佛山高明河水环境多环芳烃的分布特征与通量研究

利用液液萃取法和气相色谱-质谱方法对佛山境内高明河水环境多环芳烃（PAHs）进行了测定,并对PAHs的分布特征与通量进行了初步研究.结果表明高明河水环境中16种优控PAHs的浓度范围在41.6～375.6 ng/l之间,从上游到下游总体呈递增的趋势,其下游浓度偏高可能与荷城街道较为密集的工业和人口分布有关.高明河水环境PAHs的总含量高于欧美一些低污染水域,但低于国内一些主要河流.高明河PAHs年通量约为333.8 kg.     

基于土壤气调查的废弃工业场地人体健康风险评估研究

土壤气采样和分析是蒸气侵入评估的一个常用的工具.以某废弃化工场地为研究区,采集污染区域10个点位处的土壤气（编号SG1至SG10）,并分析土壤气中的苯、乙苯、四氯化碳、三氯乙烯、四氯乙烯和三氯甲烷等挥发性有机物.根据测定的土壤气体浓度,结合Johnson ＆amp;Ettinger（J＆amp;E）侵入模型评估了该废弃场地土壤气中挥发性有机物侵入带来的人体健康风险.风险评估结果表明,SG5与SG6处非致癌风险指数大于1,而10个采样点位中有9个（除SG8处）的单一污染物可接受致癌风险均超过1.0E-6.相对于非致癌风险,致癌风险存在面更加广泛,同时程度也比较严重,在进行场地再开发之前需要考虑场地修复等风险管理措施.     

贵州典型酸雨城市大气降水化学组成特征

本研究于2012年3月~2013年2月,采集了贵州省典型酸雨城市—都匀市的大气降水,分析了其中pH、阴阳离子及重金属元素等分布特征及可能来源。研究结果表明:都匀市降水存在一定酸化现象,40.4%降水样品pH5.6。阴离子以SO42-和NO3-为主,平均含量分别为180.7μmol/L、50.7μmol/L,SO42-/NO3-值为1.44~15.62,降水属于硫酸-硝酸混合型。阳离子以NH4+是最主要的,平均值为129.8μmol/L,占无机阳离子总量的50.8%。降水中重金属元素(Cu、Zn、As、Cd、Pb、Cr)含量较低,与国内其他地区相比,Hg的含量偏高。降水中总离子浓度表现为冬、春季较高,夏、秋季较低。相关性分析表明:降水中化学组分以CaSO4、MgSO4、NH4SO4、Ca(NO3)2等为主。Ca2+与Mg2+主要来自陆源性颗粒物,NO3-、SO42-、F-主要来自化石燃料燃烧及金属冶炼,重金属元素主要来源于燃煤以及人为活动污染。     

不同离子对黑土胶体在土壤中运移的影响

黑土样品采自于黑龙江海伦市,提取胶体并对其主要理化性质进行定性定量表征,通过淋滤实验研究胶体在土柱中的运移特征以及不同离子及其强度对胶体运移的影响。结果显示:所提取胶体粒径与理论计算基本吻合,粒径主要分布在2~5μm;当pH由4上升到9时,胶体的zeta电位则由-26.43mV降低到-34.52mV;红外光谱显示胶体颗粒的有机机团主要为-OH、CH-、C=O、多糖;X射线衍射表明其主要矿物组成是石英(56.9%)。不同离子及其强度对胶体的在土壤中的运移有较为明显的影响,当pH由4增加到9时,k值由6.020×10-4降低至3.858×10-4,Ca2+、K+、Na+当离子强度由0.5mmol/L变化到0.001mmol/L时,k值分别由6.087×10-4降低至4.024×10-4、5.518×10-4降低至3.818×10-4、5.401×10-4降低至4.109×10-4。     

氧化亚铁硫杆菌对黄铜矿的生物氧化研究

针对矿区硫化矿氧化产生的酸性矿山废水(AMD)对生态环境造成严重影响的问题,以矿区常见的黄铜矿(CuFeS2)为研究对象,采用已筛选的氧化亚铁硫杆菌(Acidithiobacillus ferrooxidans,简称A.f菌)为实验菌株,探讨在A.f菌作用下黄铜矿的氧化过程。实验结果表明,A.f菌可显著促进黄铜矿的氧化,第18天有菌体系中的铜离子浓度是无菌体系中的5倍;同时细菌可促进溶液中Fe2+氧化为Fe3+,使氧化还原电位升高,从而对黄铜矿保持较高的氧化速率,并导致体系的pH值降低;还发现黄铜矿的氧化过程中可形成中间产物方黄铜矿(CuFe2S3),而细菌氧化还可产生硫磷化钴(CoPS),中间产物的形成并没有明显延缓黄铜矿的氧化速率;生物氧化可造成矿样表面侵蚀多坑,可能是细菌对黄铜矿的直接氧化作用造成的。由于黄铜矿的生物氧化明显控制其氧化进程,抑制黄铜矿的生物氧化对酸性矿山废水的源头治理具有十分重要的意义。     

Fouling distribution in forward osmosis membrane process

Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis （FO） membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic （alginate） fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process.     

