Measurement of the pesticide methomyl by modified quartz crystal nanobalance with molecularly imprinted polymer

A simple and cost-effective analysis method based on quartz crystal nanobalance (QCN) coated with a molecularly imprinted polymer (MIP) for measurement of methomyl was investigated. In the first part of this study, a sensitive, selective and reliable quartz crystal nanobalance (QCN) sensor was designed for the selective determination of methomyl in aqueous solutions. In the second part, in order to demonstrate the applicability and performance of the fabricated sensor in the real world situation, it was successfully applied for the determination of methomyl residual in photo catalytic degradation by ZnO powders in aqueous solutions. The fabricated sensor presents a high selectivity and sensitivity (4.56 Hz per mg L^?1) for methomyl and it can be used for determination of methomyl concentration ranged between 1 to 45 mg L^?1. Furthermore, good reproducibility, R.S.D. = 2.14% (n = 5) was observed. To investigate the performance of the sensor, the change in the insecticide concentration during the photocatalytic degradation of methomyl by ZnO was investigated by QCN and UV/Vis spectroscopy. Results obtained from QCN sensor and UV/Vis spectroscopy measurement are in good mutual agreement. So the fabricated sensor may provide an efficient, low cost, easy-to-use method for the in-field evaluation of specific targeted analytes in aqueous solutions which in turn may lead to improved food and water safety.     

不同CDPF贵金属负载量对柴油公交车VOCs组分排放影响

基于重型底盘测功机,利用质子转移反应质谱(PTR-MS)研究了柴油公交车在中国典型城市公交车循环(CCBC)下,不同CDPF贵金属负载量对尾气中挥发性有机物(VOCs)组分排放特性的影响.结果表明,柴油公交车VOCs主要组分为含氧有机物(OVOCs)、芳香烃和烯烃等,且OVOCs占比达50%以上;在贵金属成分、配比相同时,VOCs减排率随CDPF贵金属负载量增加而增加:贵金属负载量为15 g·ft~(-3)(A型后处理装置)、25 g·ft~(-3)(B型)和35 g·ft~(-3)(C型)时,VOCs总量的减排率依次为36.2%、40.1%和41.4%.C型后处理装置对烷烃全循环减排率高达70.2%,且对OVOCs的催化有微弱优势;对于不饱和烃类,3种不同贵金属负载量的后处理装置均有一定催化效果,但无明显差异;A型对含氮有机物减排率可达50.5%,但减排率随贵金属负载量增加而降低.采用DOC+CDPF后能较好地降低公交车VOCs排放量进而降低臭氧生成潜势(OFP).同时考虑不同方案减排效果与成本因素,当加权系数分别为0.8和0.2时,B型为最优方案.     

容积负荷对ABR-MBR工艺反硝化除磷性能的影响

采用连续流ABR-MBR组合工艺处理生活污水,研究不同容积负荷(volume loading rate,VLR)对该工艺反硝化除磷性能的影响,获得最佳工艺参数.试验考察ABR进水容积负荷(以COD计,下同)分别为0.76、1.01、1.51和2.27 kg·(m~3·d)~(-1)时系统去碳脱氮除磷的性能,并在各ABR容积负荷条件下考察MBR容积负荷对MBR反应器硝化性能的影响.结果表明,在ABR进水容积负荷为1.51 kg·(m~3·d)~(-1)的条件下,系统A2隔室COD去除量最大,并在MBR容积负荷为0.462 kg·(m~3·d)~(-1)时,MBR反应器中实现了短程硝化,系统NH_4~+-N和TN去除率分别达到90%和72%以上,厌氧释磷量为7.41 mg·L~(-1),缺氧吸磷量达到15.42 mg·L~(-1),出水PO_4~(3-)-P浓度低于0.5 mg·L~(-1),这表明短程硝化更有利于强化ABR-MBR系统的反硝化除磷性能.     

