Algal toxicity induced by effluents from textile-dyeing wastewater treatment plants

This research aimed to evaluate the alga Scenedesmus obliquus toxicity induced by textiledyeing effluents(TDE).The toxicity indicator of TDE in alga at the physiological(algal growyth),biochemical(chlorophyll-a(Chl-a) synthesis and superoxide dismutase(SOD) activity) and structural(cell membrane integrity) level were investigated.Then we further study the relationship among toxicity indicators at physiological and biochemical level,and supplemented by research on algal biomacromolecules.According to the analysis of various endpoints of the alga,the general sensitivity sequence of toxicity endpoints of Scenedesmus obliquus was:SOD activity Chl-a synthesis algal growth.The stimulation rate of SOD activity increased from day 3(57.25%～83.02%) to day 6(57.25%～103.81%),and then decreased on day 15(-4.23%～-32.96%),which indicated that the antioxidant balance system of the algal cells was destroyed.The rate of Chl-a synthesis inhibition increased gradually,reaching19.70%～79.39% on day 15,while the rate of growth inhibition increased from day 3(-12.90%～10.16%) to day 15(-21.27%～72.46%).Moreover,the algal growth inhibition rate was positively correlated with the inhibition rate of SOD activity or Chl-a synthesis,with the correlation coefficients were 0.6713 and 0.5217,respectively.Algal cells would be stimulating to produce excessive reactive oxygen species,which would cause peroxidation in the cells,thereby destroying chloroplasts,inhibiting chlorophyll synthesis and reducing photosynthesis.With increasing exposure time,irreversible damage to algae can lead to death.This study is expected to enhance our understanding of the ecological risks through algal tests caused by TDE.     

UV/H2O2 oxidation of tri(2-chloroethyl) phosphate: Intermediate products, degradation pathway and toxicity evaluation

Tri(2-chloroethyl) phosphate (TCEP) with the initial concentration of 5 mg/L was degraded by UV/H₂O₂ oxidation process. The removal rate of TCEP in the UV/H₂O₂ system was 89.1% with the production of Cl^? and PO₄^3? of 0.23 and 0.64 mg/L. The removal rate of total organic carbon of the reaction was 48.8% and the pH reached 3.3 after the reaction. The oxidative degradation process of TCEP in the UV/H₂O₂ system obeyed the first order kinetic reaction with the apparent rate constant of 0.0025 min^?1 (R²=0.9788). The intermediate products were isolated and identified by gas chromatography-mass spectrometer. The addition reaction of HO? and H₂O and the oxidation reaction with H₂O₂ were found during the degradation pathway of 5 mg/L TCEP in the UV/H₂O₂ system. For the first time, environment risk was estimated via the “ecological structure activity relationships” program and acute and chronic toxicity changes of intermediate products were pointed out. The luminescence inhibition rate of photobacterium was used to evaluate the acute toxicity of intermediate products. The results showed that the toxicity of the intermediate products increased with the increase of reaction time, which may be due to the production of chlorine compounds. Some measures should be introduced to the UV/H₂O₂ system to remove the highly toxic Cl-containing compounds, such as a nanofiltration or reverse osmosis unit.     

Ozone pollution characteristics and sensitivity analysis using an observation-based model in Nanjing, Yangtze River Delta Region of China

Ground-level ozone (O₃) has become a critical pollutant impeding air quality improvement in Yangtze River Delta region of China. In this study, we present O₃ pollution characteristics based on one-year online measurements during 2016 at an urban site in Nanjing, Jiangsu Province. Then, the sensitivity of O₃ to its precursors during 2 O₃ pollution episodes in August was analyzed using a box model based on observation (OBM). The relative incremental reactivity (RIR) of hydrocarbons was larger than other precursors, suggesting that hydrocarbons played the dominant role in O₃ formation. The RIR values for NO_X ranged from –0.41%/% to 0.19%/%. The O₃ sensitivity was also analyzed based on relationship of simulated O₃ production rates with reductions of VOC and NO_X derived from scenario analyses. Simulation results illustrate that O₃ formation was between VOCs-limited and transition regime. Xylenes and light alkenes were found to be key species in O₃ formation according to RIR values, and their sources were determined using the Positive Matrix Factorization (PMF) model. Paints and solvent use was the largest contributor to xylenes (54%), while petrochemical industry was the most important source to propene (82%). Discussions on VOCs and NO_X reduction schemes suggest that the 5% O₃ control goal can be achieved by reducing VOCs by 20%. To obtain 10% O₃ control goal, VOCs need to be reduced by 30% with VOCs/NO_X larger than 3:1.     

