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Récupération de la matière organique biodégradable présente dans l'effluent d'un MBBR à forte charg

Posted on:2016-05-23Degree:M.A.ScType:Thesis
University:Ecole Polytechnique, Montreal (Canada)Candidate:Brosseau, CatherineFull Text:PDF
GTID:2471390017480404Subject:Civil engineering
Abstract/Summary:
High-rate processes are receiving great interest due to their potential to favor the energy balance of water resource recovery facilities (WRRFs) either for their design or retrofit. Anaerobic digestion is a process that allows the valorization of organic biodegradable matter contained in sludge into biogas. This process also produces a stabilized sludge named digestate or biosolids that can be reused for agriculture purposes.;This project proposed a secondary treatment train composed of a high-rate moving bed biofilm reactor (HR-MBBR) to biotransform colloidal and soluble biodegradable organics into particulate matter followed by an enhanced and compact physico-chemical separation process to recover mainly particulate organics and a part of the colloidal matter. A high-rate biological process operated at a low hydraulic retention time aimed at transforming colloidal and soluble fractions of organic matter into a particulate fraction for recovery by downstream separation process. The HR-MBBR effluent solids are known for their poor settleability, therefore requiring an efficient separation process downstream to ensure their recovery and to meet the effluent discharge regulations.;The global objective of this project was to maximize the recovery of organic biodegradable matter for valorization into biogas by anaerobic digestion with an innovative treatment train combining an HR-MBBR and a separation process. The specific objectives of this report were 1) to characterize the HR-MBBR effluent solids and 2) to determine the efficiency of several physico-chemical separation processes combined with unbiodegradable or natural based coagulants and polymers.;Effluents of lab-scale HR-MBBR fed with a synthetic soluble or domestic wastewater influent and the effluent of a full-scale HR-MBBR were used to evaluate the efficiency of separation processes adapted at bench-scale in jar-tests experiments. The processes studied were conventionnal settling, ballasted flocculation, dissolved air flotation and an innovative enhanced flotation process. Unlike conventional settling and dissolved air flotation, ballasted flocculation and enhanced flotation use a ballasted or flotation agent to accelerate the sludge settling or flotation rate.;The original scientific hypothesis of this project is that the combination of enhanced flotation and natural based chemicals can meet a target total suspended solids (TSS) concentration of less or equal to 10 mg TSS/L in the clarified effluent of an HR-MBBR. The separation processes efficiencies were evaluated based on their TSS recoveries. Monitoring the chemical oxygen demand (COD) fractions allowed to better understand the underlying mechanisms of organic matter biotransformation and capture throughout the proposed treatment train.;The concentration of solids expressed in TSS concentration in the MBBR effluent with a synthetic soluble influent was kept very low, from 27 to 61 mg TSS/L, which is about 2 to 9 times less than the expected concentration for an MBBR fed with domestic wastewater. Without the presence of particulate matter in the influent, the particulate matter in the MBBR effluent represented only the production of biomass detached by the shearing forces between the carriers. The TSS concentration and the efficiency of colloidal and soluble matter biotransformation into particulate matter increased with the MBBR hydraulic retention time.;Wide volumetric particle size distributions ranging from 5 to 1000 mum in the lab-scale MBBR effluent were observed with a higher proportion of particles larger than 100 mum for a synthetic feed, and a higher proportion of small size particles of 30 mum for a domestic wastewater feed. The presence of lots of small size particles was attributed to unsettleable solids in the influent unchanged in the reactor. Despite the high proportion of large size particles for the MBBR with a synthetic feed, poor settleability of effluent solids was observed as static settling could only achieve TSS recoveries between 35 to 78%. Hence, coagulating agents were necessary to enhance the solids recovery.;The combination of the innovative enhanced flotation process and unbiodegradable chemicals allowed to achieve TSS recovery efficiencies up to 97%. The enhanced flotation efficiency was reduced when using natural based chemicals, especially the natural based polymer which was not suited to treat waters with such high TSS concentrations.;The hypothesis of the residual TSS concentration of 10 mg TSS/L was verified for half of the HR-MBBR operating conditions and the recovery efficiency did not seem to be influenced by the reactor hydraulic retention time, organic loading rate and temperature. More experiments are needed to confirm the effect of these parameters on TSS recovery efficiency.;Although natural based chemicals reduced the coagulation and flocculation efficiency, they allowed a decrease in sludge production, which can represent a significant cost benefit. These chemicals resulted in an increase of 33 to 60% of the total COD of the MBBR effluent, compared to the unbiodegradable chemicals which only contributed about 2%.;Natural based chemicals are recommended over unbiodegradable ones to promote the use of high biodegradability potential chemicals and to reduce the production of chemical sludge. However, to offset the increase of total COD, it may be required to add a treatment downstream to meet target secondary treatment COD concentration.;Conventionnal settling and ballasted flocculation offered similar TSS recovery efficiencies to enhanced flottation (88% TSS recovery efficiency). The efficiency was reduced by 34% when using the dissolved air flotation process, much lower than the ones expected for such a separation process. The efficiency reduction was attributed to non-optimized and unadapted flotation lab-scale setups to treat medium strength wastewater.;A similar innovative treatment train is currently being tested at pilot-scale in order to evaluate its carbon footprint and its potential to be eventually transposed to full-scale. Furthermore, the biodegradability and the biochemical methane production of the natural based chemicals are being determined.;This project allowed to determine the potential of the innovative enhanced flotation process to recover the HR-MBBR solids when combined with natural based chemicals which are currently not often used in wastewater treatment for resource recovery.
Keywords/Search Tags:MBBR, Recovery, Natural based chemicals, Effluent, Process, TSS, Solids, Hydraulic retention time
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