氨水循环增强电动力学技术去除土壤中的氟

为了探讨氨水增强电动力学技术修复氟污染土壤的效果及对土壤p H值的影响,在自制的电动力学装置中,1V/cm电解电压下,以氨水作电解液,采用连续循环的方式进行研究。结果显示,氨水连续循环不仅增大了修复过程中的电流值,且使通过土壤的电流更加稳定,在提高土壤氟迁移效率的同时降低了能耗。在设定的浓度中(0、0.01、0.1和0.2mol/L),土壤氟的去除率随着氨水浓度的升高而增加,0.2 mol/L氨水具有最大电流值26.8 m A,土壤氟的去除率也达到57.9%,氨水循环增强时两极土壤p H值差异减小。采用氨水循环增强电动力学技术,可有效修复氟污染土壤,土壤中剩余氨还可以提高土壤肥力。     

镉污染胶东棕壤的电动力学修复研究

在Cd污染的胶东棕壤土体两端加以1 V/cm的直流电压梯度进行电动力学修复.考察了电动力学修复过程中阴阳极电解液pH、电渗流量和电流密度的变化,并将处理后的土体分6段进行了分析,主要参数为pH、电导率、土壤中Cd的浓度及其形态分析.结果表明,经过445.0 h的电动力学修复,阳极附近3段土壤中Cd的去除率分别达到98.19%、97.01%和96.24%;阴极附近3段土壤中出现了Cd富集现象,且pH为5.88的土壤段Cd的富集率最高.     

矿化垃圾修复石油污染土壤的影响因素及污染物的去除机制

利用矿化垃圾对石油污染土壤进行修复研究,以期在低成本、易操作、修复效果好的前提下达到以废治废的目的。分别研究了矿化垃圾与石油污染土壤的混合比例、土壤含盐量、含油量和含水率对矿化垃圾修复石油污染土壤的影响,并通过3D-EEM(三维荧光)和GC-MS(气相-质谱)技术分析了体系石油污染物的去除特性。结果表明:矿化垃圾对石油污染土壤具有较好的修复效果,在矿化垃圾与石油污染土壤的混合比例为6:4、土壤不添加盐分、含油量为4%、含水率为30%的条件下,运行94 d后土壤中石油去除率最高可达58.61%;同时,基于3D-EEM分析发现土壤中石油类物质的荧光峰位置在处理前后均出现在Ex/Em=300 nm/330 nm处,其去除率为44.89%,表明矿化垃圾床对三环及其同系物和单环及其同系物的芳烃去除效果较好;另外,基于GC-MS技术分析得出,经矿化垃圾修复后,土壤中石油总去除率为66.57%,除正十八烷去除率(19.84%)较低外,其他烷烃的去除率均高于56.8%。     

微波催化氧化修复技术处理有机氯污染土壤

采用微波催化氧化修复技术处理常州某农药厂有机氯农药污染场地和南通某化工厂有机氯污染场地土壤,考察不同参数条件下实验装置对污染土壤的处理效能。结果表明,在微波功率18kW、微波辐射时间20min、土壤处理量400kg/h、土壤含水率15%、活性炭添加量0.03kg/kg的最佳条件下,实验装置运行稳定,有机氯农药污染土壤中氯丹去除率可达70%左右;有机氯污染土壤中邻二氯苯、石油烃总量、1,2-二氯乙烷、苯酚去除率分别可达到99.98%、91.29%、98.52%、74.74%。研发的污染土壤微波催化氧化修复技术及实验装置对有机氯污染土壤的修复具有一定的普适性。     

石油污染土壤胶体特征及其稳定性

采集辽河油田石油污染土壤样品并用离心法提取胶体,定性和定量研究了石油污染土壤胶体的主要物理化学性质,通过间歇实验研究了不同p H(p H=4~9)、不同价态阳离子(Na+、Ca2+和Fe3+)和不同价态阴离子(NO-3、SO2-4和PO3-4)存在下的胶体稳定性,比较了阳离子存在下石油污染土壤胶体和未受污染土壤胶体稳定性。研究结果表明,该石油污染土壤胶体总石油烃含量为123.24 mg/g,石油烃主要为直链烷烃和环烷烃。相同p H条件下石油污染土壤胶体Zeta电位负值比未受污染土壤胶体Zeta电位负值高。石油污染土壤胶体稳定性随p H值增加而增加,随着阳离子价数升高而减小,随阴离子价数升高而增大。Ca2+和Cu2+存在下,石油污染土壤胶体比未受污染土壤胶体稳定性更小。Na+和Fe3+存在下,石油污染土壤胶体比未受污染土壤胶体稳定性更大。     

