Enhancing anoxic denitrification of low C/N ratio wastewater with novel ZVI composite carriers

External organic carbon sources are needed to provide electron donors for the denitrification of wastewater with a low COD/NO₃^--N（C/N） ratio, increasing the treatment cost. The economic strategy is to enhance the bioactivity and/or biodiversity of denitrifiers to efficiently utilize organic substances in wastewater. In this study, novel zero-valent iron（ZVI） composite carriers were prepared and implemented in a suspended carrier biofilm reactor to enhance the bioactivity an...     

长江宜昌江段几种鱼类体中六六六、滴滴涕的残留水平

利用毛细管电子捕获气相色谱法测定了长江宜昌江段采集的几种鱼样组织内六六六(HCHs)、滴滴涕(DDTs)的残留量.结果表明,在鱼体肌肉、脂肪和肝脏这三种组织中,HCHs、DDTs主要蓄积在鱼体肝脏,其次是脂肪组织,肌肉组织中残留量较低.鱼体肌肉组织中HCHs残留量低于0.5 ng/g,肝脏中的HCHs是其脂肪组织的2倍,最高为27.6 ng/g,主要为悛睭CH所贡献,猹睭CH和洫睭CH未检出.DDTs在鱼体肌肉、脂肪和肝脏组织中的残留量分别为0.4～14.8、12.5～147、33.4～286 ng/g.鱼体组织中DDTs主要以p,p′-DDE的形式存在,p,p′-DDE残留量占∑DDTs的70%左右.与国内外不同水域的鱼体中HCHs、DDTs残留量相比较,长江宜昌江段鱼体肌肉中HCHs和DDTs残留水平较低.     

Steady performance of a zero valent iron packed anaerobic reactor for azo dye wastewater treatment under variable influent quality

Zero valent iron (ZVI) is expected to help create an enhanced anaerobic environment that might improve the performance of anaerobic treatment. Based on this idea, a novel ZVI packed upflow anaerobic sludge blanket (ZVI-UASB) reactor was developed to treat azo dye wastewater with variable influent quality. The results showed that the reactor was less influenced by increases of Reactive Brilliant Red X-3B concentration from 50 to 1000 mg/L and chemical oxygen demand (COD) from 1000 to 7000 mg/L in the feed than a reference UASB reactor without the ZVI. The ZVI decreased oxidation-reduction potential in the reactor by about 80 mV. Iron ion dissolution from the ZVI could buffer acidity in the reactor, the amount of which was related to the COD concentration. Fluorescence in situ hybridization test showed the abundance of methanogens in the sludge of the ZVI-UASB reactor was significantly greater than that of the reference one. Denaturing gradient gel electrophoresis showed that the ZVI increased the diversity of microbial strains responsible for high efficiency.     

SPME-G C法测试TCE、PCE条件的正交优化试验研究

运用正交设计方法对SPME-GC法测试三氯乙烯、四氯乙烯的固相微萃取条件进行优化。首先选择样品量、NaCl用量、萃取温度、萃取时间、解析温度等因素,设计5因素3水平正交试验方案。分析数据得到优化条件为NaCl用量30 g/L,萃取温度25℃,解析温度210℃,同时得出样品量与萃取时间是对试验结果具有显著意义的影响因素,采用二次回归正交组合设计试验对其进一步优化,并对结果进行回归分析,得到最优条件为样品量为5.5 mL,萃取时间为20.13 min。     

VOCs气体在活性炭上的二元吸附过程研究

采用穿透曲线法研究了4种VOCs在活性炭上的的二元吸附过程。研究表明:对于甲苯-苯、甲苯-丙酮、甲苯-乙酸乙酯、苯-丙酮、丙酮-乙酸乙酯二元吸附体系,吸附过程存在置换作用,即随着高沸点组分在床层内吸附量的逐渐增加,相对挥发性大的低沸点组分重新汽化而脱附,出现高沸点组分置换低沸点组分的现象,表现为被置换组分的穿透曲线上出现峰值。之后随着高沸点组分吸附趋于饱和,置换作用停止,低沸点组分吸附也趋于平衡。但对于沸点相近的苯-乙酸乙酯二元体系,吸附过程没有明显的置换现象。吸附量的计算结果表明,有机物在二元体系中的吸附量较同等条件时的单组分吸附量均有不同程度的降低,其中被置换组分降低程度较大,但总吸附量可近似按照浓度为二元组分总浓度低沸点组分的平衡吸附量的近似法计算,平均误差为7.9%。     

