Biological nitrogen and organic matter removal from tannery wastewater in pilot plant operations in Ethiopia

A whole-cell biotransformation system for the conversion of d-fructose to d-mannitol was developed in Escherichia coli by constructing a recombinant oxidation/reduction cycle. First, the mdh gene, encoding mannitol dehydrogenase of Leuconostoc pseudomesenteroides ATCC 12291 (MDH), was expressed, effecting strong catalytic activity of an NADH-dependent reduction of d-fructose to d-mannitol in cell extracts of the recombinant E. coli strain. By contrast whole cells of the strain were unable to produce d-mannitol from d-fructose. To provide a source of reduction equivalents needed for d-fructose reduction, the fdh gene from Mycobacterium vaccae N10 (FDH), encoding formate dehydrogenase, was functionally co-expressed. FDH generates the NADH used for d-fructose reduction by dehydrogenation of formate to carbon dioxide. These recombinant E. coli cells were able to form d-mannitol from d-fructose in a low but significant quantity (15 mM). The introduction of a further gene, encoding the glucose facilitator protein of Zymomonas mobilis (GLF), allowed the cells to efficiently take up d-fructose, without simultaneous phosphorylation. Resting cells of this E. coli strain (3 g cell dry weight/l) produced 216 mM d-mannitol in 17 h. Due to equimolar formation of sodium hydroxide during NAD⁺-dependent oxidation of sodium formate to carbon dioxide, the pH value of the buffered biotransformation system increased by one pH unit within 2 h. Biotransformations conducted under pH control by formic-acid addition yielded d-mannitol at a concentration of 362 mM within 8 h. The yield Y _{D-mannitol/D-fructose}was 84 mol%. These results show that the recombinant strain of E. coli can be utilized as an efficient biocatalyst for d-mannitol formation.     

Anaerobic treatment of wastewater with high salt content from a pickled-plum manufacturing process

Anaerobic treatment of wastewater with a high salt content generated during a pickled-plum manufacturing process (TOC, 14g/l; ash, 150g/l; pH 2.7, hereafter called pickled-plum effluent) was investigated for its effect on the high salt content of the wastewater. The synthetic wastewater, including NaCl up to 30g/l, was treated anaerobically by a draw and fill method (treatment temperature, 37°C; volumetric loading rate of organic matter, 2g/l·d). The TOC removal efficiency and rate of gas evolution then gradually decreased as salt content increased, although stable operation was maintained. At NaCl concentrations above 30g/l, TOC removal efficiency decreased rapidly and stable operation could not be maintained. Five-fold-diluted pickled-plum effluent was treated by the same method at a volumetric TOC loading rate of 2.9g/l·d with a TOC removal efficiency of 71%. Five-fold-diluted pickled-plum effluent was also treated in an anaerobic fluidized-bed reactor (AFBR) at a maximum volumetric TOC loading rate of 3.0g/l·d, which gave almost the same results as the draw and fill method. However, ten-fold-diluted pickled-plum effluent could be treated in the AFBR at a maximum volumetric TOC loading rate of 11.1g/l·d with a TOC removal efficiency of 84.6%. The red pigment in the pickled-plum effluent was completely decolorized by the anaerobic treatment.     

Nitrogen removal from wastewater with a low COD/N ratio at a low oxygen concentration

The goal of the study was to determine the effectiveness of nitrification and denitrification and the kinetics of ammonia removal from a mixture of wastewater and anaerobic sludge digester supernatant in an SBR at limited oxygen concentration. In addition, the COD removal efficiency and sludge production were assessed.In the SBR cycle alternating aerobic and anaerobic phases occurred; in the aeration phase the dissolved oxygen (DO) concentration was below 0.7 mg O₂/L. The low DO concentration did not inhibit ammonia oxidation-nitrification and the efficiency was ca. 96-98%. However, a relatively high COD concentration in the effluent was detected. The values of K_m and V_max, calculated from the Michaelis-Menten equation, were 43 mg N-NH₄/L and 15.64 mg N-NH₄/L h, respectively. Activated sludge production was almost stable (0.62-0.66 g MLVSS/g COD). A high net biomass production resulted from a low specific biomass decay rate of 0.0015 d⁻¹.     

