Fe-Ni-TiO2/AC粒子电极的制备及可见光光电催化协同降解RhB

制备Fe-Ni-TiO2/AC粒子电极,应用于可见光助三维电极/电Fenton(Vis-3D/EF)光电催化体系中,以RhB为目标污染物,研究了可见光光电催化对RhB的协同降解.实验优化了Fe-Ni-TiO2/AC粒子电极的制备条件,并与活性炭粒子电极、活性炭负载TiO2粒子电极在Vis-3D/EF体系中的光电催化性能进行对比,结果表明:TiO2浸渍液浓度为2g/L,Fe-Ni掺杂比为5:5,Fe:Ni:TiO2物质的量比为0.5:0.5:100的条件下制备的粒子电极在Vis-3D/EF体系中表现出最优的光电催化性能,60min对RhB的去除率达92.58%,优于活性炭粒子电极和活性炭负载TiO2粒子电极.自制粒子电极在Vis-3D/EF体系比在3D/EF体系对RhB的去除率提高29.46%,表现出明显的光催化和三维电极/电Fenton协同处理效果,协同指数为1.18,说明了自制粒子电极应用在Vis-3D/EF组合技术中,实现对RhB的可见光光电协同降解是可行的.     

超高效液相色谱-串联质谱法测定污水中14种有机磷酸酯阻燃剂

建立了超高效液相色谱-串联质谱(UPLC-MS/MS)联用法同时测定污水中14种有机磷酸酯阻燃剂(OPEs)的分析方法.样品采集后,经GF/C膜过滤,HLB固相萃取小柱净化后进样分析.以BEH C18色谱柱为分离柱,乙腈和水混合液为流动相(0.2 mL min-1)梯度洗脱,15 min内可完成14种OPEs的分离.在电喷雾正离子模式下,采用多反应监测模式(MRM)进行质谱测定.在加标浓度为1.0μg·L-1时,14种OPEs在污水处理厂进水和出水中的回收率分别为52.1%—119%、43.6%—114%,相对标准偏差(RSD)分别为1.2%—16.2%、0.4%—9.2%,方法的检出限(LOD)在0.3—6.0 ng·L-1间.方法精密度好,准确度高,可满足同时对污水样品中的14种OPEs进行定性及定量分析的要求.     

利用蚀刻废液生产碱式氯化铜过程中二英类污染物的去除

针对蚀刻废液及其回收后生产的碱式氯化铜产品中二英(PCDD/Fs)和二英类多氯联苯(dl-PCBs)进行了分析研究,并比较了采用去除工艺前后两类污染物含量水平的变化特征.利用高分辨气相色谱/高分辨质谱对样品中PCDD/Fs和dl-PCBs进行分析,结果表明,氯化铜废液中PCDD/Fs和dl-PCBs的平均总浓度分别为264、139 pg·mL-1,而铜氨液中浓度分别为0.09、0.50 pg·mL-1;碱式氯化铜产品中浓度分别为106 pg·g-1(2.79 pg WHO-TEQ2005·g-1)和27.8 pg·g-1(0.69 pg WHO-TEQ2005·g-1);而经过吸附和过滤等去除工艺后,产品中PCDD/Fs和dl-PCBs的TEQ浓度水平分别降低至0.10—0.25 pg WHO-TEQ2005·g-1和0.05—0.72 pg WHO-TEQ2005·g-1,满足欧盟对于矿物源性饲料添加剂中PCDD/Fs和dl-PCBs的限量标准要求.研究表明该工艺能够有效去除利用蚀刻废液生产碱式氯化铜过程中的二英类污染物.     

