Immobilisation of cells in a linear polyacrylamide matrix: Degradation of a mixture of volatile fatty acids byAlcaligenes denitrificans.

Summary Cells of a potent volatile fatty acid degrading strain of the organismAlcaligences denitrificans were immobilised in a linear, prepolymerised, derivatised polyacrylamide gel, cross linked with glyoxal. The beads formed were structurally strong, and immobilised cells had an increased ability compared to an equivalent quantity of free cells, to degrade a mixture of volatile fatty acids at concentrations up to 6 g/l.     

Anaerobic formation of volatile acids in a chemostat

Summary If anaerobic digestion of waste can be performed as a two-step fermentation it becomes possible to optimize the separate steps. As the CH₄ formation is assumed to be the slower step and the step more sensitive to substrate composition, an improvement of the overall process could be achieved by control of the effluent from the preceding step, in which volatile acids are formed. In this paper it is demonstrated that the composition of volatile acids from a chemostat varies to a great extent with dilution rate, so that, if an optimal composition of volatile acids exists for the CH₄-forming step, it might be obtained by proper choice of dilution rate. The best substrate for CH₄-formations is discussed.     

Improved method for simultaneous determination of alcohols, volatile fatty acids, lactic acid or 2,3-butanediol in biological samples

A rapid and sample procedure was developed to determine, by gas-liquid chromatography, the concentrations of C₂---C₄ alcohols, C₂---C₆ volatile fatty acids (VFA) and lactic acid or 2,3-butanediol in fermentation liquids. both lactic acid and 2,3-butanediol are oxidized to acetaldehyde by periodic acid and acetaldehyde was eluted before ethanol. A complete separation of the alcohols and acids was performed in <15 min on a column packed with 80/100 Chromosorb WAW, having GP 10% SP-1200/1% H₃PO₄ as the liquid phase. The method was suitable for the analysis of rumen fluid and fermentation products from microbial cultures. The detection limits for all compounds were <0.13 nmol · injection⁻¹.     

Bile acid sulfates in serum bile acids determination.

Some bile acid sulfates were synthesized and characterized. The configuration of sulfate groups at C-3, C-7 and C-12 positions was confirmed by Nuclear Magnetic Resonance analysis. These sulfates were utilized in a study of their chemical behaviour in different analytical procedures currently used for serum bile acids determination. Procedures for bile acids extraction from serum with ethanol or Amberlite XAD-2 result in an important loss of the most polar sulfated bile acids. Complete separation of unsulfated from sulfated bile acids on Sephadex LH-20 is not achieved when deconjugation of the most polar bile acid sulfate is slow but does not produce artifacts. Enzymatic determination of bile acids gives positive response with some bile acid sulfates. The current procedures of serum bile acids determination are discussed in consideration of these results.     

Retention of components in a mixture of volatile organic substances by maltodextrins

The effect of composition and origin of maltodextrins on the retention of 38 components in a mixture of volatile organic substances (odorants) during 6-month storage was studied by means of capillary gas-liquid chromatography. The retention of esters increased with an increase in their molecular weight. The retention of lactones, phenols, linalool, menthone, and damascone was 75–85%. Storage of aldehydes was accompanied by oxidation, and the retention of these substances did not exceed 55%. The retention of odorants increased with a decrease in the molecular weight of maltodextrins. The maximum retention was typical of maltodextrin from amylopectin starch not containing amylose.     

Retention of components in a mixture of volatile organic substances by maltodextrins

The effect of composition and origin of maltodextrins on the retention of 38 components in a mixture of volatile organic substances (odorants) during 6-month storage was studied by means of capillary gas-liquid chromatography. The retention of esters increased with an increase in their molecular weight. The retention of lactones, phenols, linalool, menthone, and damascone was 75-85%. Storage of aldehydes was accompanied by oxidation, and the retention of these substances did not exceed 55%. The retention of odorants increased with a decrease in the molecular weight of maltodextrins. The maximum retention was typical of maltodextrin from amylopectin starch not containing amylose.     

Thermal condensation of a mixture of six amino acids

Amino acids can be converted to peptides by the process of heating if the mixture is dry and if the appropriate proportion of glutamic acid as the dominant monomer is present. Three thermal peptide fractions of the diffusible fraction were isolated in this study. Trifluoracetic acid (TFA) hydrolysis was utilized to open the blocked N-terminal group before performing the dansylation reaction. When the molecular weight of the thermal peptide increased, the proportion of neutral amino acids increased slightly, with a decrease in the concentration of glutamic acid. Quantitative analysis of amino acid composition is also reported.     

Biofiltration of a mixture of volatile organic compounds on granular activated carbon

The performance of a biofilter packed with Active Carbon (AC) was evaluated. The effluent (alcohol, ketones, esters, aromatic and chlorinated compounds) treated was a representative mixture of most common industrial emissions. To achieve a better knowledge of multicomponent adsorption mechanisms, and to underline the interest of inoculating AC, a control abiotic humidified filter had been operated in the same conditions as the biofilter. For a load of 110 g VOC m(-3) AC h(-1), after 55 days of operation, the removal efficiency was higher in the biotic than in the abiotic filter (85% vs 55%, respectively). Moreover, in the biofilter, at steady state, the elimination of all compounds was almost complete except for chlorinated compounds and p-xylene (removal efficiency of 25% and 64%, respectively). The microbial colonization of AC involved a decrease of the adsorption sites accessibility and enhanced the treatment of VOCs (volatile organic compounds) having a lower affinity for activated carbon. Moreover, while aromatic compounds and MIBK were eliminated along the overall height of the biofilter, pollutants with reduced affinity for AC, such as methanol, acetone, and halogenated compounds were only treated on the second half of the reactor. Thus, the affinity for activated carbon was an important parameter controlling the biodegradation process. Nevertheless, the use of AC as packing material in biofilters treating complex mixtures of VOCs is limited. Actually, similar removal efficiency could be reached, in the same conditions, for a biofilter packed with granular peat. Furthermore, for the biofilter packed with AC, the column height necessary to remove biodegradable compounds, with reduced affinity for the support, was important.     

