高含氮印染废水强化脱氮处理组合工艺

为考察UASB-A/LO/O（缺氧/低氧/好氧）组合工艺的实际应用效果,将该工艺应用到规模为6 000 t/d的实际工程中,考察其对高含氮印染废水处理效果,同时采用微生物高通量测序对A/LO/O工艺中的微生物菌群结构进行解析.结果表明:在前处理废水进水流量为100 m3/h,染色废水进水流量为150 m3/h,同时A/LO/O工艺污泥回流比为50%左右情况下,COD_Cr、NH₃-N和TN的去除率分别达到91.6%、95.5%和73.5%;染色和前处理废水在改良UASB内均实现了高效厌氧氨化,染色废水厌氧出水中ρ（NH₃-N）/ρ（TN）保持在80%以上,前处理废水厌氧出水保持在85%以上;调节UASB运行参数可对VFAs（挥发性脂肪酸）进行有效调控,从而为后段反硝化工艺提供高品质碳源,实现高效脱氮;A/LO/O系统对COD_Cr、NH₃-N、TN有较好的去除效果,其脱氮性能主要靠变性菌门（Proteobateria）发挥作用,该系统中低氧池的微生物种类最为丰富且发生短程硝化反硝化,对污染物去除贡献最大,当低氧池△ρ（COD_Cr）/△ρ（TN）在18.6左右时,TN去除率最高,达到82%.研究显示,该组合工艺对工程中高含氮印染废水的脱氮效果良好.      

同步脱氮除磷系统中两种颜色好氧颗粒污泥的微生物群落特征

为研究同步脱氮除磷系统中出现的WG（白色好氧颗粒污泥）外形特点及微生物群落特征,探究其成因,利用SEM（扫描电子显微镜）表征了系统中的WG与YG（黄色好氧颗粒污泥）的微观形态,并采用Illumina HiSeq 2500高通量测序平台对两种好氧颗粒污泥中细菌与真菌的群落组成进行研究.结果表明:WG结构疏松外形不规则,颗粒表面分布大量杆菌;而YG饱满紧实轮廓清晰,颗粒表面分布大量球菌.WG与YG的细菌群落组成相似,但真菌组成差异较大.与YG相比,WG具有更高的细菌和真菌多样性.变形菌门（Proteobacteria）和拟杆菌门（Bacteroidetes）为WG和YG中的细菌优势门,其在WG中的相对丰度分别为68.85%和26.61%,在YG中的相对丰度分别为82.52%和12.30%.Candidatus competibacter、Candidatus accumulibacter和Chiayiivirga为WG中的优势属,相对丰度分别为22.13%、8.95%和7.37%;Candidatus competibacter、Chiayiivirga和Xanthomonas为YG中的优势属,相对丰度分别为47.94%、6.95%和7.06%.子囊菌门（Ascomycota）和Rozellomycota分别为WG与YG中真菌优势门,其在两个样品中的相对丰度分别为50.10%和81.77%.在属水平,WG中存在大量青霉属（Penicillium）和假丝酵母属（Candida）等丝状真菌,为WG的形成提供了框架.研究显示,当YG破碎成为小菌胶团后,附着在真菌框架上,造成了WG的快速形成,同时WG中Candidatus competibacter的相对丰度较低,使其外形疏松、透光性较好,呈现出白色.      

Method to assess component contribution to toxicity of complex mixtures: Assessment of puberty acquisition in rats exposed to disinfection byproducts

A method based on regression modeling was developed to discern the contribution of component chemicals to the toxicity of highly complex, environmentally realistic mixtures of disinfection byproducts(DBPs). Chemical disinfection of drinking water forms DBP mixtures.Because of concerns about possible reproductive and developmental toxicity, a whole mixture(WM) of DBPs produced by chlorination of a water concentrate was administered as drinking water to Sprague–Dawley(S–D) rats in a multigenerational study. Age of puberty acquisition,i.e., preputial separation(PPS) and vaginal opening(VO), was examined in male and female offspring, respectively. When compared to controls, a slight, but statistically significant delay in puberty acquisition was observed in females but not in males. WM-induced differences in the age at puberty acquisition were compared to those reported in S–D rats administered either a defined mixture(DM) of nine regulated DBPs or individual DBPs. Regression models were developed using individual animal data on age at PPS or VO from the DM study. Puberty acquisition data reported in the WM and individual DBP studies were then compared with the DM models. The delay in puberty acquisition observed in the WM-treated female rats could not be distinguished from delays predicted by the DM regression model, suggesting that the nine regulated DBPs in the DM might account for much of the delay observed in the WM. This method is applicable to mixtures of other types of chemicals and other endpoints.     

