Topic
Trickling filter
About: Trickling filter is a research topic. Over the lifetime, 1098 publications have been published within this topic receiving 20219 citations.
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TL;DR: The mechanisms of this type of reactor are not yet fully understood as discussed by the authors, and most of the models proposed in the literature are totally or partially empirical and rather far from the actual complexity of the phenomena.
13 citations
TL;DR: In this paper, the influence of temperature and chemical oxygen demand (COD) loading on the nitrification and denitrification performance of the process is discussed through experimental and empirical modeling approaches.
Abstract: To cut down aeration power for nitrification, we constructed a biological nitrification–denitrification process with a trickling filter for nitrification and an anaerobic biological filter for denitrification. The influences of temperature and chemical oxygen demand (COD) loading on the nitrification and denitrification performance of the process are discussed in this paper through experimental and empirical modeling approaches. The model constants were determined by the experimental data of the process using municipal wastewater in Ryukoku University. Then, the influences of temperature and COD loading were estimated by the model. The COD levels required for NO3–N removal depended on both, the temperature and influent COD/NO3–N ratio. A lower temperature and higher influent COD/NO3–N ratio increased the COD requirement, because of the different responses between denitrifying bacteria and heterotrophic bacteria against temperature, COD, and NO3–N concentrations. In addition, our experimental system could satisfy the Japanese effluent standard at temperatures higher than 12 °C. The dissolved nitrogen (DN) concentration in the final effluent was more strongly affected by the NH4–N discharged from the trickling filter than it was by the residual NO3–N in the effluent from the denitrification tank. Therefore, the enhancement of the nitrification efficiency in the trickling filter was inferred to enhance the nitrogen removal efficiency. To prevent a low nitrogen removal efficiency at temperatures lower than 15 °C, it was necessary to set the low hydraulic loading.
13 citations
TL;DR: Evidence is provided that the removal of organic and inorganic particulate matter in a TF bioreactor follows a first-order bioflocculation rate equation and the statistical analysis of data obtained from the pilot TF fits the dispersion model to suspended solids and PCOD remaining in the pilotTF.
Abstract: Understanding that there is a significant presence of extracellular polymeric substances at the biofilm/wastewater interface and that the primary constituent of chemical oxygen demand (COD) in domestic wastewaters is organic particulates, this research describes the kinetics of particulate removal in a pilot-scale trickling filter (TF) and the role of bioflocculation in the removal process. Recent research has described the role of bioflocculation on particulate COD (PCOD) removal in suspended growth biological wastewater treatment systems. However, no research pertaining to PCOD removal by bioflocculation in attached growth systems was identified prior to this study. For this study, experiments were conducted using both bench- and pilot-scale biofilm reactors and provided evidence that the removal of organic and inorganic particulate matter in a TF bioreactor follows a first-order bioflocculation rate equation. The statistical analysis of data obtained from the pilot TF fits the dispersion model to suspended solids and PCOD remaining in the pilot TF.
13 citations
TL;DR: In this article, the ability of a pilot-scale hybrid system to treat real (non-synthetic) winery wastewater was evaluated using an attached growth bioreactor and a constructed wetland.
Abstract: The objective of this work was to determine the ability of a pilot-scale hybrid system to treat real (non-synthetic) winery wastewater. The experimental treatment system consisted of two stages: An attached growth pilot-scale bioreactor (biological trickling filter with plastic support material) was initially used to remove a significant amount of dissolved chemical oxygen demand (d-COD) from winery wastewater, and then a pilot-scale, horizontal subsurface flow constructed wetland (CW) was examined as a post-treatment step for further d-COD removal. Results from the biofilter revealed that the recirculation rate of 1.0 L/min lead to higher d-COD removal rates than that of 0.5 L/min for all feed d-COD concentrations tested (3500, 7500, 9000 and 18,000 mg d-COD/L). Experiments in the CW were performed using feed d-COD concentrations of about 1500 mg/L (equivalent to biofilter effluent when initial filter feed d-COD concentrations are 18,000 mg/L). The wetland polishing stage managed to further remove d-COD and produced effluent concentrations below current legislation limits for safe disposal. Furthermore, the presence of zeolite in CW (one third of the length of CW) enhanced ammonium removal. The experimental results indicate that the combination of a biological trickling filter and a constructed wetland could effectively treat effluents originating from small wineries typical of the Mediterranean region.
13 citations
TL;DR: It was found that BDOC fraction was independent of the initial DOC concentration and was dependent on the source of wastewater and/or the types of wastewater treatment, while the amount of BDOC in the wastewater depended not on the concentration of DOC, but on the effectiveness of pretreatment.
Abstract: Biodegradable dissolved organic carbon (BDOC) analyses and abiotic adsorption of dissolved organic carbon (DOC) from different wastewater effluent were conducted to evaluate biotic and abiotic removal mechanisms as a function of the initial DOC concentration and source of DOC using soil batch reactors. To obtain high DOC concentrations, a laboratory-scale reverse osmosis unit was used. It was found that BDOC fraction was independent of the initial DOC concentration and was dependent on the source of wastewater and/or the types of wastewater treatment. The BDOC fractions varied from 9 to 73%. Trickling filter effluent (Tucson, Arizona) showed the highest BDOC, ranging from 65 to 73% biodegradable, while wastewater treated by the soil aquifer treatment (SAT) (NW-4) was found to be most refractory, with DOC removals of 9 to 14%. For nitrified/denitrified tertiary effluent (Mesa, Arizona) and secondary effluent (Scottsdale, Arizona), 36 to 42% removal of DOC was observed during the BDOC test. The amount of BDOC in the wastewater depended not on the concentration of DOC, but on the effectiveness of pretreatment. Abiotic adsorption capacity of wastewater effluent varied from 6 to 18%. Molecular weight distribution analyses showed that more than 50% of DOC in the Scottsdale concentrate had a molecular weight of less than 1000 Da, and no significant change in distribution profiles occurred after approximately 12% abiotic adsorption with both soils with acclimated microorganisms (SAT soil) and soils without acclimated microorganisms (non-SAT soils). Hence, preferential adsorption was not observed and the presence of acclimated microbes did not influence adsorption.
13 citations