriuretic peptide during control of glomerular filtration.

Studies were performed in anesthetized dogs (N = 7) to determine the effects of synthetic atrial natriuretic peptide (ANP) on sodium excretion in the presence and absence of control of glomerular filtration rate produced by suprarenal aortic clamping. Intrarenal infusion of synthetic atrial natriuretic peptide (0.3 micrograms/kg/min) significantly increased glomerular filtration rate from 29.3 +/- 3.0 to 43.2 +/- 4.4 ml/min, urinary sodium excretion from 20.1 +/- 10.3 to 223.3 +/- 52.3 microEq/min, fractional sodium excretion from 0.47 +/- 0.19 to 3.75 +/- 0.59%. In contrast, aortic clamping blocked the increase in glomerular filtration rate in association with an attenuated natriuresis. Urinary sodium excretion increased from 6.3 +/- 2.3 to 68.3 +/- 23.4 microEq/min and fractional sodium excretion increased from 0.15 +/- 0.04 to 0.90 +/- 0.30%. Despite this differential response in glomerular filtration rate and sodium excretion, whole kidney fractional delivery of sodium from the proximal tubule as estimated by the fractional excretion of lithium increased during both unclamped (17.7 +/- 1.8 to 30.4 +/- 0.8%) and clamped (12.9 +/- 2.1 to 23.9 +/- 2.7%) periods. These studies demonstrate that atrial natriuretic peptide-induced natriuresis is importantly mediated by an increase in glomerular filtration rate and decrease in tubular reabsorption.

Animals↗