活化过硫酸钠原位修复浅层石油烃类污染土壤的模拟研究

以过硫酸钠为氧化剂,硫酸亚铁为活化剂,通过箱体实验,结合农业滴灌技术,原位化学氧化修复浅层石油烃(TPH)污染土壤,考察修复过程中土壤TPH、含水率、电导率、pH的变化情况。结果表明,硫酸亚铁活化过硫酸钠对土壤中TPH具有较好的去除作用,通过40d的原位修复处理,表层土和中层土中的TPH去除率分别达到44.6%、44.1%;修复过程中,表层土含水率、电导率呈先上升后下降的趋势,中层土含水率、电导率则先上升后波动变化,表层土、中层土pH均呈先下降后上升的趋势;土壤TPH与含水率、电导率、pH间均存在相互制约的关系。     

油浸泥土热脱附修复小试实验条件的探索

针对油浸泥土中石油烃去除机制不清的问题,利用自制热解炉小试装置,研究了不同条件下油浸泥土中石油烃的处理效果,通过调节加热温度、时间、初始含油率和初始含水率等参数,模拟油浸泥土热脱附过程。结果表明:利用小试装置,当初始含油率为11.3%、初始含水率为20%时,热脱附温度300°C、热脱附时间4 h为最佳处理工艺,处理后油浸泥土中的含油率可降低至0.7%,远低于《油气田含油污泥综合利用污染控制要求》(DB 65/T 3998-2017)中2%的修复标准,石油烃的去除率可达到93.8%;在常见油浸泥土含水率20%及最佳处理工艺下,随着初始含油率的升高,热脱附处理后的固相含油率逐渐升高,但石油烃去除率基本保持不变。适中的油浸泥土含水率有利于热脱附处理,最佳初始含水率为10%～20%。     

超声波/Fenton处理含酚废水的影响因素

实验研究主要影响因素对超声波/Fenton试剂处理苯酚废水效果的影响,确定工艺参数。以人工配制的模拟苯酚废水为实验水样,通过静态实验研究p H值、Fe SO4·7H2O投加量、H2O2投加量和超声时间对苯酚和COD去除率的影响。研究结果表明,对于苯酚浓度为200 mg/L,COD为476.6 mg/L苯酚废水,在实验用水量为1 000 m L,p H值为6,Fe SO4·7H2O投加量为800 mg/L,H2O2投加量为Qth,超声时间为30 min的条件下,苯酚去除率可达到92.27%,COD去除率可达到82.48%,处理后苯酚浓度为14.80 mg/L,COD为83.50 mg/L。p H值、Fe SO4·7H2O投加量、H2O2投加量和超声时间对超声/Fenton工艺处理苯酚废水均有较显著地影响,工程应用时应给予足够的重视。     

微生物燃料电池修复石油污染盐碱土壤

生物电化学技术修复石油污染土壤并同步产出电能是一种新兴的污染土壤生态修复技术。对石油污染土壤通过其微生物燃料电池的构造,利用电化学阻抗谱分析了土壤的欧姆内阻,拟合估算了土壤的电导率,并考察了土壤微生物燃料电池的产电性能和修复效果。结果表明:采用丙酮清洗过的阳极并有水封的情况下,土壤微生物燃料电池的欧姆内阻下降了52%,电导率升高了1倍;在启动后的120 h内,最大电压和累计产出电量分别达189 m V和36 C,与对照相比分别增加了20和29倍。输出电压随着阴极与阳极之间距离的增大而减小。经过30 d的生物电化学处理,土壤中的总石油烃去除率是开路对照的3.3倍。该研究是石油污染盐碱土壤生物电化学修复的初步探索,以为污染土壤的生态修复提供新的思路。     

