复合工艺在城市污水处理厂改造中的应用

水污染控制的主要任务是有机物的降解和氮磷的去除。我国现有污水处理厂大多采用传统活性污泥法 ,对于氮、磷的去除往往不能达到新实施的《城镇污水处理厂污染物排放标准 (GB18918- 2 0 0 2 )》的要求。而生物膜、活性污泥复合工艺为我国城市污水处理厂的扩建和改造提供了一条经济、高效的途径。     

Precipitation assessment in wastewater treatment plants operated for biological nutrient removal: a case study in Murcia, Spain

The Murcia Este Wastewater Treatment Plant is the largest wastewater treatment plant in Murcia (Spain). The plant operators have continuously found pipe blockage and accumulation of solids on equipment surfaces during the anaerobic digestion and post-digestion processes. This work studies the precipitation problems in the Murcia Este Wastewater Treatment Plant in order to locate the sources of precipitation and its causes from an exhaustive mass balance analysis. The DAF thickener and anaerobic digester mass balances suggest that most of the polyphosphate is released during excess sludge thickening. Despite the high concentrations achieved in the thickened sludge, precipitation does not occur at this point due to the low pH. The increases in ammonium and pH during anaerobic digestion cause precipitation to take place mainly inside the digesters and in downstream processes. This study shows that 50.7% of the available phosphate is fixed in the digester of which 52.0% precipitates as ammonium struvite, 39.2% precipitates as hydroxyapatite and the remaining 8.8% is adsorbed on the surface of the solids. Thermodynamic calculations confirm the precipitation of struvite and hydroxyapatite and also confirm that potassium struvite does not precipitate in the anaerobic digesters.     

UASB处理离子交换树脂生产废水的试验研究

本研究主要介绍，尝试采用UASB（Upflow Anaerobic Sludge Bed）反应器厌氧工艺处理某离子交换树脂生产废水试验。研究表明，在中温（37℃±1）环境下，容积负荷在6．0-7．0kgCODcr·m^-3·d^-1时，CODcr去除率维持在80％左右，运行稳定。本试验取得的试验效果，为以后的利用厌氧技术处理离子交换树脂生产废水提供了重要依据。     

Disintegration of waste activated sludge by different applications of Fenton process

Oxidative disintegration of municipal waste activated sludge (WAS) using conventional Fenton (Fe²⁺ + H₂O₂, CFP) and Fenton type (Fe⁰ + H₂O₂, FTP) processes was investigated and compared in terms of the efficiency of sludge disintegration and enhancement of anaerobic biodegradability. The influences of different operational variables namely sludge pH, initial concentration of Fe²⁺ or Fe⁰, and H₂O₂ were studied in detail. The optimum conditions have been found as catalyst iron dosage = 4 g/kg TS, H₂O₂ dosage = 40 g/kg TS and pH = 3 within 1 h oxidation period for both CFP and FTP. Kinetics studies were performed under optimal conditions. It was determined that the sludge disintegration was happened in two stages by both processes: rapid and subsequent slow disintegration stages and rapid sludge disintegration stage can be described by a zero-order kinetic model. The effects of oxidative sludge disintegration under the optimum conditions on anaerobic digestion were experienced with biochemical methane potential (BMP) assay in batch anaerobic reactors. Total methane production in the CFP and FTP pre-treated reactors increased by 26.9% and 38.0%, relative to the untreated reactor (digested the raw WAS). Furthermore, the total chemical oxygen demand reductions in the pre-treated reactors were improved as well.     

重金属Cd在再生水—土壤—蔬菜体系中的迁移

通过小区试验种植了小白菜和萝卜,以再生水灌溉和污泥施肥,采用修正的BCR法测定了再生水、污泥、土壤、蔬菜中重金属Cd的5种形态含量,分析Cd在再生水(污泥)-土壤-蔬菜体系中的迁移和累积特征。结果表明:灌溉用清水和再生水中Cd的总量均未超出国家农田灌溉水质标准(GB5084-2005)的规定,但水样中的Cd主要以水溶态存在,生物有效性系数K≥0.85。经再生水灌溉和污泥施肥后土壤中Cd的形态和总量均发生了变化。蔬菜地上部分中Cd以水溶态B0和可氧化态B3的形式存在,B0>B3;而地下部分以B0、B2和B3为主,B0相似文献   

A strategy for enhancing anaerobic digestion of waste activated sludge: Driving anodic oxidation by adding nitrate into microbial electrolysis cell

Cathodic reduction of CO₂ and anodic oxidation of organic matters are crucial to methane-producing microbial electrolysis cell (MEC) applied in anaerobic digestion of waste activated sludge. However, cathodic CO₂ reduction is usually restrained by slow metabolism rates of H₂-utilizing methanogens and low electron-capturing capacity of CO₂, which consequently slows down the anodic oxidation that participates to sludge disintegration. Herein, a strategy with adding nitrate as electron acceptor to foster electronic transfer between the anode and cathode was proposed to improve anodic oxidation. Results showed that the average efficiency of anodic oxidation in the nitrate-added MEC increased by 55.9%. Accordingly, volatile suspended solid removal efficiency in the nitrate-added MEC was 21.9% higher than that of control MEC. Although the initial cumulative methane production in the nitrate-added MEC was lower than that of control MEC, the cumulative methane production in 24?days was 8.9% higher. Fourier transform infrared spectroscopy analysis indicated that anodic oxidation of MEC with nitrate accelerated the disintegration of sludge flocs and cell walls. Calculation on current signal further revealed that anodic oxidation driven by cathodic nitrate reduction was the main mechanism responsible for the improved sludge digestion.     

