RESUMO
There is a great interest for replacing petroleum-derived chemical processes with biological processes to obtain fuels and plastics from industrial waste. Accordingly, Rhodopseudomonas species are capable of producing hydrogen and polyhydroxybutyrate. Culture conditions for production of both hydrogen and polyhydroxybutyrate with Rhodopseudomonas pseudopalustris (DSM 123) from tequila vinasses were analyzed. The production of hydrogen using tequila vinasses was higher with respect to two synthetic media. Replacing the headspace with N2 increased the production of hydrogen with respect to Argon, while a higher concentration of polyhydroxybutyrate was achieved using Argon as compared to N2. A higher concentration of phosphates increased the production of hydrogen (250 mL), while the highest concentration of polyhydroxybutyrate (305 mg/L) was accomplished when the bacteria were cultivated only with phosphates contained in tequila vinasses. This study revealed that the culture conditions for Rhodopseudomonas pseudopalustris (DSM 123) for production of hydrogen are the opposite of those for production of polyhydroxybutyrate.
Assuntos
Rodopseudomonas , Hidrogênio , Resíduos Industriais/análise , NutrientesRESUMO
Vinasses from the tequila industry are wastewaters with highly elevated organic loads. Therefore, to obtain value-added products by yeast fermentations, such as 2-phenylethanol (2-PE) and 2-phenylethylacetate (2-PEA), could be interesting for industrial applications from tequila vinasses. In this study, four yeasts species (Wickerhamomyces anomalus, Candida glabrata, Candida utilis, and Candida parapsilosis) were evaluated with two different chemically defined media and tequila vinasses. Differences in the aroma compounds production were observed depending on the medium and yeast species used. In tequila vinasses, the highest concentration (65 mg/L) of 2-PEA was reached by C. glabrata, the inhibitory compounds decreased biomass production and synthesis of 2-PEA, and biochemical and chemical oxygen demands were reduced by more than 50 %. Tequila vinasses were suitable for the production of 2-phenylethylacetate by the shikimate pathway. A metabolic network was developed to obtain a guideline to improve 2-PE and 2-PEA production using flux balance analysis (FBA).
RESUMO
A hybrid (continuous-discrete) cascade control is proposed to regulate both, volatile fatty acids (VFA) and chemical oxygen demand (COD) concentrations in two-stage (acidogenic-methanogenic) anaerobic digestion (TSAD) processes. The outer loop is a discrete controller that regulates the COD concentration of the methanogenic bioreactor by using a daily off-line measurement and that modifies the set-point tracked by inner loop, which manipulates the dilution rate to regulate the VFA concentration of the acidogenic bioreactor, estimated by continuous on-line conductivity measurements, avoiding acidification. The experimental validation was conducted in a TSAD process for the treatment of tequila vinasses during 110days. Results showed that the proposed cascade control scheme was able to achieve the VFA and COD regulation by using conventional measurements under different set-point values in spite of adverse common scenarios in full-scale anaerobic digestion processes. Microbial composition analysis showed that the controller also favors the abundance and diversity toward methane production.
Assuntos
Análise da Demanda Biológica de Oxigênio , Reatores Biológicos , Ácidos Graxos Voláteis/química , Anaerobiose , Reatores Biológicos/microbiologia , Ácidos Graxos Voláteis/análise , Metano/análiseRESUMO
This study examines the performance of an anaerobic fixed-film bioreactor under seasonal operating conditions prevailing in medium and small size Tequila factories: start-up, normal operation and particularly, during the restart-up after a long stop and starvation period. The proposed start-up procedure attained a stable biofilm in a rather short period (28 days) despite unbalanced COD/N/P ratio and the use of non-acclimated inoculum. The bioreactor was restarted-up after being shut down for 6 months during which the inoculum starved. Even when biofilm detachment and bioreactor clogging were detected at the very beginning of restart-up, results show that the bioreactor performed better as higher COD removal and methane yield were attained. CE-SSCP and Q-PCR analyses, conducted on the biofilm prokaryotic communities for each operating condition, confirmed that the high COD removal results after the bioreactor clogging and the severe starvation period were mainly due to the stable archaeal and resilient bacterial populations.