Valorization of Glucose-Based Wastewater Through Production of Hydrogen, Volatile Fatty Acids and Alcohols

The production of hydrogen in an anaerobic fluidized bed reactor (AFBR) was evaluated under different organic loading rates (OLRs) with the addition of 1 g L−1 sodium bicarbonate for pH control. Expanded clay was used as the support material for microbial attachment. Two AFBRs were operated with glucose concentrations of 10 and 25 g L−1 and a hydraulic retention time (HRT) decreasing from 8 to 1 h at a controlled temperature of 30°C. A linear correlation was observed between the hydrogen production rate (HPR) and the OLR, except for the reactor operated with 25 g L−1 glucose. The maximum HPR of 1.58 L h−1 L−1 was obtained with an HRT of 1 h, and the maximum H2 yield of 1.32 mol H2 mol−1 glucose was obtained with an HRT of 2 h, in the reactor operated with 10 g L−1 glucose

Produção de biohidrogênio a partir de efluentes de laticínios, lactose isolada e soro de queijo em reatores anaeróbios em batelada em temperature termófilas

 A demanda energética é crescente no mundo moderno e o hidrogênio surge como uma fonte alternativa de energia limpa. Os resíduos agroindustriais apresentam grande concentração de material orgânico e seu lançamento pode comprometer a qualidade ambiental. Nesse sentido, a produção biológica de hidrogênio tem sido apontada como uma alternativa para o tratamento destes resíduos. O objetivo deste trabalho foi aplicar o resíduo agroindustrial de laticínios e os resíduos sintéticos de lactose e soro do queijo em reatores anaeróbios em batelada sob temperatura termófilas para a produção biológica de hidrogênio. O efluente sintético de lactose mostrou melhor desempenho com taxa de produção máxima e rendimento específico de hidrogênio de, respectivamente, 21.65 mmolH2/dia e 1,84molH2/mol de carboidratos . Etanol e ácido acético foram os metabolitos solúveis de maior concentração, o que indica que a rota da produção de hidrogênio foi a do etanol. A produção a partir do efluente bruto de laticínios mostrou-se satisfatória.Palavras-chave: hidrogênio, reatores anaeróbios, laticínios

Effect of Substrate Concentration on Dark Fermentation Hydrogen Production Using an Anaerobic Fluidized Bed Reactor

The effect of substrate (glucose) concentration on the stability and yield of a continuous fermentative process that produces hydrogen was studied. Four anaerobic fluidized bed reactors (AFBRs) were operated with a hydraulic retention time (HRT) from 1 to 8 h and an influent glucose concentration from 2 to 25 gL(-1). The reactors were inoculated with thermally pre-treated anaerobic sludge and operated at a temperature of 30 degrees C with an influent pH around 5.5 and an effluent pH of about 3.5. The AFBRs with a HRT of 2 h and a feed strength of 2, 4, and 10 gL(-1) showed satisfactory H-2 production performance, but the reactor fed with 25 gL(-1) of glucose did not. The highest hydrogen yield value was obtained in the reactor with a glucose concentration of 2 gL(-1) when it was operated at a HRT of 2 h. The maximum hydrogen production rate value was achieved in the reactor with a HRT of 1 h and a feed strength of 10 gL(-1). The AFBRs operated with glucose concentrations of 2 and 4 gL(-1) produced greater amounts of acetic and butyric acids, while AFBRs with higher glucose concentrations produced a greater amount of solvents.FAPESPFAPESPCNPqCNPqCAPESCAPE

Desempenho de reator anaeróbio-aeróbio de leito fixo (RAALF) utilizando conchas de sururu (Mytella charruana) como meio suporte para remoção de carbono e nitrificação de esgoto sanitário

O estudo avaliou a atuação de um reator anaeróbio-aeróbio de leito fixo (RAALF) e fluxo ascendente, vertical, operado de modo contínuo, em escala de bancada, preenchido com argila expandida e conchas de sururu como meio suporte para imobilização da biomassa, no tratamento de esgoto doméstico. A utilização da concha de sururu se deu pela importância de testar o desempenho do reator usando material de baixo custo e fácil acesso. O reator utilizado teve resposta efetiva na nitrificação; as conchas de sururu permitiram a manutenção da alcalinidade no substrato e a elas se atribui também o comprometimento da desnitrificação, pois o aumento no pH do efluente pode ter reduzido a velocidade do processo. Os resultados demonstram que o reator gerou efluente com matéria orgânica reduzida e a concha de sururu favoreceu a conversão de nitrogênio, comprovando a viabilidade do uso do material como suporte principal em RAALF no tratamento de esgoto doméstico

