Simultaneous organic carbon removal-nitrification by an activated sludge process with cross-flow filtration

Simultaneous organic carbon removal-nitrification was carried out by an activated sludge process with cross-flow filtration while retaining a higher concentration of activated sludge. Operating the unit at ca. 0.10 gBOD·gVSS⁻¹·d⁻¹ made the sludge retention time very long and simultaneous carbon removal-nitrification was achieved quite well. Compared with conventional activated sludge processes, the present process made possible nearly twice the organic volumetric loading by increasing the sludge concentration five-fold. A nitrification rate of ca. 0.30 gTKN·l⁻¹·d⁻¹ was attained. More than 27% of the oxidized nitrogen in the reactor was denitrified at the same time in most cases.     

Characteristics of granular methanogenic sludge grown on phenol synthetic medium and methanogenic fermentation of phenolic wastewater in a UASB reactor

The growth of granules on a phenol synthetic medium and the methanogenic fermentation of industrial phenolic wastewater from a steel factory in an upflow anaerobic sludge blanket (UASB) reactor were investigated. Total granular sludge concentration retained in the UASB reactor was 6.7 g MLSS/l (6.0 g MLVSS/l) during the 10 months' operation on the phenol synthetic medium. This realized a maximum phenol removal rate of 2.2 g/l·d (phenol concentration of influent = 500 mg/l), which corresponded to 5.2 g COD/l·d at space velocity (SV) of 4.4 d⁻¹. The granules formed were of relatively small size ranging from 0.61 to 0.77 mm, and had a relatively low density of 0.013–0.023 g MLVSS/cm³ and low specific gravity (1.11) due to very low ash content (8.7–11.9%). Electron microscopic analysis showed that Methanothrix spp. appeared dominantly on the granule surface as well as within it. The specific metabolic activities of bacterial trophic groups were the highest for H₂ followed by acetate, benzoate, phenol, and propionate. In the case of industrial phenolic wastewater, although phenol efficiency was only 50% at SV of 0.4 d⁻¹, when the wastewater was diluted twofold and the treated wastewater was recycled at SV of 7.3 d⁻¹, the removal efficiencies of phenol and CODcr were restored to 90% (influent=400 mg/l) and 80% (influent=5,000 mg/l), respectively. It was suggested that recycling of the treated wastewater might be improved by partly degrading unknown toxic compounds contained in phenolic wastewater.     

Improved performance of a hybrid design over an anaerobic filter for the treatment of dairy industry wastewater at laboratory scale

A combined system designed by converting the flow mixing chamber of an anaerobic filter into an UASB resulted in an increased efficiency of removal of organic matter of 92% and in a gas production of 4.64 l·l⁻¹·d⁻¹, at the highest organic loading rate tested compared with that of the unmodified anaerobic filter. Both reactors were tested using dairy industry wastewater at identical operating conditions at 30°C and organic loading rate between 1 to 8 g COD·l⁻¹·d⁻¹.     

Potential availability of anaerobic treatment with digester slurry of animal waste for the reclamation of acid mine water containing sulfate and heavy metals

The use of an anaerobic digester slurry of cattle waste for the reclamation of acid mine water was examined. When the digester slurry was mixed with acid mine water, anaerobic digestion, including sulfate reduction and methanogenesis, was enhanced. In the mixture of acid mine water and the digester slurry, sulfate reduction proceeded without diminishing methanogenesis. The digester slurry and its supernatant (SDF-sup) showed a significant capacity to act as a strong alkaline reagent, and the pH of the acid mine water was markedly elevated by the addition of the digester slurry of SDF-sup even at the low ratio of 1% (v/v). Precipitation of heavy metals in the acid mine water occurred as the pH was elevated by the addition of SDF-sup. When the digester slurry was added at the ratio of 5% (v/v) to acid mine water which had been pretreated with SDF-sup, the rate of sulfate reduction increased with increasing the concentration of sulfate in the mixture up to about 1,400 mg·l⁻¹. In acid mine water pretreated with SDF-sup and supplemented with the digester slurry at the ratio of 5% (v/v), the maximum amount of sulfate reduced within 20 d of incubation was about 1,000 mg·l⁻¹, and the maximum rate of sulfate reduction was about 120 mg SO₄²⁻·l⁻¹·d⁻¹.     

