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Applied Microbiology and Biotechnology (v.48, #3)


Bacterial alginates: biosynthesis and applications by B. H. A. Rehm; S. Valla (pp. 281-288).
Alginate is a copolymer of β-d-mannuronic acid and α-l-guluronic acid (GulA), linked together by 1–4 linkages. The polymer is a well-established industrial product obtained commercially by harvesting brown seaweeds. Some bacteria, mostly derived from the genus Pseudomonas and belonging to the RNA superfamily I, are also capable of producing copious amounts of this polymer as an exopolysaccharide. The molecular genetics, regulation and biochemistry of alginate biosynthesis have been particularly well characterized in the opportunistic human pathogen Pseudomonas aeruginosa, although the biochemistry of the polymerization process is still poorly understood. In the last 3 years major aspects of the molecular genetics of alginate biosynthesis in Azotobacter vinelandii have also been reported. In both organisms the immediate precursor of polymerization is GDP-mannuronic acid, and the sugar residues in this compound are polymerized into mannuronan. This uniform polymer is then further modified by acetylation at positions O-2 and/or O-3 and by epimerization of some of the residues, leading to a variable content of acetyl groups and GulA residues. In contrast, seaweed alginates are not acetylated. The nature of the epimerization steps are more complex in A. vinelandii than in P. aeruginosa, while other aspects of the biochemistry and genetics of alginate biosynthesis appear to be similar. The GulA residue content and distribution strongly affect the physicochemical properties of alginates, and the epimerization process is therefore of great interest from an applied point of view. This article presents a survey of our current knowledge of the molecular genetics and biochemistry of bacterial alginate biosynthesis, as well as of the biotechnological potential of such polymers.

Biological phosphate removal processes by M. C. M. van Loosdrecht; C. M. Hooijmans; D. Brdjanovic; J. J. Heijnen (pp. 289-296).
Biological phosphate removal has become a reliable and well-understood process for wastewater treatment. This review describes the historical development of the process and the most important microbiological and process-engineering aspects. From a microbiological point of view, the role of␣poly(hydroxyalkanoates) as storage material in a dynamic process and the use of polyphosphate as an energy reserve are the most important findings. From a process-engineering point of view, the study of biological phosphate removal has shown that highly complex biological processes can be designed and controlled, provided that the importance of the prevailing microbiological ecological processes is recognised.

High rates of microbial sulphate reduction in a mesophilic ethanol-fed expanded-granular-sludge-blanket reactor by A. De Smul; J. Dries; L. Goethals; H. Grootaerd; W. Verstraete (pp. 297-303).
In a mesophilic (30–35 °C), sulphidogenic, ethanol-fed expanded-granular-sludge-blanket reactor, sulphate, at loading rates of up to 10.0–12.0 g Sl−1␣day−1, was removed with an average efficiency of more than 80%. The pH was between 7.7 and 8.3 and the maximal total dissolved sulphide concentration was up to 20 mM S (650 mg S/l). The alkaline pH was maintained by either a pH-control unit with sodium hydroxide or by stripping part of the sulphide and CO2 from the recycle with nitrogen gas. The superficial upstream liquid velocity (v up) was 3.0–4.5 m/h. The ratio of ethanol to sulphur was near stoichiometry. At alkaline pH, the activity of the acetotrophic sulphate-reducing bacteria, growing on acetate, was strongly enhanced, whereas at pH below 7.7 the acetotrophic sulphate-reducing bacteria were inhibited by aqueous H2S. With regard to the removal efficiency and operational stability, external stripping with N2 and pH control were equally successful.

Effects of directly soluble and fibrous rapidly acidifying chemical oxygen demand and reactor liquid surface tension on granulation and sludge-bed stability in upflow anaerobic sludge-blanket reactors by H. Grootaerd; B. Liessens; W. Verstraete (pp. 304-310).
 In recent years, it has become clear that the rapidly acidifying chemical oxygen demand (RACOD) content of the waste water and the surface tension of the reactor liquid contribute to the phenomenon of granular growth in upflow anaerobic sludge-blanket reactors (UASB). By adding 20% of directly soluble RACOD, in the form of a sucrose/starch mixture, on top of the original COD load and by adjusting the reactor liquid surface tension below 50 mN m−1 with linear alkylbenzenesulphonate, granular growth and sludge-bed stability could be enhanced significantly within 40 days. Carrot pulp, a waste product having a high short-chain fatty acid precursor potential, was applied as an alternative fibrous RACOD source. Best results were obtained when adding the carrot pulp freshly to the laboratory-scale UASB reactor in an in-recycle liquefying chamber. This concept of adding carrot pulp waste product as a granular growth supplement by means of an in-recycle liquefying chamber therefore merits testing in practice.

