Screening of plant species for the phytotreatment of wastewater containing sulphonated anthraquinones

Sulphonated anthraquinones are known to be recalcitrant to biodegradation and are not eliminated by traditional wastewater treatment plants, leading to their accumulation in fresh water. Due to the high cost and limited efficiency of existing physical-chemical treatments, alternative cheaper processes are required to remove these compounds from industrial effluents. Four plant species were tested under hydroponic conditions for their ability to treat model effluents contaminated with mono- and disulphonated anthraquinones. Among them, Rheum rabarbarum (rhubarb) showed the most promising results and was chosen for further investigation. The apparent transpiration stream concentration factor obtained with this plant species reached up to 2.5, indicating a strong phytotreatment potential that should be further explored then exploited.     

Economic evaluation of alternative wastewater treatment plant options for pulp and paper industry

Excessive water consumption in pulp and paper industry results in high amount of wastewater. Pollutant characteristics of the wastewater vary depending on the processes used in production and the quality of paper produced. However, in general, high organic material and suspended solid contents are considered as major pollutants of pulp and paper industry effluents. The major pollutant characteristics of pulp and paper industry effluents in Turkey were surveyed and means of major pollutant concentrations, which were grouped in three different pollution grades (low, moderate and high strength effluents), and flow rates within 3000 to 10,000 m³/day range with 1000 m³/day steps were used as design parameters. Ninety-six treatment plants were designed using twelve flow schemes which were combinations of physical treatment, chemical treatment, aerobic and anaerobic biological processes. Detailed comparative cost analysis which includes investment, operation, maintenance and rehabilitation costs was prepared to determine optimum treatment processes for each pollution grade. The most economic and technically optimal treatment processes were found as extended aeration activated sludge process for low strength effluents, extended aeration activated sludge process or UASB followed by an aeration basin for medium strength effluents, and UASB followed by an aeration basin or UASB followed by the conventional activated sludge process for high strength effluents.     

Treatment of organic pollution in industrial saline wastewater: a literature review

Many industrial sectors are likely to generate highly saline wastewater: these include the agro-food, petroleum and leather industries. The discharge of such wastewater containing at the same time high salinity and high organic content without prior treatment is known to adversely affect the aquatic life, water potability and agriculture. Thus, legislation is becoming more stringent and the treatment of saline wastewater, both for organic matter and salt removal, is nowadays compulsory in many countries. Saline effluents are conventionally treated through physico-chemical means, as biological treatment is strongly inhibited by salts (mainly NaCl). However, the costs of physico-chemical treatments being particularly high, alternative systems for the treatment of organic matter are nowadays increasingly the focus of research. Most of such systems involve anaerobic or aerobic biological treatment. Even though biological treatment of carbonaceous, nitrogenous and phosphorous pollution has proved to be feasible at high salt concentrations, the performance obtained depends on a proper adaptation of the biomass or the use of halophilic organisms. Another major limit is related to the turbidity problems inherent in saline effluents. For this reason, the major need for research in the future will be the combination of physico-chemical/biological treatment of saline industrial effluents, with regard to the global treatment chain, in order to meet the regulations.     

Greenhouse gas production: a comparison between aerobic and anaerobic wastewater treatment technology

Anaerobic wastewater treatment offers improved energy conservation with potential reduction in greenhouse gas emissions. Pitfalls exist in that the methane produced in anaerobic treatment can offset any reductions in carbon dioxide emissions, if it is released to the environment. This paper analyzes greenhouse gas emissions from both aerobic and anaerobic treatment systems, including sludge digestion and the losses of dissolved methane in digested biosolids and process effluents. There exists cross over points, ranging from 300 to 700 mg/L influent wastewater BODu, which are functions of the efficiency of the aerobic treatment system. Anaerobic treatment becomes favorable when treating influents higher in concentrations than the cross over values. A technology to recover dissolved methane would make anaerobic treatment favorable at nearly all influent strengths.     

Biodegradability of kraft mill TCF biobleaching effluents: Application of enzymatic laccase-mediator system

The great amount of pollutants released from kraft pulp processes, mainly from cooking and bleaching stages, is one of the most relevant environmental problems in this type of industry. New bleaching sequences are being studied based on the use of oxidative enzymes from fungal cultures. In this study, the bleaching systems consisting of Laccase and different mediators such as 1-hydroxybenzotriazole, violuric acid, syringaldehyde and methyl syringate in the bleaching sequence of Eucalyptus globulus kraft pulp were applied. The main objective of this study is to evaluate the aerobic and anaerobic biodegradability and toxicity to Vibrium fischeri of generated L-stage and total bleaching sequence effluents.The highest levels of aerobic and anaerobic degradation of the generated effluents were achieved for treatments with laccase plus violuric acid, with 80% of aerobic degradation and 68% of anaerobic biodegradation. V. fischeri toxicity was remarkably reduced for all the effluents after aerobic degradation.     