Effects of an external magnetic field on the flock size and sedimentation of activated sludge

Effects of an external magnetic field on sedimentation enhancement were investigated using three kinds of practical activated sludge. An indoor experiment was setup (3.5l aeration vessel) equipped with a broth circulation system and 800 G of external magnetic field. The application of an external magnetic field to the activated sludge enhanced the sedimentation irrespective of the nature of the activated sludge. At the same time, the flock size of the sludge was enlarged by the external magnetic field. However, the surface zeta potentials of the sludge were not changed by the external magnetic field. Addition of FeCl₃ to the sludge enhanced the effects of the external magnetic field. Based on these results, the following mechanism for the enhancement of sedimentation by the external magnetic field is suggested: activated sludge containing iron was magnetized during entry to the magnetic field and coagulated with the magnetic force. As a consequence, the flock size was enlarged. Almost the same sedimentation enhancement by external magnetization was confirmed by a pilot scale magnetization system (2.0 m³ of aeration vessel) when the airlift type of mild broth circulation system was equipped with a 5000 G magnetic field.     

Biosorption and biodegradation of pentachlorophenol (PCP) in an upflow anaerobic sludge blanket (UASB) reactor

In order to understand the fate of PCP in upflow anaerobic sludge blanket reactor (UASB) more completely, the sorption and biodegradation of pentachlorophenol (PCP) by anaerobic sludge granules were investigated. The anaerobic granular sludge degrading PCP was formed in UASB reactor, which was seeded with anaerobic sludge acclimated by chlorophenols. At the hydraulic retention time (HRT) of 20–22 h, and PCP loading rate of 200–220 mg l⁻¹ d⁻¹, UASB reactor exhibited good performance in treating wastewater which containing 170–180 mg l⁻¹ PCP and the PCP removal rate of 99.5% was achieved. Sequential appearance of tetra-, tri-, di-, and mono-chlorophenol was observed in the reactor effluent after 20 mg l⁻¹ PCP introduction. Sorption and desorption of PCP on the anaerobic sludge granules were all fitted to the Freundlich isotherm equation. Sorption of PCP was partly irreversible. The Freundlich equation could describe the behavior of PCP amount sorbed by granular sludge in anaerobic reactor reasonably well. The results demonstrated that the main mechanism leading to removal of PCP on anaerobic granular sludge was biodegradation, not sorption or volatization.     

Biodegradation of nitrobenzene by a sequential anaerobic-aerobic process

Nitrobenzene was completely degraded by mixed cultures using a sequential anaerobic-aerobic treatment process. Under anaerobic conditions in a fixed-bed column aniline was formed from nitrobenzene through gratuitous reduction by cells of sewage sludge. This reaction was accelerated by the addition of glucose. Complete mineralization of aniline was accomplished by subsequent aerobic treatment using activated sludge as inoculum. The maximum degradation rate of nitrobenzene (4.5 mM) in the two-stage system was 552 mg l^–1d^–1, referring to 154 mg of nitrobenzene per gram of glucose. In a second experimental phase glucose as cosubstrate and H-donor was replaced by synthetic waste containing ethanol, methanol, isopropanol and acetone. Again, nitrobenzene (1.9 mM) was completely degraded (maximum degradation rate of 237 mg l^–d^–1, referring to 251 mg per gram of solvents). The major advantage of the described two-stage process is that the reduction of nitrobenzene by anaerobic pretreatment drastically reduces emission by stripping during aerobic treatment.Abbreviations HRT hydraulic retention time - OD₅₄₆ optical density at 546 nm     

