A review of the sustainable value of effluents and sludges from wastewater stabilization ponds

Sludges and liquids from wastewater stabilization ponds are cost effective by-products useful for agriculture, aquaculture and for manufacturing building materials. They represent valuable sustainable resources as raw materials to support fisheries for human consumption, to produce animal feed derived from single cell algal proteins and aquatic weeds. Biogas from waste fermentation represents a significant tertiary product.Stabilization ponds are dynamic, low-cost waste recycling ecosystems comprising complex communities of algae, virus, protozoa, rotifers, insects, crustaceans and fungi. These organisms interact and modify the organic content of the waste to produce effluents which need little further investment in treatment.The economic, societal and sustainable value of stabilization ponds is governed by the management regime and the use for which the sludge and effluent is intended. Fish, ducks, prawn and algal protein production rely upon adequately treated effluent. This is particularly valuable for irrigation in arid and semi-arid climates, where natural waters are insufficient and nutrient depleted. Oxidation ponds provide sustainable mechanisms for dealing with sewage and for reducing the risk of infection from parasites and the effects of toxins. The resulting sludges can be used as fertilizer or be composted with local vegetation. Aerobic and anaerobic digestion, lime treatment and pasteurisation are used to improve sludge acceptability and utility to enhance its value as a sustainable resource.     

Algae flocculation in reservoir water

Removal of algae in the reservoir water was studied by electroflocculation using a bipolar cell with aluminum electrodes and flocculation by treatment with commercial alum. Comparison of both the methods is discussed.     

Cadmium tolerance and antibiotic resistance in Escherichia coli isolated from waste stabilization ponds

The incidence pattern of cadmium tolerance and antibiotics resistance by Escherichia coli was examined periodically from the samples of water, sludge and intestine of fish raised in waste stabilization ponds in a sewage treatment plant. Samples of water and sludge were collected from all the selected ponds and were monitored for total counts of fecal coliform (FC), total coliform (TC) and the population of Escherichia coli, which was also obtained from the intestine of fishes. Total counts of both FC and TC as well as counts of E. coli were markedly reduced from the facultative pond to the last maturation pond. Tolerance limit to cadmium by E. coli tended to decline as the distance of the sewage effluent from the source increased; the effective lethal concentration of cadmium ranged from 0.1 mM in split chamber to 0.05 mM in first maturation pond. E. coli isolated from water, sludge and fish gut were sensitive to seven out of ten antibiotics tested. It appears that holistic functions mediated through the mutualistic growth of micro algae and heterotrophic bacteria in the waste stabilization ponds were responsible for the promotion of water quality and significant reduction of coliform along the sewage effluent gradient.     

Flocculation of microalgae in brackish and sea waters

Flocculation is an essential step in the concentration and harvesting of microalgae from aquatic media. Salinity of brackish water and sea water requires high flocculant dosages and renders flocculation less effective than in freshwater algal media. Experiments with the marine microalgae Isochrysis galbana and Chlorella stigmatophora showed that effective alum or ferric chloride flocculation was obtained only with dosages which are 5 to 10 times higher than the dosages required for the flocculation of freshwater microalgae. The flocculant dosages required for removing over 90% of the algae from suspensions were found to increase linearly with salinity as expressed in ionic strength. High salinity was found to inhibit flocculation with polyelectrolytes which are quite effective in freshwater algae flocculation. This inhibition was diminished at reduced salinity levels and effective flocculation was attained at salinity levels of 5 g/liter and below, which is typical of desert brackish water. Two methods were found to induce flocculation in sea water: (a) combining polyelectrolytes with inorganic flocculants such as ferric chloride or alum, and (b) ozone oxidation pretreatment followed by flocculation with inorganic flocculants.     

Positively charged filters for virus recovery from wastewater treatment plant effluents.

Positively charged Zeta Plus filters were used to concentrate enteroviruses from 19 liters of effluent from activated sludge units. Neither the addition of salts nor the acidification of the effluent was required for adsorption of viruses to the filters. Viruses adsorbed to the filters were eluted by treating the filters with a solution of 4 M urea buffered at pH 9 with 0.05 M lysine. Eluted viruses were concentrated into final volumes of 1 to 2 ml by using a two-step concentration procedure that employed inorganic and organic flocculation. Approximately 50% of the viruses added to effluents could be recovered in the final sample. The procedure was used to monitor effluents from activated sludge units at two wastewater treatment plants for the presence of enteroviruses.     

