Effect of chloride and condensable tannin in anaerobic degradation of tannery wastewaters

Toxic effect due to chloride and condensable tannin on anaerobic digestion of vegetable tanning wastewater was investigated at different hydraulic retention times viz 24, 48 and 60 hr respectively. The toxicity to anaerobic contact filter was observed at a chloride concentration of 4500 mg/l and tannin concentration of 790 mg/l respectively under synergistic condition. In the case of constant influent tannin concentration of 600 mg/l, the toxicity due to chloride on anaerobic contact filter was observed at 5500 mg/l. The COD removal percent ranged from 50% to 79% at 48 hr and 67% to 91% at 60 hr HRT respectively. In the case of constant influent chloride concentration of 4000 mg/l and at an increasing influent COD concentration, the toxicity due to tannin on anaerobic contact filter was observed at 1180 mg/l. The COD removal percent ranged from 64% to 89% at 48 hr and 78% to 96% at 60 hr HRT respectively. The results showed that at least 60 hr HRT would be desirable to have good COD removal percent.     

Continuous anaerobic treatment of wastewaters containing formaldehyde and urea

The toxicity of formaldehyde (FA) in batch assays, using volatile fatty acids (VFA) as co-substrate, and the continuous anaerobic treatment of wastewaters containing FA in upflow anaerobic sludge blanket (UASB) reactors was investigated. In batch studies, FA exerted a 50% methanogenic toxicity on VFA at concentrations of around 100 mg/l, 2.5 times lower than values reported with sucrose. Although at FA concentrations higher than 200 mg/l methanogenesis was completely inhibited, a partial recovery of the bacterial activity was observed after 250 h when the FA had been removed from the medium. The continuous anaerobic degradation of FA at concentrations up to 2 g/l, using 1.6 g/l of glucose as co-substrate, was studied in a UASB reactor. A stable and efficient operation was observed at organic loading rates (OLR) of 6.0 g COD/l·d and with a COD/FA ratio as low as 1.4. A synthetic substrate with the same characteristics as the effluents produced during fibreboard adhesives manufacturing (based on urea-FA), i.e. 0.95 g FA/l and 0.35 g urea/l, was treated in a UASB reactor. The applied OLR and nitrogen loading rate (NLR) were 3.45 g COD/l·d and 0.58 g N/l·d, respectively. COD removal efficiencies were maintained at 90–95%, FA and urea being completely degraded.     

Biotechnology developments for the treatment of toxic and inhibitory wastewaters

The cost-effectiveness of biological processes has encouraged many researchers to consider biotreatment for the stabilization of toxic or recalcitrant wastewaters. However, to ensure adequate removal of trace contaminants and satisfactory performance with high strength inhibitory industrial wastewaters, conventional biotechnology is being re-evaluated. This review summarizes selected recent contributions to the development of appropriate biotechnology for toxic wastewater treatment. Microbiological constraints and potential solutions are examined. Assessments of conventional biological processes for contaminant control are reviewed, and several new developments in bioreactor design for inhibitory wastes are presented.     

Development of anaerobic filters for treatment of high strength agro-industrial wastewaters

The suitability and advantages of anaerobic filters for the treatment of various agro-industrial wastewaters are discussed. Recent developments in reactor design and typical operating parameters and performance data are given for reactors operated in the up- and downflow mode. The distribution of the most important process parameters throughout the reactor height is discussed and methods for process optimization are presented.     

A double-feed anaerobic filter for the treatment of high strength wastewaters

Summary An Upflow Anaerobic Filter (UAF) treating cheese whey showed a non-homogeneous biomass distribution and COD degradation along the reactor. Higher biomass concentration with a higher methanogenic activity was present in the lower than in the upper part of the filter. In order to increase the methanogenic capacity of the filter, a double-feed system was tested. The UAF with the double feeding presented higher methane production and completely homogeneous characteristics regarding biomass distribution and activity as well as COD removal along the reactor.     