Weak acid permeability of a villous membrane: Formic acid transport across rat proximal tubule

Chloride/formate exchange, in parallel with Na⁺/H⁺ exchange and nonionic diffusion of H₂CO₂, has been proposed as a mechanism of electroneutral transcellular Cl⁻ reabsorption by the proximal tubule. However, the measured brush border H₂CO₂ permeability of the rat proximal tubule is at least an order of magnitude too low to support sufficient H₂CO₂ recycling. To investigate the possibility that an unstirred layer within the brush border might depress the measured H₂CO₂ permeability, we constructed a mathematical model of a villous membrane. Axial fluxes along villous and intervillous spaces were specified by Nernst-Planck diffusion equations. Model parameters were set to achieve agreement with ion and water fluxes measured in the rat proximal tubule. The equations were solved numerically to generate steady-state concentration profiles in the villous and intervillous spaces. An apparent brush border H₂CO₂ permeability was determined by perturbing luminal [H₂CO₂] and calculating the change in H₂CO₂ flux. Overall, the ratio of apparent brush border H₂CO₂ permeability to cell membrane H₂CO₂ permeability was greater than 90%. Contributing to the small decrease in apparent permeability are finite diffusion coefficients, folding of the membrane, and acidification of the luminal solution. An approximate analysis of this system shows the critical parameters of brush border formate transport to be the actual membrane H₂CO₂ permeability, and the diffusion coefficients of HCO ₃ ⁻ and HCO ₃ ⁻ . Nevertheless, decreasing the diffusion coefficients by one order of magnitude failed to depress apparent brush border H₂CO₂ permeability by more than an additional 25%. We conclude that although permeability is systematically underestimated across a villous membrane, unstirred layer effects in the brush border are still too small to resolve the discrepancy between the measured value of H₂CO₂ permeability and the value needed to allow recycling.     

Biotreatment of a gas-phase volatile mixture from fibreglass and composite manufacturing industries

Acetone, toluene and styrene (ATS) are representative air pollutants emanating during the production process in fibreglass and composite manufacturing industries. In this study, the performance of a steady-state biofilter inoculated with the fungus Sporothrix variecibatus was tested at different empty bed residence times (EBRTs), and at different inlet concentrations of ATS, corresponding to total pollutant loading rates ranging from 30 to 490 gm(-3)hour(-1). Styrene was somewhat better removed (47-100%) in the biofilter than acetone (34-100%) and toluene (42-100%), with maximum elimination capacities (EC(max)) of 108, 72 and 144 gm(-3)hour(-1), for ATS, respectively. Besides, it was observed that, although increasing the concentration of ATS decreased their removal, the presence of toluene also decreased the EC(max) of both acetone and toluene in the ternary mixture. During transient operations, the biofilter was subjected to intermittent shutdown and re-start operations where the gas-phase pollutant flow was stopped for either 5 or 16d. It was observed that, for longer shutdown periods (16d), the biofilter required nearly 8-10d to reach similar removal patterns to those observed before the shutdown phase. Batch biodegradation tests were conducted, using Sporothrix-like microorganisms present in the leachate of the biofilter, with a mixture of ATS as the sole carbon source. Complete removal of ATS was observed within the test period of 168 hours. Styrene was degraded faster, with a specific substrate utilization rate of 0.9 mg styrenemg biomass(-1)hour(-1), followed by toluene (0.6) and acetone (0.44). The effectiveness of the biofilter to reach high total EC (321.3 gm(-3)hour(-1)), and withstand transient operations shows the robustness of this fungal-bioreactor and its suitability to handle emissions from a fibreglass and composite manufacturing industry.     

Treatment of odorous volatile fatty acids using a biotrickling filter

In this study, a novel fibrous bioreactor was developed for treating odorous compounds present in contaminated air. The first stage of this work was a preliminary study which aimed at investigating the feasibility of using the fibrous bioreactor for the removal of malodorous volatile fatty acids (VFA) that is a common odorous contaminant generated from anaerobic degradation of organic compounds. The kinetics of microbial growth and VFA degradation in the selected culture, and the performance of the submerged bioreactor at different VFA mass loadings were studied. Above 95% of VFA removal efficiencies were achieved at mass loadings up to 22.4 g/m(3)/h. In the second stage, the odour treatment process was scaled up with system design and operational considerations. A trickling biofilter with synthetic fibrous packing medium was employed. The effects of inlet VFA concentration and empty bed retention time (EBRT) on the process performance were investigated. The bioreactor was effective in removing VFA at mass loadings up to 32 g/m(3)/h, beyond which VFA started to accumulate in the recirculation liquid, indicating the biofilm was unable to degrade all of the VFA introduced. Although VFA accumulated in the liquid phase, the removal efficiency remained above 99%. This suggested that the biochemical reaction rather than gas-liquid mass transfer was the limiting step of the treatment process. In addition, the biotrickling filter was stable for long-term operation with relatively low and steady pressure drop, no clogging and degeneration of the packing material occurred during the four-month study.