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   

深圳大学城园区典型OVOCs污染特征与来源解析

采用质子转移反应质谱仪（PTR-MS）对深圳大学城园区2017年不同季节（分干湿两季）的6种典型OVOCs和其他非甲烷烃类（NMHCs）进行连续在线监测,分析其干湿季的浓度特征与日变化规律,并应用光化学龄的参数化方法开展OVOCs的来源解析.结果表明,在观测的6种OVOCs中,甲醇的平均浓度最高,达10×10^-9~12×10^-9,其次是乙酸、丙酮和乙醛,约2~5×10^-9,甲酸和丁酮的含量最低,仅1×10^-9~2×10^-9.通过日变化观察到的OVOCs湿季峰值浓度时间明显早于干季,乙醛表现出与臭氧（O₃）相似的日变化特征,揭示了其可能存在二次来源;甲醇和丁酮的峰值浓度时间均早于O₃,可能存在重要的一次排放源.采用光化学龄模型解析出日间污染物来源比例：在污染较重的干季,甲醇、乙醛、丙酮和丁酮的人为一次源占主导,甲酸和乙酸的二次源是主要贡献者;在较清洁的湿季,天然源成为乙醛、丙酮、丁酮、甲酸和乙酸的主要来源.     

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.      

污染场地地下水中汞污染反应运移模拟

汞（Hg）是人们持续关注的全球环境污染物之一,其对地下水的污染严重威胁着与地下水相关的生态环境系统.汞在地下水系统中的物理与地球化学反应过程的准确刻画是研究汞迁移转化规律的重点和难点.基于某工业场地汞污染数据,首先采用PHREEQC研究地下水中无机二价汞的存在形态,然后利用PHT3D程序建立汞污染物反应性溶质运移二维剖面模型.该模型考虑了汞污染物在地下水系统中的对流、弥散过程及地球化学反应过程（包括水相络合作用、表面络合吸附作用及受动力学控制的氧化还原作用）.结果表明,无机二价汞的存在形态以HgCl₂和Hg（OH）Cl占主导地位,氧化还原作用是影响地下水中汞污染反应性运移的主要控制因素;另一方面,水合氧化铁HFO对汞迁移的阻滞影响较小,而溶解性有机质对汞较强的络合作用不能忽视.本文研究成果可为预测与评估特定污染场地地下水汞污染的变化趋势及制定相应的修复策略提供科学依据.     

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.     

基于化学反应动力学的饮用水铝形态分布模型研究

目前饮用水中的总铝超标现象十分严重,其危害与铝的存在形态密切相关.本研究利用三层前反馈式的人工神经网络技术,建立了基于化学反应动力学的铝形态预测模型.结果表明,无机单核铝和溶解铝的浓度变化速率与反应时间及水温、pH、总铝、氟离子、磷酸根和硅酸根等水质参数密切相关,二者的反应级数均为三级.通过人工神经网络可有效地进行饮用水中无机单核铝和溶解铝反应动力学参数的预测;反应速率常数k和初始浓度项1/c02的计算值和模型预测值的相关系数R均大于0.999.由M市管网水铝形态的预测结果可知:当总铝浓度0.05mg·L-1时,模型对无机单核铝浓度的预测误差较大;而当总铝浓度0.05mg·L-1时,模型有较好的预测能力,无机单核铝和溶解铝的相对预测误差分别为±15%和±10%.     

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.     

光助Fenton反应催化剂Fe/Al2O3的制备及其对六氯苯的催化活性研究

采用超声促进浸渍法制备了光助Fenton催化剂Fe/Al2O3,利用该催化剂对六氯苯（HCB）进行光助Fenton氧化降解,考察了浸渍液浓度、浸渍温度、灼烧温度和灼烧时间等制备条件对其催化降解六氯苯的活性的影响,确定了制备Fe/Al2O3的工艺条件,并对制得的催化剂进行表征。结果表明,超声促进浸渍法制备非均相光助Fenton反应催化剂Fe/Al2O3的最佳工艺条件为：浸渍液浓度25mmol/L,浸渍温度40℃,焙烧温度500℃,焙烧时间3h。在此条件下制备的催化剂对六氯苯的降解具有较高的催化活性。     

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.