Compositions and sources of organic acids in fine particles (PM2.5) over the Pearl River Delta region, south China

Organic acids as important constituents of organic aerosols not only influence the aerosols' hygroscopic property, but also enhance the formation of new particles and secondary organic aerosols. This study reported organic acids including C14–C32fatty acids, C4–C9dicarboxylic acids and aromatic acids in PM2.5collected during winter 2009 at six typical urban, suburban and rural sites in the Pearl River Delta region. Averaged concentrations of C14–C32fatty acids, aromatic acids and C4– C9 dicarboxylic acids were 157, 72.5 and 50.7 ng/m3, respectively. They totally accounted for 1.7% of measured organic carbon. C20–C32fatty acids mainly deriving from higher plant wax showed the highest concentration at the upwind rural site with more vegetation around, while C14–C18fatty acids were more abundant at urban and suburban sites, and dicarboxylic acids and aromatic acids except 1,4-phthalic acid peaked at the downwind rural site. Succinic and azelaic acid were the most abundant among C4–C9dicarboxylic acids, and 1,2-phthalic and 1,4-phthalic acid were dominant aromatic acids. Dicarboxylic acids and aromatic acids exhibited significant mutual correlations except for 1,4-phthalic acid, which was probably primarily emitted from combustion of solid wastes containing polyethylene terephthalate plastics. Spatial patterns and correlations with typical source tracers suggested that C14–C32fatty acids were mainly primary while dicarboxylic and aromatic acids were largely secondary. Principal component analysis resolved six sources including biomass burning, natural higher plant wax, two mixed anthropogenic and two secondary sources; further multiple linear regression revealed their contributions to individual organic acids. It turned out that more than 70% of C14–C18fatty acids were attributed to anthropogenic sources, about 50%–85% of the C20–C32fatty acids were attributed to natural sources, 80%–95% of dicarboxylic acids and 1,2-phthalic acid were secondary in contrast with that 81% of 1,4-phthalic acid was primary.     

Effect of a high strength chemical industry wastewater on microbial community dynamics and mesophilic methane generation

A high strength chemical industry wastewater was assessed for its impact on anaerobic microbial com- munity dynamics and consequently mesophilic methane generation. Cumulative methane production was 251 mL/g total chemical oxygen demand removed at standard temperature and pressure at the end of 30 days experimental period with a highest recorded methane percentage of 80.6% of total biogas volume. Volatile fatty acids （VFAs） analysis revealed that acetic acid was the major intermediate VFAs produced with propionic acid accumulating over the experimental period. Quantitative analysis of microbial communities in the test and control groups with quantitative real time polymerase chain reaction highlighted that in the test group, Eubacteria （96.3%） was dominant in comparison with methanogens （3.7%）. The latter were dominated by Methanomicrobiales and Methanobacteriales while in test groups increased over the experimental period, reaching a maximum on day 30. Denaturing gradient gel electrophoresis profile was performed, targeting the 16S rRNA gene of Eubacteria and Archaea, with the DNA samples extracted at 3 different time points from the test groups. A phylogenetic tree was constructed for the sequences using the neighborhood joining method. The analysis revealed that the presence of organisms resembling Syntrophomonadaceae could have contributed to increased production of acetic and propionic acid intermediates while decrease of organisms resembling Pelotomaculum sp. could have most likely contributed to accumulation of propionic acid. This study suggested that the degradation of organic components within the high strength industrial wastewater is closely linked with the activity of certain niche microbial communities within eubacteria and methanogens.     

Debromination of decabromodiphenyl ether by organo-montmorillonite-supported nanoscale zero-valent iron：Preparation, characterization and influence factors

An organo-montmorillonite-supported nanoscale zero-valent iron material(M-NZVI) was synthesized to degrade decabromodiphenyl ether(BDE-209). The results showed that nanoscale zero-valent iron had good dispersion on organo-montmorillonite and was present as a core-shell structure with a particle size range of nanoscale iron between 30–90 nm, characterized by XRD, SEM, TEM, XRF, ICP-AES, and XPS. The results of the degradation of BDE-209 by M-NZVI showed that the efficiency of M-NZVI in removing BDE-209 was much higher than that of NZVI. The efficiency of M-NZVI in removing BDE-209 decreased as the pH and the initial dissolved oxygen content of the reaction solution increased, but increased as the proportion of water in the reaction solution increased.     

Removal of phosphate from wastewater using alkaline residue

Alkaline residue(AR) was found to be an efficient adsorbent for phosphate removal from wastewater. The kinetic and equilibrium of phosphate removal were investigated to evaluate the performance of modified alkaline residue. After treatment by NaOH(AR-NaOH), removal performance was significantly improved, while removal performance was almost completely lost after treatment by HCl(AR-HCl). The kinetics of the removal process by all adsorbents was well characterized by the pseudo second-order model. The Langmuir model exhibited the best correlation for AR-HCl, while AR was effectively described by Freundlich model. Both models were well fitted to AR-NaOH. The maximum adsorption capacities calculated from Langmuir equation were in following manner: AR-NaOH AR AR-HCl. Phosphate removal by alkaline residue was pH dependent process. Mechanisms for phosphate removal mainly involved adsorption and precipitation, varied with equilibrium pH of solution. For AR-HCl, the acid equilibrium pH( 6.0) was unfavorable for the formation of Ca-P precipitate, with adsorption as the key mechanism for phosphate removal. In contrast, for AR and ARNaOH, precipitation was the dominant mechanism for phosphate removal, due to the incrase on pH( 8.0) after phosphate removal. The results of both XRD and SEM analysis confirmed CaHPO4·2H2O formation after phosphate removal by AR and AR-NaOH.