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Träfflista för sökning "L773:1432 0614 OR L773:0175 7598 srt2:(2000-2004)"

Sökning: L773:1432 0614 OR L773:0175 7598 > (2000-2004)

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1.
  • Bengtsson, Göran, et al. (författare)
  • Contribution of suspended and sorbed groundwater bacteria to degradation of dissolved and sorbed aniline
  • 2001
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 1432-0614 .- 0175-7598. ; 57:1-2, s. 234-241
  • Tidskriftsartikel (refereegranskat)abstract
    • The influence of sorption on the mineralisation of 50 mug aniline l(-1) was examined in an aquifer material under batch conditions. The study was designed to distinguish the rates and extent of biodegradation of the sorbed and the dissolved trace organic and the contribution of sorbed and suspended bacteria to the degradation. Four different mathematical models were developed with different assumptions about the partitioning of aniline degradation and bacterial activity between the solid and the aqueous phases. The models were developed by combining an expression for logistic growth of the degrading population with Michaelis-Menten kinetics for the transformation of aniline. It was tested by a series of laboratory experiments conducted with C-14-labelled aniline, aseptically treated aquifer sand and filter-sterilised groundwater in different proportions and bacteria isolated from pristine groundwater. Model evaluation of the experimental data suggested that the fate of aniline was mainly controlled by suspended bacteria degrading both the dissolved and sorbed fractions. The degradation was slow. with a first-order degradation rate equal to 10(-6) h(-1).
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2.
  • Björnsson, Lovisa, et al. (författare)
  • Evaluation of parameters for monitoring an anaerobic co-digestion process
  • 2000
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 1432-0614 .- 0175-7598. ; 54:6, s. 844-849
  • Tidskriftsartikel (refereegranskat)abstract
    • The system investigated in this study is an anaerobic digester at a municipal wastewater treatment plant operating on sludge from the wastewater treatment, co-digested with carbohydrate-rich food-processing waste. The digester is run below maximum capacity to prevent overload. Process monitoring at present is not extensive, even for the measurement of on-line gas production rate and off-line pH. Much could be gained if a better program for monitoring and control was developed, so that the full capacity of the system could be utilised without the risk of overload. The only limit presently set for correct process operation is that the pH should be above 6.8. In the present investigation, the pH was compared with alkalinity, gas production rate, gas composition and the concentration of volatile fatty acids (VFA). Changes in organic load were monitored in the full-scale anaerobic digester and in laboratory-scale models of the plant. Gas-phase parameters showed a slow response to changes in load. The VFA concentrations were superior for indicating overload of the microbial system, but alkalinity and pH also proved to be good monitoring parameters. The possibility of using pH as a process indicator is, however, strongly dependent on the buffering capacity. In this study, a minor change in the amount of carbohydrates in the substrate had drastic effects on the buffering effect of the system.
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3.
  • Bostrom, M., et al. (författare)
  • Process design for recombinant protein production based on the promoter, P-malK
  • 2004
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 0175-7598 .- 1432-0614. ; 66:2, s. 200-208
  • Tidskriftsartikel (refereegranskat)abstract
    • P-malK is induced through activation of MalT, by the formation of maltotriose and cyclic adenosine monophosphate ( cAMP). The possibility to influence endogenous inducer levels is used to vary the production rates in specifically designed production protocols. Induction based on a batch process protocol on maltose gives low production rates, as the result of a lack of cAMP, which is shown to be of major importance to fully induce this promoter. Two mechanisms are thus used to influence the levels of maltotriose and/or cAMP formation: ( 1) catabolite derepression achieved from low glucose concentration and ( 2) catabolite derepression/inducer exclusion from diauxic growth on glucose/maltose. Fed-batch processes based on limited amounts of glucose result in product accumulation of up to 10% of the total protein. Depending on the feed of limiting glucose, different production profiles are developed. The initial increase in the production rate is due to maltotriose formation from endogenous glycogen degradation while, later in the process, production can be further supported by elevated levels of cAMP, provided the feed rate is sufficiently low. The introduction of maltose after a preceding fed-batch process on glucose can be efficiently used to produce maltotriose in combination with cAMP formation in the event of catabolite derepression. This leads to higher production rates and a further increase in product accumulation of up to 30% of the total protein. The diauxic growth phase resulting from the shift in carbon source can be shortened and even avoided by the design of the preceding feed-rate of glucose. It is postulated that proper design of the inoculum and initial phases of production can reduce basal levels of product formation. With this promoter, the production rate can be as high as 65 units mg(-1) h(-1) and the time to reach a maximal production rate can be designed to take up to 8 h. Furthermore, the duration of the production rate can be as long as 7 h.
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4.