Effects of ethanol concentration and stripping temperature on continuous fermentation rate by F. Taylor; M. J. Kurantz; N. Goldberg; J. C. Craig Jr. (pp. 311-316).
The operation of a pilot plant consisting of a 14-l fermentor, 10-cm packed column and condenser for continuous fermentation and stripping of ethanol was stable for more than 100 days. The feed consisted of a non-sterile solution of 560 g/l glucose with 100 g/l corn steep water. Fouling of the packing in the column with attached growth of yeast cells was controlled by in situ washing at intervals of 3–6 days. A computer simulation of the pilot plant was developed and used to analyze the data. The productivity of the continuous fermentor varied from 14 g ethanol to 17 g ethanol l−1 h−1. The yield was equal to the maximum theoretically possible: 0.51 g ethanol/g glucose consumed. Results are fit to linear models for the effects of ethanol concentration on specific growth rate and cell yield, and for the effect of stripping temperature on specific growth rate.

Production, purification and characterization of a 50-kDa extracellular metalloprotease from Serratia marcescens by P. R. Salamone; R. J. Wodzinski (pp. 317-324).
The extracellular metalloprotease (SMP 6.1) produced by a soil isolate of Serratia marcescens NRRL B-23112 was purified and characterized. SMP 6.1 was purified from the culture supernatant by ammonium sulfate precipitation, acetone fractional precipitation, and preparative isoelectric focusing. SMP 6.1 has a molecular mass of approximately 50 900 Da by sodium dodecyl sulfate/polyacrylamide gel electrophoresis (SDS-PAGE). The following substrates were hydrolyzed: casein, bovine serum albumin, and hide powder. SMP 6.1 has the characteristics of a metalloprotease, a pH optimum of 10.0, and a temperature optimum of 42° C. The isoelectric point of the protease is 6.1. Restoration of proteolytic activity by in-gel renaturation after SDS-PAGE indicates a single polypeptide chain. SMP 6.1 is inhibited by EDTA (9 μg/ml) and not inhibited by antipain dihydrochloride (120 μg/ml), aprotinin (4 μg/ml), bestatin (80 μg/ml), chymostatin (50 μg/ml), E-64 (20 μg/ml), leupeptin (4 μg/ml), Pefabloc SC (2000 μg/ml), pepstatin (4 μg/ml), phosphoramidon (660 μg/ml), or phenylmethylsulfonyl fluoride (400 μg/ml). SMP 6.1 retains full activity in the presence of SDS (1% w/v), Tween-20 (1% w/v), Triton X-100 (1% w/v), ethanol (5% v/v), and 2-mercaptoethanol (0.5% v/v). The extracellular metalloprotease SMP 6.1 differs from the serratiopeptidase (Sigma) produced by S. marcescens ATCC 27117 in the following characteristics: isoelectric point, peptide mapping and nematolytic properties.

Parameters affecting polymerase chain reaction detection of waterborne Cryptosporidium parvum oocysts by S. D. Sluter; S. Tzipori; G. Widmer (pp. 325-330).
Cryptosporidium parvum is an enteric protozoan parasite of medical and veterinary importance. Dissemination of environmentally resistant oocysts in surface water plays an important role in the epidemiology of cryptospridiosis. Although the polymerase chain reaction (PCR) is a well-established technique and is widely used for detecting microorganisms, it is not routinely applied for monitoring waterborne C. parvum. In order to facilitate the application of PCR to the detection of waterborne C. parvum oocysts, a comparison of published PCR protocols was undertaken and different sample-preparation methods tested. The sensitivity of a one-step PCR method, consisting of 40 temperature cycles, was 10 purified oocysts or fewer than 100 oocysts spiked in raw lake water. The detection limit of two primer pairs, one targeting the ribosomal small subunit and another specific for a C. parvum sequence of unknown function, was approximately ten-fold lower than achieved with a primer pair targeting an oocyst shell protein gene. Three cycles of freezing/thawing were sufficient to expose oocyst DNA and resulted in higher sensitivity than proteinase K digestion, sonication or electroporation. Inhibition of PCR by surface water from different local sources was entirely associated with the soluble fraction of lake water. Membrane filtration was evaluated in bench-scale experiments as a means of removing lake water inhibitors and improving the detection limit of PCR. Using gel and membrane filtration, the molecular size of inhibitory solutes from lake water was estimated to less than 27 kDa.

