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| Author(s): |
Gunther Brucha
Total Authors: 1
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| Document type: | Doctoral Thesis |
| Press: | São Carlos. |
| Institution: | Universidade de São Paulo (USP). Escola de Engenharia de São Carlos (EESC/SBD) |
| Defense date: | 2007-10-01 |
| Examining board members: |
Rosana Filomena Vazoller;
Márcia Helena Rissato Zamariolli Damianovic;
Eugenio Foresti;
Dácio Roberto Matheus;
Vivian Helena Pellizari
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| Advisor: | Rosana Filomena Vazoller |
| Abstract | |
The research presented here aimed to determine the optimal nutritional conditions for the use of sediment from the Santos-São Vicente estuary in the state of São Paulo, Brazil, as an inoculum for a horizontal-flow anaerobic immobilized biomass reactor (HAIB) applied to the anaerobic degradation of pentachlorophenol (PCP), seeking to apply the technology on the real scale and to identify the microbial groups involved in the process. To this end, sediment with methanogenic characteristics from the Santos-São Vicente estuary was used. The microorganisms from the estuarine sediment were enriched under methanogenic and halophilic conditions, aiming to use the sediment as an inoculum in nutritional assays and in the operation of HAIB reactors. Biota saline culture medium supplemented with glucose and formiate was used to develop the halophilic methanogenic microbial community. PCP degradation tests were carried out previously under different concentrations of nitrogen and phosphorus in order to gain a better understanding of the optimal N:P ratio for the anaerobic process. The findings on the microbial diversity of the domain Bacteria at the various ratios tested here indicated the selection of distinct microbial communities, resulting in different PCP degradation velocities. The N:P ratio utilized was 10:1 since it presented the best results not only in terms of faster PCP degradation than the other ratios but also highest diversity of microorganisms. The HAIB reactor was then operated with a mean inflow of approximately 44 mL/hour, using the biota saline mineral medium with a COD:N:P ratio of 1000:130:45 in R1 (reactor 1) and a COD:N:P ratio of 1000:10:1 in R2. Two distinct strategies were adopted to start up the reactors. In R1 PCP was added at an initial concentration of 10.0 mg/L for 100 days, causing destabilization of the methanogenesis and accumulation of PCP, requiring a 90-day intervention for the reactor\'s recovery. To start up R2, the PCP concentration was increased gradually from 0.5 mg/L to 12.0 mg/L for 52 days. After methanogenesis was established, R1 was fed for 270 days with 5.0 mg of PCP/L, followed by 41 days with 8.0 mg/L and 59 days with 12 mg/L. The mass balance in R1 indicated that 0.52% of the added PCP exited through the reactor\'s outflow and that adsorption of the system did not occur. 22.34 mg of 2,4,6 TCP, an intermediary of PCP degradation, was adsorbed in the bioparticles. The results of the analysis of microbial diversity indicated a change in the microbial community of the domain Bacteria along the operational period, with fluorescent bacilli morphologies resembling Methanobacterium sp present in the reactor. PCP degradation in R2 was 100% up to a concentration of 10.0 mg/L. At the end of the phase with 12.0 mg PCP/L, the effluent concentration was 1.4 mg PCP/L, with a mean removal efficiency of 93.2 \'+ or -\' 5,5%. 2,4,6 TCP was the main intermediary in the reactor\'s effluent. 4.06% of the PCP added to the system was found in the effluent and 15.94% was absorbed in the bioparticles of the reactor. Therefore, it was concluded that 80% of the added PCP underwent microbial anaerobic degradation. The presence of Methanocalcullus and Methanosaeta microorganisms in the final operating phase of R2, which was determined in the collected sediment, was considered fundamental for maintaining the reactor\'s stability. This discovery contributes to the body of information about the real microbial diversity of tropical ecosystems, above all in anaerobic habitats, and about the nutritional conditions and procedures involved in confining these microorganisms in reactors and using them in bioremediation processes. (AU) | |