催化湿式氧化中负载型催化剂的稳定性与应用

催化剂在应用过程中必须具有良好的催化活性和稳定性.优化制备的CuO/γ-Al2O3催化剂用于处理高浓度难降解的乳化液废水时具有良好的催化活性,在200℃时反应2 h,TOC去除率为81.3%,比未加催化剂的湿式氧化提高了14.9%.该催化剂对分散兰废水具有更高的活性和稳定性:在220℃反应1.5 h后,COD和TOC去除率分别为68.8%和56.5%,比非催化氧化分别提高了18.7%和18.9%.     

Effect of surfactants at low concentrations on the sorption of atrazine by natural sediment.

A series of experiments were carried out to determine the effect of surfactants at low concentrations on the sorption of atrazine by natural sediments. With surfactant concentrations ranging from 0 to 20 mg/ L, anionic and cationic surfactants appreciably reduce the adsorption of atrazine, while nonionic surfactant decreases the adsorption of atrazine at concentrations equal to or less than 1 mg/L and increases adsorption at higher concentrations. Desorption of atrazine in the presence of different sodium dodecylbenzene sulfonate (SDBS) concentrations shows that a portion of the bound pesticide resists desorption in the SDBS free system. However, the addition of SDBS accelerates the desorption of atrazine. Furthermore, the nature of sediment and the contacting sequence of SDBS, at 10 mg/L, with the sediment, also influence the adsorption of atrazine. The conclusions in this study could be explained partially by the effect of the type and concentration of surfactants and the characteristics of sediments.     

Characterization of submicron particles during autumn in Beijing, China

In this study, we performed a highly time-resolved chemical characterization of nonrefractory submicron particles(NR-PM_1) in Beijing by using an Aerodyne high-resolution time-of-flight aerosol mass spectrometer(HR-ToF-AMS). The results showed the average NR-PM_1 mass concentration to be 56.4 ± 58.0 μg/m~3, with a peak at 307.4 μg/m~3. Due to the high frequency of biomass burning in autumn, submicron particles significantly increased in organic content, which accounted for 51% of NR-PM_1 on average. Secondary inorganic aerosols(sulfate + nitrate + ammonium) accounted for 46% of NR-PM_1, of which sulfate,nitrate, and ammonium contributed 15%, 20%, and 11%, respectively. To determine the intrinsic relationships between the organic and inorganic species, we used the positive matrix factorization(PMF) model to merge the high-resolution mass spectra of the organic species and NO+and NO_2~+ions. The PMF analysis separated the mixed organic and nitrate(NO+and NO_2~+) spectra into four organic factors, including hydrocarbon-like organic aerosol(HOA), oxygenated organic aerosol(OOA), cooking organic aerosol(COA), and biomass burning organic aerosol(BBOA), as well as one nitrate inorganic aerosol(NIA) factor. COA(33%) and OOA(30%) contributed the most to the total organic aerosol(OA) mass, followed by BBOA(20%) and HOA(17%). We successfully quantified the mass concentrations of the organic and inorganic nitrates by the NO+and NO2+ions signal in the organic and NIA factors. The organic nitrate mass varied from 0.01-6.8 μg/m~3, with an average of 1.0 ±1.1 μg/m~3, and organic nitrate components accounted for 10% of the total nitrate mass in this observation.     

Investigating missing sources of glyoxal over China using a regional air quality model (RAMS-CMAQ)

Currently, modeling studies tend to significantly underestimate observed space-based glyoxal(CHOCHO) vertical column densities(VCDs), implying the existence of missing sources of glyoxal. Several recent studies suggest that the emissions of aromatic compounds and molar yields of glyoxal in the chemical mechanisms may both be underestimated, which can affect the simulated glyoxal concentrations. In this study, the influences of these two factors on glyoxal amounts over China were investigated using the RAMS-CMAQ modeling system for January and July 2014. Four sensitivity simulations were performed, and the results were compared to satellite observations. These results demonstrated significant impacts on glyoxal concentrations from these two factors.In case 1, where the emissions of aromatic compounds were increased three-fold,improvements to glyoxal VCDs were seen in high anthropogenic emissions regions. In case 2, where molar yields of glyoxal from isoprene were increased five-fold, the resulted concentrations in July were 3–5-fold higher, achieving closer agreement between the modeled and measured glyoxal VCDs. The combined changes from both cases 1 and 2 were applied in case 3, and the model succeeded in further reducing the underestimations of glyoxal VCDs. However, the results over most of the regions with pronounced anthropogenic emissions were still underestimated. So the molar yields of glyoxal from anthropogenic precursors were considered in case 4. With these additional mole yield changes(a two-fold increase), the improved concentrations agreed better with the measurements in regions of the lower reaches of the Yangtze River and Yellow River in January but not in July.     

