A new approach for the fractionation of water-soluble organic carbon in atmospheric aerosols and cloud drops

A novel approach is described for the fractionation of water-soluble organic carbon (WSOC) in atmospheric aerosols and cloud drops. The method is based on the preliminary adsorption of the sample, acidified at pH 2, on a polymeric styrene-divinylbenzene resin (XAD-2) and subsequent elution with a series of solvents, which leads to the fractionation of the sample into three classes of compounds. The method was set up using synthetic mixtures of organic compounds and then applied to selected samples of atmospheric aerosols and cloud drops. All samples and collected fractions were analysed using size exclusion chromatography (SEC). This method proved particularly useful both in providing information on the organic content of the samples and for the characterisation of the macromolecular compounds (MMCs) in the samples. Synthetic samples were prepared using humic, fulvic and tannic acid to simulate naturally occurring MMCs. In the first fraction, eluted with HCl, only the most soluble organic compounds (oxalic acid, formic acid and acetic acid) were collected. In the second fraction, eluted with methanol, the major part of the organic material was collected together with the more hydrophilic constituents of the humic substances. In the third fraction, it was possible to separately recover the more hydrophobic component of the humic substances. A large number of atmospheric samples (fog, aerosol, cloud) were then analysed using SEC. Most of these samples evidenced a noteworthy chromatogram at 254 nm. Moreover, the chromatographic area evidenced a clear linear correlation with the total organic carbon (TOC) values. The fractionation method on XAD-2 was finally applied to selected atmospheric samples, yielding three classes of organic compounds. In each sample, a non-negligible amount of compounds with dimensional and chemical properties similar to humic substances were collected in the third fraction. The carbon content in this latter fraction was estimated both by TOC and by means of the correlation between TOC and SEC area.     

北京市控制大气污染四期紧急措施环境有效性分析

对北京市控制大气污染的四期紧急措施进行量化,分别计算出各项控制措施实施后的排放削减量,建立排放清单.采用空气质量模型,模拟了紧急措施实施的各阶段市区内一次大气污染物SO₂、NO_x和PM10浓度的时空分布情况,分析和评价了四期紧急措施的环境有效性.结果表明,四期紧急措施对SO₂和NO_x的控制效果较好,PM10的环境浓度下降不明显.     

中国地表水酸化敏感性的区划

地表水体的酸化与集水区的许多环境因子密切相关,如土壤对酸的缓冲能力、基岩中和酸沉降的能力以及土地利用方式等.其中,土壤的抗酸化能力是关键因素.因此可以根据集水区土壤、基岩和土地利用方式等信息来评估地表水在不同流量下发生酸化的可能性.本研究成功地应用已有资料和数据得到了我国地表水对酸沉降的敏感性等级,并绘制了地表水酸化敏感性区划图.结果表明,我国大部分地表水对酸化并不敏感.极易酸化和较易酸化的地表水主要分布在东北的北部地区,占所有国土面积的2.67%,是该地区强酸性漂灰土、酸性母岩和针叶林植被共同作用的结果.对酸化敏感性为中级和低级,即不易酸化的地表水主要分布在东北暗棕壤地区和南方富铝土区域,占所有国土面积的15.2%.其余82.11%国土面积上的地表水对酸化不敏感,完全不可能发生酸化.北方地区主要是由于土壤的强缓冲能力,而在南方,石灰质土壤以及耕作农田的广泛分布是最重要因素.南方重酸雨区由于土壤对酸化并不很敏感,因此在短期内不会出现大面积水体酸化现象.由于东北近年来频频出现酸雨,因此东北的酸沉降必须及早防治,以免出现大面积酸化水体.     

应用动态模型确定酸沉降临界负荷的探讨

任何一个天然生态系统都是一个稳定系统.在一定酸沉降量的作用下,生态系统最终会平衡在一个新的稳定状态.动态模型可以模拟不同酸沉降量下生态系统化学状态的变化趋势.根据信号与系统理论,这种趋势可以用一阶指数衰减函数进行模拟,以得到系统达到稳定状态时的化学指标值.根据不同酸沉降量和所对应的稳态化学指标值之间的剂量-响应曲线,可以求出当系统稳态化学指标值达到临界化学值时的酸沉降量,即为系统的酸沉降临界负荷.应用这种方法,以MAGIC模型为例,计算了四川峨眉山顶水和重庆南山湖泊的硫沉降临界负荷,分别为1.54和6.5     

SO2对Ag/Al2O3催化剂上CH3OH还原NO性能的影响

用溶胶-凝胶混合法制备了Ag负载量为5%的Ag/A1₂O₃催化剂.研究了富氧条件下,SO₂对CH₃OH在催化剂上还原NO性能的影响.结果表明,反应气不含SO₂和H₂O时,NO还原活性温度较低,有显著量N₂O生成,这被归因为反应过程中,部分氧化态Ag被还原为金属Ag.添加SO₂或同时添加SO₂和H_{2相似文献}   

油污染土壤气体抽排去污模型及影响因素

为了开展适合我国实际情况的有机污染土壤气体抽排净化技术研究,在对油污染土壤的通风去污过程机理进行分析的基础上,建立了一个简化机理模拟模型.以华北地区典型土壤为实验土样,油污染物为例,通过一维土柱实验,研究了抽排气体流速、土壤含水率和土质对去污过程的影响.实验表明抽排气体流速存在最佳值,土壤含水率对不同土质土壤净化时间影响不同,对粉砂土,含水率升高,净化效率增强;而对粘质土壤,结果正好相反.对模型预测结果进行实验验证表明,本文建立的模拟模型在实验限定条件范围内是准确和适用的.     