山东省临沂市土壤有机氯农药滴滴涕残留量与空间分布特征

通过对临沂市全区表层土壤每36 km2进行样品收集,测试分析了DDTs、Org C、N等指标,主要研究了区域表层土壤DDTs的残留现状、组成和来源、影响因素、空间分布和环境质量特征.结果表明,调查区表层土壤中DDTs检出率为71.75%,平均含量为0.035μg·g-1;检出样品中p,p'-DDT和p,p'-DDE为主要残留物,平均残留分别为0.033μg·g-1和0.010μg·g-1,分别占检出样的60.99%和34.62%.DDTs降解率指示区域58%表层土壤为新近输入区,新近输入区在调查区中南部分布尤为明显;而p,p'-DDD/p,p'-DDE指示区域DDTs降解以氧化环境为主,o,p'-DDT/p,p'-DDT指示71.37%区域土壤DDTs输入可能与工业级DDTs有关.相关分析表明,影响土壤DDTs分布的外在因素包括土壤Org C、N、C和p H等指标,且DDTs中p,p'-DDT组分占比越高,影响越明显.DDTs的空间分布具明显点源特征,市县周围均出现明显浓集中心,中南部部分区域浓度明显较高.全区DDTs土壤环境质量污染程度较低,主要以一二类土壤为主,分别占78.95%和21.05%.     

微生物燃料电池改性阳极处理PTA废水

探讨了不同改性阳极对微生物燃料电池(microbial fuel cell,MFC)产电性能及其对MFC处理难降解废水能力的影响.以单室空气阴极为基础,利用0.1 g电气石、质量分数75%二氧化锰/埃洛石纳米管(manganese bioxide/halloysite nanotube,MnO_2/HNT)和多壁碳纳米管-羧基(multi-walled carbon nanotube-carboxyl,MWCNT-COOH)对MFC阳极进行修饰.结果表明,不同改性阳极的MFC对含精对苯二甲酸(purified terephthalic acid,PTA)废水的去除率均高于70%,且化学需氧量(chemical oxygen demand,COD)去除率在79%以上.相较于其他几种改性阳极,以MWCNT-COOH改性材料作阳极的MFC产生的最大输出电压最高,获得的最大功率密度最高,分别为529 mV和252.73 mW·m~(-2).     

重庆市夏秋季VOCs对臭氧和二次有机气溶胶生成潜势的估算

为估算重庆市夏秋季VOCs（挥发性有机物）对O₃和SOA（二次有机气溶胶）的生成潜势,利用在线GC-MS/FID在2015年8月22日-9月23日对重庆市区点和郊区点VOCs开展了为期一个月的实时观测,获得市区点和郊区点$ \varphi $（TVOCs）（总挥发性有机物）分别为41.35×10-9和22.72×10-9,其中市区点以烷烃（35.2%）和烯炔烃（25.2%）为主,郊区点以含氧挥发性有机物（oxygenated volatile organic compounds,OVOCs）（30.6%）和烷烃（26.0%）为主.结合最大增量反应活性量化市区点和郊区点VOCs的OFPs（臭氧生成潜势）分别为149.11×10-9和71.09×10-9,市区点OFPs最大的是乙烯、丙烯、甲苯、C8和C9的芳香烃等,郊区点OFPs最大的VOCs是丙烯醛、异戊二烯和甲基乙烯基酮.结合气溶胶生成系数量化郊区点和市区点VOCs对SOA的生成贡献分别为0.36和1.26 μg/m3,相比国内其余城市VOCs的SOAP（二次有机气溶胶生成潜势）较小,主要以甲基环己烷、正壬烷、正葵烷和十一烷等高碳烷烃,以及甲苯、苯、二甲苯和乙苯等芳香烃的SOAP为主.研究显示,控制烯炔烃和芳香烃的浓度有助于控制重庆市O₃的生成,控制高碳烷烃和芳香烃则有助于控制重庆市SOA的生成.      

Control of aliphatic halogenated DBP precursors with multiple drinking water treatment processes: Formation potential and integrated toxicity

