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1.
Anaerobe ; 59: 145-153, 2019 Oct.
Artigo em Inglês | MEDLINE | ID: mdl-31254652

RESUMO

Glycerol, the main residue of biodiesel production, can be used to produce organic acids and energy through anaerobic digestion. This study aimed to assess microbial structure, diversity, productivity, and stability and the influence of these parameters on the performance of an anaerobic reactor. The experimental setup consisted of an upflow anaerobic sludge blanket (UASB) reactor fed residual glycerol and nutrients. The organic loading rate (OLR) was gradually increased through five stages, and sludge samples were collected at each, followed by DNA extraction and PCR denaturing gradient gel electrophoresis (PCR-DGGE). The resulting bands were excised, amplified, and purified. The results showed increased bacterial diversity and richness from the inoculum (Rr 38.72 and H 2.32) and along stages I and II, reaching the highest populational parameters (Rr 194.06 and H 3.32). The following stages promote decreases in richness and diversity, achieving the lowest populational parameters on this study (Rr 11.53 and H 2.04). Biogas production increased along with functional organization due to the specialization of the bacterial community and a decrease in the methanogenic population, both promoted by the increase in OLR.


Assuntos
Archaea/classificação , Archaea/isolamento & purificação , Bactérias Anaeróbias/classificação , Bactérias Anaeróbias/isolamento & purificação , Reatores Biológicos/microbiologia , Biota , Glicerol/metabolismo , Anaerobiose , Ácidos Carboxílicos/metabolismo
2.
Biotechnol Lett ; 36(7): 1381-90, 2014 Jul.
Artigo em Inglês | MEDLINE | ID: mdl-24737072

RESUMO

The fermentative production of H2 from residual glycerol is an attractive alternative for clean energy production from a waste product. Selection of operational variables for microbial populations with an adequate diversity in order to improve H2 yields is an issue faced during optimization of biological production of H2. Operational and environmental factors affect both microbial diversity and the activity of specific enzymes. Therefore, these variables must be controlled to obtain the best H2 yields. This review covers the main variables involved in the fermentative production of H2 from crude glycerol and the biochemistry of the anaerobic digestion of glycerol, with a focus on the microbial diversity involved in this process.


Assuntos
Bactérias/crescimento & desenvolvimento , Bactérias/metabolismo , Biotecnologia/métodos , Gases/metabolismo , Glicerol/metabolismo , Hidrogênio/metabolismo , Biodiversidade , Fermentação
3.
Water Sci Technol ; 66(10): 2217-22, 2012.
Artigo em Inglês | MEDLINE | ID: mdl-22949254

RESUMO

Crude glycerol, the main by-product of the biodiesel industry, is a material containing compounds considered recalcitrant to microorganisms. The aims of this study were to determine the anaerobic biodegradability and the methane production potential (MPP) of different crude glycerols generated from the transesterification of oils from several kinds of seeds and/or beans, and the anaerobic toxicity of crude glycerol obtained from a mixture of soybean and cottonseed oils. All tests were based on specific methanogenic activity assays (SMA). The biodegradability tests and the MPP assays lasted 30 days. Toxicity was evaluated through the statistical technique of factorial design and a response surface was generated in which the concentrations of crude glycerol and glucose were the independent variables and SMA was the dependent variable. The results showed that the type of seed or bean, as well as the transesterification process, affected the anaerobic biodegradability. Biodegradability ranged between 65.9 and 85.6% and MPP, between 0.220 and 0.322 m(3) CH(4)/kg crude glycerol. The toxicity test showed that crude glycerol was not toxic to anaerobic sludge.


Assuntos
Biodegradação Ambiental , Biocombustíveis/análise , Glicerol/metabolismo , Metano/metabolismo , Anaerobiose , Glicerol/química , Resíduos Industriais , Metano/química , Eliminação de Resíduos Líquidos/métodos , Poluentes Químicos da Água
4.
Water Sci Technol ; 64(9): 1935-41, 2011.
Artigo em Inglês | MEDLINE | ID: mdl-22020490

RESUMO

This work aims to evaluate the hydrodynamic properties of the sludge bed of Upflow Anaerobic Sludge Blanket (UASB) reactors based on its settleability and expansion characteristics. The methodologies used for the evaluation of the settleability of aerobic activated sludge, and for the expansibility of a sludge bed of Expanded Granular Sludge Bed reactors and Fluidised Bed Reactors were adapted and applied to the particular characteristics of the sludge of UASB reactors. An easy-to-build experimental set-up was developed to assess the parameters necessary for the equations of settleability and of expansibility. The results obtained from the sludges of seven differently operated reactors show that, for the treatment of low strength wastewater, settleability increased and expansibility decreased at decreased hydraulic retention time, from 6 to 1 h, and/or increased influent concentrations, from 136 to approximately 800 mg chemical oxygen demand/L. The results also show that it is useless to design an UASB reactor with a longer hydraulic retention time to cope with hydraulic shock loads, as a more expansible sludge will develop at such condition.


