长江经济带突发水污染风险分区研究

长江经济带突发水污染事件频发,对区域人群健康和生态安全造成严峻挑战.环境风险分区是环境风险管理的基础和有效工具.本研究以2015年为基准年,基于环境统计数据、DEM数据、水质监测断面数据和基础地理数据,综合考虑了水系流向、水系级别及水质等因素,以1 km×1 km的网格为基本单元,对长江经济带开展突发水污染风险分区.结果表明:①高风险区面积为3348.9 km~2,占评估区总面积的0.16%;较高风险区面积为26030.7 km~2,占比1.27%;中风险区面积为97971.1 km~2,占比4.79%;低风险区面积为1916838.7 km~2,占比93.77%;②从沿长江干流两岸分布来看,高风险区面积沿长江上游至下游呈逐渐增加趋势,主要集中分布在重庆市中部、湖北省东部、安徽省东部、江苏省中西部、浙江省北部、上海市西部等地;③从沿长江主要支流两岸分布来看,高风险区主要分布在嘉陵江南段、乌江南段、汉水东段、湘江北段、赣江北段等.研究结果可为长江经济带生态环境管理提供科学依据.     

不同来源土样胶体对氯霉素吸附行为的影响

选取不同来源沉积物或土壤样品（沉积物A1和A2,天然土壤B1和B2,市售营养土B3）,采用切向超滤与多种纳米分析技术相结合的方法,分析了不同土样中胶体的理化特征及其对氯霉素（CAP）吸附行为的影响.荧光区域积分法结果显示,土样胶体的荧光组分以色氨酸类蛋白质、类富里酸和类腐殖酸为主,络氨酸类蛋白质和溶解性微生物代谢物质存在较少.吸附实验结果表明,B3胶体对CAP的吸附率最大（36.25%）,在胶体浓缩液和超滤液中的分配比例最高（1.91）,但其有机碳归一化结合系数最低（3.93）.与天然土壤相比,河湖沉积物胶体的吸附率较高,但其与CAP的结合能力却较低.冗余分析结果表明,胶体对CAP的吸附主要与其芳香度、有色溶解性有机质丰度、溶解性有机碳浓度及分子量有关;此外,胶体的腐殖化程度、芳环上羧基、羰基等官能团的比重及荧光物质中溶解性微生物代谢产物和类腐殖酸对CAP的吸附行为也具有较大影响.     

地下水波动带中细菌群落结构与水质响应关系

为揭示地下水波动带中细菌群落结构特征及其与地下水环境相互作用关系,选取哈尔滨市第一水源地作为研究区,采集地下水样品以及波动带不同深度（0~5m非饱和带和6~50m饱和带）含水介质样品,分别用于水化学分析和16S rRNA细菌高通量测序,依托冗余分析定量表述地下水质参数与细菌群落相关性.水化学分析结果显示,研究区地下水主要污染物为Fe、Mn、NH₄⁺和有机质,Fe、Mn超标与研究区特定地质背景有关,NH₄⁺和有机质主要来源于人类活动.微生物分析结果显示,非饱和带和饱和带的细菌群落结构差异性显著,非饱和带细菌群落丰度和多样性显著高于饱和带,Proteobacteria、Bacteroidetes、Actinobacteria、Firmicutes和Acidobacteria为研究区优势门,在非饱和带和饱和带的累积相对丰度分别为82.89%和98.64%.冗余分析（RDA）结果显示,门水平上非饱和带中与水质演化强相关的细菌类群是Bacteroidetes、Proteobacteria、Actinobacteria、Verrucomicrobia,贡献率分别为15%、14.8%、8.9%和5.2%;饱和带中对地下水质演化起主要作用的类群为Bacteroidetes、Acidobacteria、Actinobacteria和Firmicutes,贡献率分别为38.4%、19.0%、10.8%和9.1%.属水平上非饱和带中的Pseudomonas和饱和带中的Flavobacterium对Fe、Mn、NH₄⁺生物转化起主导作用.本研究为揭示地下水波动带中生物地球化学作用对地下水环境的影响提供了科学依据,对地下水污染修复具有重要的意义.     