Pollution control in pulp and paper industrial effluents using integrated chemical–biological treatment sequences

The main objective of the present study was to improve the quality of pulp and paper industrial wastewater of two local mills RAKTA and El-Ahlia, Alexandria, Egypt, and to bring their pollutant contents to safe discharge levels. Quality improvement was carried out using integrated chemical and biological treatment approaches after their optimization. Chemical treatment (alum, lime, and ferric chloride) was followed by oxidation using hydrogen peroxide and finally biological treatment using activated sludge (90 min for RAKTA and 60 min for El-Ahlia effluents). Chemical coagulation produced low-quality effluents, while pH adjustment during coagulation treatment did not enhance the quality of the effluents. Maximum removal of the tested pollutants was achieved using the integrated treatment and the pollutants recorded residual concentrations (RCs) of 34.67, 17.33, 0.13, and 0.43 mg/l and 15.0, 11.0, 0.0, and 0.13 mg/l for chemical oxygen demand (COD), biochemical oxygen demand (BOD₅), tannin and lignin, and silica in RAKTA and El-Ahlia effluents, respectively, all of which were below their maximum permissible limits (MPLs) for the safe discharge into water courses. Specific oxygen uptake rate (SOUR) and sludge volume index (SVI) values reflect good conditions and healthy activated sludge. Based on the previous results, optimized conditions were applied as bench scale on the raw effluents of RAKTA and El-Ahlia via the batch chemical and the biological treatment sequences proposed. For RAKTA effluents, the sequence was as follows: (1) coagulation with 375 mg/l FeCl₃, (2) oxidation with 50 mg/l hydrogen peroxide, and (3) biological treatment using activated sludge with 2,000 mg/l initial concentration and 90 min hydraulic retention time (HRT), while for El-Ahlia raw effluents, the sequence was (1) coagulation with 250 mg/l FeCl₃, (2) oxidation with 45 mg/l hydrogen peroxide, and (3) biological treatment using activated sludge with 2,000 mg/l initial concentration and 60 min HRT. In conclusion, results confirmed that the application of the proposed sequential treatments removed almost all COD, BOD₅, high molecular weight compounds, and silica from RAKTA and El-Ahlia influents and produced high-quality effluents, thus achieving the main objective of this study.     

Performance of constructed wetlands in the reduction of cadmium in a sewage treatment cum fish farm at Kalyani, West Bengal, India

The distribution pattern of cadmium was investigated in waste stabilization ponds designed for three-step sewage treatment processes. The overall mean concentration of cadmium in water and sludge was reduced by 30% and 33%, respectively, from the inlet of the anaerobic pond to the final outlet of the maturation pond. The level of cadmium in water hyacinth, plankton and fish remained higher in all the samples collected from the anaerobic or facultative pond compared to the last maturation pond. It may be reasonable to conclude that three-step ecological treatments accompanied by physical, chemical and biological processes of the waste stabilization ponds were effective in reducing the load of cadmium from sewage effluents.     

用藻类监测和评价图们江的水污染

在图们江上、中游进行了人工基质着生藻类调查和室内栅藻检测,以监测和评价水污染状况。在所采用的野外监测指标中,以着生藻类总数与污染程度的关系最为明显。为便于比较和综合,采用了相对藻类总数(PN) 根据调查结果,提出了可作为图们江污染的指示种类。多样性指数与污染的关系,因受到其他非污染因子的影响,并不稳定。研究结果表明:图们江的主要污染源是尾矿废水(悬浮物)和纸浆废水(悬浮物、色度和有毒物质)。最严重污染江段为菜队到图们江段,次之为南坪江段。       

Advanced primary treatment of waste water using a bio‐flocculation‐adsorption sedimentation process

An advanced primary treatment process for a municipal waste water was systematically studied, using a bio‐flocculation‐adsorption, sedimentation and stabilzation process (BSS). It was shown that the organic removal efficiency was higher than that of the traditional primary treatment processes but lower than that of the traditional secondary treatment processes. Both adsorption and bio‐flocculation played an important role in the removal of pollutants. The activated sludge within the bio‐flocculation‐adsorption tank could be considered a bio‐flocculent which improved the quality of the effluent from the primary treatment process. As the effluent of the BSS process did not meet the requirements for a typical secondary effluent, the process may be regarded as an advanced (or enhanced) primary treatment process, suitable for waste water containing a high concentration of suspended solids and colloidal particles.     