On-going nitrification in chloraminated drinking water distribution system (DWDS) is conditioned by hydraulics and disinfection strategies

Within the drinking water distribution system (DWDS) using chloramine as disinfectant, nitrification caused by nitrifying bacteria is increasingly becoming a concern as it poses a great challenge for maintaining water quality. To investigate efficient control strategies, operational conditions including hydraulic regimes and disinfectant scenarios were controlled within a flow cell experimental facility. Two test phases were conducted to investigate the effects on the extent of nitrification of three flow rates (Q = 2, 6, and 10 L/min) and four disinfection scenarios (total Cl₂=1 mg/L, Cl₂/NH₃-N=3:1; total Cl₂=1 mg/L, Cl₂/NH₃-N=5:1; total Cl₂=5 mg/L, Cl₂/NH₃-N=3:1; and total Cl₂=5 mg/L, Cl₂/NH₃-N=5:1). Physico-chemical parameters and nitrification indicators were monitored during the tests. The characteristics of biofilm extracellular polymetric substance (EPS) were evaluated after the experiment. The main results from the study indicate that nitrification is affected by hydraulic conditions and the process tends to be severe when the fluid flow transforms from laminar to turbulent (2300<Re<4000). Increasing disinfectant concentration and optimizing Cl₂/NH₃-N mass ratio were found to inhibit nitrification to some extend when the system was running at turbulent condition (Q = 10 L/min, Re = 5535). EPS extracted from biofilm that was established at the flow rate of 6 L/min had greater carbohydrate/protein ratio. Furthermore, several nitrification indicators were evaluated for their prediction efficiency and the results suggest that the change of nitrite, together with total organic carbon (TOC) and turbidity can indicate nitrification potential efficiently.     

餐厨垃圾生物有机肥对贫瘠黄褐土改良的研究

为了阐明餐厨垃圾生物有机肥改良贫瘠土壤的作用机制,以贫瘠黄褐土为研究对象,通过不施肥、长期（>5 a）施用化肥、中长期（5 a）施用少量餐厨垃圾生物有机肥和短期（1 a）施用大量餐厨垃圾生物有机肥4种施肥方式,分别记为CK组、CF组、LOF-5组和MOF-1组,对比分析不同施肥方式对土壤OM（有机质）、活性有机碳、营养元素和团聚体等的影响.结果表明:①施用餐厨垃圾生物有机肥可显著提高土壤OM、活性有机碳含量,其中,MOF-1组提高效果最显著,与CK组相比,w（OM）可提高173.29%,w（ROC）（ROC为易氧化有机碳）增加了39.17%,w（POC）（POC为颗粒有机碳）和w（DOC）（DOC为可溶性有机碳）分别是CK组的13.85和10.32倍.②中长期（5 a）施用少量餐厨垃圾生物有机肥可增加土壤中较大粒径团聚体的占比,且更有利于提高土壤团粒结构的稳定性,LOF-5组>2 mm粒级的团聚体占比是CK组的4.68倍;与CK组相比,LOF-5组MWD（平均重量直径）增加了100.00%,GMD（几何平均直径）增加了82.98%,>0.25 mm水稳定性团聚体质量占比（DR_0.25）增加了27.20%.③中长期（5 a）施用少量餐厨垃圾生物有机肥可增加土壤中w（TN）（TN为全氮）和w（AN）（AN为速效氮）,与CK组相比,LOF-5组w（TN）和w（AN）分别增加了77.42%和20.82%.施用餐厨垃圾有机肥也可同时增加土壤中w（AP）（AP为速效磷）和w（AK）（AK为速效钾）,MOF-1组增加效果较佳,w（AP）和w（AK）分别是CK组的9.43和3.39倍.研究显示,中长期（5 a）施用少量餐厨垃圾生物有机肥可提升土壤固碳能力,提高土壤养分利用的有效性,从而提升耕地土壤质量,减少化肥施用量,是我国贫瘠黄褐土改良的有效施肥模式.      

污泥腐殖酸对Cd2+的吸附特性

为了促进污水处理厂剩余污泥的资源化利用,探索S-HA（sludge-based humic acid, 污泥腐殖酸）对溶液中重金属Cd2+的吸附特性.采用国际腐殖酸协会（IHSS）推荐的方法提取S-HA,通过元素分析、FT-IR（傅里叶红外光谱分析）和SEM-EDS（外观形态分析）等方法,考察溶液pH和共存阳离子对吸附过程的影响,并对吸附过程分别进行了吸附动力学模型、等温吸附模型和吸附热力学模型拟合,同时通过对比S-HA吸附前后的红外光谱和扫描电镜-能谱图片,探索S-HA对Cd2+的吸附机制.结果表明:①S-HA表面呈松散的簇团状,含有大量的羧基、醇羟基和酚羟基等含氧官能团,芳香度较高,含有较多的脂肪链结构;S-HA在吸附水中Cd2+的过程中,Cd2+与S-HA表面上的酚羟基、羧基等官能团发生了络合作用.②S-HA对Cd2+的吸附量随溶液pH升高而增加,溶液中Na+、NH₄+和Ca2+等共存阳离子的存在不利于S-HA对Cd2+的吸附,其中Ca2+的存在对S-HA吸附Cd2+影响最大.③S-HA对Cd2+的吸附由快吸附、慢吸附和吸附平衡3个阶段组成,吸附平衡时间为12 h;吸附过程符合准二级动力学模型,其整体吸附速度由液膜扩散和颗粒内扩散共同控制;吸附等温线符合Freundlich等温吸附模型,25℃下的最大吸附量为19.29 mg/g,Cd2+在S-HA上的吸附是自发吸热反应.研究显示:污水处理厂剩余污泥提取的S-HA对Cd2+具有较好的吸附效果;S-HA对Cd2+的吸附过程同时存在着物理吸附和化学吸附;高pH对S-HA吸附Cd2+有促进作用,而高离子强度对S-HA吸附Cd2+有抑制作用.      