  • Dey, Estera, et al. (författare)
  • Artificial carrier for oxygen supply in biological systems
  • 2004
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 1432-0614 .- 0175-7598. ; 64:2, s. 187-191
  • Tidskriftsartikel (refereegranskat)abstract
    • Several poly (dimethylsiloxanes) (PDMS) copolymers of dimethylsiloxane (DMS) with ethylene or propylene oxide were tested as artificial carriers for the delivery of oxygen to biological systems. Copolymers with a DMS content of 33% or lower enhanced glucose oxidation by 200% in contrast to the 25% increase produced by the same concentration of perfluorodecalin. When 0.05% of the copolymer with 18% DMS was included in the growth media of Bacillus thuriginensis, the biomass (growth rate) increased 1.5-fold. With 0.1% of this copolymer, actinorhodin production by Streptomyces coelicolor A3 (2) occurred in half the normal time and with an increased yield. In conclusion, these PDMS copolymers are a good alternative to perfluorodecalin as oxygen carriers in biotechnological processes.
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5.
  • Eriksson, M., et al. (författare)
  • Biological degradation of selected hydrocarbons in an old PAH/creosote contaminated soil from a gas work site
  • 2000
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 0175-7598 .- 1432-0614. ; 53:5, s. 619-626
  • Tidskriftsartikel (refereegranskat)abstract
    • An old PAH/creosote contaminated soil (total similar to 300 mu g PAH/g soil) from a former gas work site in Stockholm, Sweden, has been treated at 20 degrees C with the addition of various nutrients and inoculated with bacteria (isolated from the soil) to enhance the degradation of selected hydrocarbons. Microcosm studies showed that the soil consisted of two contaminant fractions: one available, easily degraded fraction and a strongly sorbed, recalcitrant one. The bioavailable fraction, monitored by headspace solid phase microextraction, contained aromatics with up to three rings, and these were degraded within 20 days down to non-detectable levels (ng PAH/g soil) by both the indigenous bacteria and the externally inoculated samples. The nutrient additives were: a minimal medium (Bushnell-Haas), nitrate, nitrite, potting soil (Anglamark, Sweden), sterile water and aeration with Bushnell-Haas medium. After 30 days treatment most of the sorbed fractions were still present in the soil. Stirring or mechanical mixing of the soil slurries had the greatest effect on degradation, indicating that the substances were too strongly sorbed for the microorganisms. When stirring the choice of nutrient seemed less important. For the non-stirred samples the addition of nitrate with the bacterial inoculum showed the best degradation, compared to the other non-stirred samples. At the end of the experiments, accumulations of metabolites/degradation products, such as 9H-fluorenone, 4-hydroxy-9H-fluorenone, 9,10-phenanthrenedione and 4H-cyclopenta[def]phenanthrenedione were detected. The metabolite 4-hydroxy-9H-fluorenone increased by several orders of magnitude during the biological treatments. Microbial activity in the soil was measured by oxygen consumption and carbon dioxide production.
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6.
  • Fernandes, S, et al. (författare)
  • Beta-galactosidase from a cold-adapted bacterium: purification, characterization and application for lactose hydrolysis.
  • 2002
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 1432-0614 .- 0175-7598. ; 58:3, s. 313-321
  • Tidskriftsartikel (refereegranskat)abstract
    • The enzyme beta-galactosidase was purified from a cold-adapted organism isolated from Antarctica. The organism was identified as a psychrotrophic Pseudoalteromonas sp. The enzyme was purified with high yields by a rapid purification scheme involving extraction in an aqueous two-phase system followed by hydrophobic interaction chromatography and ultrafiltration. The beta-galactosidase was optimally active at pH 9 and at 26 degrees C when assayed with o-nitrophenyl-beta-D-galactopyranoside as substrate for 2 min. The enzyme activity was highly sensitive to temperature above 30 degrees C and was undetectable at 40 degrees C. The cations Na+, K+, Mg2+ and Mn2+ activated the enzyme while Ca2+, Hg2+, Cu2+ and Zn2+ inhibited activity. The shelf life of the pure enzyme at 4 degrees C was significantly enhanced in the presence of 0.1% (w/v) polyethyleneimine. The pure beta-galactosidase was also evaluated for lactose hydrolysis. More than 50% lactose hydrolysis was achieved in 8 h in buffer at an enzyme concentration of 1 U/ml, and was increased to 70% in the presence of 0.1% (w/v) polyethyleneimine. The extent of lactose hydrolysis was 40-50% in milk. The enzyme could be immobilized to Sepharose via different chemistries with 60-70% retention of activity. The immobilized enzyme was more stable and its ability to hydrolyze lactose was similar to that of the soluble enzyme.
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7.
