A straightforward synthesis in aqueous medium of enantiomerically enriched S(-)2,2′-dihydroxy-1,1′-binaphthyl

Chiral, atropisomeric 2,2'-dihydroxy-1,1'-binaphthyl has been extensively used to direct asymmetric processes. Its key role in asymmetric catalysis has spurred efforts to synthesize it in the optically pure form, but the reported synthetic routes have a significant environmental impact. In an aqueous peroxydase-cyclodextrin system the oxidative coupling of 2-naphthol took place very rapidly in almost quantitative yield and resulted in an enantiomeric excess. This one-pot synthesis do not require any organic solvents and oxidising metal cations.     

曝气生物滤池去除有机物与反应常数及膜厚的关系

推导了BAF前置反硝化工艺简化动力学模型,揭示了BAF去除有机物与反应速率常数与膜厚的关系。同时以生物膜中活性物质与非活性物质增长生物数学模型体系为基础,从理论上推导了BAF最佳膜厚的范围。     

利用水泥处理垃圾渗滤液生物处理出水的研究

利用水泥的表面吸附和水化反应性质处理垃圾渗滤液生物处理出水可以取得很好的效果,COD的去除率可达69.5%.处理效果与水灰比、反应时间密切相关,低水灰比和较长反应时间对COD的去除更为有利.对处理前后水样的COD和TOC分析表明,水泥对非TOC贡献的COD有很强的去除效果.     

生物膜与A／O工艺耦合快速降解氨氮

应用由城市污水处理厂序批式间歇反应器（SBR）中筛选得到的4株特殊氨氧化菌，分别在SBR和有回流的生物膜与A／O工艺耦合体系培养中，考察其降解低碳高氨氮废水的功能。结果表明，自养硝化与异养氨氧化菌的混合菌群较单一自养硝化菌株降解氨氮速率快；在生物膜与A／O工艺耦合系统中，自养硝化与异养氨氧化菌协同代谢加速氨氮氧化脱除，氨氮脱除速率远比SBR系统快。对生物膜与A／O工艺耦合系统中氨氮脱除动力学进行了研究，模拟了NH4^＋、NO2^-；质量浓度与氨氮脱除比速率之间的关系，模型得到了较好的验证。     

用呼吸速率控制SBR反应时问的基础研究

以人工配水为对象，研究了SBR工艺反应过程中呼吸速率的变化规律，探讨了用呼吸速率控制SBR反应时间长度的可行性，结果证明，呼吸速率在SBR反应过程中有明显特征变化可以作为SBR反应结束的标志。把呼吸速率与其他物理变量结合起来可以更加有效地控制SBR，提高其运行效率。     

Modelling biodegradation of hydrocarbons in aquifers: when is the use of the instantaneous reaction approximation justified?

In-situ bio-remediation is a viable cleanup alternative for aquifers contaminated by hydrocarbons such as BTEX. Transport models of varying complexity and capabilities are used to quantify their degradation. A model that has gained wide acceptance in applications is BIOPLUME II, which assumes that oxygen-limited biodegradation takes place as an instantaneous reaction. In this work we have employed theoretical analysis, using non-dimensional variables, and numerical modelling to establish a quantitative criterion demarcating the range of validity of the instantaneous reaction approximation against biodegradation kinetics. Oxygen was the limiting species and sorption was ignored. This criterion relates (o), the Dahmk?hler number at oxygen depletion, to O(o)*, the ratio of initial to input oxygen concentration, (o) > or = 0.7(O(o)*)(2) + 0.1O(o)* + 1.8. The derived (o) reflects the intrinsic characteristics of the physical transport and of the biochemical reaction, including the effect of biomass density. Relative availability of oxygen and hydrocarbons exerts a small influence on results. Theory, verified and refined via numerical simulations, showed that significant deviations of instantaneous reactions from kinetics are to be expected in the space-time region s相似文献   