典型电子垃圾拆解区二噁英污染特征、相分配及暴露风险

选取南方某典型电子垃圾拆解区不同作业区为研究对象,重点研究了拆解地大气中二噁英的污染特征、气相-颗粒相分配及呼吸暴露风险。通过对5个采样点（包括1个背景点）的研究发现,电子垃圾拆解作业区颗粒相ΣPCDD/Fs的质量浓度为：20.64-56.14 pg·m^-3,毒性当量为：I-TEQ 0.293-1.490 pg·m^-3;气相ΣPCDD/Fs的质量浓度为：3.861-19.29 pg·m^-3,毒性当量为：I-TEQ 0.384-2.150 pg·m^-3。背景点大气中二噁英浓度相对较低,颗粒相和气相样品中质量浓度值分别为：3.734 pg·m^-3和2.637 pg·m^-3,毒性当量仅为I-TEQ 0.176-0.267 pg·m^-3;要明显低于电子垃圾拆解区。基于污染物气相-颗粒相分配系数与蒸汽压的关系对二噁英的气-固分配行为研究显示,除了拆解混合作业区有较好的分配系数（-0.64）外,其它监测点位二噁英的气-固平衡状态较弱（-0.27--0.03）,更多的是以低分子量的单体化合物赋存于气相样品中。对拆解区二噁英呼吸暴露风险研究结果表明,儿童呼吸暴露风险要高于成年人;同时无论是儿童还是成年人,其二噁英的呼吸暴露量均要高于国内外城市报道的二噁英人体呼吸暴露量,说明本次监测的电子垃圾拆解区存在的潜在健康风险不容忽视。     

Investigation on sampling artifacts of particle associated PAHs using ozone denuder systems

Polycyclic aromatic hydrocarbons （PAHs） are complex organic compounds which are identified as significant carcinogenic to human health. PAHs （mainly in particle phase） are susceptible to atmospheric oxidant gases, especially ozone, nitrogen oxides （NOx）, hydroxyl radical （OH）, and could be degraded on filters during sampling process, leading to an underestimation of ambient PAH concentrations. The goal of this work was to investigate particle associated PAHs sampling artifacts caused by ozone in summer of Beijing. Comparative sampling systems were operated simultaneously during the whole campaign, one with activated carbon ozone denuder, the other being set as conventional sampling system. Activated carbon denuder was testified to be highly efficient to eliminate ozone from air stream. In general, nine particle-bound PAHs observed from conventional sampler were all lower than those from ozone denuder system. The total PAHs （particle phase） concentration was averagely underestimated by 35.9% in conventional sampling procedure. Benzo[a]pyrene （BaP） had the highest percentage of mass loss. founded to have influences Ambient temperature was on PAHs sampling artifacts. High temperature can increase loss of particle associated PAHs during sampling.     

Limiting explosible concentration of hydrogen–oxygen–helium mixtures related to the practical operational case

This paper presents data on the limiting (minimum) concentrations of hydrogen in oxygen, in the presence of added helium, at elevated temperature and pressure related to the practical operational case. A 5 L explosion vessel, an ignition sub-system and a transient pressure measurement sub-system were used. Through a series of experiments carried out using this system, the limiting concentrations of hydrogen in oxygen and helium at different initial pressures and temperatures for the practical operational case were studied, and the influence of ignition energy and initial temperature on the limiting concentration of hydrogen in oxygen and helium was analyzed and discussed. The variation of ignition energy within the studied range is found to have a significant effect on the limiting concentration of hydrogen in oxygen and helium at lower initial temperature. However, when the ignition energy is higher than 32 mJ, the limiting hydrogen concentration remains almost changeless as the initial temperature increases from 21 °C to 90 °C. The limiting explosible concentration of hydrogen–oxygen–helium mixture decreases as the ignition energy increases when the initial temperature is lower. When the initial temperature is higher, the ignition energy has little effect on the limiting hydrogen concentration of hydrogen–oxygen–helium mixtures. When the initial temperature reaches 90 °C, the limiting hydrogen concentration remains almost changeless with an increase in ignition energy. The limiting explosible concentration of hydrogen in the mixtures, at the initial temperature of 21 °C and the ignition energy of 0.5 mJ, is 8.5% and that of oxygen is 11.25%.     

