Humanpharmakawirkstoffe in der Umwelt: Einträge, Vorkommen und der Versuch einer Bestandsaufnahme

Background

The presence of a large spectrum of pharmaceutical agents has been reported for aquatic environments (surface—and groundwater) and other aquatic media (influents and effluents of sewage treatment plants) in Germany and beyond, including their occurrence in drinking water. Considering the large number of pharmaceuticals produced for human use and released into the environment, various authors (Sattelberger 1999, Hanisch et al. 2004, Castiglioni et al. 2006, IWW 2006, Stockholm County Council 2006) tried to compile ‘priority lists’ focusing on those substances with environmental relevance. The following agents are included in all lists: ciprofloxacine, clarythromycine (antibiotics), carbamazepine (anti-epileptic agent), bezafibrate (lipid reducer), clofibric acid (lipid reducer metabolite), ethinylestradiol (sex hormone) and cylophosfamide (cytostatic agent). The agents erythromycine and sulfamethoxazole (antibiotics), ibuprofen, indometacine, propyphenazone (analgesics), atenolol (beta-blocker) and ifosfamide (cytostatic agent) can be found in three of four priority lists.

Results

Pharmaceuticals mainly enter the aquatic environment via effluent water, coming from wastewater treatment plants (including hospital and household sewerage), untreated discharges (e.g, secondary transfer of active agents into ground- and surface waters via sewage sludge application in agriculture and via landfill leachate) and leakages in the municipal sewer network.

Discussion

Potential activities towards a reduced release of pharmaceuticals into the environment should consider primarily the origin of the exposure to allow a separation of drug containing flows already at the source. Following the latter it would be possible to minimize the contamination of spring-, ground- and surface waters which serve as raw water resources for drinking water supply. However, considering the actual water pollution with pharmaceuticals and other substances, ‘end-of pipe’ techniques in the sewage and drinking water treatment are absolutely essential.

Conclusions

Sustainability criteria (e.g. protection of drinking water resources, habitats and biocoenoses, recycling and economizing use of resources) and economic aspects of modern sewage disposal concepts require a useful choice and combination of technical measures as components of centralized and decentralized sewage and drinking water treatment methods. It is though not realistic to cover and eliminate all pharmaceutical agents of environmental relevance equally effective even if a catalogue of potential technical treatment methods is elaborated thoroughly. Therefore, a concentration of efforts on selected drug agents, at least following initially some of the priority lists, is recommended.

Recommendations and Perspectives

The contamination of the water cycle with pharmaceuticals is nevertheless not exclusively to be solved via the application of technical methods. The BMBF (Federal Ministry for Education and Research) funded project start (Management Strategies for Pharmaceuticals in Drinking Water, www.start-project.de) therefore tries by implementation of a transdisciplinary approach to integrate technical-, behavioral-, and agent-orientated management strategies towards a more comprehensive and sustainable problem solution.     

Verhalten von Nanosilber in Kläranlagen und dessen Einfluss auf die Nitrifikationsleistung in Belebtschlamm