长沙市近郊莲花镇土壤重金属生态风险评价

选择长沙市近郊的莲花镇作为研究对象,采集了镇域范围内54个土壤样品,运用综合的生态风险评价方法对Hg、Cd、As、Pb、Cr 5种土壤重金属元素污染程度及对人体的健康危害程度进行评价。结果表明:1)5种重金属元素的污染程度排序为Cd > Hg > Pb > As > Cr,Cd呈现重度污染;Cd和Pb空间变异显著,其来源受人为干扰程度高。2)5种重金属元素的潜在生态危害排序为Cd > Hg > As > Pb > Cr,Cd和Hg处于强生态危害程度,是研究区域土壤重金属污染的主要因子;研究区域综合潜在生态风险达到强生态危害等级。3)"手-口"摄入是土壤重金属暴露的主要途径,儿童的非致癌暴露剂量远大于成人。5种重金属对儿童和成人所产生的非致癌风险商和非致癌风险指数均<1,不存在非致癌健康风险。4)Cr的致癌风险指数>10-4,具有极高的致癌风险;Cd和As的致癌风险指数为10-6~10-4,处于可以接受的风险范围。Cr、As的污染有不断加剧的趋势,成为影响人体健康的主要因子,应引起关注。     

博斯腾小湖最低生态水位与水量盈缺分析

近年来,博斯腾湖小湖水位大幅波动引发了湖区生态环境问题,基于最低生态水位的湖泊水量盈缺分析对小湖水量调度和生态保护有积极意义。基于1991—2019年达吾提闸实测小湖水位数据,结合湖盆DEM数据和遥感NDVI数据,分别采用年保证率设定法、湖泊地形分析法和曲线相关法计算小湖区最低生态水位;并利用其他水文、气象和农业活动和湖区水量调控数据,使用主成分分析法解析小湖缺水的主要驱动因子。结果表明:博斯腾湖小湖最低生态水位为1047.18 m,多年平均满足率为31.03%。1991—1998年、2005—2015年和2017年间博斯腾小湖区发生了生态缺水,平均缺水量为0.69×108 m3。上游来水量是小湖生态需水保证情势的主要驱动因素,农业活动和宝浪苏木水量调节活动次之,气候变化影响相对较小。2000年之前,生态缺水主要由湖区水位调控产生;2000年之后,灌区农业取水成为生态缺水主要诱因。该研究结果可以为博斯腾湖小湖水量调控和湿地生态系统恢复保护提供科学依据。     

基于模糊PI控制的瞬态高温控制策略研究

目的通过地面环境试验研究气动热引起的瞬态高温环境对飞行器结构的影响。方法设计基于石英灯和离心机的瞬态高温-加速度复合试验系统,研究温度和加速度同步控制系统的结构和原理,分析无制冷装置环境下瞬态高温控制的难点,提出基于模糊PI控制器的温度控制策略。结果通过MATLAB仿真验证,设计的模糊PI控制器相比传统的PI控制器能够有效提高温度控制的动态性能与精确性。结论将基于模糊PI控制的瞬态加热控制策略应用于瞬态高温控制是可行、有效的,能为地面气动热模拟环境试验提供技术保障。     

石期河流域地下水化学特征及物质来源分析

为明确典型岩溶溶丘洼(谷)地区域地下水化学特征及其成因,以石期河流域为研究对象,运用Gibbs图、Piper图、端元分析及离子比例系数等方法,对地下水水化学特征及物质来源进行了定性和定量分析.结果表明,研究区内地下水pH值介于6.06～8.07之间,Ca~(2+)、 Mg~(2+)和HCO~-_3是地下水中的主要离子,其质量浓度范围分别为2.61～108.7、 0.54～27.61和8.1～370.74mg·L~(-1),符合岩溶水高钙弱碱性特征;地下水物质成分中, Ca~(2+)和Mg~(2+)主要受到碳酸参与的灰岩和白云岩风化作用的控制, Na~+主要来源于硅酸盐岩的溶解,同时, Ca~(2+)和Na~+在地下水流动过程中进行阳离子交替吸附作用; K~+、 Cl~-和NO~-_3主要受到农业化肥施放和生活废水排放的影响.此外,大气降水作为该区域地下水的主要补给来源,对当地地下水化学特征和物质来源也有一定的影响.