Assuntos
Reatores Biológicos , Hidrodinâmica , Esgotos/análise , Purificação da Água/instrumentação , Purificação da Água/métodos , Cinética , Projetos Piloto
5.
Water Sci Technol ; 59(9): 1841-6, 2009.
Artigo em Inglês | MEDLINE | ID: mdl-19448321

RESUMO

The market for coconut water causes environmental problems as it is one of the major agro-industrial solid wastes in some developing countries. With the aim of reusing the coconut husk, Embrapa developed a system for processing this raw material. During the dewatering stage Coconut Husk Liquor (CHL) is generated with chemical oxygen demand (COD) varying from 60 to 70 g/L due to high concentrations of sugars and tannins. The present study evaluated the feasibility of anaerobic treatment of CHL through Anaerobic Toxicity Assay and the operation of a lab-scale Upflow Anaerobic Sludge Blanket (UASB) reactor. Results showed that CHL can be treated through a UASB reactor operating with an OLR that reaches up to 10 kg/m3.d and that is maintained stable during the whole operation. With this operational condition, the removal efficiency was higher than 80% for COD and approximately 78% for total tannins, and biogas production was 20 m3 of biogas or 130 KWh per m3 of CHL. Seventy-five percent of the biogas composition was methane and toxicity tests demonstrated that CHL was not toxic to the methanogenic consortia. Conversely, increasing the concentration of CHL leads to increased methanogenic activity.


Assuntos
Reatores Biológicos , Cocos , Eliminação de Resíduos Líquidos/métodos , Anaerobiose
6.
Water Sci Technol ; 59(9): 1847-53, 2009.
Artigo em Inglês | MEDLINE | ID: mdl-19448322

RESUMO

The effects of hydraulic retention time (HRT) and influent COD concentration (CODInf) on Specific Methanogenic Activity (SMA) and the biodegradability of an anaerobic sludge need to be elucidated because of the discordant results available in literature. This information is important for the operation of anaerobic reactors and design of the sludge post-treatment unit. For this study, sludge samples obtained from eight pilot-scale Upflow Anaerobic Sludge Blanket (UASB) reactors were tested. The reactors were fed with municipal wastewater and operated with different sets of HRT and influent concentrations until the steady state was established. The results show that at a lower HRT, sludge with relatively higher SMA develops. A slight trend of declining SMA at increasing CODInf was found for reactors operated at longer HRTs; however, further experiments are necessary for more definitive conclusions. The sludge from reactors operated at longer HRTs and with lower CODInf resulted in lower biodegradability. Results also showed that it is ineffective to design a UASB reactor with a longer HRT to cope with organic shock loads.


Assuntos
Reatores Biológicos/microbiologia , Metano/metabolismo , Eliminação de Resíduos Líquidos/métodos
7.
Water Sci Technol ; 54(2): 49-55, 2006.
Artigo em Inglês | MEDLINE | ID: mdl-16939083

RESUMO

In this investigation, the robustness and stability of UASB reactors was evaluated on the basis of four indicators: (i) COD removal efficiency; (ii) effluent variability; (iii) pH stability; and (iv) recovery time. The experiments were carried out using six pilot-scale UASB reactors fed with domestic sewage and operated under different operational conditions. After establishment of a "steady-state", organic and hydraulic shock loads (six times the loading rate during six hours) were imposed. The results show that the UASB reactors are robust systems with regards to COD removal efficiency and pH stability when exposed to shock loads. However, this reactor cannot attenuate the imposed fluctuation in the influent COD. A secondary treatment unit is needed to retain the expelled sludge occurring as a result of a hydraulic shock load, or prior to the shock, a sufficient amount of sludge needs to be discharged from the reactor.


Assuntos
Anaerobiose , Esgotos , Concentração de Íons de Hidrogênio , Projetos Piloto
8.
Water Sci Technol ; 52(1-2): 299-305, 2005.
Artigo em Inglês | MEDLINE | ID: mdl-16180442

RESUMO

In this investigation, the performance of Upflow Anaerobic Sludge Blanket (UASB) reactors treating municipal wastewater was evaluated on the basis of: (i) COD removal efficiency, (ii) effluent variability, and (iii) pH stability. The experiments were performed using 8 pilot-scale UASB reactors (120 L) from which some of them were operated with different influent COD (CODInf ranging from 92 to 816 mg/L) and some at different hydraulic retention time (HRT ranging from 1 to 6 h). The results show that decreasing the CODInf, or lowering the HRT, leads to decreased efficiencies and increased effluent variability. During this experiment, the reactors could treat efficiently sewage with concentration as low as 200 mg COD/L. They could also be operated satisfactorily at an HRT as low as 2 hours, without problems of operational stability. The maximum COD removal efficiency can be achieved at CODInf exceeding 300 mg/L and HRT of 6h.


Assuntos
Bactérias Anaeróbias/metabolismo , Reatores Biológicos/microbiologia , Eliminação de Resíduos Líquidos/métodos , Brasil , Estudos de Avaliação como Assunto , Metano/metabolismo , Esgotos/microbiologia , Fatores de Tempo
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