Phenol degradation in an anaerobic fluidized bed reactor packed with low density support materials

The objective of this research was to study phenol degradation in anaerobic fluidized bed reactors (AFBR) packed with polymeric particulate supports (polystyrene - PS, polyethylene terephthalate - PET, and polyvinyl chloride - PVC). The reactors were operated with a hydraulic retention time (HRT) of 24 h. The influent phenol concentration in the AFBR varied from 100 to 400 mg L-1, resulting in phenol removal efficiencies of similar to 100%. The formation of extracellular polymeric substances yielded better results with the PVC particles; however, deformations in these particles proved detrimental to reactor operation. PS was found to be the best support for biomass attachment in an AFBR for phenol removal. The AFBR loaded with PS was operated to analyze the performance and stability for phenol removal at feed concentrations ranging from 50 to 500 mg L-1. The phenol removal efficiency ranged from 90-100%.FAPESPCAPESCNP

Performance and composition of bacterial communities in anaerobic fluidized bed reactors for hydrogen production: Effects of organic loading rate and alkalinity

This study evaluated the effects of the organic loading rate (OLR) and pH buffer addition on hydrogen production in two anaerobic fluidized bed reactors (AFBRs) operated simultaneously. The AFBRs were fed with glucose, and expanded clay was used as support material. The reactors were operated at a temperature of 30 degrees C, without the addition of a buffer (AFBR1) and with the addition of a pH buffer (AFBR2, sodium bicarbonate) for OLRs ranging from 19.0 to 140.6 kg COD m(-3) d(-1) (COD: chemical oxygen demand). The maximum hydrogen yields for AFBR1 and AFBR2 were 2.45 and 1.90 mol H-2 mol(-1) glucose (OLR of 84.3 kg COD m(-3) d(-1)), respectively. The highest hydrogen production rates were 0.95 and 0.76 L h(-1) L-1 for AFBR1 and AFBR2 (OLR of 140.6 kg COD m(-3) d(-1)), respectively. The operating conditions in AFBR1 favored the presence of such bacteria as Clostridium, while the bacteria in AFBR2 included Clostridium, Enterobacter, Klebsiella, Veillonellaceae, Chryseobacterium, Sporolactobacillus, and Burkholderiaceae. Copyright (C) 2012, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.CNPqCNPqCAPESCAPESFAPESPFAPES

Rationale, study design, and analysis plan of the Alveolar Recruitment for ARDS Trial (ART): Study protocol for a randomized controlled trial

Background: Acute respiratory distress syndrome (ARDS) is associated with high in-hospital mortality. Alveolar recruitment followed by ventilation at optimal titrated PEEP may reduce ventilator-induced lung injury and improve oxygenation in patients with ARDS, but the effects on mortality and other clinical outcomes remain unknown. This article reports the rationale, study design, and analysis plan of the Alveolar Recruitment for ARDS Trial (ART). Methods/Design: ART is a pragmatic, multicenter, randomized (concealed), controlled trial, which aims to determine if maximum stepwise alveolar recruitment associated with PEEP titration is able to increase 28-day survival in patients with ARDS compared to conventional treatment (ARDSNet strategy). We will enroll adult patients with ARDS of less than 72 h duration. The intervention group will receive an alveolar recruitment maneuver, with stepwise increases of PEEP achieving 45 cmH(2)O and peak pressure of 60 cmH2O, followed by ventilation with optimal PEEP titrated according to the static compliance of the respiratory system. In the control group, mechanical ventilation will follow a conventional protocol (ARDSNet). In both groups, we will use controlled volume mode with low tidal volumes (4 to 6 mL/kg of predicted body weight) and targeting plateau pressure <= 30 cmH2O. The primary outcome is 28-day survival, and the secondary outcomes are: length of ICU stay; length of hospital stay; pneumothorax requiring chest tube during first 7 days; barotrauma during first 7 days; mechanical ventilation-free days from days 1 to 28; ICU, in-hospital, and 6-month survival. ART is an event-guided trial planned to last until 520 events (deaths within 28 days) are observed. These events allow detection of a hazard ratio of 0.75, with 90% power and two-tailed type I error of 5%. All analysis will follow the intention-to-treat principle. Discussion: If the ART strategy with maximum recruitment and PEEP titration improves 28-day survival, this will represent a notable advance to the care of ARDS patients. Conversely, if the ART strategy is similar or inferior to the current evidence-based strategy (ARDSNet), this should also change current practice as many institutions routinely employ recruitment maneuvers and set PEEP levels according to some titration method.Hospital do Coracao (HCor) as part of the Program 'Hospitais de Excelencia a Servico do SUS (PROADI-SUS)'Brazilian Ministry of Healt

