Oscar Monroy

Multiple syntrophic interactions in a terephthalate-degrading methanogenic consortium

Terephthalate (TA) is one of the top 50 chemicals produced worldwide. Its production results in a TA-containing wastewater that is treated by anaerobic processes through a poorly understood methanogenic syntrophy. Using metagenomics, we characterized the methanogenic consortium inside a hyper-mesophilic (that is, between mesophilic and thermophilic), TA-degrading bioreactor. We identified genes belonging to dominant Pelotomaculum species presumably involved in TA degradation through decarboxylation, dearomatization, and modified β-oxidation to H2/CO2 and acetate. These intermediates are converted to CH4/CO2 by three novel hyper-mesophilic methanogens. Additional secondary syntrophic interactions were predicted in Thermotogae, Syntrophus and candidate phyla OP5 and WWE1 populations. The OP5 encodes genes capable of anaerobic autotrophic butyrate production and Thermotogae, Syntrophus and WWE1 have the genetic potential to oxidize butyrate to CO2/H2 and acetate. These observations suggest that the TA-degrading consortium consists of additional syntrophic interactions beyond the standard H2-producing syntroph–methanogen partnership that may serve to improve community stability.

Accumulation of intermediates in a denitrifying process at different copper and high nitrate concentrations

NO2- accumulation occurred in an upflow anaerobic sludge blanket reactor at 500, 1000 and 1500 mg NO3- -N/l, but not after copper in the medium was increased to 28 μg Cu2/l. N2O release was not avoided even with 56 μg Cu2/l, at 1500 and 2500 mg NO3- -N/l and reached 251 mg N2O-N/l•d.

The impact of ammonia nitrogen concentration and zeolite addition on the specific methanogenic activity of granular and flocculent anaerobic sludges.

This work presents the effect of ammonia nitrogen concentration and zeolite addition on the specific methanogenic activity (SMA) of different anaerobic sludges with various physical structures (granular and flocculent), operating in batch conditions. Piggery, malting production and urban sludges derived from full-scale anaerobic reactors were tested in the experiment as the source of inoculum in batch digesters. It was found that piggery sludge was the most affected by the increase of ammonia nitrogen concentration while malting producing and municipal sludges were less affected. In general, the addition of zeolite at doses in the range of 0.01–0.1 g/g VSS reduced the inhibitory effect of N-NH4 + for piggery sludge (P.S.). For this sludge, the propionic:acetic ratio increased when the concentration of N-NH4 + increased, indicating that methanogenesis was affected. Finally, a study of the microbial population involved in this study for P.S. by using 16S rRNA based molecular techniques revealed a presence of microorganisms following the order: Methanococcaceae > Methanosarcina > Methanosaeta.

Influence of ammonium on the performance of a denitrifying culture under heterotrophic conditions

The effect of ammonium on a denitrifying reactor of the upflow anaerobic sludge blanket type was studied. At a constant nitrate loading rate (2500 mg NO3−-N/[L · d]), using acetate as organic electron donor and at a C/NO3−-N ratio of 1.23, an increase in the N2 production rate was observed when the ammonium loading rate was increased (25, 250, and 500 mg NH4+-N/[L · d]). Dissimilatory nitrate reduction to ammonium (DNRA) was not observed, and the N2 production efficiency was increased from 84 to 100% or higher. Since NH4+ in the output was lower than in the input, it was suggested that it was used for nitrate reduction. At constant NH4+-N/NO3−-N and C/NO3−-N ratios of 0.2 and 1.63, respectively, the molecular nitrogen production rate was increased at 300 and 500 mg NH4+-N/(L · d), whereas at 200 mg NH4+-N/(L · d) DNRA took place probably owing to culture conditions of low reductive power. Molecular nitrogen production was not observed under autotrophic conditions, and the addition of acetate to the culture recovered its high nitrogen removal rate. Experimental results and balances indicated that the consumed ammonium was used as an additional reductive source.

Phormidium treatment of anaerobically treated swine wastewater

Abstract The ability of hormidium sp. to grow in anaerobically digested swine waste medium and the use of this organism for tertiary biotreatment of wastewater was evaluated. In addition to monitoring the growth of Phormidium, the removal of total phosphorus (total P), orthophosphate (PPO4) nitrates (NNO3) and ammonium (NNH4) were also measured. Dilutions from 50 to 10% of the secondary effluent were tested and results compared with Dautas medium which was used as a control. Results obtained at 25% dilution in 21. graduated cylinders were: 100% removal of orthophosphate, 87% of nitrate, 68% of total phosphate and 48% of ammonium ion. Removals obtained in a carrousel type reactor were: 48% for orthophosphate, 30% for nitrate, 63% for total phosphorus and 100% for ammonium ion. These removals were higher in both cases than those obtained in Dautas medium. The total ammonium uptake for the 25% dilution by Phormidium sp. was 7.65 mg/l-d in the glass cylinders and 19.93 mg/l-d in the carrousel reactor.