Dominance of yeast in activated sludge under acidic pH and high organic loading

Flow cytometry-fluorescent in situ hybridization (FC-FISH) was used to investigate the effect of controlled pH and/or varied organic loading on the content of yeast and bacterial cells in an activated sludge system (AS) individually operating in continuous and batch mode for treatment of high-strength industrial wastewater. Specifically, we attempted to develop a yeast-predominant activated sludge system (Y-AS). For the batch-mode AS, bacteria-dominated AS (B-AS) obtained at pH 6.5–7.5 induced higher chemical oxygen demand (COD) removal than Y-AS obtained at acidic pH (5.0–6.0 and 4.0–5.0). For the continuous-mode AS operating at COD loadings of 2.5–2.8 kg COD m⁻³ d⁻¹, it was difficult to achieve a Y-AS solely by controlling the pH level at 7.0 to 5.1 then to 4.1 because bacteria stably accounted for greater than 98% of the total cells, regardless of the pH levels. Therefore, the effects of varied COD loadings (2.1, 8.7 and 21.0 kg COD m⁻³ d⁻¹) on continuous-mode AS operation at acidic pH (4.5) was investigated. Both acidic pH and high COD loading levels were found to be prerequisites for yeast to dominate the sludge microbial community in the continuous-mode AS.     

Investigation on the formation and kinetics of glucose-fed aerobic granular sludge

Aerobic granular sludge was cultivated in a glass sequencing batch reactor (SBR) with glucose synthetic wastewater. The spherical shaped granules were observed on 4th day with the mean diameter of 0.1 mm. With the increase of chemical oxygen demand (COD) concentration of the influent, aerobic granules grew matured, the size of which ranged from 1.2 to 1.9 mm. The aerobic granular sludge could sustain high organic loading rate (about 4.0 g COD L⁻¹ d⁻¹), with good settling ability (settling velocity 36 m/h) and high biomass concentration (MLSS 6.7 ±0.2 g/L). Experimental data indicated that the substrate utilization and biomass growth kinetics followed Monod's kinetics model approximately. The corresponding kinetic coefficients of maximum specific substrate utilization rate (k), half velocity coefficient (K_s), growth yield coefficient (Y) and decay coefficient (K_d) were 13.2 d⁻¹, 275.8 mg/L, 0.183–0.250 mg MLSS/mg COD and 0.023–0.075 d⁻¹, respectively, which made aerobic granules have short setup period, high rate of substrate utilization and little surplus sludge.     

Factors affecting accumulation and loss of zinc by the aquatic moss Rhynchostegium riparioides (Hedw.) C. Jens.

Reciprocal transplants of the moss Rhynchostegium riparioides (Herw.) C. Jens. between populations from streams with high (0.27 mg l⁻¹) and low (0.05 mg l⁻¹) concentrations of Zn showed that Zn uptake over the first 12 h was twice as fast as loss and reached an asymptotic value sooner. However, Zn accumulation was lower in a nutrient-rich (high nitrate and phosphate) than a nutrient-poor stream (4.5 vs. 7.0 mg g⁻¹). Shoots from a high-Zn site (0.70 mg l⁻¹) contained increased Zn concentrations on passing away from the apex and higher concentrations in leaves than stems (6.5 vs. 3.3 mg g⁻¹). Shoots freshly exposed to 1.0 mg l⁻¹ Zn in the laboratory showed similar Zn concentrations at different positions along the stem after exposure for 2 h, but by 24 h the gradient was similar to that found in field material. Ca, Mg, Mn and chelating agents (EDTA, humic acids) all decreased Zn accumulation in the laboratory, but neither nitrate nor phosphate over concentration ranges of two orders of magnitude had any influence.A greater proportion of Zn accumulated over a 24-h period was lost than that accumulated over a 10-day period (66 vs. 45%), even though the total Zn was similar (ca. 3.8 mg g⁻¹) at the beginning of the loss experiments. Studies with NiCl₂ as an eluting agent indicate that this and other observations may be interpreted by assuming that an ‘exchangeable’ Zn fraction becomes converted with time to a ‘residual’ Zn fraction.     