Background, aim and scope The application of nanosilver is increasing. Knowledge on the fate and behavior of nanosilver in wastewater and wastewater treatment plants is scarce. Studies under real world conditions are completely lacking. We studied (1) the impact of nanosilver on the nitrification of sewage sludge, (2) quantified the mass flow of nanosilver in a pilot-plant, and (3) verified the mass balance in a full-scale municipal wastewater treatment plant where nanosilver is introduced to the municipal plant by an indirect discharger. Materials and Methods The addition of four different nanosilver additives on ammonia oxidation in activated sludge has been studied in batch-reactors at two concentrations (1, 100?mg/L Ag) with two exposure times (2?h, 6?days). The pilot-plant treating 70 population equivalents of domestic wastewater is operated with a 12?day sludge age. Nanosilver was applied to the activated sludge tank within two sludge ages. The silver concentrations were measured in sludge and effluent samples during dosing and the following two sludge ages. The adsorption and speciation of silver particles has been analyzed using scanning electron microscopy (SEM) coupled with energy dispersive X-ray spectroscopy (EDX). Influent, effluent and sludge were sampled on a full-scale plant (60?000 equivalent inhabitants) and analyzed for silver. Results Silver nitrate, metallic nanosilver, nano-scaled silver chloride and microcomposite silver did not show any effect on ammonia oxidation after the addition of 1?mg/L Ag to the activated sludge (corresponding to 250?mg Ag per kg solids). In contrast, 100?mg/L Ag inhibited the nitrification process by 100?% after the addition of silver nitrate and 20–30?% after addition of colloidal polymer-coated nanosilver. A complete mass balance of the pilot-plant, a steady-state system with known fluxes, demonstrates significant enrichment of silver in the sewage sludge (96?%) after the addition of silver chloride to the plant and small losses of silver into the secondary effluent (4?%). The mass fluxes are similar to metallic colloidal nanosilver investigated under the same conditions. The mass balance has been consistently confirmed by the full-scale study in a municipal wastewater treatment plant. The silver fluxes correspond to the fluxes of the suspended solids in sludge and effluent. Overall, it is estimated that from public wastewater treatment plants about 4–40?mg/a Ag per inhabitant equivalent are discharged annually to the receiving water. The analysis by SEM-EDX demonstrates adsorption and incorporation of nanosilver on biological flocs. This method yields first insight into complex building and transformation of silver associated with sulfide after adding metallic nanosilver and silver chloride to wastewater. Discussion Silver ions released from nanosilver react immediately with large amounts of chloride present in wastewater to form silver chloride. Silver ions may react with organic ligands or sulfide groups additionally. Consequently, even silver nitrate added with 1?mg/L Ag (250?mg Ag/kg TS) to activated sludge did not inhibit nitrification activity. Very high amounts of nanosilver, i.?e. 100?mg/L Ag, overburdened the system and equilibrium condition between silver ion release and ligands was not reached. The mass balance reflects the excellent attachment of nanosilver to activated sludge and biological flocs. Therefore, the main elimination process of nanosilver is attachment to the activated sludge. The elimination of nanosilver is high compared to organic and inorganic micro pollutants omnipresent in wastewater. Any further reduction of suspended solids in the effluent water will reduce the silver load. Conclusions Generally, in wastewater nanosilver occurs bonded to activated sludge flocs and therefore the elimination of nanosilver is efficient under operation conditions typical for wastewater treatment plants. The major fraction of nanosilver is removed from the system by the excess sludge withdrawal. Nonetheless, the efficiency may be further improved by a tertiary filtration step. All analyses of influent, effluent and sludge confirmed that silver exists as silver sulfide. Due to a negligible water solubility of this silver species, silver ions are not subsequently released. Recommendations and perspectives Nanosilver research should be driven to the identification of transformation processes in real environmental matrices and the influence of coatings on the adsorption behavior. There is no need for action to take special measures for nanosilver removal in the area of municipal wastewater treatment plants compared to ubiquitous hazardous organic pollutants may present in wastewater. Nevertheless, source control measures following the precautionary principle should be performed.     

Occurrence and behavior of pharmaceuticals in sewage treatment plants in eastern China

The occurrence and removal efficiency of seven pharmaceuticals (norfloxacin, trimethoprim, roxithromycin, sulfamethoxazole, ibuprofen, diclofenac and carbamazepine) were determined in three sewage treatment plants (STPs) with anaerobic/anoxic/oxic, anoxic/oxic and oxidation ditches processes in Xuzhou City, Eastern China. The results showed that seven pharmaceuticals were detected in the influent samples with concentrations ranging from 93 to 2540 ng·L⁻¹. The removal of these substances among the three different STPs varied from 36 to 84%, with the highest performance obtained by the wastewater treatment works with tertiary treatment (sand filtration). Most of the compounds were removed effectively during biologic treatment while sand filtration treatment also made a contribution to the total elimination of most pharmaceuticals. The efficiency comparison of the three sewage treatment processes showed that the STP which employed anaerobic/anoxic/oxic was more effective to remove pharmaceuticals than the oxidation ditches and anoxic/oxic.     