Identification and chemical characterization of specific organic indicators in the effluents from chemical production sites

The structural diversity of the wastewater composition was described by the use of detailed non-target screening analyses of industrial effluents from chemical production sites. Determination of the indicative organic compounds acting as potential molecular indicators for industrial emissions from chemical production industries has been possible due to (i) detailed characterisation of industrial contaminants and identification of compounds with high source specificity, (ii) quantitative determination of the organic constituents in the industrial effluents and (iii) the review of their industrial applications. The determination of potential site-specific markers and industrial molecular indicators corresponding to certain production processes (production of starting materials for manufacturing paper and printing inks, powder coatings as well as epichlorohydrin production) was performed in this work.The results of this study allowed significant contributions to the chemical characterisation of industrial contaminants and isolation of indicators that can act as representatives of industrial effluents in the aquatic environment.     

Characteristics of effluents from healthcare waste treatment with alkaline hydrolysis

Although alkaline hydrolysis emerges as an alternative process to treat healthcare waste (HCW), information about its emissions is scarce, namely as regards effluents production. This work aims to characterize the effluents from alkaline hydrolysis tests with samples of components usually present in HCW, under a temperature of 110°C and with 1 M NaOH aqueous solutions. Some of the regulatory parameters for discharging effluents were determined; also, tests for assessing aerobic and anaerobic biodegradation of those effluents were carried out. The effluents showed values lower than threshold values for almost all the parameters except pH, total nitrogen, TOC, COD and BOD₅. Although with high organic load, the effluents from discarded medical components (DMC) and animal tissues (AT) showed a percentage of aerobic biodegradation of 50.5 and 52.9%, respectively. The anaerobic biodegradability obtained for the effluents from DMC were 22.3 and 42.2% for those with AT.     

Techno-Economic Assessment Of Biological Treatment And Water Reuse Of Effluent From The Food Industries

Treatment of high strength wastewater generated by food plants requires a development of cost effective wastewater treatment schemes and exploration of viable means for treated water reuse. This paper addresses the techno-economic aspects of a combined biological treatment scheme comprising anaerobic digestion and aerobic biological filters. Advanced water treatment for reuse includes multimedia filtration, activated carbon adsorption and membrane separation. Analysis of the results of the combined performance of the anaerobic/aerobic treatment indicates that treating high strength wastewater could be achieved by an upflow anaerobic sludge blanket (UASB) reactor and high rate trickling filter. Typical biological treatment capital and operating costs are about 1.3 million dollars and 131,000 dollars, respectively, for a treatment facility of about 4000 v m 3 /day to produce effluents of COD about 30 v mg/l. Water reuse costs ranged from US$ 0.034 to US$ 0.38/m 3 based on the salt content and residual dissolved organic matter.     

Efficiency of industrial minerals on the removal of mercury species from liquid effluents

Increasing attention has been given, by the industrial sector, to the removal of heavy metals from liquid effluents to satisfy environmental regulations. For this purpose, the most common methods utilized include: chemical precipitation, cementation, ion exchange, adsorption and solvent extraction. All these methods have limitations such as slow kinetics, low adsorption capacity and they are usually very expensive. Thus, new technologies for heavy metal removal are of great interest. This study consisted on a screening of industrial minerals to check their efficiencies to remove mercury from liquid effluents. The methodology employed a batch adsorption technique. The tested minerals included: atapulgites, zeolites, magnetites, kaolin, vermiculite and bentonite. Results show relatively high efficiencies of magnetite and zeolite on mercury removal. These minerals were capable to remove mercury species from effluents with concentrations reaching 1,000 ppm, corresponding to a sorption capacity of 10,000 mg Hg/kg. The sorption maximum was not reached in these tests. In addition, it became evident the importance of mercury speciation at the solid:liquid interface, with relevant consequences on the application of this technology to effluent treatment.     

Study on the treatment of the sulfite pulp CEH bleaching effluents with the coagulation-anaerobic acidification-aeration package reactor

The coagulation-anaerobic acidification-aeration package reactor was designed for the treatment of pulp CEH bleaching effluents, the efficiencies in CODcr, BOD(5), AOX and toxicity removal achieved were 88.1%, 81.0%, 98.4% and 92.0%, respectively, with 15 h HRT. The toxicity and AOX were removed mainly through coagulation and anaerobic process, while the COD and BOD(5) were removed mainly through coagulation and aerobic process. The pretreatment of coagulation precipitation decreased the following organic load, which decreased the following treatment retention time and increased the stability of the system.The results of GC-MS showed: pollutants of wastewater were mainly chlorinated organics, most of AOX and the toxicity were removed by reductive dechlorination and acidified hydrolysis in anaerobic unit, the high COD removal in aerobic unit showed further degradation of pollutants. Chlorine atoms in the ortho position were preferentially dechlorination, that in para position were difficult to remove from chlorinated phenols during biological treatment.     