Long-term, high-rate anaerobic biological treatment of whey wastewaters at psychrophilic temperatures

Two laboratory-scale anaerobic hybrid reactors, R1 and R2, treated low- (1 kg COD m-3) and high-strength (10 kg COD m-3) whey-based wastewaters, respectively, in a 500-day trial. The chemical oxygen demand (COD) removal efficiencies of R1 averaged 70-80%, at organic loading rates of 0.5-1.3 kg COD m-3 day-1, between 20 and 12 degrees C. The COD removal efficiencies of R2 exceeded 90%, at organic loading rates up to 13.3 kg COD m-3 day-1, between 20 and 14 degrees C. Lowering the operating temperature of R2 to 12 degrees C resulted in a decrease in COD removal efficiency, to between 50% and 60%, and a disintegration of granular sludge. The decline in performance, and granule disintegration, was reversed by decreasing the organic loading rate of R2 to 6.6 kg m-3 day-1. Specific methanogenic activity profiles revealed mesophilic (37 degrees C) temperature optima for biomass in both reactors, even after 500 days of psychrophilic operation, although the development of psychrotolerance in the biomass was noted.     

Thermophilic anaerobic digestion of high strength wastewaters

Investigations on the thermophilic anaerobic treatment of high-strength wastewaters (14-65 kg COD/m(3)) are presented. Vinasse, the wastewater of alcohol distilleries, was used as an example of such wastewaters. Semicontinuously fed digestion experiments at high retention times revealed that the effluent quality of digestion at 55 degrees C is comparable with that at 30 degrees C at similar loading rates. The amount of methane formed per kilogram of vinasse drops almost linearly with increasing vinasse concentrations. This can be attributed to increasing concentrations of inhibitory compounds, resulting in increasing volatile fatty acid (VFA) concentrations in the effluent. The treatment of vinasse was also investigated using upflow anaerobic sludge blanket (UASB) reactors. Thermophilic granular sludge, cultivated on sucrose, was used as seed material. The sludge required a 4-month adaptation period, during which the size of the sludge granules decreased significantly. However, the settling characteristics remained satisfactory. After adaptation, high loading and methane generation rates could be accommodated at satisfactory treatment efficiencies, namely, 86.4 kg COD/m(3) day and 26 m(3) CH(4)(STP)/m(3) day, respectively. As in the semicontinuously fed digesters, the effluent VFA concentrations were virtually independent of the loading rates applied, indicating that the toxicity of the vinasse is more important than the loading rate in determining the efficiency of the conversion of vinasse to methane.     

The role of sulphidogenesis in anaerobic treatment phase of tannery wastewater treatment in advanced integrated wastewater pond system

An outdoor experiment was conducted to study the competitionbetween Sulphate Reducing Bacteria (SRB) and Methanogenic Archaea (MA) in anaerobictreatment phase of tannery wastewater treatment in pilot-scale Advanced FacultativePond (AFP). The relative electron flow towards sulphate reduction was higher (59–83%) than towardsmethanogenesis (17–41%), although the COD recovery within thereactor varied between 15 and 90%. The results also demonstrated that the flow of electrons towards SRBincreased with increase of the sulphate concentration and decrease of the COD : SO₄ ⁼ ratio.     

Feasibility studies on the treatment of dairy wastewaters with upflow anaerobic sludge blanket reactors

The feasibility of using upflow anaerobic sludge blanket (UASB) reactors for the treatment of dairy wastewaters was explored. Two types of UASBs were used--one operating on anaerobic sludge granules developed by us from digested cowdung slurry (DCDS) and the other on the granules obtained from the reactors of M/s EID Parry treating sugar industry wastewaters. The reactors were operated at HRT of 3 and 12 h and on COD loading rates ranging from 2.4 kg per m3 of digester volume, per day to 13.5 kg m(-3) d(-1). At the 3 h HRT, the maximum COD reduction in the DCDS-seeded and the industrial sludge-seeded reactors was 95.6% and 96.3%, respectively, better than at 12 h HRT (90% and 92%, respectively). In both the reactors, the maximum, the second best, and the third best COD reduction occurred at the loading rates of 10.8, 8.6 and 7.2 kg m3 d(-1), respectively. At loading rates higher than 10.8 kg, the reactor performance dropped precipitously. Whereas in the first few months the reactors operating on sludge from EID Parry achieved better biodegradation of the waste, compared to the reactors operated on DCDS, the performance of the latter gradually improved and matched with the performance of the former.     