生物强化处理石油污染土壤理化性质和微生物学特性的纵向分布特征

采用原位强化生物修复技术对某区块石油污染土壤进行为期16个月的生物修复,考察了处置后污染土壤理化性质、微生物学特性以及石油烃组成的纵向分布特征。实验结果表明,经过修复后各土层的石油烃去除率是表层土IN-3(50.42%)中层土IN-2(23.54%)底层土IN-1(10.51%);IN-1处于缺氧环境,存在硫酸盐还原和反硝化作用,使得土壤pH值从7.86±0.03降低至7.27±0.03,土壤总氮从2.53±0.13 g/kg降低至0.77±0.04 g/kg;厌氧菌的种群数量是IN-1(10.43±0.71×104CFU/g)IN-3(6.74±0.39×104CFU/g)IN-2(5.15±0.42×104CFU/g),放线菌数量与石油烃含量显著负相关(r=-0.989,p=0.0110.05);IN-3对饱和份和芳香份的降解率最高,分别达到了70.27%和54.52%,远高于IN-2和IN-1;模拟蒸馏结果表明,IN-3正构烷烃得到了很大程度的去除,缺氧的IN-1对正构烷烃去除得较少;厌氧菌数量与胶质和沥青质去除率之间成正相关关系,对于污染源较为分散的污染区域,采用原位生物强化修复时可以考虑引入厌氧修复。     

Estimation of uncertainty of sampling for analysis of pesticide residues

Abstract

A computer model was used to take random samples from primary sample populations obtained from field trials to simulate the uncertainty of sampling for residue analysis of plant commodities and soil. The results indicate about 40%, 30% and 20% relative uncertainty when random samples of size 5, 10 and 25 are taken respectively, from a single lot. Therefore the sample size should be the same for establishing and enforcing legal limits.     

不同泥源对厌氧氨氧化反应器启动的影响

采用2套上流式生物膜反应器,分别接种少量厌氧氨氧化污泥和大量硝化污泥,考察其对厌氧氨氧化反应器启动的影响。污泥接种入反应器后,测得接种厌氧氨氧化污泥的反应器(R1)内MLSS为0.22 g/L,另一个反应器(R2)MLSS为2.7 g/L。与直接接种厌氧氨氧化污泥相比,R1经过72 d的运行才显现出厌氧氨氧化特性。经过114 d的培养,前者氮去除速率由0.23 kg/(m3.d)提升到5.29 kg/(m3.d),总氮去除率大于89%;R2的氮去除速率由0.01 kg/(m3.d)提升到1.1 kg/(m3.d),总氮去除率大于84.6%。说明普通污泥启动需要一个较长的筛选过程,直接接种少量的厌氧氨氧化污泥比接种普通的污泥能够更快启动厌氧氨氧化反应器。     

次氯酸钠发生器的研制

介绍了电解法生产次氯酸钠的原理 ,并在原有生产工艺的基础上进行了重新设计和对设备的重新选择、改造 ,得出了各个工艺参数的最佳值 ,生产出高品质的次氯酸钠     

An application of the theory of kinematics of mixing to the study of tropospheric dispersion

The most common technique used for numerical simulations of tracer mixing is that of the numerical solution of the advection–diffusion equation with the unresolved fluxes parameterized using the similarity theory. Despite correct predictions of the overall directions of transport, models based on a numerical solution of the advection–diffusion equation lack sufficient accuracy to correctly reproduce the coupling of mixing with small scale processes which are sensitive to the microstructure of the tracer distribution. The objective of this paper is to revisit the basic formalism employed in numerical models used to investigate atmospheric tracers. The main mathematical method proposed here is the theory of kinematics of mixing which could be applied effectively for simulations of atmospheric transport processes. At the beginning of the paper, we introduce simple mathematical transformations in order to demonstrate how complex topological structures are created by mixing processes. These idealistic flow systems are essential to explain transport properties of much more complex three-dimensional geophysical flows. An example of the application of the kinematics of mixing to the analysis of tracer transport on a planetary scale is presented in the following sections. The complex filamentary structures simulated in the numerical experiment are evaluated using some commonly applied statistical measures in order to compare the results with the data published in the literature. The results of the experiment are also analysed with the help of simple conceptual models of fluid filaments. The microstructure of the tracer distribution introduced in the paper is essential to increase our understanding of atmospheric transport and to develop more realistic parameterizations of small-scale mixing. The presented results could also be used to improve calculations of the coupling between microphysical processes and tracer mixing.     