Hazards of Industrial Anaerobic Digester Effluent Discharges to Sewer

With the increase in use of anaerobic digesters in industry, there is concern that the direct discharge of effluents (from such plants) to sewer could cause explosive conditions because of increased methane production. The study explored this issue by undertaking laboratory analyses of methane-production rates of sewage and anaerobic digester effluents. A particular sewer was studied and basic calculations were undertaken to try and establish the risk of methane build-up to dangerous levels.     

Anaerobic filter reactor performance for the treatment of complex dairy wastewater at industrial scale

The wastewaters discharged by raw milk quality control laboratories are more complex than the ones commonly generated by dairy factories because of the presence of certain chemicals such as sodium azide or chloramphenicol, which are used for preserving milk before analysis. The treatment of these effluents has been carried out in a full-scale plant comprising a 12 m(3) anaerobic filter (AF) reactor and a 28 m(3) sequential batch reactor (SBR). After more than 2 years of operation, a successful anaerobic treatment of these effluents was achieved, without fat removal prior to the anaerobic reactor. The organic loading rates maintained in the AF reactor were 5-6 kg COD/m(3) d, with COD removal being higher than 90%. No biomass washout was observed, and most of the fat contained in the wastewaters was successfully degraded. The addition of alkalinity is crucial for the maintenance of a proper buffer medium to ensure pH stability. The effluent of the AF reactor was successfully treated in the SBR reactor, and a final effluent with a COD content below 200 mg/l and total nitrogen below 10mg N/l was obtained.     

Mineralization of organic matter and other chemical effects of chlorination

Selected river waters, estuarine waters and effluents from wastewater treatment plants, collected during various seasons, have been treated with 0.14 mM (10 ppm) chlorine in order to determine the reactive components involved in chlorine decay reactions. Mineralization of organic matter, detected by measuring evolved CO₂, was universal and constituted the most significant decay process observed. In most cases, loss of ammonia, primary organic amines and nitrite occurred, but removal of these components was not complete. Nitrate was usually produced, but the increases were small relative to initial concentrations. Ammonia in secondary effluent retards chlorine decay and suppresses carbon mineralization. After a week, renewed microbial growth began in anaerobic river water treated with monochloramine even though residual monochloramine remained. The onset of growth coincided with accelerated decay of the monochloramine residual, suggesting that reducing agents were being produced biologically. The faster decay of residual chlorine in denitrified secondary effluents, with low ammonia, demonstrates an additional environmental benefit of denitrification.     

Biodegradation of pollutants in the effluents of food industry enterprises

The article has investigated the processes of obtaining biogas by means of anaerobic fermentation of the effluents of food production in periodic and continuous modes with their subsequent add-on treatment by the method of aerobic fermentation.     

An expert system for monitoring and diagnosis of anaerobic wastewater treatment plants

In this paper, an expert system (ES) developed for the monitoring and diagnosis of anaerobic wastewater treatment plants (AWT), is presented. The system was evaluated in a hybrid pilot plant of 1.1 m3 located in an industrial environment for the treatment of wastewaters from a fibreboard production factory. The reactor is a hybrid USBF, combining an upflow anaerobic sludge blanket (UASB) in the lower part and an upflow anaerobic filter (UAF) at the top.     

Treatment of sewage and industrial wastewater effluents by the cyanobacteria Nostoc muscorum and Anabaena subcylinderica

The potential of two cyanobacteria, Nostoc muscorum and Anabaena subcylindrica to treat sewage and industrial wastewater effluents was investigated. Two different sites were selected for this study which are located at the drains of sewage plant, a salt and soda production company at Kafr El-Zayat city. All samples were taken from the sewage and/or industrial effluents before treatment. Treatment of the sewage and industrial wastewater effluents by using cyanobacteria (N. muscorum, A. subcylindrica and mixed culture of both) revealed that the pH value of the biologically treated wastewater increased, the electrical conductivity was recovered in a range between (4.7–23.9%) and the total dissolved solids were reduced by (4.4–23.3%). The reduction of turbidity level was in a range between (40–96.4%). The removal efficiency of organic matter (COD, PV) was in a range between (20–57.1%) and (25.7–66.7%), respectively. Phosphorus reduction, nitrate treatment and ammonia elimination efficiencies by cyanobacterial system were (20.8–95%), (19.6–80%) and (20.9–96%), respectively. With respect to the treatment efficiency of wastewater by using single or mixed cultures of cyanobacteria, it was observed that the single cultures in most cases was better than the mixed cultures and this may be due to the competition between mixed cultures for nutrients. However, it could be concluded from the presented data that the treatment of wastewater by cyanobacteria is a fruitful method to produce an effluent of high quality to be used for irrigation.     