Prodigiosin formation by Serratia marcescens in a chemostat

In a study of the control of metabolite formation, prodigiosin production by Serratia marcescens was used as a model. Specific production rates of prodigiosin formation were determined using batch culture technique. Sucrose as carbon source and NH₄NO₃ as nitrogen source resulted in a specific production rate of 0.476 mg prodigiosin (g cell dry weight)⁻¹ h⁻¹. Prodigiosin formation and productivity was inversely correlated to growth rate when the bacterium was grown under carbon limitation on a defined medium in a chemostat culture. The maximum specific growth rate (μ_max) was 0.54 h⁻¹ and prodigiosin was formed in amounts over 1 mg l⁻¹ up to a growth rate (μ) of 0.3 h⁻¹ at steady state conditions. At a dilution rate of 0.1 h⁻¹ growth at steady state with carbon and phosphate limitation supported prodigiosin formation giving a similar specific yield [1.17 mg prodigiosin (g cell dry weight)⁻¹ and 0.94 mg g⁻¹, respectively], however, cells grown with nitrogen limitation [(NH₄)₂SO₄] did not form prodigiosin. Productivity in batch culture was 1.33 mg l⁻¹ h⁻¹ as compared to 0.57 mg l⁻¹ h⁻¹ in the chemostat.     

Comparison of startup and anaerobic wastewater treatment in UASB, hybrid and baffled reactor

An experimental study was carried out to compare the performance of selected anaerobic high rate reactors operated simultaneously at 37?°C. The three reactors, namely upflow anaerobic sludge bed reactor (UASB), hybrid of UASB reactor and anaerobic filter (anaerobic hybrid reactor – AHR) and anaerobic baffled reactor (ABR), were inoculated with the anaerobic digested sludge from municipal wastewater treatment plant and tested with synthetic wastewater. This wastewater contained sodium acetate and glucose with balanced nutrients and trace elements (COD 6000?mg?·?l^?1). Organic loading rate (B _v ) was increased gradually from an initial 0.5?kg?·?m^?3?·?d^?1 to 15?kg?·?m^?3?·?d^?1 in all the reactors. From the comparison of the reactors' performance, the lowest biomass wash-out resulted from ABR. In the UASB, significant biomass wash-out was observed at the B _v 6?kg?·?m^?3?·?d^?1, and in the AHR at the B _v 12?kg?·?m^?3?·?d^?1. The demand of sodium bicarbonate for pH maintenance in ABR was two times higher as for UASB and AHR. The efficiency of COD removal was comparable for all three reactors – 80–90%. A faster biomass granulation was observed in the ABR than in the other two reactors. This fact is explained by the kinetic selection of filamentous bacteria of the Methanotrix sp. under a high (over 1.5?g?·?l^?1) acetate concentration.     

Production of peroxidase with horseradish hairy root cells in a two step culture system

Horseradish hairy root cells transformed by a soil bacterium Agrobacterium rhizogenes had peroxidase (POD) activity comparable to that of the original plant root tubers. To enhance POD production by the hairy root culture, various additives to the medium were tested including casein hydrolysates and plant extracts. Polypepton addition had a significant effect on the growth and POD production; at low concentrations (below 1 g/l) the growth was stimulated, while at high concentrations (3–10 g/l), POD activity in the cells was enhanced in spite of a low growth rate. Therefore, the hairy roots were at first cultured in the medium with 1 g/l Polypepton, and then 5 g/l Polypepton was added to enhance intracellular POD activity. POD activity in this two step culture system was 5.4 times higher than that in conventional culture in Polypepton-free medium.     

Effect of fusicoccin on proton co-transport of sugars in the phloem loading of Ricinus communis L.

The loading of [¹⁴C] sucrose into the phloem from the apoplast of hollow Ricinus petioles was stimulated by fusicoccin (FC, 10 mg l⁻¹), by indole-3-acetic-acid (IAA; 10⁻² mol m⁻³) and inhibited by abscisic acid (ABA 10⁻² mol m⁻³) when added to a buffered perfusing solution of 2% sucrose and 30 mol m⁻³ KCl. A proton efflux was detected in the hollow petiole which was stimulated by FC in the presence of K⁺, insensitive to IAA, and inhibited by ABA, when present in the perfusing solution.The observed results are consistent with an H⁺/K⁺ exchange between the phloem sap and the apoplast which is responsible for the high pH and high [K⁺ of phloem saps. The resultant pH gradient between the phloem sap and the apoplast provides the energy for the proton co-transport of sucrose in phloem loading.     