含氮有机物在污水处理过程中的生物转化机制与模型研究进展

随着市政污水处理厂的提标改造,出水总氮浓度逐渐降低,但溶解性有机氮(Dissolved Organic Nitrogen,DON)在总氮中的占比却越来越高,对含氮消毒副产物的生成和受纳水体富营养化的潜在贡献不可忽视.正因如此,近年来有关污水处理系统中DON的研究不断增加.本文重点综述了污水处理厂DON特征、生成转化规律...     

Anaerobic treatment of low-strength municipal wastewater by a two-stage pilot plant under psychrophilic conditions

A two-stage anaerobic treatment pilot plant was tested for the treatment of raw domestic wastewater under temperatures ranging from 21 to 14 degrees C. The plant consisted of a hydrolytic upflow sludge bed (HUSB) digester (25.5m3) followed by an upflow anaerobic sludge blanket (UASB) digester (20.36m3). The hydraulic retention time (HRT) varied from 5.7 to 2.8h for the first stage (HUSB digester) and from 13.9 to 6.5h for the second stage (UASB digester). Total suspended solids (TSS), total chemical oxygen demand (TCOD), and biochemical oxygen demand (BOD) removals ranged from 76% to 89%, from 49% to 65%, and from 50% to 77%, respectively, for the overall system. The percentage of influent COD converted to methane was 36.1%, the hydrolysis of influent volatile suspended solids (VSS) reached 59.7% and excess biomass was 21.6% of the incoming VSS. Plant performance was influenced by the wastewater concentration and temperature, yet better results were obtained for influent COD higher than 250mg/l.     

Anaerobic treatment of low-strength wastewater with a high fraction of particulate matter in an unconventional two-phase ASBRs system

The results of a two-phase anaerobic system using anaerobic sequencing batch reactors (ASBRs), treating low-strength wastewater (COD ∼ 500 mg/L) with a high fraction of particulate organic matter (70%, COD basis), are presented. Two reactors in series were used; the first one was hydrolytic–acidogenic, while the second one was methanogenic. This configuration was proposed to promote high efficiency solids removal. During the experiment, 69% and 50% efficiencies of total COD removal were obtained for OLRs of 0.63 and 1.22 kgCOD/(m³ d), respectively. Values of the solubilized organic fraction (SOF) achieved in the hydrolytic–acidogenic reactor were within the range of 0.3–0.6 gCOD_solubilized/gpCOD_removed, and the average acidified organic fraction (AOF) was 0.6 gCOD_VFA-produced/gsCOD_fed. The methanogenic reactor had a VFA removal fraction (VFARF) between 0.4 and 0.6 gCOD_VFA-removed/gCOD_VFA-fed for the OLR of 0.63 and 1.22. The two-phase ASBR system is suitable, and can be implemented, for the anaerobic treatment of this kind of wastewater.     

Reuse of effluent water from a municipal wastewater treatment plant in microalgae cultivation for biofuel production

This study assessed the usability of effluent water discharged from a secondary municipal wastewater treatment plant for mass cultivation of microalgae for biofuel production. It was observed that bacteria and protozoa in the effluent water exerted a negative impact on the growth of Chlorella sp. 227. To reduce the effect, filtration or UV-radiation were applied on the effluent water as pre-treatment methods. Of all the pretreatment options tested, the filtration (by 0.2 μm) resulted in the highest biomass and lipid productivity. To be comparable with the growth in the autoclaved effluent water, the filtration with a proper pore size filter (less than 0.45 μm) or UV-B radiation of a proper dose (over 1620 mJ cm⁻²) are proposed. These findings led us to conclude that the utilization can be realized only when bacteria and other microorganisms are greatly reduced or eliminated from the effluent prior to its use.     