Heterologous gene expression of bovine plasmin in Lactococcus lactis by J. Arnau; E. Hjerl-Hansen; H. Israelsen (pp. 331-338).
Heterologous production of bovine plasmin was studied in the industrially relevant bacterium Lactococcus lactis. Two sets of lactococcal gene expression signals were coupled to the region of the plasmin gene coding for the serine protease domain. When the promoter region of the prtP gene was used, plasmin was detected mainly intracellularly in strain BPL25 by Western blot hybridization. The intracellular presence of plasmin led to physiological stress. Expression of the plasmin gene driven by the promoter and complete signal sequence of the lactococcal usp45 gene resulted in efficient plasmin secretion in strain BPL420. Cell lysis was observed in strains producing plasmin fragments including the catalytic domain, but not in control strains, which only produced a non-catalytic region of plasmin. The plasmin produced was shown to be biologically active.

Improved efficiency and stability of multiple cloned gene insertions at the δ sequences of Saccharomyces cerevisiae by F. W. F. Lee; N. A. Da Silva (pp. 339-345).
Two δ-integration vectors were evaluated for the insertion of an inducible expression cassette (the yeast CUP1 promoter fused to the Escherichia coli lacZ structural gene, CUP1p-lacZ) and a bacterial neomycin-resistance gene (neo) into the genome of Saccharomyces cerevisiae via homologous recombination. Cells containing integrations were selected by resistance to the aminoglycoside G418. The first vector was a traditional construct containing only one δ sequence; with this vector, the transformation efficiency and the number of integrations per cell were quite low. The second carried two δ sequences flanking the desired insert, and the unneeded bacterial sequences were removed by restriction-enzyme digestion immediately before transformation. When this double δ vector was employed, the integrated copy number was more than doubled relative to the single δ system and final β-galactosidase levels exceeded those obtained with the 2μ-based plasmid. Furthermore, the integrations appeared more stable in long-term sequential culture (both with and without induction of the lacZ gene) than those obtained via the single δ vector.

Elucidation of the mechanism of lactic acid growth inhibition and production in batch cultures of Lactobacillus rhamnosus by L. M. D. Gonçalves; A. Ramos; J. S. Almeida; A. M. R. B. Xavier; M. J. T. Carrondo (pp. 346-350).
Batch cultures of Lactobacillus rhamnosus were carried out at different pH values in order to study the limitation of growth and lactic acid production by the hydrogen ion, non-dissociated lactic acid and internal lactate concentrations. The effect of pH between 5 and 6.8 was studied at non-limiting concentrations of glucose; this is more significant for the lactic acid fermentation rate than for the maximum specific growth rate, as shown by the incomplete substrate consumption at lower values of medium pH and by the constant maximum cell mass obtained within the range of pH values studied. To check whether these results were a direct consequence of the different concentrations of the non-dissociated form of lactic acid at different external pH values, specific growth rates and lactic acid productions rates were calculated for each external pH value. The same specific growth rates were observed at the same non-dissociated lactic acid concentrations only at pH values of 5 and 5.5. For higher values of pH (pH > 6) the specific growth rate falls to zero as the non-dissociated lactic acid concentration decreases. This shows that generalisations made from studies performed within very narrow ranges of pH are not valid and that the non-dissociated form of lactic acid is not the only inhibiting species. The internal pH was measured experimentally for each external pH value in order to calculate the internal lactate ion concentration. This form is described to be the inhibitory one. The results obtained confirmed that the specific growth rate reached zero at approximately the same lactate concentration for all the pH values studied.