活性污泥胞外聚合物的组成与结构特点及环境行为

在活性污泥处理系统中,微生物大多以污泥絮体的形式悬浮在水中。胞外聚合物(EPS)作为污泥絮体的重要组成部分,以其独特的聚合结构和化学组成,在污水生物处理系统中起到重要作用。为了更好的描述EPS的环境行为,文章综合了近年来国内外相关的研究成果,首先分析了EPS的来源、化学组成及结构分布,得出EPS中包含蛋白质、多糖、腐殖酸、核酸、糖醛酸及脂类大分子等化学物质,其中蛋白质和多糖之和占总有机物含量的70%~80%;在结构上,EPS分为SB-EPS、LB-EPS和TB-EPS,三者与细胞结合的紧密程度递增,其中所含化学成分比例的不同将使其具有不同的理化特性。其次,文章对EPS的理化特征对污水处理系统的影响,如对系统中微生物降解特性的影响、磷和重金属的吸附等进行了讨论,并总结了EPS中相关的官能团对上述环境行为的贡献。同时,文章还论述了EPS中官能团的亲疏水特性及化学成分对污泥絮体的脱水性、絮凝沉降性能的影响。     

高效代谢解偶联剂的筛选及对SBR系统综合运行效能的影响

活性污泥法是最常用的污水处理技术,但它同时会产生大量的剩余污泥,需要进行额外的处理和处置.活性污泥的解偶联代谢能有效地减少剩余污泥的产量.比较了5种代谢解偶联剂,即2,4-二硝基苯酚(DNP)、邻氨基苯酚(AP)、2,4,6-三氯苯酚(TCP)、3,3',4,5-四氯水杨酰苯胺(TCS)、丙二酸的污泥减量效果和对COD去除能力的影响.结果表明,当它们在各自的最佳质量浓度20、1 5、4、1.2、15 mg/L时,污泥的表观增长系数分别降低了62.39%、63.75%、59.40%、34.58%和53.75%,而COD去除率仅有轻微下降.重点研究了15 mg/L的丙二酸和4 mg/L的TCP对SBR系统运行效能和污泥沉降性能的影响.发现在长期运行过程中,两者都能有效降低系统的污泥产量,而对COD去除率的影响较低,但使用丙二酸6 d后极大地影响了污泥的沉降性能,而TCP对污泥的沉降性能影响很小.     

污泥低温热解技术在德国的应用实践

本文介绍污泥低温热解技术的原理和工程应用。德国的工程实践表明,这项技术在经济性、可再生能源回收以及设备稳定性方面具有明显的优势。这对我国的污泥处置有较好的借鉴作用。     

Assessment of characteristic distribution of PCDD/Fs and BFRs in sludge generated at municipal and industrial wastewater treatment plants

The presence of polychlorinated dibenzo-p-dioxins and furan (PCDD/Fs) and brominated flame retardants (BFRs) in sludge generated at municipal wastewater treatment plants (MWTPs) and industrial wastewater treatment plants (IWTPs) was investigated. The concentrations of these pollutants were in the following ranges: 5.38-7947 ng kg⁻¹ dw (0.02-49.9 ng WHO-TEQ kg⁻¹ dw) for 17 PCDD/Fs, 17.5-66 761 μg kg⁻¹ dw for 27 polybrominated diphenyl ethers (PBDEs), 1.55-29 604 μg kg⁻¹ dw for hexabromocyclododecanes (HBCDs) (α-, β-, and γ-diastereomers), and 4.01-618 μg kg⁻¹ dw for tetrabromobisphenol A (TBBPA). Generally, the levels of each compound in the sewage-sludge samples were higher than those in the industrial-sludge samples with some exceptions. The characteristic distribution profiles of target compounds were observed for different types of sludge and different sources of wastewater. High-chlorinated PCDD/Fs were dominant in all samples except those from the textile industry. The distribution of the BFRs in industrial-sludge samples varied, whereas that of the BFRs in sewage-sludge samples was consistent. The proportion of penta-BDEs in sewage sludge was higher than that in industrial sludge, even though BDE-209 was the most dominant congener in all the samples. For HBCDs, the distribution of diastereomers (α-, β-, and γ-HBCD) was similar across sludge samples that had the same source of wastewater and treatment processes.