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1.
J Appl Microbiol ; 123(4): 903-915, 2017 Oct.
Artigo em Inglês | MEDLINE | ID: mdl-28772337

RESUMO

AIMS: To achieve the functional specialization of a microalgae community through operational tuning of an open photobioreactor used for biogas upgrading under alkaline conditions. METHODS AND RESULTS: An open photobioreactor was inoculated with an indigenous microalgae sample from the Texcoco Soda Lake. A microalgae community was adapted to fix CO2 from synthetic biogas through different culture conditions reaching a maximum of 220 mg CO2  l-1 per day. Picochlorum sp. and Scenedesmus sp. were identified as the prominent microalgae genera by molecular fingerprinting (partial sequencing of 16S rRNA and 18S rRNA genes) but only the first was detected by microscopy screening. Changes in the microalgae community profile were monitored by a range-weighted richness index, reaching the lowest value when biogas was upgraded. CONCLUSIONS: A robust microalgae community in the open photobioreactor was obtained after different culture conditions. The specialization of microalgae community for CO2 fixation under H2 S presence was driven by biogas upgrading conditions. SIGNIFICANCE AND IMPACT OF THE STUDY: The alkaline conditions enhance the CO2 absorption from biogas and could optimize specialized microalgae communities in the open photobioreactor. Denaturing gradient gel electrophoresis fingerprinting and richness index comparison are useful methods for the evaluation of microalgae community shifts and photosynthetic activity performance, particularly in systems intended for CO2 removal from biogas where the CO2 assimilation potential can be related to the microbial richness.


Assuntos
Biocombustíveis , Dióxido de Carbono/metabolismo , Microalgas/crescimento & desenvolvimento , Fotobiorreatores , Lagos/microbiologia , Microalgas/metabolismo , RNA Ribossômico 16S , Scenedesmus/crescimento & desenvolvimento , Scenedesmus/isolamento & purificação , Scenedesmus/metabolismo
2.
Water Sci Technol ; 59(7): 1415-21, 2009.
Artigo em Inglês | MEDLINE | ID: mdl-19381008

RESUMO

The biological sulfide removal from wastewater caustic streams can be achieved without significant dilution by alkaliphilic microorganisms which usually show lower growth and oxidation rates as compared with acidic and neutral bacteria. To improve volumetric removal rates under alkaline condition (pH 10), an Alkaliphilic Sulfide-oxidizing Bacteria Consortium (ASBC) was studied in a Packed Recycling Reactor (PRR). A commercial Nylon fiber resulted to be a convenient packing support for biofilm development as it has high specific area and similar hydrophobic propertie. The PRR reached a maximum sulfide oxidation rate of 100 mmol L(-1) d(-1) with efficiency close to 100%, representing an enhancement of 56% from the maximum sulfide oxidation rate reached for a free cell continuous culture. Higher sulfide loading rates induced oxygen limiting conditions reducing the biological activity despite the considerable biofilm attached on the nylon fiber.


Assuntos
Reatores Biológicos/microbiologia , Sulfetos/isolamento & purificação , Eliminação de Resíduos Líquidos/métodos , Purificação da Água/métodos , Aerobiose , Biodegradação Ambiental , Conservação dos Recursos Naturais , Concentração de Íons de Hidrogênio , Sulfetos/metabolismo , Bactérias Redutoras de Enxofre/metabolismo
3.
Environ Technol ; 29(8): 847-53, 2008 Aug.
Artigo em Inglês | MEDLINE | ID: mdl-18724639

RESUMO

This work describes the design and performance of a thiosulfate-oxidizing bioreactor that allowed high elemental sulfur production and recovery efficiency. The reactor system, referred to as a Supernatant-Recycling Settler Bioreactor (SRSB), consisted of a cylindrical upflow reactor and a separate aeration vessel. The reactor was equipped with an internal settler and packing material (structured corrugated PVC sheets) to facilitate both cell retention and the settling of the formed elemental sulfur. The supernatant from the reactor was continuously recirculated through the aerator. An inlet thiosulfate concentration of 100 mmol l(-1) was used. The reactor system was fed with 89 mmol l(-1) d(-1) thiosulfate reaching 98 to 100% thiosulfate conversion with an elemental sulfur yield of 77%. Ninety-three percent of the produced sulfur was harvested from the bottom of the reactor as sulfur sludge. The dry sulfur sludge contained 87% elemental sulfur. The inclusion of an internal settler and packing material in the reactor system resulted in an effective retention of sulfur and biomass inside the bioreactor, preventing the oxidation of thiosulfate and elemental sulfur to sulfate in the aerator and, therefore, improving the efficiency of elemental sulfur formation and recovery.


Assuntos
Reatores Biológicos , Enxofre/metabolismo , Tiossulfatos/metabolismo , Biomassa , Oxirredução , Oxigênio/metabolismo , Esgotos , Eliminação de Resíduos Líquidos/métodos
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