Anionic surfactants in treated sewage and sludges: risk assessment to aquatic and terrestrial environments

Compared to low concentrations of anionic surfactants (AS) in activated sludge process effluents (ASP) (<0.2 mg/L), upflow anaerobic sludge blanket-polishing pond (UASB-PP) effluents were found to contain very high concentrations of AS (>3.5 mg/L). AS (or linear alkylbenzen sulfonate, LAS) removals >99% have been found for ASP while in case of UASB-PP it was found to be < or = 30%. AS concentrations averaged 7347 and 1452 mg/kg dry wt. in wet UASB and dried sludges, respectively. Treated sewage from UASB based sewage treatment plants (STPs) when discharged to aquatic ecosystems are likely to generate substantial risk. Post-treatment using 1-1.6d detention, anaerobic, non-algal polishing ponds was found ineffective. Need of utilizing an aerobic method of post-treatment of UASB effluent in place of an anaerobic one has been emphasized. Natural drying of UASB sludges on sludge drying beds (SDBs) under aerobic conditions results in reduction of adsorbed AS by around 80%. Application of UASB sludges on SDBs was found simple, economical and effective. While disposal of treated UASB effluent may cause risk to aquatic ecosystems, use of dried UASB sludges is not likely to cause risk to terrestrial ecosystems.     

Remediation of dyes in textile effluent: a critical review on current treatment technologies with a proposed alternative

The control of water pollution has become of increasing importance in recent years. The release of dyes into the environment constitutes only a small proportion of water pollution, but dyes are visible in small quantities due to their brilliance. Tightening government legislation is forcing textile industries to treat their waste effluent to an increasingly high standard. Currently, removal of dyes from effluents is by physio-chemical means. Such methods are often very costly and although the dyes are removed, accumulation of concentrated sludge creates a disposal problem. There is a need to find alternative treatments that are effective in removing dyes from large volumes of effluents and are low in cost, such as biological or combination systems. This article reviews the current available technologies and suggests an effective, cheaper alternative for dye removal and decolourisation applicable on large scale.     

Treatment of APMP pulping effluent based on aerobic fermentation with Aspergillus niger and post-coagulation/flocculation

A novel two-stage biological/flocculation process was developed for treating the pulping effluent from the alkaline peroxide mechanical pulping (APMP) process. In the first biological stage, the aerobic fermentation by using Aspergillus niger can decrease the chemical oxygen demand (COD) by about 60% while producing about 7 g/l of solid biomass. In the second stage (post-coagulation/flocculation), the residual COD, turbidity and color, can be further decreased by using alum and polyacrylamide (PAM). The overall removal efficiencies of COD, color and turbidity from the APMP pulping effluent by the above two-stage biological-coagulation/flocculation process were 93%, 92% and 99%, respectively, under the conditions studied.     

Distribution of heavy metals in a sewage oxidation pond and their adsorption in residual solid (sewage sludge ash)

Abstract

Electrometric studies were carried out on the interaction of heavy metal ions such as manganese, chromium, nickel, copper, zinc, cadmium and lead with the extracted organic matter, humic and fulvic acid from the sludge in a sewage oxidation pond. The distribution of heavy metals was between 60 and 97%, which is associated with the solid waste (sludge) of the oxidation pond. The adsorption/removal efficiency of metal ions onto the sludge ash was more than 90% and 97%, respectively, in the pure system. To obtain the ash, the sludge was burnt at 500°C, treated with nitric acid (1+1) to leach out all the metals and then filtered; the residue left on the filter paper was the pure ash. Both this and that coated with organic matter were studied. The adsorption isotherm for metals, humic/fulvic acids and metal-humic/fulvic acid complexes in the metal-free sludge ash and in the organic matter in the pure system were studied using the Freundlich relationship. Good agreement was found suggesting that sediment and humic/fulvic acids have an important role in the mobility, dispersion and sedimentation of metal ions in an aquatic environment. More of these heavy metals are removed in the pure system than in the natural system. This may be due to the lesser availability of humic and fulvic acids in the lagoons during the short detention time of sewage in suspension in the oxidation pond, whereas the sludge which has settled to the bottom of the pond for several years contains rich decomposed organic matter in the form of humic and fulvic acids containing heavy metals. Such pure systems could be useful for the effective removal of heavy metals.     