  • Fredlund, E., et al. (författare)
  • Metabolite profiles of the biocontrol yeast Pichia anomala J121 grown under oxygen limitation
  • 2004
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer. - 0175-7598 .- 1432-0614. ; 64:3, s. 403-409
  • Tidskriftsartikel (refereegranskat)abstract
    • The biocontrol yeast Pichia anomala J121 prevents mould growth during the storage of moist grain under low oxygen/high carbon dioxide conditions. Growth and metabolite formation of P. anomala was analyzed under two conditions of oxygen limitation: (a) initial aerobic conditions with restricted oxygen access during the growth period and (b) initial microaerobic conditions followed by anaerobiosis. Major intra- and extracellular metabolites were analyzed by high-resolution magic-angle spinning (HR-MAS) NMR and HPLC, respectively. HR-MAS NMR allows the analysis of major soluble compounds inside intact cells, without the need for an extraction step. Biomass production was higher in treatment (a), whereas the specific ethanol production rate during growth on glucose was similar in both treatments. This implies that oxygen availability affected the respiration and not the fermentation of the yeast. Following glucose depletion, ethanol was oxidized to acetate in treatment (a), but continued to be produced in (b). Arabitol accumulated in the culture substrate of both treatments, whereas glycerol only accumulated in treatment (b). Trehalose, arabitol, and glycerol accumulated inside the cells in both treatments. The levels of these metabolites were generally significantly higher in treatment (b) than in (a), indicating their importance for P. anomala during severe oxygen limitation/anaerobic conditions.
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8.
  • Galbe, Mats, et al. (författare)
  • A review of the production of ethanol from softwood
  • 2002
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 1432-0614 .- 0175-7598. ; 59:6, s. 618-628
  • Forskningsöversikt (refereegranskat)abstract
    • Ethanol produced from various lignocellulosic materials such as wood, agricultural and forest residues has the potential to be a valuable substitute for, or complement to, gasoline. One of the major resources in the Northern hemisphere is softwood. This paper reviews the current status of the technology for ethanol production from softwood, with focus on hemicellulose and cellulose hydrolysis, which is the major problem in the overall process. Other issues of importance, e.g. overall process configurations and process economics are also considered.
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9.
  • Guieysse, B., et al. (författare)
  • Degradation of acenaphthene, phenanthrene and pyrene in a packed-bed biofilm reactor
  • 2000
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 0175-7598 .- 1432-0614. ; 54:6, s. 826-831
  • Tidskriftsartikel (refereegranskat)abstract
    • Biofilm reactors are particularly suitable for the treatment of large amounts of diluted effluent, such as groundwater contaminated with scarcely soluble pollutants. A packed-bed column reactor was tested for the degradation of acenaphthene, phenanthrene and pyrene provided at their aqueous solubility concentrations. Acenapthene and phenanthrene were removed to more than 99% efficiency from this reactor whilst pyrene was removed to 90%. Pollutant disappearance was also recorded in the control reactor and was probably caused by the adsorption of pollutants into the reactor. The measurement of oxygen consumption in both reactors confirmed that microbial degradation of the pollutants was indeed occurring in the inoculated reactor. Physical adsorption is not however unwanted, as it could help with the formation of a biofilm at an early stage of the treatment.
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10.
  • Katapodis, P., et al. (författare)
  • Biosynthesis of fructo-oligosaccharides by Sporotrichum thermophile during submerged batch cultivation in high sucrose media
  • 2004
  • Ingår i: Applied Microbiology and Biotechnology. - : Springer Science and Business Media LLC. - 0175-7598 .- 1432-0614. ; 63:4, s. 378-382
  • Tidskriftsartikel (refereegranskat)abstract
    • A feruloyl esterase (StFAE-A) produced by Sporotrichum thermophile was purified to homogeneity. The purified homogeneous preparation of native StFAE-A exhibited a molecular mass of 57.0±1.5 kDa, with a mass of 33±1 kDa on SDS-PAGE. The pI of the enzyme was estimated by cation-exchange chromatofocusing to be at pH 3.1. The enzyme activity was optimal at pH 6.0 and 55–60 °C. The purified esterase was stable at the pH range 5.0–7.0. The enzyme retained 70% of activity after 7 h at 50 °C and lost 50% of its activity after 45 min at 55 °C and after 12 min at 60 °C. Determination of k cat/K m revealed that the enzyme hydrolyzed methyl p-coumarate 2.5- and 12-fold more efficiently than methyl caffeate and methyl ferulate, respectively. No activity on methyl sinapinate was detected. The enzyme was active on substrates containing ferulic acid ester linked to the C-5 and C-2 linkages of arabinofuranose and it hydrolyzed 4-nitrophenyl 5-O-trans-feruloyl-α-l-arabinofuranoside (NPh-5-Fe-Araf) 2-fold more efficiently than NPh-2-Fe-Araf. Ferulic acid (FA) was efficiently released from destarched wheat bran when the esterase was incubated together with xylanase from S. thermophile (a maximum of 34% total ferulic acid released after 1 h incubation). StFAE-A by itself could release FA, but at a level almost 47-fold lower than that obtained in the presence of xylanase. The potential of StFAE-A for the synthesis of various phenolic acid esters was tested using a ternary water-organic mixture consisting of n-hexane, 1-butanol and water as a reaction system.
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