Feasibility of expanded granular sludge bed reactors for the anaerobic treatment of low-strength soluble wastewaters

The application of the expanded granular sludge bed (EGSB) reactor for the anaerobic treatment of low-strength soluble wastewaters using ethanol as a model substrate was investigated in laboratory-scale reactors at 30oC. Chemical oxygen demand (COD) removal efficiency was above 80% at organic loading rates up to12 g COD/L . d with influent concentrations as low as 100 to 200 mg COD/L. These results demonstrate the suitability of the EGBS reactor for the anaerobic treatment of low-strength wastewaters. The high treatment performance can be attributed to the intense mixing regime obtained by high hydraulic and organic loads. Good mixing of the bulk liquid phase for the substrate-biomass contact and adequate expansion of the substrate-biomass contact and adequate expansion of the sludge bed for the degassing were obtained when the liquid upflow velocity (V(up)) was greater than 2.5 m/h. Under such conditions, an extremely low apparent K(s) value for acetoclastic methanogenesis of 9.8 mg COD/L was observed. The presence of dissolved oxygen in the wastewater had no detrimental effect on the treatment performance. Sludge piston flotation from pockets of biogas accumulating under the sludge bed occurred at V(up) lower than 2.5 m/h due to poor bed expansion. This problem is expected only in small diameter laboratory-scale reactors. A. more important restriction of the EGSB reactor was the sludge washout occurring at V(up) higher than 5.5 m/h and which was intensified at organic loads higher than 7 g COD/L. d due to buoyancy forces from the gas production. To achieve an equilibrium between the mixing intensity and the sludge hold-up, the operation should be limited to an organic loading rate of 7 g COD/L d. and to a liquid up-flow velocity between 2.5 and 5.5 m/h (c) 1994 John Wiley & Sons, Inc.     

Identification of toxic metals in affected algal cells in assays of wastewaters

Chlorella fusca was the test species used in assays of two wastewaters, one characterized by a high concentration of free metal ions, and the other by high concentrations of free metal ions and chlorinated organic compounds. Fine structural damage in cells exposed for six days to the effluents was examined using an electron microscope. In the presence of organic toxicity, the affected cells displayed a characteristically large build-up of starch grains. At high metal concentrations, the chloroplasts were the only organelles altered. Within the chloroplast, there were disruptions of the thylakoidal membranes and enlargement of interthylakoidal spaces. Excess metals, detected by X-ray microanalysis in the polyphosphate (poly-P) bodies of cells where chloroplast damage was observed, were regarded as harmful. X-ray scanning of particulate material in effluent samples is proposed as a useful and low cost addition to surveillance programmes.     

A pilot scale anaerobic upflow reactor treating distillery wastewaters

Summary A two-stage pilot reactor has been tested for the anaerobic digestion of distillery wastewater with a COD of-10,000 mg/1. In the first stage (residence time 16–72 hours), carbohydrates are fermented to low molecular weight metabolites. The second stage is an upflow reactor (residence time 14 hours) in which these metabolites are converted to biogas. Overall COD elimination is 84% (BOD, 92%) with biogas production 5–7 times the active volume of the upflow reactor per day. The process withstands temporary stress conditions fairly well. The results indicate that anaerobic treatment in the upflow reactor qualifies as an efficient and low cost method for distillery wastewater treatment.     