The comprehensive control efficiency for the formation potentials(FPs) of a range of regulated and unregulated halogenated disinfection by-products(DBPs)(including carbonaceous DBPs(C-DBPs), nitrogenous DBPs(N-DBPs), and iodinated DBPs(I-DBPs)) with the multiple drinking water treatment processes, including pre-ozonation, conventional treatment(coagulation–sedimentation, pre-sand filtration), ozone-biological activated carbon(O_3-BAC) advanced treatment, and post-sand filtration, was investigated. The potential toxic risks of DBPs by combing their FPs and toxicity values were also evaluated.The results showed that the multiple drinking water treatment processes had superior performance in removing organic/inorganic precursors and reducing the formation of a range of halogenated DBPs. Therein, ozonation significantly removed bromide and iodide,and thus reduced the formation of brominated and iodinated DBPs. The removal of organic carbon and nitrogen precursors by the conventional treatment processes was substantially improved by O_3-BAC advanced treatment, and thus prevented the formation of chlorinated C-DBPs and N-DBPs. However, BAC filtration leads to the increased formation of brominated C-DBPs and N-DBPs due to the increase of bromide/DOC and bromide/DON.After the whole multiple treatment processes, the rank order for integrated toxic risk values caused by these halogenated DBPs was haloacetonitriles(HANs)》haloacetamides(HAMs) haloacetic acids(HAAs) trihalomethanes(THMs) halonitromethanes(HNMs) 》I-DBPs(I-HAMs and I-THMs). I-DBPs failed to cause high integrated toxic risk because of their very low FPs. The significant higher integrated toxic risk value caused by HANs than other halogenated DBPs cannot be ignored.     

焙烧温度对CeO_2(ZrO_2)/TiO_2选择性催化脱硝性能的影响

采用溶胶-凝胶法并以不同温度焙烧制备一系列CeO_2(ZrO_2)/TiO_2(CZT)催化剂,考察了CZT催化剂固相结构、酸量、比表面积等性能与催化活性的关系。采用XRD、BET、NH3-TPD、H2-TPR以及XPS等表征技术对催化剂进行表征。结果表明:焙烧温度为450℃时CZT催化剂具有最高的催化活性,其在240~400℃的温度窗口内活性均高于90%,且具有较好的抗水和抗硫中毒能力。随着焙烧温度的提高,催化剂表面的Ce和Zr原子进入体相晶格且Ce0.5Zr0.5O2向Ce0.75Zr0.25O2转变,导致催化剂的储释氧能力和氧化还原性能降低。另外,锐钛矿和金红石型TiO_2晶粒尺寸的增加,催化剂的有效比表面积和总酸量降低,因此CZT催化活性随着焙烧温度的提高而有所降低。换言之,大的比表面积、良好的氧化还原性能、表面Ce4+的富集以及酸性位的增多均有利于NH3-SCR活性的提高。     

Effects of sludge retention time, carbon and initial biomass concentrations on selection process: From activated sludge to polyhydroxyalkanoate accumulating cultures

Four sequence batch reactors (SBRs) fed by fermented sugar cane wastewater were continuously operated under the aerobic dynamic feeding (ADF) mode with different configurations of sludge retention time (SRT), carbon and initial biomass concentrations to enrich polyhydroxyalkanoate (PHA) accumulating mixed microbial cultures (MMCs) from municipal activated sludge. The stability of SBRs was investigated besides the enrichment performance. The microbial community structures of the enriched MMCs were analyzed using terminal restriction fragment length polymorphism (T-RFLP). The optimum operating conditions for the enrichment process were: SRT of 5 days, carbon concentration of 2.52 g COD/L and initial biomass concentration of 3.65 g/L. The best enrichment performance in terms of both operating stability and PHA storage ability of enriched cultures (with the maximum PHA content and PHA storage yield (Y_PHA/S) of 61.26% and 0.68 mg COD/mg COD, respectively) was achieved under this condition. Effects of the SRT, carbon concentration and initial biomass concentration on the PHA accumulating MMCs selection process were discussed respectively. A new model including the segmentation of the enrichment process and the effects of SRT on each phase was proposed.     

工业园区综合难降解废水深度处理实验研究

某工业园区综合废水处理厂设计规模5.0×104m3/d,原设计出水执行《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准,需将出水标准提高到一级A排放标准.分别采用混凝沉淀法和高级氧化法深度处理二级生化出水.小试试验结果表明:二级生化出水CODcr在62~75 mg/L左右,PAC、Al2(SO4)3及PFS三种絮凝沉淀药剂处理出水CODcr去除效果均不明显,不能稳定达到一级A排放标准.芬顿催化氧化的pH=5,FeSO4+H2O2投加量为(200+100)mg/L;臭氧氧化的O3投加量33 mg/L,其出水CODcr均能达到一级A排放标准.