Volatilization characteristics of organic solutes in stirred solution

The effects of turbulence intensity (velocity gradient, G (s⁻¹)), Henry's law constant (H), and molecular weight (M) on the volatilization rates of organic compounds are examined using changes in the mass transfer coefficients (K_OL (cm/min)) under specific liquid-mixing intensities. The selected compounds were divided into three groups according to their H values (mole in gas/mole in liquid, dimensionless), which ranged from 10² to 10⁻⁵. The relationship of the K_OL relative to G, H and M was obtained via multiple regression. The obtained values of these parameters indicate that the primary factor affecting the K_OL values of the high H compounds is their M values. The effects of the H values on the K_OL values of the high H compounds can be neglected. On the other hand, the H value is the major factor determining the K_OL values of the low H compounds. The changes in the K_OL values of the different H compounds exhibit different profiles as the liquid-mixing intensity increases. The M and H values of middle H compounds possibly affect their K_OL values. The effects of the liquid-mixing intensity on the K_OL values of the organic compounds increase with increasing H values. The variation in the K_OL values might be a result of the concentration of the organic compounds at the interface between the liquid and gas films. The empirical relationship between K_OL and some selected parameters, G, H and M, is examined in this study. The obtained results can help to estimate volatilization loss of organic solutes in wastewater treatment facilities.     

Influence of organic loading on an anaerobic sequencing biofilm batch reactor (ASBBR) as a function of cycle period and wastewater concentration

The effect of organic loading on the performance of a mechanically stirred anaerobic sequencing biofilm batch reactor (ASBBR) has been investigated, by varying influent concentration and cycle period. For microbial immobilization 1-cm polyurethane foam cubes were used. An agitation rate of 500 rpm and temperature of 30+/-2 degrees C were employed. Organic loading rates (OLR) of 1.5-6.0gCODl(-1)d(-1) were applied to the 6.3-l reactor treating 2.0 l synthetic wastewater in 8 and 12-h batches and at concentrations of 500-2000mgCODl(-1), making it possible to analyze the effect of these two operation variables for the same organic loading range. Microbial immobilization on inert support maintained approximately 60 gTVS in the reactor. Filtered sample organic COD removal efficiencies ranged from 73 to 88% for organic loading up to 5.4gCODl(-1)d(-1). For higher organic loading (influent concentration of 2000mgCODl(-1) and 8-h cycle) the system presented total volatile acids accumulation, which reduced organics removal efficiency down to 55%. In this way, ASBBR with immobilized biomass was shown to be efficient for organic removal at organic loading rates of up to 5.4gCODl(-1)d(-1) and to be more stable to organic loading variations for 12-h cycles. This reactor might be an alternative to intermittent systems as it possesses greater operational flexibility. It might also be an alternative to batch systems suspended with microorganisms since it eliminates both the uncertainties regarding granulation and the time necessary for biomass sedimentation, hence reducing the total cycle period.     

有机废气治理技术的研究进展

有机废气治理问题是当前废气处理的难点问题之一。本文首先介绍了几类传统有机废气处理技术的发展现状,包括吸附法、吸收法、催化氧化法、生物处理法等。对这几类有机废气治理技术的应用机理、适用范围以及现存问题进行了综合地比较与分析。最后,对于近年来出现的几类新型有机废气处理技术,如膜分离法、光催化氧化法、综合处理法的发展前景进行了一定的展望并列举了几类新技术的工程应用实例。     

Production costs and operative margins in electric energy generation from biogas. Full-scale case studies in Italy

The purpose of this study was to observe the economic sustainability of three different biogas full scale plants, fed with different organic matrices: energy crops (EC), manure, agro-industrial (Plants B and C) and organic fraction of municipal solid waste (OFMSW) (Plant A). The plants were observed for one year and total annual biomass feeding, biomass composition and biomass cost (€ Mg^?1), initial investment cost and plant electric power production were registered. The unit costs of biogas and electric energy (€ Sm^?3_biogas, € kW h^?1_EE) were differently distributed, depending on the type of feed and plant. Plant A showed high management/maintenance cost for OFMSW treatment (0.155 € Sm^?3_biogas, 45% of total cost), Plant B suffered high cost for EC supply (0.130 € Sm^?3_biogas, 49% of total cost) and Plant C showed higher impact on the total costs because of the depreciation charge (0.146 € Sm^?3_biogas, 41% of total costs). The breakeven point for the tariff of electric energy, calculated for the different cases, resulted in the range 120–170 € MW h^?1_EE, depending on fed materials and plant scale. EC had great impact on biomass supply costs and should be reduced, in favor of organic waste and residues; plant scale still heavily influences the production costs. The EU States should drive incentives in dependence of these factors, to further develop this still promising sector.     