Effect of glucose concentration and alkalinity in the hydrogen production in anaerobic fluidized bed

O objetivo deste estudo foi avaliar o efeito da adição de alcalinidade, da concentração da glicose e da taxa de carregamento orgânico na produção de hidrogênio e ácidos orgânicos em reator anaeróbio de leito fluidificado (RALF), contendo argila expandida (2,8 - 3,35 mm) como material suporte para adesão microbiana. Foram utilizados oito reatores idênticos, sendo quatro deles operados sem adição de alcalinidade, e com concentração de glicose de 2000, 4000, 10000 e 25000 mg/L, respectivamente. Outros quatro reatores operados com adição de alcalinidade, e com as mesmas concentrações de glicose cada um. Os reatores foram inoculados com lodo anaeróbio pré-tratado termicamente, operado com tempo de detenção hidráulica (TDH) decrescente de 8 h a 1 h à temperatura controlada de 30°C. Foi constatada produção volumétrica de hidrogênio máxima de 1,58 L/h.L, para o reator operado com 10000 mg/L de glicose com adição de alcalinidade (R10CA) e um rendimento máximo de 2,52 mol \'H IND.2\'/mol glicose, para o reator operado com 4000 mg/L de glicose com adição de alcalinidade (R4CA). O biogás produzido foi composto de \'H IND.2\' e \'CO IND.2\'. Em ambos os reatores, o conteúdo de hidrogênio aumentou com a redução do TDH de 8 h para 1 h, alcançando valor máximo de 77%, para o reator operado com 4000 mg/L sem adição de alcalinidade (R4SA). Os reatores operados com altas concentrações de glicose produção de hidrogênio, o qual predominou o ácido acético e butírico. Neste mesmo reator, o rendimento da produção de hidrogênio foi superior aos outros reatores. As análises de clonagem e sequenciamento do consórcio bacteriano revelaram semelhanças com Clostridium, Klebsiella, Enterobacter e bactérias não cultivadas.This study evaluated the effect alkalinity addition, glucose concentration and organic loading rate in the hydrogen production and organic acids in an anaerobic fluidized bed reactor (AFBR), containing expanded clay (2.8 - 3,35 mm) as support material for microbial adhesion. We used eight identical reactors, four of them operated without the addition of alkalinity, and concentration of glucose in 2000, 4000, 10000 and 25000 mg/L, respectively. Another four reactors operated with the addition of alkalinity, and with the same concentrations of glucose each. The reactors were operated with hydraulic retention times (HRT) ranging from 8 h at 1 h, and temperature of 30°C. It has been found for hydrogen production rate maximum 1.58 L/h.L for the reactor operated with 10000 mg/L glucose with the addition of alkalinity (R10CA) and a maximum yield of 2.52 mol \'H IND.2\'/mol glucose to the reactor operated with 4000 mg/L glucose with the addition of alkalinity (R4CA). The biogas produced was composed of \'H IND.2\' and \'CO IND.2\'. In both reactors, the hydrogen content increased with the reduction of HRT of 8 h at 1 h, reaching a maximum of 77% for the reactor operated from 4000 mg/L without added alkalinity (R4SA). The reactors operated with high glucose concentrations (10000 mg/L and 25000 mg/L) had higher proportions of solvents such as soluble metabolites. There was a linear correlation between the hydrogen production rate and organic loading rate in all reactors. The yield, the hydrogen production rate and distribution of soluble metabolites in both reactors, were influenced by the glucose concentration. The reactor operated with 4000 mg/L and addition of alkalinity, presented the most favorable distribution of soluble metabolites to hydrogen production, which was predominant acetic and butyric acid. In the same reactor, the hydrogen yield was higher than other reactors. The cloning and sequencing analysis bacterial consortium revealed the presence of Clostridium, Klebsiella, Enterobacter and uncultivated bacteria

Performance of anaerobic reactor of fluidized bed operated under conditions of progressive increase of the organic load in the phenol treatment