造纸废水混凝处理中SFT助凝替代性研究

中小造纸厂废水处理常用PAC作混凝剂 ,PAM作助凝剂。由于PAM成本很高 ,影响了处理设备的投运率。用超细滑石粉 (SFT)替代PAM助凝 ,与混凝剂PAC配合 ,其混凝处理效果基本相当 ,但是处理成本降低 0 .10元 /m3 。由于SFT属环境无害材料 ,不会给排泥带来二次污染     

红土吸附砷对其动电电位的影响

研究了遵义红土吸附砷对其动电电位的影响 ,从砷酸根浓度和体系pH对红土动电电位影响的角度作了探讨 ,结果表明 ,砷酸根离子浓度越大 ,Zata电位下降幅度越大 ,Zata电位也越低 ;随着体系pH的升高 ,氧化铁胶体动电电位逐渐下降 ,甚至改变了表面电位的符号。由此得出了红土吸附砷属于专性吸附的结论。     

活性炭三维电极法对印染废水的处理研究

对三维电极方法处理印染废水进行了实验研究,初步探讨了活性炭三维电极法处理印染废水的机理,对影响处理效果的各种要素,如反应时间、槽电压和pH值等进行了条件实验,得出了活性炭三维电极法处理印染废水的最佳运行条件为:停留时间120-180 min,槽电压25～30 V,进水pH值6.5～7.5。结果表明,该反应器能有效地降低废水色度,有较高的COD去除效率,并能提高印染废水的可生化性。     

生物质快速热裂解主要参数对生物油产率的影响

以松木木屑为原料,在自制的小型流化床上,开展了生物质热裂解温度、生物质粒径和进料速率对生物油产率的影响实验研究.结果表明,在热裂解温度分别为450、475、500、525和550℃条件下,当热裂解温度为500℃时,生物油产率最高,平均产率达到53.33%(质量百分比).反应温度越高,炭产量越低,不可冷凝气体产量越高,气体发热值越高;粒径＜1 mm的生物质其粒径对生物油产率影响不大;生物质进料速率增加时,生物油产率增加.本研究为生物能的利用提供了新的途径.     

Evaluation of the presence of drugs of abuse in tap waters

A total of seventy samples of drinking water were tested for non-controlled and illicit drugs. Of these, 43 were from Spanish cities, 15 from seven other European countries, three from Japan and nine from seven different Latin American countries. The most frequently detected compounds were caffeine, nicotine, cotinine, cocaine and its metabolite benzoylecgonine, methadone and its metabolite EDDP. The mean concentrations of non-controlled drugs were: for caffeine 50 and 19 ng L⁻¹, in Spanish and worldwide drinking water respectively and for nicotine 13 and 19 ng L⁻¹. Illicit drugs were sparsely present and usually at ultratrace level (<1 ng L⁻¹). For example, cocaine has mean values of 0.4 (Spain) and 0.3 ng L⁻¹ (worldwide), whereas for benzoylecgonine, these mean values were 0.4 and 1.8 ng L⁻¹, respectively. Higher concentrations of benzoylecgonine were found in Latin American samples (up to 15 ng L⁻¹). No opiates were identified in any sample but the presence of methadone and EDDP was frequently detected. Total mean values for EDDP were 0.4 ng L⁻¹ (Spain) and 0.3 ng L⁻¹ (worldwide). Very few samples tested positive for amphetamines, in line with the reactivity of chlorine with these compounds. No cannabinoids, LSD, ketamine, fentanyl and PCP were detected.     

Visualisation of the complexity of EUSES

The interdependencies of parameters applied in the models of EUSES are visualised in a directed connectivity graph. The parameters (inputs, defaults, state variables, outputs) are represented by boxes (nodes) and their relations by lines (edges). The visualisation, on the one hand, clarifies the complexity of the models in EUSES and, on the other hand, creates an overview and transparency. The parameters’ relations to each other can be recognised faster, and the models can be better understood. The complexity was quantified by the number (variety), kind (substance parameter, physico-chemical parameter, concentration, other parameters), and depth (dimension) of the parameter and the number of relations (connectivity). The variety of EUSES (without the modelsSimple Treat andSimple Box whose interior structure is not documented and without the effect and risk characterisation) amounts to 466, the connectivity to 961, and the maximal dimension is 21.