Arzneimittel in der aquatischen Umwelt

The German Environmental Advisory Council evaluated German water protection policies in its last environmental report (2004) concluded that despite some great successes in this area there is still considerable need for action. Specifically, diffuse nutrient and chemical substances inputs remain an unsolved problem. The contamination of surface and groundwater with pharmaceuticals has been identified as an environmental risk increasing in pertinence. Pharmaceuticals and their metabolites are being detected in the whole aquatic environment, which they enter through sewage, soil contamination by agriculture, and waste storage facilities. Different pharmaceuticals have been tested for acute toxicity on various aquatic organisms, but almost nothing is known about chronic toxicity of these contaminants. This knowledge, however, is essential for estimating the ecotoxicological potential of pharmaceutical residues. In the opinion of the Environmental Council different strategies are necessary, to reduce the contamination of the environment with pharmaceuticals. Farmers should refrain from using pharmaceuticals for prophylactic purposes or from using hormonally or antibiotically active substances in livestock feed additives, so as to reduce inputs of veterinary drugs. As regards human medications, packaging should better correspond to appropriate dosage amounts, and environmentally responsible disposal measures should be followed. Still under discussion are a programme for the risk evaluation of existing pharmaceuticals and a ban on the use of sewage sludge in agriculture. In the future, improvement of sewage treatment facilities, for instances through membrane technologies, will offer further potential to reduce inputs of hazardous substances.     

Possible solutions for sludge dewatering in China

In China, over 1.43×10⁷ tons of dewatered sewage sludge, with 80% water content, were generated from wastewater treatment plants in 2007. About 60% of the COD removed during the wastewater treatment process becomes concentrated as sludge. Traditional disposal methods used by municipal solid waste treatment facilities, such as landfills, composting, or incineration, are unsuitable for sludge disposal because of its high water content. Disposal of sludge has therefore become a major focus of current environmental protection policies. The present status of sludge treatment and disposal methodology is introduced in this paper. Decreasing the energy consumption of sludge dewatering from 80% to 50% has been a key issue for safe and economic sludge disposal. In an analysis of sludge water distribution, thermal drying and hydrothermal conditioning processes are compared. Although thermal drying could result in an almost dry sludge, the energy consumption needed for this process is extremely high. In comparison, hydrothermal technology could achieve dewatered sewage sludge with a 50%–60% water content, which is suitable for composting, incineration, or landfill. The energy consumption of hydrothermal technology is lower than that required for thermal drying.     

制革废水处理系统各级出水的生态毒性评价

采用生态毒理学常用的大型溞（Daphnia magna）和活性污泥（activated sludge）作为试验系统,对制革废水处理系统各个环节出水进行毒性试验,以评价其处理效果。按照OECD标准试验方法,选取本实验室繁殖的大型溞（溞龄小于24 h）,和采自以处理生活污水为主的污水处理厂活性污泥,分别使用重铬酸钾和3,5-二氯酚作为参比物验证大型溞和活性污泥的毒性敏感性。以大型溞活动抑制和活性污泥呼吸抑制作为毒性终点,利用48 h静态试验和3 h曝气试验分别评价水样对于大型溞活动和活性污泥呼吸作用的急性毒性效应。统计各试验组大型溞的活动情况和活性污泥的呼吸速率,分别将其与空白对照组进行比较,计算大型溞的活动抑制率和活性污泥的呼吸抑制率,采用Bliss法统计制革废水处理系统各个环节出水对大型溞和活性污泥的半数抑制浓度（EC50）。结果表明：制革废水依次经过厌氧脱硫反应器、脱色厌氧反应器、微曝气反应器和厌氧氨氧化反应器的生物处理系统处理,其出水对大型溞和活性污泥的急性毒性已大为降低。进水、厌氧脱硫反应器出水、脱色厌氧反应器出水、微曝气反应器出水和厌氧氨氧化反应器出水对大型溞活动抑制试验的48 h-EC50分别为41.3%、32.2%、48.0%、91.2%和无抑制作用;活性污泥呼吸抑制试验3 h-EC50则分别为178.2%、101.5%、689.7%、184.6%和无抑制作用。总体上毒性呈现逐渐降低的趋势,而且大型溞比活性污泥更为灵敏。大型溞和活性污泥的生态毒性结果与化学分析的结果相互补充,可为制革废水处理提供预警和效果评价提供科学依据。     

