纺织印染厂废水的深度处理中试及工程应用

采用曝气生物滤池(BAF)-臭氧-曝气生物滤池工艺对广东某大型纺织印染厂的常规水解酸化-接触生物氧化处理出水进行深度处理回用中试,在中试研究成功的基础上,设计了每小时处理5 t的工业化试验装置。试验运行结果表明:进水COD为100~150 mg/L,色度约80倍,浊度约10 NTU,在前BAF水力停留时间3 h,中间化学氧化池中臭氧投加量40 mg/L,后BAF水力停留时间2 h的情况下,经组合工艺处理后出水COD约30 mg/L,色度2倍,浊度<1 NTU,该工艺处理后的出水,可直接回用于对电解质浓度要求不高的生产工艺中,也可作为反渗透或纳滤膜的预处理工序。     

Partitioning of water soluble organic carbon in three sediment size fractions： Effect of the humic substances

Water soluble organic carbon (WSOC) in sediments plays an important role in transference and transformation of aquatic pollutants. This article investigated the inherent mechanisms of how sediemnt grain size affect the partitioning coeffcient (k) of WSOC. Influences of NaOH extracted humic substances were particularly focused on. Sediments were sampled from two cross-sections of the middle Yellow River and sieved into three size fractions (< 63 μm, 63-100 μm, and 100--300 μm). The total concentration of WSOC in sediments (CWSOC) and k were estimated using multiple water-sediment ratio experiments. Results show that CWSOC ranges from 0.012 to 0.022 mg/g, while k ranges from 0.8 to 3.9 L/kg. Correlations between the spectrum characteristics of NaOH extracted humic substances and k were analyzed. Strong positive correlations are determined between k and the aromaticity indicators of NaOH extracted humic substances in different sediment size fractions. Comparing with finer fractions (< 63 μm), k is higher in larger size fractions (63--100 and 100--300 μm) related to higher aromaticity degree of NaOH extracted humic substances mostly. While negative relationship between k and the area ratio of fourier transform infrared spectroscopy (FT-IR) at 3400 and 1430 cm-1 implied that the lowest k was related to the highest concentration of the acidic humic groups in particles < 63 μm. WSOC in finer fractions (< 63 μm) is likely to enter into pore water, which may further accelerate the transportation of aquatic contaminants from sediment to water.     

Combined fluorescence and electrochemical investigation on the bindinginteraction between organic acid and human serum albumin

Human serum albumin (HSA) is a plasma protein responsible for the binding and transport of fatty acids and a variety of exogenous chemicals such as drugs and environmental pollutants. Such binding plays a crucial role in determining the ADME (absorption, distribution, metabolism, and excretion) and bioavailability of the pollutants. We report investigation on the binding interaction between HSA and acetic acid (C2), octanoic acid (C8) and dodecanoic acid (C12) by the combination of site-specific fluorescent probe, tryptophan intrinsic fluorescence and tyrosine electrochemistry. Two fluorescent probes, dansylamide and dansyl-L-proline, were employed in the displacement measurement to study fatty acid interaction with the two drug-binding sites on HSA. Intrinsic fluorescence of tryptophan in HSA was monitored upon addition of the fatty acids into HSA. Electrocatalyzed response of the tyrosine residues in HSA by a redox mediator was used to investigate the binding interaction. Qualitatively, observations made by the three approaches are very similar. HSA did not show any change in either fluorescence or electrochemistry after mixing with C2, suggesting there is no significant interaction with the short-chain fatty acid. For C8, the measured signal dropped in a single-exponential fashion, indicative of independent and non-cooperative binding. The calculated association constant and binding ratio is 3.1×106 L/mol and 1 with drug binding Site I, 1.1×107 L/mol and 1 with Site II, and 7.0×104 L/mol and 4 with the tryptophan site. The measurement with C12 displayed multiple phases of fluorescence change, suggesting cooperativity and allosteric effect of C12 binding. These results correlate well with those obtained by the established methods, and validate the new approach as a viable tool to study the interactions of environmental pollutants with biological molecules.     