废钻井液污染分析及处理方法的探讨

为解决废钻井液对周围环境的污染,介绍了废钻井液的成分及对环境的影响,分析了国内外废钻井液处理方法的优缺点,详细阐述了中原油田结合本单位情况,用无害化处理技术处理废钻井液的方法和效果。试验表明：无害化处理剂中的各组分与废钻井液中各污染因子发生化学和物理作用,经３～５个月固化后可以达到无害化处理的目的。分析认为：中原油田钻井废弃物无害化处理技术是切实可行的。     

Mixing hazard evaluation of organic peroxides with other chemicals

Organic peroxides (POs) have been widely used in chemical industries as initiators of polymerization, hardening or bridge formation agents, and they are known for its self-reactive and also mixing hazard characteristics when mixed with other chemicals such as acids and alkalis. It is the purpose of this investigation to propose a simple but useful evaluation flow of mixing hazards of POs with other chemicals using conventional experimental techniques such as a glass test tube test, Dewar vessel test and DSC is proposed. 7 kinds of POs (DEPD, THP, TBEH, TBTC, MEKPO, DTBP, THHP) were mixed with sulfuric acids with various concentration, sodium hydroxide solutions, -iron(III) oxide and acrylonitrile (AN).

Based on the proposed evaluation flow the testing results were classified into 4 ranks due to the hazard criteria. Futhermore DEPD/acrylonitrile mixtures were investigated in more detail and the influences of the mixing ratio and the stirring speed were discussed.     

重点产业源增长对北部湾地区气态污染物模拟的影响

根据污染源普查资料制作北部湾地区2007年人为排放源清单,以及中期/远期参比情景(REF15/REF20)和远期调控情景(SCEi20)下的排放源清单.采用WRF-Chem模拟北部湾地区空气质量现状及未来变化.2007年SO2和NO2月平均质量浓度模拟值与监测值比较吻合.广东、广西(海南)地区污染物质量浓度较高(低).跨界污染特征表明污染物质量浓度受局地排放源的影响较大,外来排放源的贡献较小,广东对广西和海南地区的影响相对较大.未来情景下污染物质量浓度的变化主要受排放源变化的影响.REF15情景下茂名市SO2排放源减小导致SO2预测浓度降低,其它城市由于排放源增大,SO2和NO2的预测浓度均升高,O3由于化学反应比较复杂,因此不同城市质量浓度既有升高也有降低.REF20情景下各城市排放源大幅增加,因此SO2和NO2的预测浓度大幅上升,O3的预测浓度增幅较小.SCEi20情景下SO2、NO2、以及O3预测浓度的增幅略小于REF20情景.     

类二噁英物质及芳香烃受体(AhR)介导的有害结局路径(AOP)研究进展

二噁英及类二噁英物质(dioxin-like compounds,DLCs)是一类高毒性化合物的统称,对其毒理学的研究一直都是备受关注的焦点。已有证据表明,高毒二噁英及DLCs主要通过激活芳香烃受体(aryl hydrocarbon receptor,AhR),进而导致一系列生物毒性。近年来越来越多的新型有机污染物被发现具有类二噁英分子结构并存在潜在生物毒性或活性。与此同时,如何评估二噁英及DLCs对本土生态生物的危害及其风险也受到更多关注。本文综述了近几年发现的新型二噁英物质、二噁英及DLCs的AhR致毒机制、相应的有害结局路径(adverse outcome pathway,AOP)及AOP在指导探索新型物质及物种敏感性方面上的新观点和发现,同时也展望了二噁英及DLCs在生态毒理及风险评估领域的未来研究方向。     

气相色谱法测定变压器油中的多氯联苯

利用固相萃取法提取变压器油中的多氯联苯,采用浓硫酸净化、气相色谱法进行分析,根据峰型和保留时间,以多氯联苯的商业用混合物的形式进行定性、定量,可以定量检出变压器油中2mg/kg以下的多氯联苯。     

Optimization of the recovery of plastics for recycling by density media separation cyclones

Material recovery processes are presented as the optimum option for recycling plastic wastes as a means of recovering hydrocarbon resources. There exist a large variety of automated material recovery processes for recycling of such wastes but each with significant limitations. Of these, the separation based on differences in densities is advocated as the optimum process either for producing recycled products or preparing wastes for subsequent recovery processing.Density separation processes based on cyclone type density media separation (DMS) is presented as an important, potential method for increasing plastics recycling process capacities. It is demonstrated to have the capacity to separate a significantly larger range of particle sizes than those presently processed industrially. The mathematical relationship for the prediction of quality of typical LARCODEMS type density media separations by particle size and density as expressed by the Ecart Probable is presented.A proposed device configuration is presented for density media separation to optimize the recovery and purity of both density fractions produced. It is also suggested that to be economically viable, a large scale of operation is required for industrial plastics recycling operations recovering and producing a number of different plastics with a purity to be used as a substitute for virgin material.