Einsatz eines Sensors zurOnline-Bestimmung der mikrobiellen Aktivität

The activity of microorganisms in the activated sludge can be measured with a bio-activity sensor. The signal of the sensor reacts sensitively to changes in substrate concentrations and the appearance of toxic materials. With the sensor, it is possible to check biological wastewater treatment plants online with regard to their microbial activity and to supervise the flowing sewage with reference to its toxic potential.     

Dehydrogenases activity of activated sludge

A study of dehydrogenases activity of activated sludge, return activated sludge, and waste activated sludge from three sewage treatment plants was made. Dehydrogenases activity and protein content of the mixed liquor varied along the aeration basin. Chromium chloride and zinc sulfate were found to be inhibitory to dehydrogenases activity. Return activated sludge and waste activated sludge, in spite of higher content of volatile suspended solids, contained lower dehydrogenases activity. Return activated sludge when kept without aeration and addition of sewage, showed higher dehydrogenases activity; and on aeration, but without addition of sewage, it showed progressively lower dehydrogenases activity.     

What have we known so far about microplastics in drinking water treatment? A timely review

• 23 available research articles on MPs in drinking water treatment are reviewed. • The effects of treatment conditions and MP properties on MP removal are discussed. • DWTPs with more steps generally are more effective in removing MPs. • Smaller MPs (e.g.,<10 μm) are more challenging in drinking water treatment. Microplastics (MPs) have been widely detected in drinking water sources and tap water, raising the concern of the effectiveness of drinking water treatment plants (DWTPs) in protecting the public from exposure to MPs through drinking water. We collected and analyzed the available research articles up to August 2021 on MPs in drinking water treatment (DWT), including laboratory- and full-scale studies. This article summarizes the major MP compositions (materials, sizes, shapes, and concentrations) in drinking water sources, and critically reviews the removal efficiency and impacts of MPs in various drinking water treatment processes. The discussed drinking water treatment processes include coagulation-flocculation (CF), membrane filtration, sand filtration, and granular activated carbon (GAC) filtration. Current DWT processes that are purposed for particle removal are generally effective in reducing MPs in water. Various influential factors to MP removal are discussed, such as coagulant type and dose, MP material, shape and size, and water quality. It is anticipated that better MP removal can be achieved by optimizing the treatment conditions. Moreover, the article framed the major challenges and future research directions on MPs and nanoplastics (NPs) in DWT.     

Low efficiency of sewage treatment plants due to unskilled operations in India

Centralized sewage treatment plants may not be a sustainable solution for a developing country such as India. Therefore, we conducted for the first time an integrated assessment of the different technologies currently used for sewage treatment in the state of West Bengal, India. Five decentralized sewage treatment plants and one centralized sewage treatment plant located in different parts of Kolkata were evaluated. We compared influent and effluent water quality, energy consumed, capital and operating costs, and treated wastewater reuse potential. F test was used to validate results on the effect of working days and holidays and seasons on treated water quality. Wastewater management strategy was assessed by performance indicators. Our results show that treatment efficiency was lowest in anaerobic plants not because of faulty technology but due to unskilled operation. Therefore, performance improvement of plants is expected if factors such as monitoring, training of staff, regular and scrupulous desludging, reuse aspects, and rational water tariff are implemented earnestly.     

Ökonomisch-organisatorische Betrachtung der Klärschlammverwertung: Kosten — Nutzen — Ausstiegsszenarien

Goal and Scope

The controversial issue of disposing municipal sewage sludge on arable farmland and growing demand on derived fuels could result in a total or partial abandoning of sludge recycling as fertiliser. Alternative disposal strategies like incineration will cause complex changes. A material flow management framework is used to determine the economic-organisational consequences for public authorities, farmers, rural contractors, disposal firms, and population in Schleswig-Holstein.