Comparative studies on changes in lipid composition and some histological responses of gills from carp by exposure to acute level of surfactants

1. Carp (Cyprinus carpio) were exposed to four surfactants at the concentration of 0.02 mM (dodecylbenzenesulfonate (DBS); 7mg l⁻¹, sodium laurylsulfonate (LNa); 5.7mg l⁻¹, sodium stearate (SNa); 6.1 mg l⁻¹, nonylphenyl ethoxylate (EN); 13.2 mg l⁻¹).2. The changes in lipid composition of the gill were compared. No change in fatty acid composition of neutral lipids and complex lipids occurred after exposure to SNa, whereas changes did occur after DBS, EN and LNa.3. In the single case of exposure to DBS, the content of phosphatidylcholine was significantly increased as compared to control gills.4. The ratio cholesterol/total phospholipid and the ratio unsaturated fatty acid/saturated fatty acid were not changed after exposure to all surfactants tested.5. The order of gill damages was DBS > LNa > SNa > EN.     

Long-term continuous partial nitritation-anammox reactor aeration optimization at different nitrogen loading rates for the treatment of ammonium rich digestate lagoon supernatant

Dissolved oxygen (DO) is an important parameter for partial nitritation-anammox process but previously not evaluated for the treatment of digested biosolid thickening lagoon supernatant. Using intermittent aeration we investigated nitrogen removal from such supernatant in an integrated fixed film activated sludge (IFAS) process operated under a variety of hydraulic retention times (1.2–2.5 days). The overall nitrogen removal rate (NRR) was significantly increased (P < 0.01) from 0.26 ± 0.01 kg N m⁻³ d^-1 at HRT of 2.5 days to 0.50 ± 0.01 kg N m^-3 d^-1 at HRT of 1.2 day. Higher nitrogen loading rates needed higher DO concentrations in order to cope with the increased oxygen demand by ammonium-oxidizing bacteria (AOB). Enhancing the DO concentration from 0.18 mg L^-1 to 0.35 mg L^-1 improved AOB activity. However, when the bulk liquid DO was in the range of 0.28−0.35 mg L^-1, anammox activity inhibition was observed associated with a significant free nitrous acid (FNA) accumulation (21.70 ± 4.10 μg L^-1). Batch studies confirmed the inhibition of anammox activity under high DO conditions (0.28−0.35 mg L^-1). Aeration strategies, other than increasing the DO set points, should be investigated in order to be able to work at high nitrogen loading rates without compromising anammox activity.     

Impact of dissolved oxygen and loading rate on NH3 oxidation and N2 production mechanisms in activated sludge treatment of sewage

Microaerobic activated sludge (MAS) is a one-stage process operated at 0.5–1.0 mg l⁻¹ dissolved oxygen (DO) aiming at simultaneous nitrification and denitrification. We used molecular techniques and a comprehensive nitrogen (N)-transformation activity test to investigate the dominant NH₃-oxidizing and N₂-producing mechanism as well as the dominant ammonia-oxidizing bacteria (AOB) species in sludge samples individually collected from an MAS system and a conventional anoxic/oxic (A/O) system; both systems were operated at a normal loading rate (i.e. 1.0 kg chemical oxygen demand (COD) m⁻³ day⁻¹ and 0.1 kg NH₄⁺-N m⁻³ day⁻¹) in our previous studies. The DO levels in both systems (aerobic: conventional A/O system; microaerobic: MAS system) did not affect the dominant NH₃-oxidizing mechanism or the dominant AOB species. This study further demonstrated the feasibility of a higher loading rate (i.e. 2.30 kg COD m⁻³ day⁻¹ and 0.34 kg NH₄⁺-N m⁻³ day⁻¹) with the MAS process during sewage treatment, which achieved a 40% reduction in aeration energy consumption than that obtained in the conventional A/O system. The increase in loading rates in the MAS system did not affect the dominant NH₃-oxidizing mechanism but did impact the dominant AOB species. Besides, N₂ was predominantly produced by microaerobic denitrification in the MAS system at the two loading rates.     