Anaerobic treatment of starch-containing wastewater using a plate-column reactor

An anaerobic plate-column reactor, developed to retain a high concentration of biomass, was studied using starch-containing synthetic wastewaters with regard to its start-up profile and the effects of TOC-loading rate, hydraulic retention time (HRT), and temperature in a steasy state. Each operation was started up at an initial biomass concentration of ca. 0.5 mg-N/ml (ca. 5 mg-VSS/ml), 20°C, an HRT of 30 h, and a TOC-loading rate of 0.8 g/l/d. The removal defficiency of dissolved organic carbon exceeded 90% after 29 d. The efficiency reached a steady state at 98% removal after 116 d. The biomass concentration in the reactor was 2.3 mg-N/ml after 154 d. Circulation of effluent at a ratio of 1 gave a lower removal efficiency and a lower biomass concentration than the same reactor without circulation. The effect of TOC-loading rate was studied at an HRT of 30 h, 20°C, and removal efficiencies were found 91% at 1.6 g/l/d and 77% at 3.2 g/l/d. The effect of HRT was studied at a TOC-loading rate of 0.8 g/l/d, 20°C, and removal efficiencies 91% at an HRT of 12 h and 72% at an HRT of 6 h.     

Anaerobic treatment of distillery wastewater from barley-Shochu making by UASB

Distillery wastewater from barley-shochu making was anaerobically treated by a single upflow anaerobic sludge blanket (UASB), and stable operation at a volumetric TOC loading rate of 3 g/l·d could be attained by diluting raw wastewater to give a TOC concentration of less than 6,000 mg/l (18,000 mg/l as CODer). When the distribution of the concentrations of aliphatic acids at various levels within the reactor was investigated, it was found that the methanogenic gasification reaction did not occur in the sludge blanket of the reactor. Distillery wastewater from barley-shochu making with various TOC concentrations was preliminary adjusted to pH 7 and treated by a single passage without circulation of effluent to the bottom of the reactor. As a result, a maximum TOC removal rate (V_max) of 28.5 g/l·d and a saturation constant (K_s) of 0.63 g/l were obtained.     

Genetic diversity and composition of a plasmid metagenome from a wastewater treatment plant

Plasmid metagenome nucleotide sequence data were recently obtained from wastewater treatment plant (WWTP) bacteria with reduced susceptibility to selected antimicrobial drugs by applying the ultrafast 454-sequencing technology. The sequence dataset comprising 36,071,493 bases (346,427 reads with an average read length of 104 bases) was analysed for genetic diversity and composition by using a newly developed bioinformatic pipeline based on assignment of environmental gene tags (EGTs) to protein families stored in the Pfam database. Short amino acid sequences deduced from the plasmid metagenome sequence reads were compared to profile hidden Markov models underlying Pfam. Obtained matches evidenced that many reads represent genes having predicted functions in plasmid replication, stability and plasmid mobility which indicates that WWTP bacteria harbour genetically stabilised and mobile plasmids. Moreover, the data confirm a high diversity of plasmids residing in WWTP bacteria. The mobile organic peroxide resistance plasmid pMAC from Acinetobacter baumannii was identified as reference plasmid for the most abundant replication module type in the sequenced sample. Accessory plasmid modules encode different transposons, insertion sequences, integrons, resistance and virulence determinants. Most of the matches to Transposase protein families were identified for transposases similar to the one of the chromate resistance transposon Tn5719. Noticeable are hits to beta-lactamase protein families which suggests that plasmids from WWTP bacteria encode different enzymes possessing beta-lactam-hydrolysing activity. Some of the sequence reads correspond to antibiotic resistance genes that were only recently identified in clinical isolates of human pathogens. EGT analysis thus proofed to be a very valuable method to explore genetic diversity and composition of the present plasmid metagenome dataset.     