Dynamic behavior of direct spring loaded pressure relief valves in gas service: Model development,measurements and instability mechanisms

A synthesis of previous literature is used to derive a model of an in-service direct-spring pressure relief valve. The model couples low-order rigid body mechanics for the valve to one-dimensional gas dynamics within the pipe. Detailed laboratory experiments are also presented for three different commercially available values, for varying mass flow rates and length of inlet pipe. In each case, violent oscillation is found to occur beyond a critical pipe length, which may be triggered either on valve opening or closing. The test results compare favorably to the simulations using the model. In particular, the model reveals that the mechanism of instability is a Hopf bifurcation (flutter instability) involving the fundamental, quarter-wave pipe mode. Furthermore, the concept of the effective area of the valve as a function of valve lift is shown to be useful in explaining sudden jumps observed in the test data. It is argued that these instabilities are not alleviated by the 3% inlet line loss criterion that has recently been proposed as an industry standard.     

Optimization of HSE in maintenance activities by integration of continuous improvement cycle and fuzzy multivariate approach: A gas refinery

Gas refineries have been continuously focusing on Health, Safety and Environment programs to improve maintenance activities. Several researches have studied on this area with different analysis methods. This study presents an integrated approach for optimization of factors contributing to the implementation of Health, Safety and Environment (HSE) in maintenance activities. HSE managers in each sector answered standard questionnaire whit respect to HES. The methodology is based on fuzzy data envelopment analysis (FDEA) and Deming's continuous improvement cycle. Also, this method is used to rank the relevant performance efficiencies in certain and uncertain conditions of each HSE sectors whit considering HSE in maintenance activities. It corresponds and integrates its registered HSE-MS with OHSAS 18001:2007 and ISO 14001:2004 to evaluate multiple inputs and outputs of over 36 subsidiary HSE divisions with parallel mission and objectives simultaneously. Also, it determines efficient target indices and could assure continuous improvement in the organization. This is the first study that introduces an integrated approach to improve HSE management programs in a gas refinery by a robust and continuous improvement approach.     

Thermodynamic investigation and hydrate inhibition of real gas flow through orifice during depressurization

A thermodynamic procedure has been proposed which can be used to predict the gas pressure, temperature and flow rate through orifice upon chock flow condition, using equation of state (EOS). The procedure applied for emergency depressurization operation incorporating the Peng-Robinson EOS and validated by comparing flow rates of a multi-component hydrocarbon gas mixture for thirteen experimental cases. The average absolute deviations of the predicted flow rates for orifice discharge coefficients of 0.85 and 0.9, are 7.36% and 2.03%, respectively. The corresponding error for API 520 (American Petroleum Institute Recommendation Practice 520) method is 6.91%. In this work, the hydrate formation temperature and hydrate inhibitor type and its required weight fraction for preventing the hydrate formation upon orifice and its upstream conditions are evaluated by the EZ-Thermo software using the Moshfeghian–Maddox method. The results qualitatively show that the hydrate prevention is essential for the safety of the operation due to low temperature condition.     

A/O脱氮工艺实时控制对策的试验研究

以人工合成废水为研究对象,系统研究了提高A/O(anoxic/oxic)工艺氨氮和硝酸氮去除效率的实时控制对策.氨氮控制的本质是通过控制DO设定值和好氧区体积大小使出水氨氮浓度达标排放.硝酸氮控制的本质在于高效利用缺氧区反硝化潜力,为此建立了以调节内循环回流量或(和)外碳源投加量维持缺氧区末端硝酸氮浓度处于设定值的实时控制对策.系统控制采用两级结构,高水平监控层用来选择低水平执行层的设定值,而低水平执行层对DO值、好氧区体积、内循环回流量和外碳源投加量进行直接控制,试验表明上述控制对策可以显著提高系统脱氮效率,降低出水氨氮和硝酸氮浓度,并最大程度节约运行费用.