Biofilm structure and its influence on clogging in drip irrigation emittersdistributing reclaimed wastewater

Using reclaimed wastewater for crop irrigation is a practical alternative to discharge wastewater treatment plant effluents into surface waters.However,biofouling has been identified as a major contributor to emitter clogging in drip irrigation systems distributing reclaimed wastewater.Little is known about the biofilm structure and its influence on clogging in the drip emitter flow path.This study was first to investigate the microbial characteristics of mature biofilms present in the emitters and the effect of flow path structures on the biofilm microbial communities.The analysis of biofilm matrix structure using a scanning electron microscopy (SEM) revealed that particles in the matrix of the biofilm coupled extracellular polysaccharides (EPS) and formed sediment in the emitter flow path.Analysis of biofilm mass including protein,polysaccharide and phospholipid fatty acids (PLFAs) showed that emitter flow path style influenced biofilm community structure and diversity.The correlations of biofilm biomass and discharge reduction after 360 h irrigation were computed and suggest that PFLAs provide the best correlation coefficient.Comparatively,the emitter with the unsymmetrical dentate structure and shorter flow path (Emitter C) had the best anti-clogging capability.By optimizing the dentate structure,the internal flow pattern within the flow path could be enhanced as an important method to control the biofilm within emitter flow path.This study established electron microscope techniques and biochemical microbial analysis methods that may provide a framework for future emitter biofilm studies.     

Analysis of diffusion-adsorption equivalency of landfill liner systems for organic contaminants

The equivalence between multilayered barriers regarding diffusion and adsorption is analyzed by means of an analytical method. The bottom boundary of the liner system is defined by assuming concentration continuous and flux continuous conditions of the contaminant between the bottom liner layer and the underlying soil. Five different liner systems were compared in terms of solute breakthrough time. The results of the analysis show that breakthrough time of the hydrophobic organic compounds for a 2-meter-thick compacted clay liner (CCL) can be 3-4 orders of magnitude greater than the breakthrough time for a geosynthetic clay liner (GCL) composite liner. The GM/GCL and GM/CCL composite liner systems provide a better diffusion barrier for the hydrophilic organic compounds than that for the hydrophobic compounds due to their different Henry's coefficient. The calculated breakthrough times of the organic contaminants for the Chinese standard liner systems were found to be generally greater than those for the GCL alternatives, for the specific conditions examined. If the distribution coefficient increases to 2.8 for the hydrophobic compounds or 1.0 for the hydrophilic compounds, the thickness of the attenuation layer needed to achieve the same breakthrough time as the standard liner systems can be reduced by a factor of about 1.9-2.4. As far as diffusive and adsorption contaminant transport are concerned, GM or GCL is less effective than CCL.     

Characterization of organic matter in total suspended particles bythermodesorption and pyrolysis-gas chromatography-mass spectrometry

The organic matter in tropospheric aerosol plays an important role in atmospheric physical and chemical processes. The bulk oforganic matter, representing a significant proportion of the total suspended particulate (TSP) mass, is bound to polymeric materialwhose structure and properties are largely unknown. Here we used thermodesorption gas chromatography/mass spectrometry (Td-GC/MS) to study organic compounds of low molecular mass and pyrolysis gas chromatography/mass spectrometry (Py-GC/MS) tocharacterize the chemical structure of macromolecules in TSP samples collected in di erent seasons from di erent sites in Guangzhou.n-Alkanes, fatty acids and nitriles were the predominant compounds in the thermodesorption products, whereas aromatics, fatty acids,nitriles and n-alkanes/alkenes were the major compounds in the pyrolysates. The results indicated that aromatics were main units inmacromolecules. The fatty acids and nitriles formed from carboxylic ammonium salts were detected in both thermodesorption productsand pyrolysates at a certain concentration, indicating the importance of these compounds in TSP formation. The TSP source mainlydetermined the occurrence of compounds in samples from urban, suburban and forest sites, whereas the TSP source and formationprocess maybe controlled the seasonal variation in compounds detected. High levels of nitriles in summer samples from suburban andforest sites coincide with the release of ammonium from the land and of fatty acids from vegetation at these sites.     