絮凝剂用壳聚糖的中试生产研究

在实验室制备絮凝剂用壳聚糖的基础上,按工业化生产的要求对壳聚糖进行了中试生产研究.经正交试验确定了生产过程中脱钙、脱蛋白、脱乙酰等3步反应的最佳工艺参数. 由此中试工艺生产的壳聚糖的生产成本比国内同类产品下降了22%,生产周期缩短了66%,且主要性能指标均达到或超过国内外同类产品的水平.     

Impacts of emissions and meteorological changes on China’s ozone pollution in the warm seasons of 2013 and 2017

O₃ increment is mainly caused by changes in meteorology rather than emissions. Emission reduction is effective to reduce O₃ nationwide, especially in summer. Strengthened NO_x controls are necessary to meet the ambient O₃ standard. We have quantified the impacts of anthropogenic emissions reductions caused by the Air Pollution Control Action Plan and changes in meteorological fields between 2013 and 2017 on the warm-season O₃ concentration in China using a regional 3D chemical transport model. We found that the impact on daily maximum eight-hour (MDA8) O₃ concentration by the meteorological variation that mostly increased O₃ was greater than that from emission reduction, which decreased O₃. Specifically, the control measures implemented since 2013 in China have reduced SO₂, NO_x, PM_2.5, and VOC emissions by 33%, 25%, 30%, and 4% in 2017, while NH₃ emissions have increased by 7%. The changes in anthropogenic emissions lowered MDA8 O₃ by 0.4–3.7 ppb (0.8%–7.6%, varying by region and month), although MDA8 O₃ was increased slightly in some urban areas (i.e. North China) at the beginning/end of warm seasons. Relative to 2013, the average 2 m temperature in 2017 shows increments in North, North-east, East, and South China (0.34℃–0.83℃) and decreases in Central China (0.24℃). The average solar radiation shows increments in North, North-east, and South China (7.0–9.7 w/m²) and decreases in Central, South-west, and North-west China (4.7–10.3 w/m²). The meteorological differences significantly change MDA8 O₃ by -3.5–8.5 ppb (-8.2%–18.8%) with large temporal variations. The average MDA8 O₃ was slightly increased in North, North-east, East, and South China. The response surface model suggests that the O₃ formation regime transfers from NO_x-saturated in April to NO_x-limited in July on average in China.     

Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.     

Anaerobic phenanthrene biodegradation with four kinds of electron acceptors enriched from the same mixed inoculum and exploration of metabolic pathways

Anaerobic phenanthrene biodegradation enriched process was described in detail. The enriched bacterial communities were characterized under four redox conditions. The enriched archaeal communities were stated under high percentage conditions. Relatively intact pathways of anaerobic phenanthrene biodegradation were proposed. Polycyclic aromatic hydrocarbons (PAHs) are widespread and persistent contaminants worldwide, especially in environments devoid of molecular oxygen. For lack of molecular oxygen, researchers enhanced anaerobic zones PAHs biodegradation by adding sulfate, bicarbonate, nitrate, and iron. However, microbial community reports of them were limited, and information of metabolites was poor except two-ring PAH, naphthalene. Here, we reported on four phenanthrene-degrading enrichment cultures with sulfate, bicarbonate, nitrate, and iron as electron acceptors from the same initial inoculum. The high-to-low order of the anaerobic phenanthrene biodegradation rate was the nitrate-reducing conditions>sulfate-reducing conditions>methanogenic conditions>iron-reducing conditions. The dominant bacteria populations were Desulfobacteraceae, Anaerolinaceae, and Thermodesulfobiaceae under sulfate-reducing conditions; Moraxellaceae, Clostridiaceae, and Comamonadaceae under methanogenic conditions; Rhodobacteraceae, Planococcaceae, and Xanthomonadaceae under nitrate-reducing conditions; and Geobacteraceae, Carnobacteriaceae, and Anaerolinaceae under iron-reducing conditions, respectively. Principal component analysis (PCA) indicated that bacteria populations of longtime enriched cultures with four electron acceptors all obtained significant changes from original inoculum, and bacterial communities were similar under nitrate-reducing and iron-reducing conditions. Archaea accounted for a high percentage under iron-reducing and methanogenic conditions, and Methanosarcinaceae and Methanobacteriaceae, as well as Methanobacteriaceae, were the dominant archaea populations under iron-reducing and methanogenic conditions. The key steps of phenanthrene biodegradation under four reducing conditions were carboxylation, further ring system reduction, and ring cleavage.