Antimutagenic and antioxidant activities of quebracho phenolics (Schinopsis balansae) recovered from tannery wastewaters

Quebracho extracts are used in tannery due to their high concentration of phenolics. The Mexican tannery industry uses around 450 kg/m(3) of which, 150 kg/m(3) remains in wastewaters and are discharged in drain pipe systems or rivers. The quebracho phenolics recovered from tannery wastewater (QPTW) was characterized by HPLC. The antimutagenic and antioxidant activities as well as the microbiological quality were evaluated. Total phenolic content of QPTW was 621mg catechin equivalent/g sample. Gallic and protocatechuic acids were the major components characterized by HPLC. QPTW showed an inhibition range on aflatoxin B(1) mutagenicity from 16 to 60% and was dose-dependent. Antioxidant activity (defined as beta-carotene bleaching) of QPTW (64.4%) at a dose of 12.3mg/mL was similar to that of BHT (68.7%) at a dose of 0.33 mg/mL, but lower than Trolox (90.8% at a dose of 2.5mg/mL); meanwhile antiradical activity (measured as reduction of DPPH) (60.8%) was higher than that of BHT (50.8%) and Trolox (34.2%). Quebracho residues were demonstrated to be an outstanding source of phenolic acids and for research and industrial uses.     

Effect of iron compounds on the treatment of fat-containing wastewaters

Effects of iron compounds on methanogenic fermentation the water polluted with fatty acids were studied. A natural readily available source of iron applicable to biological treatment of liquid wastes was searched for. A positive effect of iron on the methanogenic fermentation of fats and their degradation products--long-chain fatty acids--in aqueous media was demonstrated. It is recommended to add iron-containing clay, as an inexpensive and easily available iron source, in amounts providing the binding of the long-chain fatty acids present in wastewaters.     

Control of sulphide during anaerobic treatment of S-containing wastewaters by adding limited amounts of oxygen or nitrate

Sulphide generated during anaerobic treatment of S-containing wastewaters represents an environmental problem. Adding limited amounts of oxygen or nitrate (or nitrite) to biologically (or chemically) oxidise sulphide forms a simple process-level strategy to control this problem. This short review evaluates the feasibility and limitations of this strategy on the basis of the results of bioreactor studies.     

微生物燃料电池在毒性物质检测中的应用

微生物燃料电池(Microbial fuel cell,MFC)利用微生物整体作为催化剂催化底物将化学能直接转化为电能,是一种极具应用前景的生物电化学技术。微生物在阳极氧化还原有机物产生电子并传递给阳极,电子通过外电路传递至阴极后将电子释放给阴极中的氧化剂,从而产生电流。当有毒物质进入MFC,微生物活性降低,电子传递量变少,电流降低,而电流的产生与微生物活性呈线性关系,据此可检测样品的毒性。本文主要介绍了微生物燃料电池在毒性物质抗生素、重金属离子、有机污染物、酸等方面的研究,并分析了微生物燃料电池存在的问题及未来研究方向,以期不久的将来微生物燃料电池能付之使用。     

Thermophilic treatment of bulk drug pharmaceutical industrial wastewaters by using hybrid up flow anaerobic sludge blanket reactor

The hybrid up flow anaerobic sludge blanket reactor was evaluated for efficacy in reduction of chemical oxygen demand (COD) and biochemical oxygen demand (BOD) of bulk drug pharmaceutical wastewater under different operational conditions. The start-up of the reactor feed came entirely with glucose, applied at an organic loading rate (OLR) 1 kg COD/m³ d. Then the reactor was studied at different OLRs ranging from 2 to 11 kg COD/m³ d with pharmaceutical wastewater. The optimum OLR was found to be 9 kg COD/m³ d, where we found 65–75% COD and 80–94% of BOD reduction with biogas production containing 60–70% of methane and specific methanogenic activity was 320 ml CH₄/g-VSS d. By the characterization studies of effluent using GC–MS, the hazardous compounds like phenol, l,2-methoxy phenol, 2,4,6-trichloro phenol, dibutyl phthalate, 1-bromo naphthalene, carbamazepine and antipyrine were present. After the treatment, these compounds degraded almost completely except carbamazepine. Thermophilic methanothrix and methanosaetae like bacteria are present in the granular sludge.