Methods and Focus

The study is based upon network analysis, analysis of agricultural and wastewater statistics and interviews. After structuring the disposal process, transaction are used to derive costs of different disposal strategies. The purification technique of sewage plant and application of metal salts for precipitation affect the fertilising quality of sludge. Therefore, all plants are classified into 4 different technical groups with decreasing fertilising effect. Now, the amount of sludge and corresponding fertilising benefit is calculated both state wide and for typical farms. Finally costs of different disposal strategies are derived.

Results

Referring to sewage plants sludge disposal in Schleswig-Holstein is characterised by a local structure since less than 10% of all 841 sewage plants produce almost the entire sludge where as many small plants especially in rural areas produce only little amounts. Usually enriched with lime, dewatered sludge fulfilling legal limits is used as organic fertilizer. The number of transactions indicates the costs.

Discussion

To reduce transaction costs, disposal firms try to offer high quantities of sludge to a limited number of farmers. Due to purification technique, the fertilising effect of half the amount of total sludge is reduced. Compared to the total demand on phosphorous, sludge can only substitute up to 4% of phosphorous. Farmers can substitute up to 50% of mineral fertiliser and increase marginal income per hektare. Although changing disposal strategy to incineration would double economic costs, fee for wastewater would remain almost constant.

Conclusions

Small wastewater plants, farmers and rural contractors would be particularly affected by ceasing sludge disposal. Small wastewater plants would have to invest in dewatering equipment, rural contractors would lose an important market segment and farmers (only a small percentage of all farmers uses sludge) would lose additional income. Changing waste management from sludge disposal with many involved parties to e.g. incineration would considerably reduce transaction costs for authorities. In case of partly changing waste management strategy, whereas sludge of small plants could be recycled, the authorities would still have to plan and control the disposal process even for small quantities of sludge. Transaction costs do not decrease proportionally to the decreasing amount of sewage sludge.

Perspectives

Quality management systems initiated by disposal firms should increase the acceptance and prevent a ban of sludge recycling. Nevertheless, the waste market develops from material to energetic use of waste. Significant resources will be lost without a phosphorous recovering from sludge as well as from other organic waste.     

A road-map for energy-neutral wastewater treatment plants of the future based on compact technologies (including MBBR)

In the paper concepts for wastewater treatment of the future are discussed by the use of a) one flow diagram based on established, compact, proven technologies (i.e. nitrification/denitrification for N-removal in the mainstream) and b) one flow diagram based on emerging, compact technologies (i.e. de-ammonification in the main stream).The latter (b) will give an energy-neutral wastewater treatment plant, while this cannot be guaranteed for the first one (a). The example flow diagrams show plant concepts that a) minimize energy consumption by using compact biological and physical/chemical processes combined in an optimal way, for instance by using moving bed biofilm reactor (MBBR) processes for biodegradation and high-rate particle separation processes, and de-ammonification processes for N-removal and b)maximize energy (biogas) production through digestion by using wastewater treatment processes that minimize biodegradation of the sludge (prior to digestion) and pretreatment of the sludge prior to digestion by thermal hydrolysis. The treatment plant of the future should produce a water quality (for instance bathing water quality) that is sufficient for reuse of some kind (toilet flushing, urban use, irrigation etc.). The paper outlines compact water reclamation processes based on ozonation in combination with coagulation as pretreatment before ceramic membrane filtration. In the paper concepts for domestic wastewater treatment plants of the future are discussed by the use of a) one flow diagram based on established, compact, proven technologies (i.e. nitrification/denitrification for N-removal in the mainstream) and b) one flow diagram based on emerging, compact technologies (i.e. de-ammonification in the main stream).The latter (b) will give an energy-neutral wastewater treatment plant, while this cannot be guaranteed for the first one (a). The example flow diagrams show plant concepts that a) minimize energy consumption by using compact biological and physical/chemical processes combined in an optimal way, for instance by using moving bed biofilm reactor (MBBR) processes for biodegradation and high-rate particle separation processes, and de-ammonification processes for N-removal and b)maximize energy (biogas) production through digestion by using wastewater treatment processes that minimize biodegradation of the sludge (prior to digestion) and pretreatment of the sludge prior to digestion by thermal hydrolysis. The treatment plant of the future should produce a water quality (for instance bathing water quality) that is sufficient for reuse of some kind (toilet flushing, urban use, irrigation etc.). The paper outlines compact water reclamation processes based on ozonation in combination with coagulation as pretreatment before ceramic membrane filtration.     