Removal of triethylamine from synthetic wastewater by acclimated mixed bacteria cultures

This aim of this study was to remove triethylamine by a biological method, as well as to understand the ability of mixed bacteria cultures to treat a triethylamine compound from synthetic wastewater. The mixed bacteria cultures could not remove triethylamine, whether the activated sludge came from an acrylonitrile–butadiene–styrene resin manufactured wastewater treatment system or a waterborne polyurethane resin manufactured wastewater treatment system. When the mixed bacteria cultures were acclimated to triethylamine, they could utilize 650 mg l⁻¹ triethylamine for growth. When the initial triethylamine concentration was below 200 mg l⁻¹, the triethylamine removal efficiency could reach 100%. The triethylamine removal rate of the acclimated GMIX sludge was faster than the acclimated EMIX sludge.     

Investigation on the properties and kinetics of glucose-fed aerobic granular sludge

Aerobic granulation is a process in which suspended biomass aggregate and form discrete well-defined granules in aerobic systems. To investigate the properties and kinetics of aerobic granular sludge, aerobic granules were cultivated with glucose synthetic wastewater in a series of sequencing batch reactors (SBR). The spherical shaped granules were observed on 8th day with the mean diameter of 0.1 mm. With the organic loading rate (OLR) being increased to 4.0 g COD L⁻¹ d⁻¹, aerobic granules grew matured with spherical shape. The size of granules ranged from 1.2 to 1.8 mm, and the corresponding settling velocity of individual granule was 24.2–36.4 m h⁻¹. The oxygen utilization rate (OUR) of mature granules was 41.90 g O₂ kg MLSS⁻¹ h⁻¹, which was two times higher than that of activated sludge (18.32 g O₂ kg MLSS⁻¹ h⁻¹). The experimental data indicated that the substrate utilization and biomass growth kinetics generally followed Monod's kinetics model. The corresponding kinetic coefficients of k (maximum specific substrate utilization rate), K_s (half velocity coefficient), Y (growth yield coefficient) and K_d (decay coefficient) were determined as follows, k_c = 23.65 d⁻¹, K_c = 3367.05 mg L⁻¹, K_N = 0.038 d⁻¹, K_N = 29.65 mg L⁻¹, Y = 0.1927–0.2022 mg MMLS (mg COD)⁻¹ and K_d = 0.00845–0.0135 d⁻¹, respectively. Those properties of aerobic granules made aerobic granules system had a short setup period, high substrate utilization rate and low sludge production.     

Nitrogen pollution of leachate at a sea-based solid waste disposal site and its nitrification treatment by immobilized acclimated nitrifying sludge

It was found that changes in the nitrogen concentration of leachate from the Osaka North Port sea based disposal site were closely related to the way in which dumping was carried out. The nitrogen concentration of the leachate was low due to the low nitrogen content and slow nitrogen dissolution rate of materials dumped previously in the landfill. The dumping of incinerator ash, noncombustible garbage, waterworks sludge and incinerated ash from sewage sludge were followed, and it was found that they caused a sharp increase in nitrogen concentration in the leachate. The main nitrogen form of leachate was NH₄-N, and its concentration reached 50 mg/l after 6 years of landfilling. Successful nitrification treatment of leachate (more than 80% nitrification) was possible by using polyvinyl alcohol immobilized acclimated marine nitrifying sludge with an NH₄-N loading rate of 2.9 mg-NH₄-N/g-pellets/d. Low NO₂-N was detected throughout the continuous nitrification experiments, so the rate limiting step in the nitrification treatment was revealed to be a nitrification step (NH₄⁺→NO₂⁻). The addition of inorganic carbon to the test leachate enabled us to perform nitrification treatment even with a high NH₄-N loading rate. Dolomite limestone was shown experimentally to be able to replace inorganic chemicals.