重庆三峡库区非点源污染评价与影响因子分析

选取重庆三峡库区4个行政建制镇进行非点源污染监测与调查,以COD、TN、TP、Cu、Zn等指标为主要研究内容对库区农村环境进行污染特性分析并且利用等标污染负荷法对其生活污水、生活垃圾、畜禽养殖、水产养殖、化肥流失、农药流失、水土流失等污染源进行非点源污染评价。结果表明:COD、TN、TP、Cu、Zn的平均排放浓度分别为22.15 mg/L、6.37 mg/L、1.49 mg/L、47.73 g/kg、85.24 g/kg,库区主要污染物依次为TN、TP、COD、Cu、Zn等,主要污染源依次是畜禽养殖、化肥流失、生活污水、生活垃圾、农药流失、水土流失、水产养殖等。采用SPSS软件对影响库区环境污染的季节、收入水平、地域、畜禽养殖规模、环境基础设施完善程度等因子进行了分析,结果显示:COD主要影响因子是地域和畜禽养殖规模,TN主要影响因子是季节、地域和畜禽养殖规模,TP主要影响因子是环境基础设施完善程度、畜禽养殖规模和地域,Cu、Zn主要影响因子均是畜禽养殖规模。该研究可为重庆三峡库区生态修复、城乡统筹下的城乡规划及产业布局提供理论基础。     

絮凝剂聚硅酸锌铁(PZFSiC)的研制和性能

在高模数水玻璃溶液中加入酸制备出聚硅酸,再引入适量的金属离子M(Zn、Fe),研制出一种新型的无毒无机复合高分子絮凝剂聚硅酸锌铁(PZFSiC).探讨了M与SiO2不同浓度比和不同pH值对PZFSiC的絮凝效果的影响,通过正交实验找出了最佳的制备工艺条件.在此基础上,进一步对两种不同的水样进行了絮凝实验,确定出水处理中最佳絮凝工艺条件.结果表明,PZFSiC具有较好的贮存稳定性,在使用PZFSiC时,适应的pH范围广.在实验过程中形成大而致密的絮体,沉降迅速,浑浊度去除率超过98%,COD去除率达93%.处理后的废水,出水水质好,水样澄清透明.在与同类絮凝剂对比实验中,效果优于PZSiC和PFSiC.     

Complexes of fulvic acid on the surface of hematite, goethite, and akaganeite: FTIR observation

The present work extended our knowledge on the binding and complexation of a fulvic acid (FA) derived from leonardite and the iron oxides (hematite, goethite and akaganeite) by Fourier transform infrared spectroscopy (FTIR). As a prerequisite, the iron oxides were firstly prepared and characterized by transmission electron micrograph (TEM). All iron phases were single and well-described crystalloid. The FTIR data obtained by two different sampling preparation methods gave the consisting evidences that under our experimental conditions the interaction mechanism was to the ligand-exchange involving carboxylic functional groups of the FA and the surfaces sites of both hematite and goethite, while no complexation can be evidenced in the case of akaganeite, only surface adsorption. In general, the binding affinities of the iron oxides with the FA was in the order of hematite>goethite>akaganeite. The present method, although associated with some uncertainties, provided an opportunity to increase the knowledge in the field of the humic chemistry.     

海洋沉积物中的天然气水合物与海底滑坡

天然气水合物是一种由天然气和水形成的类似冰状的固体物质 ,主要存在于在低温高压背景下的海底沉积物和陆地永久冻土地带中。赋存于海底沉积物中的天然气水合物虽然本身能作为准稳定的胶结物对海底有建造作用 ,但由于其稳定性对特定温度和压力的严格依赖 ,海平面的下降、海底的连续沉积、地震等自然因素以及海洋钻探等人为因素造成的海底温压条件的改变会引起其分解 ,从而使海底沉积物失稳甚至导致海底滑坡。本文详细介绍了海底天然气水合物分解导致滑坡的机制、实例以及该种海底滑坡体的特征 ,并对以后的研究进行了展望     

Comparison of CNT-PVA membrane and commercial polymeric membranes in treatment of emulsified oily wastewater

CNT-PVA membrane was fabricated and compared with polymeric membranes. The separation performance was evaluated by homemade and cutting fluid emulsions. The three membranes show similar oil retention rates. CNT-PVA membranes have higher permeation fluxes compared with polymeric membranes. CNT-PVA membrane shows higher fouling resistance. Membrane separation is an attractive technique for removal of emulsified oily wastewater. However, polymeric membranes which dominate the current market usually suffer from severe membrane fouling. Therefore, membranes with high fouling resistance are imperative to treat emulsified oily wastewater. In this study, carbon nanotube-polyvinyl alcohol (CNT-PVA) membrane was fabricated. And its separation performance for emulsified oily wastewater was compared with two commercial polymeric membranes (PVDF membrane and PES membrane) by filtration of two homemade emulsions and one cutting fluid emulsion. The results show that these membranes have similar oil retention efficiencies for the three emulsions. Whereas, the permeation flux of CNT-PVA membrane is 1.60 to 3.09 times of PVDF membrane and 1.41 to 11.4 times of PES membrane, respectively. Moreover, after five consecutive operation circles of filtration process and back flush, CNT-PVA membrane can recover 62.3% to 72.9% of its initial pure water flux. However, the pure water flux recovery rates are only 24.1% to 35.3% for PVDF membrane and 6.0% to 26.3% for PES membrane, respectively. Therefore, CNT-PVA membrane are more resistant to oil fouling compared with the two polymeric membranes, showing superior potential in treatment of emulsified oily wastewater.