Antioxidant role of astaxanthin in the green alga Haematococcus pluvialis by M. Kobayashi; T. Kakizono; N. Nishio; S. Nagai; Y. Kurimura; Y. Tsuji (pp. 351-356).
The green unicellular alga, Haematococcus pluvialis has two antioxidative mechanisms against environmental oxidative stress: antioxidative enzymes in vegetative cells and the antioxidative ketocarotenoid, astaxanthin, in cyst cells. We added a reagent that generates superoxide anion radicals (O2 ), methyl viologen, to mature and immature cysts of H. pluvialis. Tolerance to methyl viologen was higher in mature than in immature cysts. Mature (astaxanthin-rich) cysts showed high antioxidant activity against O2 in permeabilized cells, but not in astaxanthin-free cell extracts, while immature (astaxanthin-poor) cysts had very low antioxidant activities against O2 in both. The results suggested that astaxanthin accumulated in the cyst cells functions as an antioxidant against excessive oxidative stress. The same levels of antioxidant activities against O2 in both permeabilized cells and cell extracts from vegetative cells suggested the presence of antioxidative enzymes (superoxide dismutase).

Non-toluene-associated respiration in a Pseudomonas putida 54G biofilm grown on toluene in a flat-plate vapor-phase bioreactor by S. Villaverde; M. T. Fernández (pp. 357-362).
Non-toluene-associated respiration (NTAR) within a Pseudomonas putida 54G biofilm growing on toluene as sole external carbon source was evaluated using oxygen microelectrodes in a flat-plate vapor-phase biological reactor. Two fluorescent probes, 2,4-diamidino-2-phenylindole and 5-cyano-2,3-ditolyltetrazolium chloride, were used to evaluate the number of total and respiring cells respectively within the biofilm. Biofilm samples were also analyzed for viable and toluene-culturable cells by spread-plating on non-selective and selective media respectively. Fractions of viable stressed, respiring and non-respiring cells within the biofilm were evaluated. The NTAR rate was positively correlated with the fraction of viable stressed and non-respiring cells within the biofilm, which suggested the capability of some cells to grow at the expense of leakage and lysis products coming from injured and dead cells. This effect was more pronounced at higher toluene concentration. Results suggest that NTAR should be incorporated into mathematical models of biofilm reactors degrading volatile organic carbon compounds.

Synthesis of dihydroxynaphthalene isomers by microbial oxidation of 1- and 2-naphthol by D. Bianchi; A. Bernardi; A. Bosetti; R. Bortolo; D. Cidaria; E. Crespi; I. Gagliardi (pp. 363-366).
The mutant strain Pseudomonas fluorescens TTC1 (NCIMB 40605), derived from the naphthalene-degrading Pseudomonas fluorescens N3 (NCIMB 40530), was used for the oxidation of 1- and 2-naphthols to give different isomers of dihydroxynaphthalene. The oxidation reactions proceed through the formation of dihydrodiol intermediates, which are too unstable to be isolated, since they spontaneously eliminate water to give the fully aromatic dihydroxynaphthalenes. The high regioselectivity of the dehydration reaction was confirmed by the study of the acid-catalysed aromatization of a series of stable monosubstituted naphthalene cis-1,2-dihydrodiols.

Extracellular reduction of selenite by a novel marine photosynthetic bacterium by A. Yamada; M. Miyashita; K. Inoue; T. Matsunaga (pp. 367-372).
A novel purple nonsulfur bacterium strain NKPB030619, which has resistance to over 5 mM selenite, was isolated from a marine environment. An initial concentration of 1.1 mM selenite, added to the medium, was decreased to under 0.05 mM within 5 days. The color of the cell suspension turned red within 2 days. The red coloration gradually decreased and black precipitates appeared during 2 weeks of cultivation. Under these conditions, two main types of deposit were formed extracellularly. These deposits were thought to contain red amorphous selenium and black vitreous selenium. The selenite reduction to elemental selenium in this bacterium was induced by the introduction of light and l-malic acid under anaerobic conditions. These results suggest that selenite reduction is coupled with photosynthesis and l-malic acid can serve as the indirect electron donor for its reduction. Phylogenetic analysis based on the 16S rDNA sequence showed that NKPB0360619 belongs to the α subdivision of Proteobacteria and is classified into the Rhodobacter species. The highest similarity of 86.2% was observed with R. sphaeroides.

Isolation and characterization of nickel-accumulating yeasts by H. Kambe-Honjoh; A. Sugawara; K. Yoda; K. Kitamoto; M. Yamasaki (pp. 373-378).
We selected three yeast strains that efficiently remove heavy metal ions from aqueous solution. We first screened yeasts that grew in the presence of 2 mM NiCl2 among our stock of wild yeasts, and then selected those that removed Ni most efficiently from aqueous solution. These strains also removed Cu and Zn from aqueous solution and were identified as Candida species. Ni uptake was efficient at pH between 4.0 and 7.0, but less efficient at pH below 3.0. The amount of Ni taken up by the yeast cells was proportional to the initial concentration of NiCl2 below about 4 mM Ni. The cells retained the abilities to remove Ni after treatment with 10 mM EDTA or 1 M HCl for repeated usage, or after heat treatment.