Initial ecological risk assessment of eight selected human pharmaceuticals in Japan.

Eight pharmaceuticals were selected on the basis of their domestic consumption in Japan, the excretion ratio of the parent compound and the frequency of detection in the aquatic environment or wastewater treatment plant effluent. Toxicity tests on these pharmaceuticals were conducted using Japanese medaka (Oryzias latipes), daphnia (Daphnia magna), and green algae (Psuedokirchneriella subcapitata). Predicted no effect concentration (PNEC) was calculated using lethal or effect concentration 50 (LC50 or EC50) values and no effect concentration (NOEC) obtained in the toxicity tests for these compounds. Predicted environmental concentration (PEC) was also calculated from annual consumption, the excretion rate of the parent compound, and removal rate in the preliminary batch activated sludge treatment performed in this study. Maximum concentrations found in the aquatic environment or sewage effluent in Japan or foreign countries were also used for another calculation of PEC. Initial risk assessment on the selected pharmaceuticals was performed using the PEC/PNEC ratio. The results of initial risk assessment on the eight selected pharmaceuticals suggest neither urgent nor severe concern for the ecological risk of these compounds, but further study needs to be conducted using chronic toxicity tests, including reproduction inhibition and endocrine disruption assessments.     

城市污水处理厂污泥处理处置的政策分析

简要介绍了城市污水处理厂污泥处理处置技术，提出污泥产业发展政策的建议，指出土地利用是符合我国国情的污泥处置的方向之一：污泥处理技术主要有减量化、浓缩、脱水、消化、堆肥等；污泥处置技术主要有焚烧、填埋、土地利用、建材利用等。污泥处理处置应按照减量化、稳定化、无害化原则，鼓励污泥资源化综合利用。合理确定污水处理厂污泥处理处置设施的布局和设计规模；鼓励对污泥处理处置给与税、费优惠政策，明确将污泥处理处置的运营费用列入污水排污收费范围，建立科学的价格补偿机制；政府在污泥产业发展中起着较为重要的作用，主要体现为服务与监督，包括承诺、保障和协调三个方面。     

Drinking water biotic safety of particles and bacteria attached to fines in activated carbon process

In this paper, the drinking water biotic safety of particles and bacteria attached to fines in activated carbon process was investigated by actual treatment process and advanced treatment pilot trial with granular activated carbon. In the experiment, the particles were detected by IBR particle calculating instrument, the activated carbon fines were counted on the basis of the most probable number (MPN) with a microscope, the total number of bacteria was analyzed between the conventional agar culture medium and the one with R2A, and the bacteria attached to activated carbon fines was resolved by the homogenization technique. The experimental results showed that the average total number of particles was 205 CNT/mL in the activated carbon effluent during a filter cycle, of which the number of particles with sizes > 2 μm was 77 CNT/mL more than the present particle control criterion of the American drinking water product standard (50 CNT/mL). The backwash of low density and long duration lowered particle number in the effluent. The MPN of activated carbon fines in the effluent was between 400 and 600 CNT/L, which accounted for less than 5‰ of the total particles from activated carbon filtration for a poor relative level (R ² = 0.34). The microorganisms in activated carbon effluent consisted mostly of heterotrophic bacillus and the total bacteria number was five times as high as that of the inflow, i.e. the effluent from sand filter. The actual bacteria number may be truly indicated by the detection technique with R2A culture medium compared with the traditional agar cultivation. The inactivation efficiency of bacteria attached to activated carbon fines was less than 40% under 1.1 mg/L of chlorine contacting for 40 min. Results showed that the particles and bacteria attached to activated carbon fines may influence drinking water biotic safety, and that the effective control measures need to be further investigated.     