Particle size distribution of cultivable airborne microbes and inhalable particulate matter in a wastewater treatment plant facility

A field study was performed to identify the size distribution characteristics of viable, cultivable airborne microorganisms (heterotrophic bacteria, fungi, and total coliforms) at a municipal wastewater treatment facility, and their association with inhalable particulate matter (PM₁, PM_2.5, and PM₁₀), as well as hydrogen sulfide concentrations and ambient meteorological parameters. The highest concentrations of cultivable, airborne heterotrophic bacteria, total coliforms, mass and number concentration of particulate matter, as well as hydrogen sulfide were observed at the aerated grit removal chambers at the pretreatment stage (3 to 2030 times higher than the values of the background ambient air). In contrast, the mean concentrations of cultivable, airborne mesophilic fungi at the aerated grit chambers were 0.6 time lower than the background site, where fungi presented the most abundant taxonomic group in the ambient air. Although the highest concentrations of the airborne fungi were determined at aerodynamic diameters between 2.1 and 3.3 μm, a nearly equal distribution of the mean concentrations of the cultivable, airborne heterotrophic bacteria were observed in the six different size fractions at the primary settling tanks and in the ambient air. Interestingly, their size distribution profiles at the aerated grit chambers were different and showed a maximum aerodynamic diameter at the size range from 3.3 to 4.7 μm, similar to that of the cultivable, airborne total coliforms. In general, low positive or no significant linear relationships could be found between the cultivable airborne heterotrophic bacteria, total coliforms, or fungi at the two wastewater treatment stages and the ambient background microbial community.     

Anaerobic filter treatment of wastewater from mushroom cultivation on coffee pulp

Wastewater from the pre-treatment of coffee pulp for mushroom cultivation was treated in an anaerobic filter reactor at laboratory scale. The digester was fed semicontinuously with 300 to 500 ml of fresh medium per day. Organic loading rates (OLR) applied ranged widely during the study, from 0.48 to 62.93 g chemical oxygen demand (COD)/1 d. Treating wastewater from the pasteurization of pulp, the highest strength studied, a COD removal efficiency of up to 87% was attained at a high OLR of 42.868 g COD/I d; while a high biogas production rate (BPR) of 2.89 I/I d was also achieved. However, the average organic matter removal efficiency was 53% at an OLR of 23.921 g COD/1 d, which indicates that process efficiency should be improved to achieve a good quality effluent. BPR averaged 1.72 1/1 d, which shows that with technical-scale reactors, high biogas production could be obtained for further use in the pasteurizing process itself (energy recycling).     

Anaerobic degradation of adsorbable organic halides (AOX) from pulp and paper industry wastewater

Adsorbable organic halides (AOX) are generated in the pulp and paper industry during the bleaching process. These compounds are formed as a result of reaction between residual lignin from wood fibres and chlorine/chlorine compounds used for bleaching. Many of these compounds are recalcitrant and have long half-life periods. Some of them show a tendency to bioaccumulate while some are proven carcinogens and mutagens. Hence, it is necessary to remove or degrade these compounds from wastewater. Physical, chemical and electrochemical methods reported to remove AOX compounds are not economically viable. Different types of aerobic, anaerobic and combined biological treatment processes have been developed for treatment of pulp and paper industry wastewater. Maximum dechlorination is found to occur under anaerobic conditions. However, as these processes are designed specifically for reducing COD and BOD of wastewater, they do not ensure complete removal of AOX. This paper reviews the anaerobic biological treatments developed for pulp and paper industry wastewater and also reviews the specific micro-organisms reported to degrade AOX compounds under anaerobic conditions, their nutritional and biochemical requirements. It is imperative to consider these specific micro-organisms while designing an anaerobic treatment for efficient removal of AOX.     