Solubilisation and mineralisation of [14C]lignocellulose from wheat straw by Streptomyces cyaneus CECT 3335 during growth in solid-state fermentation by M. M. Berrocal; J. Rodríguez; A. S. Ball; M. I. Pérez-Leblic; M. E. Arias (pp. 379-384).
Nine Streptomyces strains were screened for their ability to solubilise and mineralise 14C-labelled lignin during growth in solid-state fermentation. Streptomyces viridosporus was confirmed as an active lignin-degrading organism along with a new isolate, Streptomyces sp. UAH 15, further classified as Streptomyces cyaneus CECT 3335. This organism was able to solubilise and mineralise the [14C]lignin fraction of lignocellulose (44.96 ± 1.77% and 3.41 ± 0.48% respectively) after 21 days of incubation. Cell-free filtrates from Streptomyces sp. grown in solid-state fermentation were capable of solubilising up to 20% of the [14C]lignin after 2 days incubation, with most of the product detected in the acid-soluble rather than in the water-soluble fraction. Identification of the extracellular enzymes produced during growth of S. cyaneus CECT 3335 revealed that extracellular peroxidase and phenol oxidase activities were present, with the activity of phenol oxidase being 100 times greater than peroxidase activity. The activity of these two enzymes was found to correlate with both solubilisation and mineralisation rates. This is the first report of phenol oxidase activity produced by a Streptomyces strain during growth in solid-state fermentation. A role for the enzyme in the solubilisation and mineralisation of lignocellulose by S. cyaneus is suggested.

Mixotrophic growth of two thermophilic Methanosarcina strains, Methanosarcina thermophila TM-1 and Methanosarcina sp. SO-2P, on methanol and hydrogen/carbon dioxide by Z. Mladenovska; B. K. Ahring (pp. 385-388).
Two thermophilic strains, Methanosarcina thermophila TM-1 and Methanosarcina sp. SO-2P, were capable of mixotrophic growth on methanol and H2/CO2. Activated carbon was, however, found to be necessary to support good growth. Both strains used hydrogen and methanol simultaneously. When methanol was depleted, hydrogen utilization continued and methane was further produced with concurrent cell growth. UV epifluorescence microscopy revealed that aggregates of both strains exhibited a bright red fluorescence besides the usual blue-green fluorescence.

Induction of submerged conidiation of the biocontrol agent Penicillium oxalicum by S. Pascual; P. Melgarejo; N. Magan (pp. 389-392).
Induction of submerged conidiation of Penicillium oxalicum has been examined using a range of synthetic and complex media and complex media supplemented with by-products of the brewing industry. Only one method (Morton's method), consisting of growth in a glucose/salts-based medium (C:N ratio 62.5, medium A) for 24 h and then transference to the same medium without a nitrogen source (medium B), induced conidiation. Levels of sporulation were significantly (P = 0.05) increased by addition of calcium or poly(ethylene glycol) 6000 to medium B. The optimum age for transference of the mycelium was 24 h and the optimum pH was 6. Calcium was an induction factor when added to medium A (C:N ratio 62.5) of Morton's method. It was concluded that nitrogen depletion and calcium addition to a medium with high C:N ratio are the factors inducing conidiation of P. oxalicum. Maximum levels of conidiation (35 × 106 spores ml−1) were obtained when the nitrogen level in medium A of Morton's method was further reduced (C:N ratio 142.9) and calcium (20 mM) was added. These results are the essential starting point to investigate liquid fermentation systems for the biocontrol agent P. oxalicum.