O fenol e seus derivados são poluentes comumente presentes nos efluentes industriais. Também são considerados poluentes orgânicos perigosos e difícieis de serem eliminados, quando presentes em altas concentrações. O processo de tratamento anaeróbio é uma alternativa para a degradação de despejos que possuem compostos persistentes, como fenóis. O objetivo deste trabalho foi estudar a viabilidade do uso de reator anaeróbio de leito fluidificado (RALF) operado sob condições de aumento progressivo da carga orgânica no tratamento de água residuária sintética contendo fenol como única fonte de carbono. O reator foi construído em acrílico com altura de 190 cm e diâmetro interno de 5 cm, e volume total de 4192 \'CM POT.3\'. O meio suporte foi constituído por partículas de poliestireno (2,2 mm). O inóculo utilizado foi lodo de abatedouro de suínos, o tempo de detenção hidráulica (TDH) foi 24 h, o RALF foi operado a 30 ± 1 ºC durante 182 dias. A adaptação do inóculo ocorreu no próprio reator, onde permitiu uma partida rápida, 14 dias, além de manter as condições de anaerobiose no reator. As concentrações de fenol tratadas foram de 50 mg/L, 100 mg/L, 200 mg/L, 300 mg/L, 400 mg/L, 500 mg/L, 600 mg/L e 700 mg/L, com taxas de carregamento orgânico real aplicadas de 0,09 a 1,29 kg fenol/\'M POT.3\'dia. O pH variou entre 6,59 e 8,21 para todo o sistema. As concentrações de alcalinidade a bicarbonato (AB) afluente e efluente foram 180 mg/L e 294 mg/L, respectivamente. Foram constatadas eficiências de remoção de fenol e de DQO superiores a 90% e 88%, respectivamente. De um modo geral, os resultados mostraram a potencialidade do sistema proposto em degradar efluentes líquidos contendo fenol.The phenol and yours derived they are pollutant commonly presents in the industrial effluents. They are also considered pollutant organic dangerous and difficult of they be eliminated, when presents in high concentrations. The process of anaerobic treatment is an alternative for the degradation of spillings that possess composed persistent, as phenols. The objective of this work was to study the viability of the use of anaerobic fluidized-bed reactor (RALF) operated under conditions of progressive increase of the organic load in the treatment of synthetic wastewater containing phenol as only source of carbon. The reactor was built in acrylic with height of 190 cm and internal diameter of 5 cm, and total volume of 4192 \'CM POT.3\'. The half supports was constituted by particles of polystyrene (2,2 mm). The used sludge was the mud of slaughterhouse of swine, the time of hydraulic detention (TDH) it was 24 h, RALF was operated 30 ± 1 ºC for 182 days. The adaptation of the sludge happened in the own reactor, where it allowed a fast departure, 14 days, besides maintaining the anaerobic conditions in the reactor. The phenol concentrations treated were of 50 mg/L, 100 mg/L, 200 mg/L, 300 mg/L, 400 mg/L, 500 mg/L, 600 mg/L and 700 mg/L, where the taxes of real organic shipment applied varied from 0,09 to 1,29 kg fenol/\'M POT.3\'dia. The pH varied between 6,59 and 8,21 for the whole system. The alkalinity concentrations to bicarbonate (AB) influent and effluent were 180 mg/L and 294 mg/L, respectively. Efficiencies of phenol removal were verified and of superior DQO to 90% and 88%, respectively. In general, the results showed the potentiality of the system proposed in degrading liquid effluent containing phenol

Anaerobic fluidized bed reactor with expanded clay as support for hydrogen production through dark fermentation of glucose

This study evaluated hydrogen production in an anaerobic fluidized bed reactor (AFBR) fed with glucose-based synthetic wastewater. Particles of expanded clay (2.8-3.35 mm) were used as a support material for biomass immobilization. The reactor was operated with hydraulic retention times (HRT) ranging from 8 to 1 h. The hydrogen yield production increased from 1.41 to 2.49 mol H(2) Mol(-1) glucose as HRT decreased from 8 to 2 h. However, when HRT was 1 h, there was a slight decrease to 2.41 mol H(2) Mol(-1) glucose. The biogas produced was composed of H(2) and CO(2), and the H(2) content increased from 8% to 35% as HRT decreased. The major soluble metabolites during H(2) fermentation were acetic acid (HAc) and butyric acid (HBu), accounting for 36.1-53.3% and 37.7-44.9% of total soluble metabolites, respectively. Overall, the results demonstrate the potential of using expanded clay as support material for hydrogen production in AFBRs. (c) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.CNPq[141197/2007-2]CNPq[130551/2007-4]CNPq[152215/2007-7]FAPESP[05/51702-9]FAPESP[07/58564-6