制药废水的可生物降解性与生物毒性研究

制药废水有机物含量高,难生物降解成分多,有些成分可抑制污泥活性或具有生物毒性.以某制药企业维生素生产的7个工段(W1 ～ W7)的排放废水为研究对象,用摇瓶试验评价了各工段废水的可生物降解性能,用瓦勃氏呼吸仪测试了各工段废水对污泥活性的抑制作用,用发光菌急性毒性试验评价了各工段废水经好氧生物处理前后的生物毒性变化.研究...     

Titanium dioxide photocatalysis for pharmaceutical wastewater treatment

Heterogeneous photocatalysis using the semiconductor titanium dioxide (TiO₂) has proven to be a promising treatment technology for water purification. The effectiveness of this oxidation technology for the destruction of pharmaceuticals has also been demonstrated in numerous studies. This review highlights recent research on TiO₂ photocatalytic treatment applied to the removal of selected pharmaceuticals. The discussions are tailored based on the therapeutic drug classes as the kinetics and mechanistic aspects are compound dependent. These classes of pharmaceuticals were chosen because of their environmental prevalence and potential adverse effects. Optimal operational conditions and degradation pathways vary with different pharmaceutical compounds. The main conclusion is that the use of TiO₂ photocatalysis can be considered a state-of-the-art pharmaceutical wastewater treatment methodology. Further studies are, however, required to optimize the operating conditions for maximum degradation of multiple pharmaceuticals in wastewater under realistic conditions and on an industrial scale.     

Co-pyrolysis of sewage sludge and biomass for stabilizing heavy metals and reducing biochar toxicity: A review

The huge amounts of sewage sludge produced by municipal wastewater treatment plants induce major environmental and economical issues, calling for advanced disposal methods. Traditional methods for sewage sludge disposal increase greenhouse gas emissions and pollution. Moreover, biochar created from sewage sludge often cannot be used directly in soil applications due to elevated levels of heavy metals and other toxic compounds, which alter soil biota and earthworms. This has limited the application of sewage sludge-derived biochar as a fertilizer. Here, we review biomass and sewage sludge co-pyrolysis with a focus on the stabilization of heavy metals and toxicity reduction of the sludge-derived biochar. We observed that co-pyrolyzing sewage sludge with biomass materials reduced heavy metal concentrations and decreased the environmental risk of sludge-derived biochar by up to 93%. Biochar produced from sewage sludge and biomass co-pyrolysis could enhance the reproduction stimulation of soil biota by 20‒98%. Heavy metals immobilization and transformation are controlled by the co-feed material mixing ratio, pyrolysis temperature, and pyrolysis atmosphere.

     

污水厂污泥制轻质陶粒研究现状及应用前景

作为污水处理厂的副产物，污泥必须进行适当的处理。在介绍了国内外污水厂污泥制轻质陶粒的研究现状的基础上，从陶粒制备工艺、技术可行性、经济效益和环境效益等方面探讨了污水厂污泥制轻质陶粒的应用前景。     

7种酚类化学物质对活性污泥的呼吸抑制作用

苯酚类化学物质是废水中常见的有机污染物,其对活性污泥的毒性数据对于污水处理厂稳定运行和化学品危害性评估具有重要意义。本研究采用活性污泥呼吸抑制试验(209)测定7种酚类化学物质对活性污泥的呼吸抑制作用。结果显示,2,6-二叔丁基苯酚和对特辛基苯酚对活性污泥未产生明显的毒性效应;2,4-二氯酚、2-苯基苯酚、4-硝基酚、4-氯酚和对甲酚等5种化学物质都对活性污泥呼吸有不同程度的抑制效应,3 h-EC50值分别为49.7、77.6、102、150.1和462 mg·L-1,构效关系分析结果表明-Cl、-NO2等官能团是导致活性污泥呼吸抑制效应增强的关键因素。在化学品生物降解性测试研究中,要确保有毒化学物质的测试浓度低于EC50值的1/10。