RESUMO
This study aimed to compare the production of hydrogen and 1,3-propanediol from crude glycerol (10 g/L) in mesophilic (30 °C) and thermophilic (55 °C) anaerobic fluidized bed reactors, namely AFBR30 °C and AFBR55 °C, respectively, at hydraulic retention times (HRT) reduced from 8 to 1 h. In AFBR30 °C, the absence or low hydrogen yields can be attributed to the production of 1,3-propanediol (maximum of 651 mmol/mol glycerol), and the formation of caproic acid (maximum of 1097 mg/L) at HRTs between 8 and 2 h. In AFBR55 °C, the hydrogen yield of 1.20 mol H2/mol glycerol consumed was observed at the HRT of 1 h. The maximum yield of 1,3-propanediol in AFBR55 °C was equal to 804 mmol/mol glycerol at the HRT of 6 h and was concomitant with the production of hydrogen (0.87 mol H2/mol glycerol consumed) and butyric acid (1447 mg/L).
Assuntos
Fermentação , Glicerol/metabolismo , Hidrogênio/isolamento & purificação , Propilenoglicóis/isolamento & purificação , Temperatura , Reatores BiológicosRESUMO
An anaerobic sequencing batch reactor containing immobilized biomass (AnSBBR) was used to produce biomethane by treating the effluent from another AnSBBR used to produce biohydrogen from glucose- (AR-EPHG) and sucrose-based (AR-EPHS) wastewater. In addition, biomethane was also produced from sucrose-based synthetic wastewater (AR-S) in a single AnSBBR to compare the performance of biomethane production in two steps (acidogenic and methanogenic) in relation to a one-step operation. The system was operated at 30 °C and at a fixed stirring rate of 300 rpm. For AR-EPHS treatment, concentrations were 1,000, 2,000, 3,000, and 4,000 mg chemical oxygen demand (COD) L(-1) and cycle lengths were 6 and 8 h. The applied volumetric organic loads were 2.15, 4.74, 5.44, and 8.22 g COD L(-1) day(-1). For AR-EPHG treatment, concentration of 4,000 mg COD L(-1) and 4-h cycle length (7.21 g COD L(-1) day(-1)) were used. For AR-S treatment, concentration was 4,000 mg COD L(-1) day(-1) and cycle lengths were 8 (7.04 g COD L(-1) day(-1)) and 12 h (4.76 g COD L(-1) day(-1)). The condition of 8.22 g COD L(-1) day(-1) (AR-EPHS) showed the best performance with respect to the following parameters: applied volumetric organic load of 7.56 g COD L(-1) day(-1), yield between produced methane and removed organic material of 0.016 mol CH4 g COD(-1), CH4 content in the produced biogas of 85 %, and molar methane productivity of 127.9 mol CH4 m(-3) day(-1). In addition, a kinetic study of the process confirmed the trend that, depending on the biodegradability characteristics of the wastewaters used, the two-step treatment (acidogenic for biohydrogen production and methanogenic for biomethane production) has potential advantages over the single-step process.
Assuntos
Bactérias Anaeróbias/metabolismo , Reatores Biológicos/microbiologia , Hidrogênio/metabolismo , Resíduos Industriais/prevenção & controle , Metano/metabolismo , Águas Residuárias/microbiologia , Purificação da Água/métodos , Biodegradação Ambiental , Hidrogênio/isolamento & purificação , Metano/isolamento & purificaçãoRESUMO
The aim of this study was to investigate the effect of the support material used for biomass attachment and bed porosity on the potential generation of hydrogen gas in an anaerobic bioreactor treating low-strength wastewater. For this purpose, an upflow anaerobic packed-bed (UAPB) reactor fed with sucrose-based synthetic wastewater was used. Three reactors with various support materials (expanded clay, vegetal coal, and low-density polyethylene) were operated for hydraulic retention time (HRT) of 0.5 and 2 h. Based on the results obtained, three further reactors were operated with low-density polyethylene as a material support using various bed porosities (91, 75, and 50 %) for an HRT of 0.5 h. The UAPB reactor was found to be a feasible technology for hydrogen production, reaching a maximum substrate-based hydrogen yield of 7 mol H2 mol(-1) sucrose for an HRT of 0.5 h. The type of support material used did not affect hydrogen production or the microbial population inside the reactor. Increasing the bed porosity to 91 % provided a continuous and cyclic production of hydrogen, whereas the lower bed porosities resulted in a reduced time of hydrogen production due to biomass accumulation, which resulted in a decreasing working volume.