Control of aliphatic halogenated DBP precursors with multiple drinking water treatment processes: Formation potential and integrated toxicity

The comprehensive control efficiency for the formation potentials(FPs) of a range of regulated and unregulated halogenated disinfection by-products(DBPs)(including carbonaceous DBPs(C-DBPs), nitrogenous DBPs(N-DBPs), and iodinated DBPs(I-DBPs)) with the multiple drinking water treatment processes, including pre-ozonation, conventional treatment(coagulation–sedimentation, pre-sand filtration), ozone-biological activated carbon(O_3-BAC) advanced treatment, and post-sand filtration, was investigated. The potential toxic risks of DBPs by combing their FPs and toxicity values were also evaluated.The results showed that the multiple drinking water treatment processes had superior performance in removing organic/inorganic precursors and reducing the formation of a range of halogenated DBPs. Therein, ozonation significantly removed bromide and iodide,and thus reduced the formation of brominated and iodinated DBPs. The removal of organic carbon and nitrogen precursors by the conventional treatment processes was substantially improved by O_3-BAC advanced treatment, and thus prevented the formation of chlorinated C-DBPs and N-DBPs. However, BAC filtration leads to the increased formation of brominated C-DBPs and N-DBPs due to the increase of bromide/DOC and bromide/DON.After the whole multiple treatment processes, the rank order for integrated toxic risk values caused by these halogenated DBPs was haloacetonitriles(HANs)》haloacetamides(HAMs) haloacetic acids(HAAs) trihalomethanes(THMs) halonitromethanes(HNMs) 》I-DBPs(I-HAMs and I-THMs). I-DBPs failed to cause high integrated toxic risk because of their very low FPs. The significant higher integrated toxic risk value caused by HANs than other halogenated DBPs cannot be ignored.     

Capability of cation exchange technology to remove proven N-nitrosodimethylamine precursors

N-nitrosodimethylamine(NDMA) precursors consist of a positively charged dimethylamine group and a non-polar moiety, which inspired us to develop a targeted cation exchange technology to remove NDMA precursors. In this study, we tested the removal of two representative NDMA precursors, dimethylamine(DMA) and ranitidine(RNTD), by strong acidic cation exchange resin. The results showed that pH greatly affected the exchange efficiency, with high removal(DMA 78% and RNTD 94%) observed at pH pk_a-1 when the molar ratio of exchange capacity to precursor was 4. The exchange order was obtained as follows: Ca~(2+) Mg~(2+) RNTD~+ K~+ DMA~+ NH_4~+ Na~+. The partition coefficient of DMA~+to Na~+was 1.41 ± 0.26, while that of RNTD~+to Na~+was 12.1 ± 1.9. The pseudo second-order equation fitted the cation exchange kinetics well. Bivalent inorganic cations such as Ca~(2+)were found to have a notable effect on NA precursor removal in softening column test. Besides DMA and RNTD, cation exchange process also worked well for removing other 7 model NDMA precursors. Overall, NDMA precursor removal can be an added benefit of making use of cation exchange water softening processes.     

覆盖金属氧化物对湖泊沉积物溶解性有机质特征的影响

为揭示不同金属氧化物对湖泊沉积物DOM（溶解性有机质）影响机制,通过室内模拟试验,在沉积物表层分别覆盖Fe、Al、Mn氧化物及湖沙后培养1 a,并利用三维荧光和紫外光谱方法进行表征.结果表明:① 覆盖Al、Fe、Mn氧化物和湖沙主要降低了0~3 cm沉积物的w（DOC）,降幅分别为8.61%、6.27%、22.38%和0.44%. ② 沉积物中DOM的类络氨酸峰（peak B₁）和类色氨酸峰（peak T₂）均产生较大变化.其中三种氧化物均显著降低了上层沉积物中DOM的peak T₂,使底层DOM的peakT₂显著增加. Mn氧化物使DOM的peak B₁降低,Fe和Al氧化物使DOM的peak B₁增加,湖沙则使两类峰均降低. ③ 覆盖金属氧化物改变了沉积物DOM结构特征,其中覆盖Fe氧化物增强了其芳香性,而覆盖Mn氧化物和Al氧化却降低其芳香性,但三者均使DOM腐质化程度及官能团数量增加,并使FI（Fluorescence Index,荧光指数）增大,表明DOM向生物源转化.研究显示,沉积物表层覆盖金属氧化物影响了沉积物中DOM迁移和转化,并促进了其降解,导致其分子量和腐殖化程度增加.      