Aptitude of cheese bacteria for volatile S-methyl thioester synthesis. II. Comparison of coryneform bacteria, Micrococcaceae and some lactic acid bacteria starters by G. Lamberet; B. Auberger; J. L. Bergère (pp. 393-397).
Various strains of coryneform bacteria, Micrococcaceae and commercial starters of Lactococcus lactis and Leuconostoc were compared for their aptitude to form S-methyl thioesters. Resting cells were incubated with methanethiol alone at pH 7 and in conjunction with a mixture of straight, branched and hydroxy short-chain fatty acids up to C6 at pH 7 and 5. Results showed that all the strains synthesized at least S-methyl thioacetate, with strains that were low and high producers in each group. This is the only thioester formed in small amount by Leuconostoc. Brevibacterium linens (six strains) and Micrococcaceae (five strains) were able to form branched-chain thioesters especially from their intracellular fatty acids at neutral pH, and straight-chain thioesters mostly from exogenous fatty acids at acid pH. Coryneform bacteria other than B. linens (four strains) and L. lactis (four starters) synthesized thioesters up to S-methyl thiobutyrate from endogenous or exogenous fatty acids but not branched-chain ones, except for one starter which formed a very little thioisovalerate. Some particular effects of pH and added fatty acids revealed differences between species or strains in their specific enzymatic systems.

Degradation of eight highly condensed polycyclic aromatic hydrocarbons by Pleurotus sp. Florida in solid wheat straw substrate by M. Wolter; F. Zadrazil; R. Martens; M. Bahadir (pp. 398-404).
The degradation of eight unlabeled highly condensed polycyclic aromatic hydrocarbons (PAH) and the mineralization of three 14C-labeled PAH by the white-rot fungus Pleurotus sp. Florida was investigated. Three concentrations containing 50, 250 or 1250 μg each unlabeled PAH/5 g straw were added to sterile sea sand. Selected treatments were added subsequently with 14C-labeled pyrene, benzo[a]anthracene or benzo[a]pyrene. The PAH-loaded sea sand was then mixed into straw substrate and incubated. The disappearance of the unlabeled four-to six-ring PAH: pyrene, benzo[a]anthracene, chrysene, benzo[b]fluoranthene, benzo[k]fluoranthene, benzo[a]pyrene, dibenz[a,h]anthracene and benzo[ghi]perylene, was determined by high-performance liquid chromatography. After 15 weeks of incubation, the recoveries were less than 25% for initial amounts of 50 μg (controls above 85%). The recoveries of unlabeled PAH increased in the inoculated samples with increasing concentrations applied. No correlation could be determined between the number of condensed rings of the PAH and the recoveries of added PAH. Pleurotus sp. Florida mineralized 53% [14C]pyrene, 25% [14C]benzo[a]anthracene and 39% [14C]benzo[a]pyrene to 14CO2 in the presence of eight unlabeled PAH (50 μg applied) within 15 weeks. During the course of cultivation, Pleurotus sp. Florida degraded more than 40% of the wheat straw substrate. Variation of the initial concentration of PAH did not influence the extent of degradation of the organic matter.

Mesophilic and thermophilic anaerobic digestion of source-sorted organic wastes: effect of ammonia on glucose degradation and methane production by C. Gallert; J. Winter (pp. 405-410).
The wet organic fraction of household wastes was digested anaerobically at 37 °C and 55 °C. At both temperatures the volatile solids loading was increased from 1 g l−1 day−1 to 9.65 g l−1 day−1, by reducing the nominal hydraulic retention time from 93 days to 19 days. The volatile solids removal in the reactors at both temperatures for the same loading rates was in a similar range and was still 65% at 19 days hydraulic retention time. Although more biogas was produced in the thermophilic reactor, the energy conservation in methane was slightly lower, because of a lower methane content, compared to the biogas of the mesophilic reactor. The slightly lower amount of energy conserved in the methane of the thermophilic digester was presumably balanced by the hydrogen that escaped into the gas phase and thus was no longer available for methanogenesis. In the thermophilic process, 1.4 g/l ammonia was released, whereas in the mesophilic process only 1 g/l ammonia was generated, presumably from protein degradation. Inhibition studies of methane production and glucose fermentation revealed a K i (50%) of 3 g/l and 3.7 g/l ammonia (equivalent to 0.22 g/l and 0.28 g/l free NH3) at 37 °C and a K i (50%) of 3.5 g/l and 3.4 g/l ammonia (equivalent to 0.69 g/l and 0.68 g/l free NH3) at 55 °C. This indicated that the thermophilic flora tolerated at least twice as much of free NH3 than the mesophilic flora and, furthermore, that the thermophilic flora was able to degrade more protein. The apparent ammonia concentrations in the mesophilic and in the thermophilic biowaste reactor were low enough not to inhibit glucose fermentation and methane production of either process significantly, but may have been high enough to inhibit protein degradation. The data indicated either that the mesophilic and thermophilic protein degraders revealed a different sensitivity towards free ammonia or that the mesophilic population contained less versatile protein degraders, leaving more protein undegraded.

