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1.
Bioprocess Biosyst Eng ; 40(4): 519-528, 2017 Apr.
Artigo em Inglês | MEDLINE | ID: mdl-28005180

RESUMO

The fungicide carbendazim is an ecotoxic agent affecting aquatic biota. Due to its suspected hormone-disrupting effects, it is considered a "priority hazard substance" by the Water Framework Directive of the European Commission, and its degradation is of major concern. In this work, a horizontal tubular biofilm reactor (HTBR) operating in plug-flow regime was used to study the kinetics of carbendazim removal by an acclimated microbial consortium. The reactor was operated in steady state continuous culture at eight different carbendazim loading rates. The concentrations of the fungicide were determined at several distances of the HTBR. At the loading rates tested, the highest instantaneous removal rates were observed in the first section of the tubular biofilm reactor. No evidence of inhibition of the catabolic activity of the microbial community was found. Strains of the genera Flectobacillus, Klebsiella, Stenotrophomonas, and Flavobacterium were identified in the biofilm; the last three degrade carbendazim in axenic culture.


Assuntos
Bactérias/metabolismo , Benzimidazóis/metabolismo , Reatores Biológicos , Carbamatos/metabolismo , Membranas Artificiais , Consórcios Microbianos , Cinética
2.
Biodegradation ; 25(3): 405-15, 2014 Jun.
Artigo em Inglês | MEDLINE | ID: mdl-24166157

RESUMO

A microbial community, selected by its ability to degrade triazinic herbicides was acclimatized by successive transfers in batch cultures. Initially, its ability to degrade prometryn, was evaluated using free cells or cells attached to fragments of a porous support. As carbon, nitrogen and sulfur sources, prometryn, (98.8 % purity), or Gesagard, a herbicide formulation containing 44.5 % prometryn and 65.5 % of adjuvants, were used. In batch cultures, a considerable delay in the degradation of prometryn, presumptively caused by the elevated concentration of inhibitory adjuvants, occurred. When pure prometryn was used, volumetric removal rates remarkably higher than those obtained with the herbicide formulation were estimated by fitting the raw experimental data to sigmoidal decay models, and differentiating them. When the microbial consortium was immobilized in a continuously operated biofilm reactor, the negative effect of adjuvants on the rate and removal efficiency of prometryn could not be detected. Using the herbicide formulation, the consortium showed volumetric removal rates greater than 20 g m(-3) h(-1), with prometryn removal efficiencies of 100 %. The predominant bacterial strains isolated from the microbial consortium were Microbacterium sp., Enterobacter sp., Acinetobacter sp., and Flavobacterium sp. Finally, by comparison of the prometryn removal rates with others reported in the literature, it can be concluded that the use of microbial consortia immobilized in a biofilm reactor operated in continuous regime offer better results than batch cultures of pure microbial strains.


Assuntos
Biofilmes/crescimento & desenvolvimento , Herbicidas/metabolismo , Consórcios Microbianos/fisiologia , Modelos Estatísticos , Prometrina/metabolismo , Poluentes Químicos da Água/metabolismo , Actinomycetales/metabolismo , Biodegradação Ambiental , Reatores Biológicos , Células Imobilizadas , Enterobacter/metabolismo , Flavobacterium/metabolismo , Cinética
3.
Bioresour Technol ; 145: 33-6, 2013 Oct.
Artigo em Inglês | MEDLINE | ID: mdl-23566464

RESUMO

In this work, an efficient degradation process for the removal of 2,4-D and ametryn, together with organic and inorganic adjuvants used in the commercial formulations of both herbicides, was developed. Although both compounds are toxic for microbial communities, ametryn is markedly more toxic than 2,4-D. In spite of this, the microbial consortium used could resist loading rates up to 31.5 mg L(-1) d(-1) of ametryn, with removal efficiencies up to 97% for both herbicides. Thus, an alternative use of this consortium could be bioaugmentation, as a tool to protect the structure and function of an activated-sludge biota against ametryn or 2,4-D shock loads. The process was carried out in a lab-scale prototype of aerobic biobarrier constructed as a compartmentalized fixed film reactor with airlift recirculation of oxygenated liquid.


Assuntos
Biodegradação Ambiental , Biofilmes , Reatores Biológicos , Herbicidas/metabolismo , Poluentes Químicos da Água/metabolismo , Purificação da Água/instrumentação , Purificação da Água/métodos , Ácido 2,4-Diclorofenoxiacético , Bioensaio , Análise da Demanda Biológica de Oxigênio , Técnicas de Cultura de Células , Clorófitas/efeitos dos fármacos , Cromatografia Líquida de Alta Pressão , Herbicidas/toxicidade , Cinética , Triazinas , Poluentes Químicos da Água/toxicidade
4.
Appl Biochem Biotechnol ; 162(6): 1689-707, 2010 Nov.
Artigo em Inglês | MEDLINE | ID: mdl-20376575

RESUMO

A microbial community able to aerobically degrade the azo dye Acid Orange 7 was selected from riparian or lacustrine sediments collected at sites receiving textile wastewaters. Three bacterial strains, pertaining to the genera Pseudomonas, Arthrobacter, and Rhizobium, constitute the selected community. The biodegradation of AO7 was carried out in batch-suspended cell culture and in a continuously operated multistage packed-bed BAC reactor. The rapid decolorization observed in batch culture, joined to a delay of about 24 h in COD removal and cell growth, suggests that enzymes involved in biodegradation of the aromatic amines generated after AO7 azo-bond cleavage (1-amino-2-naphthol [1-A2N] and 4-aminobenzenesulfonic acid [4-ABS]), are inducible in this microbial consortium. After this presumptive induction period, the accumulated byproducts, measured through COD, were partially metabolized and transformed in cell mass. At all azo dye loading rates used, complete removal of AO7 and 1-A2N was obtained in the multistage packed-bed BAC reactor (PBR).; however, the overall COD (eta ( COD )) and 4-ABS (eta ( ABS )) removal efficiencies obtained in steady state continuous culture were about 90%. Considering the toxicity of 1-A2N, its complete removal has particular relevance. In the first stages of the packed-bed BAC reactor (Fig. 4a-c), major removal was observed. In the last stage, only a slight removal of COD and 4-ABS was obtained. Comparing to several reported studies, the continuously operated multistage packed-bed BAC reactor showed similar or superior results. In addition, the operation of large-packed-bed BAC reactors could be improved by using several shallow BAC bed stages, because the pressure drop caused by bed compaction of a support material constituted by small and fragile particles can be reduced.


Assuntos
Compostos Azo/metabolismo , Bactérias/metabolismo , Benzenossulfonatos/metabolismo , Reatores Biológicos/microbiologia , Corantes/metabolismo , Microbiologia Industrial/métodos , Adsorção , Aerobiose , Bactérias/genética , Bactérias/isolamento & purificação , Biodegradação Ambiental , Carbono/química , Células Imobilizadas/metabolismo , Microbiologia Industrial/instrumentação , Povidona/química
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