Assuntos
Bactérias Anaeróbias/metabolismo , Materiais Biocompatíveis/química , Reatores Biológicos/microbiologia , Hidrogênio/metabolismo , Reologia/instrumentação , Sacarose/metabolismo , Aderência Bacteriana , Proliferação de Células , Desenho de Equipamento , Análise de Falha de Equipamento , Hidrogênio/isolamento & purificação , PorosidadeRESUMO
The present research examined the effects of initial substrate concentration and pH on the yield and productivity of hydrogen production by acidogenic fermentation. Assays were carried out at three different initial pH levels (5.5, 6.5 and 7.5) and three initial substrate concentrations (3, 5 and 10 g COD/L). Glucose was used as carbon source and the experiments were conducted at 37°C in batch tests, after a thermal pretreatment to eliminate methanogenic microorganisms. Conversions of glucose into hydrogen were between 16.75 and 27.25 percent of theoretical maximum, and high values of hydrogen productivity were obtained. An optimum value for the yield of glucose between initial pH of 6.3 and 3.7 g COD/L and productivity of the 5.95 H2/gVSS h and initial pH of 6.7 and 10 g COD/L were obtained from the response surface.
Assuntos
Concentração de Íons de Hidrogênio , Glucose/biossíntese , Glucose/metabolismo , Hidrogênio/isolamento & purificação , Digestão Anaeróbia/métodos , Fermentação , /métodosRESUMO
Our focus in the present study is to apply high specific surface area silica nanostructured porous materials (about 2200 m2/g, as synthesized, and 600-700 m2/g, after stabilization) to adsorb ammonia (NH3) for hydrogen storage and other chemical and pollution abatement applications. We describe here the synthesis, and characterization of these silica materials, and the adsorption study of N2 and NH3. These materials were obtained with the help of a modification of the Stöber-Fink-Bohn (SFB) method. The main change, made here to the SFB method, was the use of amines, i.e., triethylamine as catalysts instead of ammonium hydroxide. The silica materials have been characterized with the help of SEM and FTIR Spectrometry. The N2 adsorption study was carried out with the help of the Quantachrome-Autosorb-1 and the NH3 adsorption with the Quantachrome-Autosorb-l-C. The amount of hydrogen adsorbed in the form of NH3 in the studied silica samples at: P=760 [Torr] (1.01325 x 10(5) [Pa]), was 2 [wt.%] and the amount of hydrogen stored in the form of NH3 at about: P=7500 [Torr] (10.0 x 10(5) [Pa]), in the studied stabilized silica samples was 11 wt.%, a magnitude higher than the goal figure of 6.5 [wt.%] established by the United States of America, Department of Energy.
Assuntos
Amônia/química , Cristalização/métodos , Hidrogênio/química , Hidrogênio/isolamento & purificação , Nanoestruturas/química , Nanoestruturas/ultraestrutura , Nanotecnologia/métodos , Dióxido de Silício/química , Adsorção , Substâncias Macromoleculares/química , Teste de Materiais , Conformação Molecular , Tamanho da Partícula , Propriedades de SuperfícieRESUMO
Different experimental studies suggest that the presence of food in the alimentary tract, promote small intestinal absorption. The mechanism involved are not completely understood and might be related to motility changes or to humoral factors. Since studies have shown a decrease of small bowel motility after casein administration, the aim was to analyze the effect of this protein on small intestinal absorption and orocecal transit time. The hydrogen breath test was used to estimate d-xylose absorption. H2 production is dependent on the amount of this carbohydrate reaching the colon and therefore inversely proportional to d-xylose absorption. Six normal volunteers ingested 25 g d-xylose and 25 g de-xyllose + 30 g casein, and alveolar breath samples were obtained at 15 min intervals. Results: by adding casein to d-xylose solution a statistically significant decrease of maximal H2 concentration was observed from a mean of 40ñ11 ppm to a mean of 26ñ8 ppm. Similarly the area under the curve (which reflects the amount of xylose that was not absorbed) was also significantly decreased from a mean of 3281ñ1399 ppm to mean of 1394ñ700 ppm of H2. The orocecal transit time was significantly prolonged from 85.5ñ40 min to 112ñ38 min. Our results suggest that casein increased d-xylose absorption in normal subjects and that this effect might be related to a slower transit time
Assuntos
Humanos , Masculino , Feminino , Adulto , Xilose/metabolismo , Motilidade Gastrointestinal/efeitos dos fármacos , Caseínas/metabolismo , Testes Respiratórios , Hidrogênio/isolamento & purificaçãoRESUMO
Background: Boldo (peumus boldus Molina) is a widely used medicinal plant. However, its physiological effects are not well known. Recent studies in animals showed that certain components of boldo relax smooth muscle and prolong intestinal transit. Aim: to assess the effects of a dry boldo extract on oro cecal transit time in normal humans. Subjects and methods: twelve volunteers received 2.5 g of a dry boldo extract or a placebo (glucose) during 2 successive periods of 4 days. On the fourth day, 20 g of lactulose were administered and breath hydrogen was collected every 15 min. Oro cecal transit time was defined as the time in which breath hydrogen increased by 20 ppm over the fasting level. Results: oro cecal transit time was larger after dry boldo extract administration, compared to placebo (112.5ñ15.4 and 87ñ11.8 min respectively, paired t p<0.05). Conclusions: dry boldo extract prolongs oro cecal transit time, a possible explanation for its medicinal use