黑河流域底栖动物群落结构及水质评价

为了解黑河流域上中游底栖动物群落结构特征及其与环境因子之间的关系,于2018年8月对研究区域17个采样点的底栖动物和水体理化指标进行调查研究.共鉴定出底栖动物43种,其中节肢动物34种（79.1%）,软体动物7种（16.3%）,环节动物2种（4.6%）;就整个研究区域而言,优势种为大蚊（Tipulidae）、豆娘幼虫（Damselfly）、水蜘蛛（Argyroneta）、耳萝卜螺（Radix auricularia）、琥珀螺（Suecinea sp.）、白旋螺（Gyraulusalbus）,干、支流优势种分布趋势为干流（6种）优于支流（5种）;底栖动物平均密度和平均生物量分别为77ind/m²和3.7423g/m²现存量存在显著空间差异,整体上干流（1032ind/m²、60.0963g/m²）大于支流（276ind/m²、3.5233g/m²）,物种数干流（36种）大于支流（15种）;单因素方差分析显示,Shannon-Wiener多样性指数、Margalef丰富度指数及Pielou均匀度指数分布特征为干流大于支流.黑河流域上游支流和中游干流不同河段底栖动物物种组成呈空间异质性,而多样性指数对物种组成依赖性强,但因黑河流域底栖动物物种组成受自然因素和人类活动双重影响程度差异较大,使得Shannon-Wiener多样性指数、Margalef丰富度指数及Pielou均匀度指数不适合黑河水质评价.依据BI指数和综合污染指数评价表明,黑河上游支流水质优于中游干流.根据底栖动物与环境因子之间的相关矩阵分析并结合RDA分析表明：BOD₅、水温（WT）、电导率（EC）、DO、溶解性总固体（TDS）、COD_Mn及盐度是影响底栖动物群落结构的主要环境因子.     

MnCeOx/沸石催化剂对工业典型VOCs的催化性能

以沸石为载体制备了锰铈复合氧化物催化剂（记为:MnCeO_x/沸石催化剂）,探究了催化剂对工业典型VOCs的二元催化性能,并对催化剂进行BET、XRD及SEM表征。结果表明:Ce的加入,促进了Mn的分散,提高了MnCeO_x/沸石催化剂的活性;当n（Mn）∶n（Ce）为1∶1,负载率为20%,焙烧温度为500℃时,催化剂的活性最高,其对甲苯的起燃温度（T₅₀）和完全燃烧温度（T₉₀）分别为155,255℃;单组分实验中,催化剂对3种有机物均表现出较高活性,转化率达到90%时的反应温度均在275℃以下,其活性顺序为乙酸乙酯>甲苯>丙酮,主要受反应活化能大小及分子极性的影响;二元催化实验中,由于竞争吸附的影响,3种物质的T₅₀和T₉₀较单组分均分别提高了8~13,14~38℃。     

静态旋流强化湿法烟气脱硫研究进展

静态旋流作为湿法烟气脱硫中一种强化传质的方式,对其发展现状与趋势展开研究。分析了旋流吸收器的内部气相速度场以及强化传质的过程原理,综合比较了各类气液接触的脱硫方式、脱硫剂的特征,确定了在运行范围内脱硫剂浓度、气液流速、SO₂浓度等操作参数对于脱硫效率η和气相总体积传质系数K_ga的影响及其机理,剖析了利用传质理论进行旋流吸收的研究及发展,介绍了旋流脱硫的工业应用。结果表明:静态旋流有助于脱硫传质过程的强化,在工况范围内,吸收液浓度、气液流速的增加,提高了η和K_ga,但随着SO₂浓度的增加,η及K_ga略有下降,分别最高下降7.1%和0.75 s-1,总工况范围内η和K_ga分别为68.58%~97.63%和5.08~8.46 s-1。研究结果可对基于旋流强化的工业烟气脱硫提供参考。     

Tuning the fill percentage in the hydrothermal synthesis process to increase catalyst performance for ozone decomposition

The performance of Ce-OMS-2 catalysts was improved by tuning the fill percentage in the hydrothermal synthesis process to increase the oxygen vacancy density. The Ce-OMS-2 samples were prepared with different fill percentages by means of a hydrothermal approach (i.e. 80%, 70%, 50% and 30%). Ce-OMS-2 with 80% fill percentage (Ce-OMS-2-80%) showed ozone conversion of 97%, and a lifetime experiment carried out for more than 20?days showed that the activity of the catalyst still remained satisfactorily high (91%). For Ce-OMS-2-80%, Mn ions in the framework as well as K ions in the tunnel sites were replaced by Ce⁴⁺, while for the others only Mn ions were replaced. O₂-TPD and H₂-TPR measurements proved that the Ce-OMS-2-80% catalyst possessed the greatest number of mobile surface oxygen species. XPS and XAFS showed that increasing the fill percentage can reduce the AOS of Mn and augment the amount of oxygen vacancies. The active sites, which accelerate the elimination of O₃, can be enriched by increasing the oxygen vacancies. These findings indicate that increasing ozone removal can be achieved by tuning the fill percentage in the hydrothermal synthesis process.     