Sources and behaviour of bismuth active substances (BiAS) in a municipal sewage treatment plant

Non-ionic surfactants are widely used for household and industrial purposes. For different reasons the metabolites, e.g. 4-nonylphenol, nonylphenol monoethoxylate, nonylphenol diethoxylate and 4-tert-octylphenol, are especially considered to be endocrine disruptive and thus potentially harmful for the environment. In this study, field samples of raw wastewater from different point sources, including industrial effluents, household effluents, the influent and secondary effluent of a wastewater treatment plant that treats this wastewater were monitored simultaneously. Composite samples were taken five times over periods of 1 week at nine sample sites. The results showed that the concentrations and fluxes were varying. In addition industrial, influent and effluent samples were investigated for nonylphenol (NP). The highest concentrations of bismuth active substances (BiAS) were obtained by wastewater samples from a chemical and a cloth washing company ranging from 10,200 to 65,600 microg/l and 14,600 to 33,900 microg/l BiAS, respectively. Although the concentration of BiAS in the wastewater of the paper production was only between 460 and 1200 microg/l BiAS, the NP/BiAS ratio of 0.51% was considerably higher than in other industrial effluents. The BiAS concentration in wastewater samples from households ranged from 2200 to 7900 microg/l BiAS, but the NP concentration was quite low, 0.01% of BiAS. This could be due to the effort within the EU to phase out nonylphenol polyethoxylates in household detergents. Influent concentrations between 700 and 2200 microg/l BiAS with removal rates in the WWTP ranging from 70.7 to 99.4% with an average of 92.2% could be measured.     

Biological sulphate removal in an upflow packed bed reactor

Mine waters and industrial effluents with high sulphate concentrations create a disposal problem in terms of excess mineralization of surface waters. Removal of sulphate can be achieved by various processes including biological techniques, all of which involve appreciable costs. The purpose of this investigation was to improve on known biological methods for the removal of sulphate. Good sulphate removal was obtained by providing anaerobic conditions on a solid medium and maintaining a low hydrogen sulphide concentration by recirculating the water through a photosynthetic reactor for sulphur production.     

Nonylphenol polyethoxylate degradation in aqueous waste by the use of batch and continuous biofilm bioreactors

An aerobic bacterial consortium (Consortium A) was recently obtained from textile wastewater and was capable of degrading 4-nonylphenol and nonylphenol polyethoxylates (NPnEOs). In the perspective of developing a biotechnological process for the treatment of effluents from activated sludge plants fed with NPnEO contaminated wastewater, the capability of Consortium A of biodegrading an industrial mixture of NPnEOs in the physiological condition of immobilized cells was investigated. Two identically configured packed bed reactors were developed by immobilizing the consortium on silica beads or granular activated carbon. Both reactors were tested in batch and continuous mode by feeding them with water supplemented with NPnEOs. The two reactors were monitored through chemical, microbiological and molecular integrated methodology. Active biofilms were generated on both immobilization supports. Both reactors displayed comparable NPnEO mineralization under batch and continuous conditions. FISH analyses evidenced that the biofilms evolved with time by changing the reactor operation mode and the organic load. Taken together, the data collected in this study provide a preliminary strong indication on the feasibility of Consortium A-based biofilm technology for the decontamination of NPnEO containing effluents.     

Anaerobic/aerobic treatment of coloured textile effluents using sequencing batch reactors

Conventional biological wastewater treatment plants do not easily degrade the dyes and polyvinyl alcohols (PVOH) in textile effluents. Results are reported on the possible advantages of anaerobic/aerobic cometabolism in sequenced redox reactors. A six phase anaerobic/aerobic sequencing laboratory scale batch reactor was developed to treat a synthetic textile effluent. The wastewater included PVOH from desizing and an azo dye (Remazol Black). The reactor removed 66% of the applied total organic carbon (load F: M 0.15) compared to 76% from a control reactor without dye. Colour removal was 94% but dye metabolites caused reactor instability. Aromatic amines from the anaerobic breakdown of the azo dyes were not completely mineralised by the aerobic phase. Breakdown of PVOH by the reactor (20-30%) was not as good as previous reports with entirely aerobic cultures. The anaerobic cultures were able to tolerate the oxygen and methane continued to be produced but there was a deterioration in settlement.