染色残液电化学处理碳素阴极材料性能比较

为实现染色残液的高效处理及废水回用,鉴于染色残液良好的导电性,选用电化学处理技术,以模拟活性红X-3B染色残液为研究对象,在钌铱形稳电极为阳极和合适的电解条件下,比较石墨板、石墨毡、炭毡、ACF（活性炭纤维毡）、碳纤维电极〔CFF（碳纤维布）、CFB（碳纤维刷）〕等碳素阴极材料的电化学处理效能.结果表明:碳素阴极材料可实现染色残液的完全脱色,活性红X-3B的降解过程符合一级反应动力学特征,其中CFF为阴极时COD_Cr去除率达到86.37%,一级动力学反应常数为0.010 3 min-1,是石墨毡（0.007 3 min-1）的1.4倍.相比于石墨板电极,CFB显示出优异的二电子氧还原和产H₂O₂能力,单位面积产H₂O₂的浓度为10.40 μmol/L,是石墨板（1.08 μmol/L）的9.7倍,产生的H₂O₂导致活性红X-3B的降解,30 min内实现完全脱色.循环伏安曲线表明,碳纤维电极（包括CFF和CFB）的析氧电位明显高于其他电极,可有效抑制析氧副反应,提高有机污染物降解过程中的电催化效率,有利于降低能耗.研究显示,碳纤维可作为阴极材料应用于电化学处理染色残液,具有良好的稳定性.      

Insights into the formation of secondary organic carbon in the summertime in urban Shanghai

To investigate formation mechanisms of secondary organic carbon(SOC) in Eastern China,measurements were conducted in an urban site in Shanghai in the summer of 2015. A period of high O_3 concentrations(daily peak 120 ppb) was observed, during which daily maximum SOC concentrations exceeding 9.0 μg/(C·m~3). Diurnal variations of SOC concentration and SOC/organic carbon(OC) ratio exhibited both daytime and nighttime peaks. The SOC concentrations correlated well with O_x(= O_3+ NO_2) and relative humidity in the daytime and nighttime, respectively, suggesting that secondary organic aerosol formation in Shanghai is driven by both photochemical production and aqueous phase reactions. Single particle mass spectrometry was used to examine the formation pathways of SOC. Along with the daytime increase of SOC, the number fraction of elemental carbon(EC) particles coated with OC quickly increased from 38.1% to 61.9% in the size range of 250–2000 nm, which was likely due to gas-to-particle partitioning of photochemically generated semi-volatile organic compounds onto EC particles. In the nighttime, particles rich in OC components were highly hygroscopic, and number fraction of these particles correlated well with relative humidity and SOC/OC nocturnal peaks. Meanwhile, as an aqueous-phase SOC tracer, particles that contained oxalate-Fe(III) complex also peaked at night. These observations suggested that aqueous-phase processes had an important contribution to the SOC nighttime formation. The influence of aerosol acidity on SOC formation was studied by both bulk and single particle level measurements, suggesting that the aqueous-phase formation of SOC was enhanced by particle acidity.     

影响大气汞化学过程的敏感因子分析

为了分析汞在大气中的化学行为,在一个化学模式中加入汞的气相、气液平衡和液相反应,模拟大气汞及其化合物的演变规律,并分析了气象因子(云、光解率、温度)和化学因子(气态O3、H2O2、HO2、OH和气态零价汞Hg0(g))的初始体积分数对各形态汞及其化合物浓度和Hg0(g)转化率的影响.模拟结果表明,在中等大气污染条件下,Hg0(g)的每小时平均转化率为2.91%.敏感性试验结果表明,云量、光解率、温度、O3和Hg0(g)的初始体积分数对不同形态汞的影响较为显著.云量的增加、光解率的增加、臭氧初始体积分数的升高,各形态汞的平衡时间缩短,除气态氧化汞和一价汞离子外,其他形态汞的平衡浓度均会降低,Hg0(g)的转化率增加.温度增加将抑制Hg0(g)的转化.Hg0(g)的初始体积分数增加,各形态汞的浓度升高,但其平均转化率没有显著变化.不同因子对汞化学过程的相对作用对区域或全球大气汞的环境模拟具有指导意义.     

Evaluating the e ects of granular and membrane filtrations on chlorine demand in drinking water

In this study, chlorine decay experiments were conducted for the raw water from Nakdong River that is treated by Chilseo Water Treatment Plant (CWTP) situated in Haman, Korea as well as the e uents from sand and granular activated carbon (GAC) filters of CWTP and fitted using a chlorine decay model. The model estimated the fast and slow reacting nitrogenous as well as organic/inorganic compounds that were present in the water. It was found that the chlorine demand due to fast and slow reacting (FRA and SRA) organic/inorganic substances was not reduced significantly by sand as well as GAC filters. However, the treated e uents from those filters contained FRA and SRA that are less reactive and had small reaction rate constants. For the e uents from microfiltration, ultrafiltration, and nanofiltration the chlorine demand because FRA and SRA were further reduced but the reaction rate constants were larger compared to those of sand and GAC filter e uents. This has implications in the formation of disinfection by products (DBPs). If DBPs are assumed to form due to the interactions between chlorine and SRA, then it is possible that the DBP formation potential in the e uents from membrane filtrations could be higher than that in the e uents from granular media filters.