2001-2010年三江源区草地净生态系统生产力估算

三江源区位于青藏高原腹地,是我国长江、黄河、澜沧江三大河流的发源地.为了准确估算该地区草地生态系统的净生态系统生产力,收集整理了2001—2010年青藏高原10个通量观测站点的观测数据,构建了三江源区草地生态系统NEP（net ecosystem production,净生态系统生产力）估算模型,并在站点尺度进行了模型参数化和精度验证;结合区域尺度气象和遥感数据,估算了三江源区草地生态系统NEP.结果表明:① 2001—2010年三江源区草地生态系统多年平均NEP空间分布具有明显的空间异质性,大部分地区表现为碳汇,NEP（以C计）平均值为41.8 g/（m2·a）.② 三江源区草地生态系统NEP呈波动增加趋势,从2001年的20.0 g/（m2·a）增至2010年的82.5 g/（m2·a）;除2002年表现为弱碳源外,其余年份均表现为碳汇,并以2010年碳汇能力为最强.③ 2001—2010年三江源区草地生态系统NEP平均年增长率为5.4 g/m2;NEP年际变化率空间分布显示,大部分地区NEP呈增加趋势,仅有东南部和中部部分区域NEP呈下降趋势.研究显示,2001—2010年三江源区草地生态系统表现为碳汇,并且由于气候的暖湿化趋势,碳汇强度总体表现为增强.      

好氧MBBR处理含吲哚废水的工艺优化试验研究

为了处理制药企业废水中吲哚类有机污染物,采用好氧MBBR(移动床生物膜反应器)工艺对含吲哚废水进行了试验研究,通过考察HRT、曝气量、吲哚冲击负荷等工艺条件对吲哚、COD和NH_4~+-N等去除效果的影响,确定了好氧MBBR反应器的最佳工艺条件。实验结果表明,在HRT在6~18 h变化时,MBBR工艺对吲哚去除率在8 h以上时达到100%,COD去除率在8 h达到89.65%,而NH_4~+-N去除率在12 h达到最高。在曝气量为0.1~0.12 m L/min时,MBBR工艺对COD和NH_4~+-N去除率分别为88.88%~92.95%和65%~66.83%。进水吲哚浓度25~65 mg/L变化时,好氧MBBR对吲哚去除率保持在100%,而对COD和NH_4~+-N去除率也保持在80%和40%以上,表明好氧MBBR工艺在处理难降解有机污染物方面具有显著优势。     

大冶湖表层水和沉积物中重金属污染特征与风险评价

于2014年4月采集大冶湖表层水和表层沉积物,用原子吸收分光光度法测定其重金属含量,并基于健康风险评价模型和潜在生态风险指数法开展表层水和沉积物重金属污染的潜在健康风险和生态风险评价.结果表明,表层水和沉积物重金属(Ni、Cd、Cu和Pb)含量平均值分别为49.27、2.19、12.18、12.13μg·L~(-1)和78.46、77.13、650.13、134.22 mg·kg~(-1).富集系数显示,Cd、Cu和Pb均为重度富集,尤其是Cd累积最为明显.与国内典型湖泊重金属污染相比,表层水和沉积物中重金属元素含量均相对较高.表层水和沉积物重金属元素均表现为湖湾处含量较高,中部含量较均匀的分布规律,其来源主要受多种人为活动污染.环境风险评价显示,重金属类化学物质通过饮水途径产生健康风险范围为9.77E-08~1.63E-05 a-1,Ni和Cd是水环境健康风险的优先管理对象.沉积物重金属的潜在生态风险高低为CdCuPbNi,其中Cd是生态风险的贡献元素.     

基于污泥掺烧的某生活垃圾焚烧厂烟道气、飞灰及炉渣中的二(口恶)英特征

以我国南方某生活垃圾焚烧厂掺烧10%市政污泥的生活垃圾为研究对象,对前/后口废气、飞灰、炉渣及用于掺烧的污泥中17种二(口恶)英的含量进行了测定,并分析了其指纹分布特征.结合焚烧工况及处理设施,从生成机理角度探讨了二(口恶)英的排放特征、毒性当量浓度主成分特征及主要单体的排放因子线性关系.结果表明：掺烧10%的市政污泥后,废气中二(口恶)英的去除率为99.4%,低于国家排放标准;固体废物中二(口恶)英含量为飞灰 > 炉渣 > 污泥.这说明采用高温焚烧和"活性炭喷射+布袋除尘"装置不会影响掺烧10%污泥的达标排放.指纹分布特征表明,前口废气以1,2,3,4,6,7,8-HpCDF和OCDD为主,后口废气以OCDD和OCDF为主;飞灰、炉渣及污泥中的主要单体为OCDD、1,2,3,4,6,7,8-HpCDD、OCDF、1,2,3,4,6,7,8-HpCDF.主成分分析显示,前口废气和飞灰中的二(口恶)英毒性分布特征相似;炉渣和污泥的毒性分布特征相似;后口废气有自身的特征.这说明在相同工况条件下,经同一设施处理的废物中二(口恶)英排放特征相似.排放因子分析表明,2,3,4,7,8-PeCDF和1,2,3,6,7,8-HxCDF、1,2,3,6,7,8-HxCDD和1,2,3,7,8,9-HxCDD与总毒性排放因子具有较强的线性关系,且呋喃类（PCDFs）强于二(口恶)英类（PCDDs）.