Evolution of microbial activities and population in granular sludge from an UASB reactor

SummaryWith granular sludges grown in an UASB reactor fed with a mixture of acetate and proplonate, it is shown that (I) growth of proplonate-utilizing bacteria is responsible for the increase of the VSS content of the granular sludge, acetoclastic microfiora did not grow or little, (II) there is not a stolchlometric relationship between substrate removal and observed methane production, and (III) contrary to the common practice the best way to present data on bacterial concentrations in sludges is: bacteria/g VSS, which will provide a reliable basis for comparisons between different works from various authors.

Development of biofilms in anaerobic reactors

The development of biofilms in polyethylene sheets and particles was studied using downflow reactors with synthetic nutrient media made up of a mixture of volatile fatty acids. Results suggest a preferential immobilization of acetoclastic organisms in the inner space of the surfaces and the colonization by the butyrotrophic bacteria in the outer layers. After 101 days the bioparticles reached a specific acetociastic activity of 72.45μmol acetic acid/μg protein ·h while the biofilms had 58.80 μmol acetic acid/μg protein attached ·h. Due to the low density of the polyethylene particles low fluidization velocities would be needed (2m/h) in a downflow fluidized bed reactor.

Biological wastewater treatment for removal of polymeric resins in UASB reactor: influence of oxygen.

The biological elimination of polymeric resins compounds (PRC) such as acrylic acid and their esters, vinyl acetate and styrene under methanogenic and oxygen-limited methanogenesis conditions was evaluated. Two UASB reactors (A and B) were used and the removal of the organic matter was studied in four stages. Reactor A was used as methanogenic control during the study. Initially both reactors were operated under methanogenic conditions. From the second stage reactor B was fed with 0.6 and 1 mg/L.d of oxygen (O2). Reactor A had diminution in chemical oxygen demand (COD) removal efficiency from 75+/-4% to 37+/-5%, by the increase of PRC loading rate from 750 to 1125 mg COD/L.d. In this reactor there was no styrene elimination. In reactor B the COD removal efficiency was between 73+/-5% and 80+/-2%, even with the addition of O2 and increase of the PRC loading rate, owing to oxygen being used in the partial oxidation of these compounds. In this reactor the yields were modified from 0.56 to 0.40 for CH4 and from 0.31 to 0.60 for CO2. The O2 in low concentrations increased 40.7% the consumption rates of acrylic acid, methyl acrylate and vinyl acetate, allowing styrene consumption with a rate of 0.103 g/L.d. Batch cultures demonstrated that under methanogenic and oxygen-limited methanogenesis conditions, the glucose was not used as an electron acceptor in the elimination of PRC.

Biodegradation of 2-chlorophenol (2CP) in an anaerobic sequencing batch reactor (ASBR)

The aim of this study is to contribute to the knowledge about anaerobic digestion of 2-chlorophenol (2CP) in an anaerobic sequencing batch reactor (ASBR). Two reactors were set up (ASBR(A) and ASBR(B)). The ASBR(A) was fed with 2-chlorophenol (28-196 mg 2CP-C/L) and no other exogenous electron donor. The ASBR(B) was fed with a mixture of 2CP (28-196 mg 2CP-C/L) and phenol (28-196 mg phenol-C/L) as an electron donor. The process evaluation was conducted by three means: first by substrate consumption efficiency (E(2CP)), second, by biogas yield (Y(biogas-C/2CP-C)) and third, by the specific consumption rates (q(2CP)) as response variables. The 2CP consumption efficiency (90 ± 0.4%) was not influenced by the increase in the concentrations tested. In both reactors ASBR(A) and ASBR(B), both concentration as well as speed increased. Concentration increased from 28 to 114 mg 2CP-C/L. The specific consumption rate (q(2CP)) values were fivefold higher. However, a decrease of 37% was observed at 140 mg 2CP-C/L and one of 72% at 196 mg 2CP-C/L. The biogas yields (0.80 ± 0.06) remained stable in both reactors. In both reactors the biogas yield decreased to 78 ± 3% at 196 mg 2CP-C/L. We might assume this decrease was due to the accumulation of VFA. Finally, poor sludge settleability was determined only in the SBR(B) reactor at 140 and 196 mg 2CP-C/L. An increase was observed in both SVI ≤ 140 ± 5 mL/g and over exopolymeric protein ≤120 mg EP/L.

The effect of vinyl acetate in acetoclastic methanogenesis

The influence of vinyl acetate (VA) in the methanogenesis was evaluated, by using an upflow anaerobic sludge blanket reactor of 1.5L. The reactor was operated at 33.5 g/L volatile suspended solids to 30±2 °C, a hydraulic residence time of 1 day, an organic loading rate of 1 kgCOD/m3/d of two different mixtures of VA and glucose. The VA was methanized to 81% when its proportion was of 10% into reactor loading rate, when VA proportion increased to 25%, the methane production rate decreased to 62% and the acetate production rate increased almost 8 times. These results indicated that VA was only hydrolyzed and glucose was not used as a co-substrate. The effect of glucose on VA methanogenic degradation was evaluated through batch reactors of 60 mL, concluding that the glucose supported the methanogenesis without favoring the VA elimination. On the other hand, the results of the sludge from the reactor in the presence of VA demonstrated that VA caused an irreversibly inhibition of acetoclastic methanogenesis when the anaerobic sludge was exposed to this compound.