Respiratory activity of biofilms: measurement and its significance for the elimination of n-butanol from waste gas by U. Heinze; C. G. Friedrich (pp. 411-416).
A reaction chamber was developed to determine the respiratory activity of microorganisms immobilized on various support materials for waste gas treatment. The volumetric respiration rate was identified as a suitable parameter for estimating the degradative activity of waste gas treatment plants. A laboratory trickle-bed reactor was filled with either granular clay, polyamide beads, or sintered styrofoam. n-Butanol was used as model solvent to determine the efficiency of its elimination from the gas phase. This crucial parameter was correlated with the volumetric degradation rate, determined from the overall material balance under steady-state operating conditions. The volumetric respiration rate of n-butanol was determined with the reaction chamber, and exceeded the volumetric degradation rate of n-butanol determined from the reactor 16- to 26-fold, depending on the support material. The respiration rate was correlated to the degradation rate by the stoichiometry of n-butanol oxidation and a correlation factor of 2.6–4.3. The volumetric respiration rate appeared to be a suitable parameter to determine the degradative activity of the trickle-bed reactor used. The volumetric respiration rate can be ultimately applied to estimate the efficiency of elimination of an organic pollutant and to calculate the dimensions of a reactor required to eliminate a given organic load from waste gas.

Transformation of 1,1,1-trichloroethane in an anaerobic packed-bed reactor at various concentrations of 1,1,1-trichloroethane, acetate and sulfate by J. H. de Best; H. Jongema; A. Weijling; H. J. Doddema; D. B. Janssen; W. Harder (pp. 417-423).
Biotransformation of 1,1,1-trichloroethane (CH3CCl3) was observed in an anaerobic packed-bed reactor under conditions of both sulfate reduction and methanogenesis. Acetate (1 mM) served as an electron donor. CH3CCl3 was completely converted up to the highest investigated concentration of 10 μM. 1,1-Dichloroethane and chloroethane were found to be the main transformation products. A fraction of the CH3CCl3 was completely dechlorinated via an unknown pathway. The rate of transformation and the transformation products formed depended on the concentrations of CH3CCl3, acetate and sulfate. With an increase in sulfate and CH3CCl3 concentrations and a decrease in acetate concentration, the degree of CH3CCl3 dechlorination decreased. Both packed-bed reactor studies and batch experiments with bromoethanesulfonic acid, an inhibitor of methanogenesis, demonstrated the involvement of methanogens in CH3CCl3 transformation. Batch experiments with molybdate showed that sulfate-reducing bacteria in the packed-bed reactor were also able to transform CH3CCl3. However, packed-bed reactor experiments indicated that sulfate reducers only had a minor contribution to the overall transformation in the packed-bed reactor.

Removal of tetrachloroethylene in an anaerobic column bioreactor by C. Noftsker; M. E. Watwood (pp. 424-430).
Removal of tetrachloroethylene (perchloroethylene; C2Cl4) by microbial consortia from two sites with different C2Cl4 exposure histories was examined in a bench-scale anaerobic column bioreactor. It was hypothesized that optimal removal would be observed in the reactor packed with sediments having an extensive exposure history. Microbial consortia were enriched from hyporheic-zone (HZ) sediments from the Portneuf aquifer near Pocatello, Idaho, and from industrial-zone (IZ) sediments from a highly contaminated aquifer in Portland, Oregon. Lactate and acetate were the electron donors during experiments conducted over 9 and 7 months for HZ and IZ sediments, respectively. In the HZ bioreactor, the retention time ranged from 31 h to 81 h, and inlet C2Cl4 concentrations ranged from 0.1 ppm to 1.0 ppm. Dechlorination of C2Cl4 averaged 60% and reached a maximum of 78%. An increase in C:N from 27:1 to 500:1 corresponded to an 18% increase in removal efficiency. Trichloroethylene production corresponded to decreased effluent C2Cl4; further intermediates were not detected. In the IZ bioreactor, the retention time varied from 34 h to 115 h; the inlet C2Cl4 concentration was 1.0 ppm. C2Cl4 removal averaged 70% with a maximum of 98%. Trichloroethylene and cis-dichloroethylene were detected in the effluent. Increases in C:N from 50:1 to 250:1 enhanced dechlorination activity.
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