Pollutants removal and simulation model of combined membrane process forwastewater treatment and reuse in submarine cabin for long voyage

A laboratory scale test was conducted in a combined membrane process (CMP) with a capacity of 2.91 m3/d for 240 d totreat the mixed wastewater of humidity condensate, hygiene wastewater and urine in submarine cabin during prolonged voyage.Removal performance of chemical oxygen demand (COD), ammonia nitrogen (NH4+-N), turbidity and anionic surfactants (LAS)was investigated under di erent conditions. It was observed that the e uent COD, NH4+-N, turbidity and LAS flocculated in ranges of0.19–0.85 mg/L, 0.03–0.18 mg/L, 0.0–0.15 NTU and 0.0–0.05 mg/L, respectively in spite of considerable fluctuation in correspondinginfluent of 2120–5350 mg/L, 79.5–129.3 mg/L, 110–181.1NTU and 4.9–5.4 mg/L. The e uent quality of the CMP could meet therequirements of mechanical water and hygiene water according to the class I water quality standards in China (GB3838-2002). Theremoval rates of COD, NH4+-N, turbidity and LAS removed in the MBR were more than 90%, which indicated that biodegradationis indispensable and plays a major role in the wastewater treatment and reuse. A model, built on the back propagation neural network(BPNN) theory, was developed for the simulation of CMP and produced high reliability. The average error of COD and NH4+-N was5.14% and 6.20%, respectively, and the root mean squared error of turbidity and LAS was 2.76% and 1.41%, respectively. The resultsindicated that the model well fitted the laboratory data, and was able to simulate the removal of COD, NH4+-N, turbidity and LAS. Italso suggested that the model proposed could reflect and manage the operation of CMP for the treatment of the mixed wastewaters insubmarine.     

双室微生物燃料电池不同接种条件下处理薯蓣素废水

比较了在5种不同接种条件下,利用双室微生物燃料电池(Microbial Fuel Cells,MFCs)处理薯蓣素生产废水的污染物去除和产电效果. 结果表明,该种废水可以用作微生物燃料电池的底物,在去除有机物的同时能够获得电能;采用全混合接种对污染物的去除效果最好,在350 h时COD_Cr去除率达到90%;采用污水处理厂厌氧污泥和薯蓣素废水驯化菌液混合接种的产电效果最好,在1 000 Ω的外电阻下得到了370 mV的输出电压,最大输出功率密度达到10.32 mW/m2;不同菌属在MFCs中的作用差别显著,产电与去污功能可能由不同优势菌属承担;初步富集到优势菌菌b,菌d和菌e;PCR-DGGE和DNA序列分析结果显示,菌d和菌e与β-变形菌具有较好的同源性.      

工业废水排放量和治理投资费用的预测

利用1996—2005年相关统计数据以及专项调查数据,对重点排放行业工业废水的产生、排放特征以及治理费用函数进行分析,建立了分行业的宏观工业废水排放和治理费用预测模型,并预测了2006—2020年工业废水排放趋势、投资需求以及减排重点. 结果表明:到2010年,工业废水和COD_Cr产生量分别为646×108～658×108和1 575×104～2 031×104 t,二者的排放量将分别介于234×108～301×108和441.1×104～609.2×104 t;“十一五期间工业废水治理投资和治理费用如不能达到8 000×108元,将面临COD_Cr减排目标不能完成的风险.      

包埋类脂的吸附剂制备及吸附POPs性能

用丙酮作溶剂将三油酸甘油酯分散到醋酸纤维(CA)基体中,采用悬浮聚合的方法制备出了一种兼具亲水性,又能高倍富集持久性有机污染物的球形复合吸附剂。通过对分散剂的种类及其用量、悬浮介质的种类及其用量的研究,获得了球形复合吸附剂的最佳合成路线与工艺.球形吸附剂粒径为1～2mm。通过荧光分析和电镜扫描分析,表明三油酸甘油酯已被包埋到醋酸纤维基体中,并得到了均匀分散。采用七氯、狄氏剂、异狄氏剂、灭蚁灵为代表性的持久性有机污染物(POPs)。动力学吸附实验表明,当初始浓度为1μg/L时,在快速吸附阶段,溶液中80%的氯、狄氏剂、异狄氏剂可得到有效去除,但并没有达到吸附平衡。快速吸附完后,还在持续地进行慢速吸附。而对于灭蚁灵,吸附速度远远低于其他几种POPs。实验证明了吸附速度不仅与辛醇/水系数有关,而且还与有机污染物的分子结构有关。