Limitation of sludge biotic index application for control of a wastewater treatment plant working with shock organic and ammonium loadings

This study aimed to determine the relationship between activated sludge microfauna, the sludge biotic index (SBI) and the effluent quality of a full-scale municipal wastewater treatment plant (WWTP) working with shock organic and ammonium loadings caused by periodic wastewater delivery from septic tanks. Irrespective of high/low effluent quality in terms of COD, BOD₅, ammonium and suspended solids, high SBI values (8–10), which correspond to the first quality class of sludge, were observed. High SBI values were connected with abundant taxonomic composition and the domination of crawling ciliates with shelled amoebae and attached ciliates. High SBI values, even at a low effluent quality, limit the usefulness of the index for monitoring the status of an activated sludge system and the effluent quality in municipal WWTP-treated wastewater from septic tanks. It was shown that a more sensitive indicator of effluent quality was a change in the abundance of attached ciliates with a narrow peristome (Vorticella infusionum and Opercularia coarctata), small flagellates and crawling ciliates (Acineria uncinata) feeding on flagellates.     

Anaerobic degradation pathway and kinetics of domestic wastewater at low temperatures

The effect of temperatures below 20 °C (20, 15 and 10 °C) on the anaerobic degradation pathway and kinetics of domestic wastewater fractionated at different sizes was studied in a fluidized-bed batch reactor. The overall degradation pathway was characterized by a soluble fraction degrading according to zero-order kinetics and a colloidal fraction (between 0.45 and 4.5 μm) that first disintegrates into a particulate fraction smaller than 0.45 μm before finally degrading. The colloidal degradation processes follow a first-order kinetic. In contrast, suspended solids (bigger than 4.5 μm) degrade to soluble and colloidal fractions according to first-order kinetics. The colloidal fraction originating from suspended solids further degrades into soluble fraction. These soluble fractions have the same degradation kinetics as the original soluble fraction. The suspended solids degradation was highly affected by temperature, whereas the soluble fraction slightly affected and the colloidal fraction was not affected at all. On the other hand, the colloidal non-degradable fraction increased significantly with the decrease in temperature while the suspended solids slowly increased. The soluble non-degradable fraction was little affected by temperatures changes.     

Anaerobic treatment of antibiotic production wastewater and kinetic evaluations

In this study, the anaerobic treatment of high-strength antibiotic production wastewater and the development of a mathematical model for the treatment were attempted. Anaerobic treatability was investigated using synthetic solutions and original wastewater of which the initial chemical oxygen demand (COD) was determined. Initial COD of solutions was increased from 3,000 to 43,000 mg O(2)/liter in an anaerobic bioreactor. The bioreactor pH was maintained at 6.5-7.5. The temperature was kept constant at 37 +/- 1 degrees C. Raw materials and original wastewater containing penicillin antibiotics were obtained from Fako Pharmaceutical Factory (Fako) in Istanbul, Turkey. Anaerobic sludge used for treatment was obtained from Pakmaya Baker's Yeast Producing Factory (Pakmaya) in Izmit, Turkey and the Fako. A mathematical model based on substrate (total COD) concentration was developed assuming that only three consecutive reactions, namely, hydrolysis, acidogenesis and methanogenesis, are significant. From the experimental data, a model that can be used for COD calculation as a function of time was developed using the first- and the second-order kinetic approaches. Making use of the developed model equation, it was proved that the anaerobic treatment of high strength (COD > 25,000 mg O(2)/liter) antibiotic production wastewater fits the second-order kinetics.     

Transformation of N-phenylpiperazine by mixed cultures from a municipal wastewater treatment plant

Samples from a wastewater treatment plant were used as inocula for mixed cultures dosed with N-phenylpiperazine (NPP), a model compound containing the piperazine ring found in many fluoroquinolones. Chemical analyses showed that NPP (50 mg liter(-1)) disappeared in 12 days, with the appearance of a transient metabolite and two nitrosated compounds.     

Differential bacterial growth kinetic and nitrification of fisheries wastewaters containing high ammonium and organic matter concentration by using pure oxygen

Nitrification with pure O of fisheries wastewaters high in N-NH4+ (0.2-1g/l) and in organic matter (1-2gCOD/l) gave specific growth rates for the bacteria degrading organic matter of 0.24h and for nitrifying bacteria of 0.15h. Average organic matter abatement was 75% whereas N-NH (0.7g/l as initial concentration) oxidation to nitrite and nitrate was 20%.