Role of glycine on sulfuric acid-ammonia clusters formation: Transporter or participator

Glycine(Gly) is ubiquitous in the atmosphere and plays a vital role in new particle formation(NPF).However,the potential mechanism of its on sulfuric acid(SA)-ammonia(A)clusters formation under various atmospheric conditions is still ambiguous.Herein,a(Gly)_x·(SA)_y·(A)_z(z≤x+y≤3) multicomponent system was investigated by using density functional theory(DFT) combined with Atmospheric Cluster Dynamics Code(ACDC) at different temperatures and precursor concentrations.The results show that Gly,with one carboxyl(-COOH) and one amine(-NH_2) group,can interact strongly with SA and A in two directions through hydrogen bonds or proton transfer.Within the relevant range of atmospheric concentrations,Gly can enhance the formation rate of SA-A-based clusters,especially at low temperature,low [SA],and median [A].The enhancement(R) of Gly on NPF can be up to 340 at T=218.15 K,[SA]=10~4,[A]=10~9,and [Gly]=10~7 molecules/cm~3.In addition,the main growth paths of clusters show that Gly molecules participate into cluster formation in the initial stage and eventually leave the cluster by evaporation in subsequent cluster growth at low [Gly],it acts as an important "transporter" to connect the smaller and larger cluster.With the increase of [Gly],it acts as a "participator" directly participating in NPF.     

Adsorption of 17β-estradiol from aqueous solution by raw and direct/pre/post-KOH treated lotus seedpod biochar

Five biochars derived from lotus seedpod(LSP) were applied to examine and compare the adsorption capacity of 17β-estradiol(E2) from aqueous solution.The effect of KOH activation and the order of activation steps on material properties were discussed.The effect of contact time,initial concentration,p H,ionic strength and humic acid on E2 adsorption were investigated in a batch adsorption process.Experimental results demonstrated that the pseudo second-order model fitted the experimental data best and that adsorption equilibrium was reached within 20 hr.The efficiency of E2 removal increased with increasing E2 concentration and decreased with the increase of ionic strength.E2 adsorption on LSP-derived biochar(BCs) was influenced little by humic acid,and slightly affected by the solution p H when its value ranged from 4.0 to 9.0,but considerably affected at p H 10.0.Low environmental temperature is favorable for E2 adsorption.Chemisorption,π–π interactions,monolayer adsorption and electrostatic interaction are the possible adsorption mechanisms.Comparative studies indicated that KOH activation and the order of activation steps had significant impacts on the material.Post-treated biochar exhibited better adsorption capacity for E2 than direct treated,pretreated,and raw LSP biochar.Pyrolyzed biochar at higher temperature improved E2 removal.The excellent performance of BCs in removing E2 suggested that BCs have potential in E2 treatment and that the biochar directly treated by KOH would be a good choice for the treatment of E2 in aqueous solution,with its advantages of good efficiency and simple technology.     

Influence of floc dynamic protection layer on alleviating ultrafiltration membrane fouling induced by humic substances

Cake layer formation is inevitable over time for ultrafiltration (UF) membrane-based drinking water treatment. Although the cake layer is always considered to cause membrane fouling, it can also act as a “dynamic protection layer”, as it further adsorbs pollutants and dramatically reduces their chance of getting to the membrane surface. Here, the UF membrane fouling performance was investigated with pre-deposited loose flocs in the presence of humic acid (HA). The results showed that the floc dynamic protection layer played an important role in removing HA. The higher the solution pH, the more negative the floc charge, resulting in lower HA removal efficiency due to the electrostatic repulsion and large pore size of the floc layer. With decreasing solution pH, a positively charged floc dynamic protection layer was formed, and more HA molecules were adsorbed. The potential reasons were ascribed to the smaller floc size, greater positive charge, and higher roughness of the floc layer. However, similar membrane fouling performance was also observed for the negative and positive floc dynamic protection layers due to their strong looseness characteristics. In addition, the molecular weight (MW) distribution of HA also played an important role in UF membrane fouling behavior. For the small MW HA molecules, the chance of forming a loose cake layer was high with a negatively charged floc dynamic protection layer, while for the large MW HA molecules it was high with a positively charged floc dynamic protection layer. As a result, slight UF membrane fouling was induced.