Coagulant selection and sludge conditioning in a slaughterhouse wastewater treatment plant

Attempts were made in this study to examine the effectiveness of polymer addition to the aeration tank effluent prior to sludge flotation as practiced in a slaughterhouse wastewater treatment plant. The plant currently uses 10 mg/l of polymer prior to sludge flotation, but alternative, less-expensive, chemicals such as alum could be equally effective. Therefore, experiments were conducted using the Standard Jar test to determine the performance of both alum (Al2SO4.6H2O) and organic polymer. The dosages used for alum ranged between 0 and 1000 mg/l, whereas polymer dosages varied between 0 and 90 mg/l. The (optimal) removal efficiency for suspended solids in the mixed liquor was obtained at 400 mg/l for alum and 30 mg/l for polymer. It is evident that addition of alum or polymer results in significant removal of suspended solids reaching up to 99% for alum and 96% for polymer but alum produced a more compacted sludge. Removal of filterable COD was much lower in both cases since the chemicals used target the colloidal and suspended portion of the COD rather than the soluble (filterable) part of the COD.     

铝盐-淀粉复合絮凝剂污水处理效果研究

以模拟废水、生活污水、市政污水和制浆造纸废水为实验对象,检验了一种新合成铝盐一淀粉复合絮凝剂中试产品(CAS)的污水处理效果．结果表明,与聚合氯化铝(PAC)相比较,CAS处理不同浓度(100、400和2000mg·L^-1)高岭土模拟废水时最佳投加量分别为3．0、2．0和2．0mg·L^-1,为PAC最佳投加量的60％、50％和50％;同时CAS对该废水、生活污水、市政污水的浊度去除效果略优于PAC,但COD去除率明显高于相同剂量的PAC;处理高浓度制浆造纸污水时,CAS投加量相当于PAC用量的70％。COD处理率提高10％,污泥量减少40％.     

有机磷农药生产废水氧化塘处理的静态和动态模拟试验

马拉硫磷、对硫磷、乐果、二甲基二硫代磷酸酯和二乙基硫代磷酸酯在藻菌共生系统中是可以被分解的,它们的半分解期分别为2、5、2、42和62天。氧化塘模拟试验结果指出,废水中TOC、COD、和有机磷的去除率分别为65.1%、68.7%和67.8%。根据试验,提出了采用多级串联氧化塘处理葛店化工厂农药废水的参数以及控制鸭儿湖地区污染的方案。       

Growth of Spirulina maxima algae in effluents from secondary waste-water treatment plants

Spirulina maxima, a high protein alga, was grown in effluents from the London municipal waste treatment plant. Optimum growth conditions were developed, the composition of algae and the removal of nitrogen and phosphorus in effluents were studied. The advantages of this process in tertiary waste-water treatment and the quality of the single cell protein were investigated.     

Ettlia oleoabundans growth and oil production on agricultural anaerobic waste effluents

The feasibility of growth and oil production by Ettlia oleoabundans fed with anaerobic digester effluents of three agriculture wastes from the Arkansas Delta, catfish processing waste, soybean field waste, and rice hulls, was studied. Compared to standard BBM medium, all three effluents were deficient in phosphate and nitrate, but rich in ammonia and urea. Best growth was on 2% (v/v) soy effluent, but scant oil was produced on any of the effluents. When the three effluents were mixed, growth did not substantially increase, but oil content increased up to sixfold, depending on age of the effluent. Similar to growth in BBM, the main fatty acids produced were palmitic, oleic, and linoleic. These results show that anaerobically digested agricultural wastes can potentially support both growth and high oil productivity in E. oleoabundans.     

Purification of coal gasification combined with brewery waste waters in upflow anaerobic sludge blanket digesters

Laboratory-scale upflow anaerobic sludge blanket (UASB) digesters containing granular sludge adapted to brewery effluent were fed increasing concentrations of artificial coal gasification (CG) waste water in brewery effluent and were effective at purifying this combined waste water up to a CG effluent concentration of 15%. At higher CG waste water concentrations and flow rates, performance declined rapidly.