Behaviors and kinetics of toluene adsorption‐desorption on activated carbons with varying pore structure

This work was undertaken to investigate the behaviors and kinetics of toluene adsorption and desorption on activated carbons with varying pore structure. Five kinds of activated carbon from different raw materials were selected. Adsorption isotherms and breakthrough curves for toluene were measured. Langmuir and Freundlich equations were fitted to the equilibrium data, and the Freundlich equation was more suitable for simulating toluene adsorption. The process consisted of monolayer, multilayer and partial active site adsorption types. The effect of the pore structure of the activated carbons on toluene adsorption capacity was investigated. The quasi-first-order model was more suitable for describing the process than the quasi-second-order model. The adsorption data was also modeled by the internal particle diffusion model and it was found that the adsorption process could be divided into three stages. In the external surface adsorption process, the rate depended on the specific surface area. During the particle diffusion stage, pore structure and volume were the main factors affecting adsorption rate. In the final equilibrium stage, the rate was determined by the ratio of meso-and macro-pores to total pore volume. The rate over the whole adsorption process was dominated by the toluene concentration. The desorption behavior of toluene on activated carbons was investigated,and the process was divided into heat and mass transfer parts corresponding to emission and diffusion mechanisms, respectively. Physical adsorption played the main role during the adsorption process.     

不同培养方式下絮状污泥颗粒化特性和灰色关联度分析

为探索好氧颗粒污泥形成机理,开展了不同培养方式下絮状污泥颗粒化特性研究.选取3种培养方式:人工配水培养、海藻酸钠强化培养和农村模拟污水培养,利用灰色关联分析法,对比3种不同培养方式下,污泥颗粒化过程中各影响因素灰色关联度系数,筛选好氧颗粒污泥培养的关键因素.研究发现,人工配水培养方式下经过40 d成功出现好氧颗粒污泥,投加海藻酸钠强化培养方式下经过20 d出现好氧颗粒污泥,农村模拟污水经过55 d培养出好氧颗粒污泥.3种培养方式下出现的好氧颗粒污泥均具有密实的结构和较好的沉降性能,同时可实现对污染物的高效去除.利用数据处理系统(Data Processing System,DPS)对各影响因素的灰色关联度进行分析,发现不同培养方式下污泥颗粒化过程中起主导作用的影响因素并非唯一,水力停留时间和胞外聚合物在各培养方式中均具有较高的关联度系数,对好氧颗粒污泥的形成具有关键作用.     

双酚A和邻苯二甲酸二正丁酯在纸类上的吸附特性研究

采用序批式实验,考察了报纸对双酚A(BPA)和邻苯二甲酸二正丁酯(DnBP)的吸附能力,用Freundlich、Langmuir、Dubinin-Radushkevich(D-R)、Flory-Huggins(F-H)、BET、Temkin 6种吸附等温线模型对实验数据进行了拟合.并选择了回归系数(R2)、均方根差(RMSE)和卡方检验(X2检验)3种非线性回归方法评价了模型拟合度.结果表明,Freundlich和Temkin吸附等温线模型能很好地描述BPA和DnBP在纸类表面的吸附,BPA和DnBP的R2均大于0.95(P<0.01),RMSE和X2分别小于0.05和0.02;吸附能力与吸附质的疏水性呈正相关.由D-R和F-H吸附等温线模型拟合结果可知,BPA和DnBP的吸附平均自由能分别为1.484和1.609 kJ/mol;Gibbs自由能分别为-6.559和-7.021 kJ/mol.说明BPA和DnBP在纸类上的吸附为自发的物理吸附.BPA和DnBP在纸类上的Freundlich吸附常数k分别为0.147和0.502 mg(1-n)·L"·g-1,均高于文献报道的底泥等的吸附常数,说明生活垃圾填埋场中纸类会阻碍BPA和DnBP的迁移和生物可利用性.     

广西发展燃料乙醇产业总体方案替代方案优选

规划环评的目的不是减小规划对环境的影响,而是通过比较,选出规划对环境影响最小的替代方案。本文运用AHP-模糊数学法,结合广西发展燃料乙醇产业总体方案,从大气环境、水环境、废弃物、资源承载力、资源能源消耗和生态环境保护等六个方面,合理选取指标,建立了方案布局合理性指标体系,并用AHP-模糊数学法对四种替代方案进行了计算,得出方案一的结果为77．44,方案二的结果为78．62,方案三的结果为78．23,方案四的结果为82．13。方案四为“零作为”方案,计算结果为环境本底参照值。论文以方案四为参照,同时结合各方案的隶属度,选出了最佳替代方案。     

荣钢节水减排集成技术研究与实践

针对钢铁企业耗水量大、供水资源匮乏等问题,以荣钢集团为研究实体,调查其用水分布与工序,进行水量平衡测试及基础数据的统计,在分析荣钢水资源利用状况基础上,优化水资源配置,研究钢铁行业节水减排集成技术与实施措施,通过一水多用、串级使用、加强节水控污、建立多水源处理再生系统等方法,节约了水资源,提高了水资源的利用率,使企业节水减排取得较好的成效。     

小城镇污水处理厂升级改造技术分析

随着城镇化进程加快,经济快速发展的同时严重的环境污染问题随之出现,主要表现在小城镇污水处理率较低,各地区发展不平衡等方面。因此对小城镇的污水处理厂的升级改造势在必行。根据小城镇工业污水的特征及处理要求,提出了几种易于在小城镇推广的经济、高效、节能和简便易行的污水处理改造工艺。针对江阴市小城镇污水集中处理水质特点及工艺的进行研究,根据新的排放标准,提出与改造相应的技术组合思考,达到进一步改善小城镇污水处理效率的目的。